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Home My WebLink AboutCT 00-06; BRESSI RANCH MASTER TENTATIVE VOL II; BRESSI RANCH MASS GRADING; 2003-02-01It i� • f�k � DRAINAGE REPORT FQR BRESSI RANCH MASS GRADING CARLSBAD, CALIF4RNIA CT 00-06 � � Dwg 400-SA, 400-SC, 400-SD FEBRUARY 2003 voLUME il Prepared for LENNAR COMMUNITIES c/o LENNAR BRESS� VENTURE, LLC S7&0 F7eet Street, Suite 320 Carlsbad, CA 92008 Prepared By: PROJECTDESIGN CONSULTANTS 701 `B' Street, Surte 800 San Diego, CA 92101 (619) 235-6471 Job No. 224�.00 Adolph Lugo ' RCE 50998 Registration Expires 09/30/05 v �" �"o � �? � �' �-. G� � � � � 0 c� w� C� � � �� ` � . DRAINAGE REPORT FOR BRESSI RANCH MASS GRADING CARLSBAD, CALIFORNIA CT 00-06 Dwg 400-$A, 400-8C, 400-8D FEBRUARY 2003 VOLUME II u Prepared for LENNAR COMMUNITIES clo LENNAR BRESSI VENTURE, LLC 5780 Fleet Street, Suite 320 Carlsbad, CA 92008 Prepared By: PROJECTDESIGN C4NSULTANTS 701 `B' Street, Suite 800 San Diego, CA 921Q1 (619)235-6471 Job No. 2244.00 �� Adolph Lugo RCE 50998 Registration Expires 09/30/05 � �� APPENDICES L� • VOLUME Il AES Pipeflow Computer Output � � \, / l� 0 � � �� w �, �./ � � i� I � APPENDZX 4 AES PIPEFLOV�' COMPUTER OUTPUT � .� � . � � APPENDIX 4.1 ULTiMATE CONDITIQN % �\ �� NODE NUMBER COMPARISON SYSTEM 100 AES Pi efiow A�S Rational Method AES Pi eflow AE5 Rational Method 100.d0 125.00 140.00 105.00 100.05 125.00 140.1 d 105.00 100.10 125.Q0 1402Q 105.1 � l 0a.i 5 125.b� 144.50 105A0 i Od.20 1 � 7.OQ 14a.64 105. � 1 100.30 117.00 i 4d.90 105.00 103.00 -- 15D.00 -- 105.00 116.00 150.90 -- 105.10 116.00 160.00 1 d2.00 105.20 116.2Q '� 60.10 1 Q2.00 i 05.50 116.00 16Q.20 102.20 105.60 � 16.04 160.50 102.30 105.90 116.00 160.fiD 1 D2.30 � Dfi.00 -- 164.90 102.34 10fi.1 D -- 170.00 101.00 10620 -- 170.90 101.OU 11 D.00 � 115.00 175.00 i 00.30 110.10 115.00 175.90 -- 110.20 112.30 176.00 -- 110.9Q 115.00 112.Oa 111.D0 112,14 111.Op 1122d 111.20 112.50 111.00 112.60 11�.10 112.90 1 i 1.00 1 i 3.00 - 1 i 4.04 -- 114.90 -- 12D.00 1 Q8.00 120.90 • 1 Q8.00 124.00 108.00 124.1 Q 107.90 124.1 � 1 Q7.91 125.Q0 1 d7.00 125.10 107.00 125.2� 106.91 125.50 1 d7.00 125.60 107.60 125.90 107.00 12fi.00 -- � 2s.so -- � T \ /' . • � \ ,� n U . NQDE NUMBER C4MPARISON SYSTE M 102 AES Pi eilow AE5 Rational Method � 02.OQ 1 i 7.30 i 02.1 Q 117. aD 10220 117.20 102.21 117.11 �D222 i�7.1� i 02.30 1 i 7.20 102.40 117.11 1 Q2.41 117.11 102.50 117. i i 102.51 � 17.11 102.fi0 117.11 102.94 — �J ►� � . • NODE NUMBER COIVIPARISON . SYSTEM 130 AES Pi efkow AES Rational Method � 30.00 106.00 130.90 10fi.D0 131.00 106.00 131.1 Q -- 132.00 i Dfi.60 132.10 i Ofi.00 132.20 106.a0 132.50 106.00 132.50 106.50 132.90 1 pfi.00 133.00 106.30 133.90 106.3a i 35.00 -- � 35.90 - 136. QO -- i 36.90 -- 137.00 -- 138.Od 106.7 4 139.00 105.50 139.1 Q 105.50 139.20 � 05.3Q 139.90 105.5d � 4 � r� � . NODE NUNIBER COMPARISON SYSTEM 200 AES Pi eflow AES Rational Method AES Pi eflow AE5 Fiational Method 20D.Q0 i 15.00 235.20 -- 203.00 204.00 235.90 203.04 2a3.90 204.04 235.91 -- 205.00 210.00 236.00 202.50 205.10 210.00 236.90 202.50 205.20 21 D.10 240.00 -- 205.50 210.00 240.20 202.D0 205.60 210.2Q 2aD.30 200.20 205.7U 210.20 240.40 202.00 205.$0 -- 240.50 201.20 205.9Q 210.00 241.00 202.00 210.Od 206.00 210.50 206.00 210.60 206.40 210.90 206.00 � 215.00 -- � 215.90 -- 22a.00 -- 22a.sa -- 2z�.00 2d5.00 225.10 2Q5.00 22520 205.10 225.50 205.2D 225.60 205.20 225.90 2Q5.OQ 235.00 2Q3.00 235.10 203.04 C � � � ri LJ l � � � • NODE NUMBER COMPARISON SYSTEM 400 AES Pi fkow AES Ratianaa Method 400.00 420.D0 401.00 420.OD 4p5.00 415.00 405.10 � 415.00 405.10 415.00 4Q5.20 415.00 40fi. 3 0 411.SD 4pg. gp 411.50 4 i 0.10 416.04 � 410.20 410.OU 41 p.30 408.30 410.40 4i O.DO 4i a.50 410.10 410.9� 410.00 �� r 1 L� �� • • • NQDE NUMBER COMPARfSON SYSTEM 414 AES Pi etlow AE5 Rational Met�od 4� 4.00 415.00 414.10 • -- 414.20 -- 415.00 -- � 415.10 -- 42a.00 405A0 424.10 405.00 42Q.20 405.2Q 424.50 405.00 420,fi0 4fl5.10 420.90 405.00 422.00 -- 422.10 -- 422.20 -- 422.30 4Q0.20 �� C� • i . NODE NUMBER COMPARISON SYSTEM 800 AES Pi flow AES Rational Method 800.00 2020.00 801.00 202a.00 $02.00 2010.04 8(}2.90 2010.00 � 843.OD 8i 0.00 845.90 810.00 8i O.OQ -- 81 D.90 - 815.00 -- 815.90 -- 820.00 809.04 820.10 809.a0 62Q.90 808.40 821.00 8Q9.00 ' 822.00 SOfi.00 822.90 606.00 823.00 1040.04 825.OD 806.Q0 825. � 0 805.00 825.50 8Q5.00 825.60 805.23 826.00 805.00 826.14 805.13 � • • NODE NUIVIBER COMPAR�SON. SYSTEM 2004 AES Pi flaw AES Rational MeShod 2aoa.00 -- 2000.20 -- 2000.50 -- 2000.60 20� 6.� 0 20d0.70 2016.10 2001.D0 2D� 5.00 20U1.10 2015.D0 2001.20 2009.00 200�.7a 2D15A0 20D1.90 2015.00 20D2.00 -- 2003.00 -- 2003.90 -- 2005.00 2047.Q0 2005.10 2d07.d0 200�.2o zoa7.2o 2oos.so 2oo�.ao 2005.60 2007. i 0 2005.90 2007.00 2006.Q0 -- 20� 4.00 __ 20� 0.90 -- 2011.00 -- 201 �.00 2006.00 2015.14 2006.10 202Q.00 20U5A0 . � • C� (/ r�� . i NODE NUMBER COMPARISON SYSTEM 4400 AES Pi ef4ow AES Raiionaf Method 400b.00 -- 4Q01.00 4010.00 4001.10 4010.00 4001.20 4pQ9.00 4001.5fl 4010.00 4001.60 4006.00 400i .70 4a10.OQ 400i .90 -- 4002.00 4007.OQ 4002.1 d 4007.00 4D02.54 400620 4002.51 400620 4002.52 a0D6.20 40Q5.00 -- � C� �� L_J • NODE NUMBER COMPARlS�N SYSTEM 5025 AES Pi eflow AES Rational Method so2o.ao �o2�.ao 5025.10 5028.30 5025.20 5028.30 5025.21 5028.20 5025.22 -- 5025.30 -- 5025.40 -- 5025.50 5423.00 5025.60 SQ23.00 5025.70 5022 • 50 5025.80 5023.00 5025.90 5422•20 � � � APPENDIX 4.1.1 SYSTEM 100 (ALINCANTE RD, `D' ST) � � **s***+�++*xt�r*t�*r*��r�t**�*�r+aiy�x*xWy***x++rtx*��x�**��tt��**t*++wa*�+� PIPE-FLOW HYD�tAULTCS COrSPViER PROGRA�1 PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION) (c} Copyright 1982-2002 Advanced Engineering 5oftware (aesJ Ver. 8.0 Release Bake: O1/O1/2a02 License Zb 1509 Analysis prepared by: P�20JECT DES7GN CONSLTLTAN'T'S 741 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 619-235-647I +�,r**+********��*�*��+*** DESCRIPTION OF STUDY ***�•***'*****«**�«+*++++* * BRESS� RANCH - ULTIE�fATE CONDITIONS * * SYSTEM 100 - DOWNSTREP.M QF CDS L3F1IT (NODES 100.0 TO 100.2 ' * 100-YEAR STORM EVF�f�T'I' ' �itt*t*t**rtrtrt+tti�y.t**�r**r******��rtrt+*w++*++++t*xt++y�tt**rr*rr�*st**+*+++� FILE NAME: p1DQDS.DAT TIt�fE/DATE OF S'I'L]DY: 13:09 O1/17/2043 *,.**�**+***�*��*�*..�**�******�*��**++.*+�++**+****�,,*��*******..**.,.*,.**��+��, GfiADUALLY VARIED FLOW AI�iALYSI5 FOR PIPE SYSTEM NODAL POINP STATUS TABLE {Note: "*" indicates nodal point data used.l UPSTREA�7 RiFN DOWNSTi�EAM RUN NODE MODEL PRESSl7RE PRESSURE+ FLOW PRE55URE+ NLTMBER PROC�SS H�T] ( FT j MOMEN`i'iTE�S ( POUNDS) DEPTH { FT) MQMENTi1�7 ( PO[TNDS ) � 100.D0- 5.36 2440fi.34 2.35* 45796.71 } FR�CTION 200.05- 5.16 2415b.32 2.32* 46465.21 } FRICTION 100.10- 9.93 Dc 23938.21 2.42* 441D2.S0 } FRICTION+$END 140.15- 9.93 Dc 23938.21 3.95* 26502.87 ] NNCTIQN 100.15- 5.26 23992.99 3.87* 26594.46 } FRTCTTpN+BEND 100.20- 4.93*Dc 23597.78 4.93*]]c 23697.78 MAXIMUM NC7MBER OF ENERGY BALANCES USED IN EACH PRdFII,E = 25 ------------------------------------------------------------------------------- NOTE: STEP,i)Y FLOW HYDRAULiC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIVE FORMULAE FAOM THE CURRENT LACRD,LACFCD, AI3D OCEt+�A DESiGN �3ANUALS. YrY� *#* t*tk**Yc*#* t*** 1� �Ir *i11*YliY YYlti i t***Yrii** k*?Yi *YiYr*?�F tfY t i�k t 1 t fY �kYr Yr i t*****k *# DUWNSTREAM PIPE FLOW CONTRpL DATA: NODE A3i3MBER = lOfl. Dfl FLpWLIi�FE ELEVATIOAI = �94. 64 PIPE FLOW = 46Q.20 CFS PIPE DIAMETER = 60.00 TNCHES ASSUA7E17 �OWNSTREAM CONTROL HGI. = 200.000 FEET ------------------------------------------------------------------------------- NODE lOD.00 : HGL =< 196.991>;EGL= � 236.99D>;FLOWLINE= � 194.640> �w+�.��.��w+*�� « �*��.+�.+�**��.��***+.�.��t+tt++�*�.�t**.+*��+t��.��*� FLOW PR�CESS FRON3 NODE 10a.00 TO NODE 1Q6.05 �S CODE = 1 UPSTREAM NODE 100.45 ELEVATION = 195.�9 {FLOW IS SUPERCRITICAI.,} ------------------------------------------------------------------------------ • CALCULATE FRICTIOAI L055ES{LACFCDJ: PIPE FLOW 460.24 CFS PIPE DIA3�iE'FER = SQ.OD INCI-IES 0 � PIPE LENGTH = 11.08 FEET MAND3ING'S N= 0.01300 --------------------_-___---____-----____- _-_------------------------------- NORM.�I, DEPTH{FTJ = 3.36 CRITICAL DEPTH(FT) = 4.93 ---------------------��_-------__�____________-------------------------------- -----------------------------------------------------------------W___--------_ UPST}2EAM CONTROL ASSUMED FLOWDEPTHIFT} = 2.32 GRAT�UALT.,X VARIED FLC?W PROFILE COMPUTED INF'ORMATION: D�STANCE FROM FLOW DEPTH VE�,OCITY SPECIFEC PRESSURE+ CONT'ROL ( F'I' ) ( FT ) { FT/ SEC }� ENERGY ( FT J t+IOMENTUM ( POUNDS j O.a00 2.324 51.972 43.989 4b465.21 11.Q86 2.351 5d.706 42.340 45796.71 -------------------------------------------------------------------------------- NODE 100.05 : HGL =< 197.514>;EGL= < 238.679>;FLOWLINE= � 195.190> +*******arx*��a,r++ra+**++*+r+*t*w**xw***++*+*r�*+**t***�w**rwrr*+s�+++*i*��*t+* �'LOW P�20CE5S FROM NODE 100.D5 TO NODE 100.10 TS CODE = 1 UPSTftEAM NODE lOQ.10 ELEI/ATIQN = 202.�4 fFJ�OW zS SUPEf2CRITICAL) CAi�CUt,ATE FRICTIQN LOSSES(LACFCDJ : ' PTPE FLOW = 460.2D CFS PIPE D�At+4ETER = 5Q.00 INCHES PTP� LENGTH = 18.80 FEET MANNING'S N- 0.01300 ------------------------------------------------------------------------------ NORMAI_, AEPTH(FT} - 1.85 CRITICAL DEPTH(FTi = 4.93 -------------------_-----------------------_..__--------------------------------- ------------------------------------------------------------------------------ 1JP5TREAM CO�PI'ROL ASS[FMED FLOWDEPTH { FT j= 2. 42 ------------------------------------------------------------------------------- GR.ADUALLY VAR�ED FLOW PROFILE Cp3+fPUTED INFpRMATIQN: DISTANCE FROM FLOW AEP'i'H VELOCITX SPECI�'IC PRESSURE+ � CONTRQL ( F'i' } { p'I' ) ( FT / SEC ) ENERGY ( F"P � MOI�4ENT[J�i { p{}jJNI?S i O.pdQ 2.429 48.760 39.365 44102.54 3.929 2.464 49.364 40.262 44627_78 8.097 2.3�7 49.963 41.195 4516b.59 12.525 2.354 50.617 42.163 45719.23 i7.24Q 2.331 51.267 A3.169 4628b.31 1$.80Q 2.324 �1.472 43.489 46465_22 ------------------------------------------------------------------------------ NODE �00.10 : HGL =< 2D4.5b4>;EGL= � 241.505>;FLOWLFNE= < 202.14Q> �*..��+�+*�.�**�*...��.�..***.,....*..*..,,.*.*��.*.�*�+****+**..�t+t+*+***�.*,. FLqW PRpCESS FROM NODE 100.10 'F`O NODE 100.35 IS COD£ = 3 [3PSTREAM NOD� 204.15 ELEVR'FION = 232.62 (FLOW I5 SUPERCRITICALi ------------------------------------------------------------------------------- CALCiFLATE PIPE-BEND LOSSESfOCEMAI: PIPE FLOW = 460.20 CFS P�PE DiAP4ETER = 60.Od INCHES CEN'd'RAL AfVGLE = 42.Ofl0 DEGREES MA�INING'S N= D.01300 _ PZPE LENGTH = $0.00 F'�E'3' ------------------------------------------------------------------------------ NOFZMAL DEPTH ( F'I'} � 3. . 83 CRITICAL DEPTH ( FT} - 9. 93 UPSTRF�M CONTROL ASSUMED FLOWDEPTH(FT� = 3.95 ---------------_---------------------------------------------------------------- ----------------------------------------------------------------__--_____------- GRI�Dl3ALLY VARIEi] FLOW PRpFILE COMPUTED IPiFORMATION: ------------------------------------------------------------------------------ DTSTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROI_, ( F"F } ( FT j ( FT / SEC ) ENERGY [ F'i 1 MOMENTUM ( POi.7DIDS J o.aaa 3.959 27.622 15.809 26502.87 3.240 3.8b9 28.216 16.239 25945.10 • 2.630 3.785 28.853 ].6.719 27427.73 4_1$7 3.744 29.535 17.254 27953.13 _�� .. . - � 5.930 3.515 34.267 17.848 28524.04 7.$84 3.53d 31.050 16.5�0 29143.52 10.075 3.945 3�.890 19.246 29815.07 12.537 3.360 32.79D 20.Db6 30542.62 15.349 3.275 33.755 24.979 31330.61 18.939 3.Z90 39.792 21.998 32i84.02 21.985 3.145 35.9D5 23.136 33�48.54 26.018 3.02Q 37.1D4 29.4Z0 34�1Q.54 30.b26 2.935 38.394 25.839 35397.32 35.921 2.854 39.787 27.446 35377.12 42.044 2.765 41.292 29.257 37559.40 49.181 2.fi80 42.921 31.304 39059.95 57.577 2.595 44.689 33.625 90�76.21 67.559 2.5�1 46.611 36.267 92237.52 79.634 2.425 48.706 39.285 99055.49 80.�00 2.424 48.760 39.3b5 99102.50 ------------------------------------------------------------------------------ NODE 100.15 : HGL =< 23b.574>,EGL= < 248.429>;FLOWLINE= � 232.620> ******+**+**+*.��*x****�**�+...+*.****+*�.+.��+w++++**+*+**x*+***+w+*w��*�*** FLOW PROCESS FROM NODE 10�.15 TO NOAE 100.15 IS CODE = 5 UPSTREAM NODE 104.15 ELEVATION = 232.62 (FLOW IS SUPERCRITICAL) ------------------------------------------------------------------------------ CAI�ULI�TE JUNCTION LQSSES : PIP£ FLOW DIAMETER ANGLE FLOWLIAIE CRIi'ICAL VELOCITY {CFS) (YNCHES] (DEGREES) £LEVATION DEP�'H{FT.} {FT/SEC) UPSTREAM 457.d0 fiQ.00 O.OD 232.62 9.93 2$.026 DC}WNSTREAM 46Q.2a b0.00 - 232.62 4.93 27.631 LATERAL #1 3.20 18.00 90.00 234.11 0.68 1.811 �ATERAL. #2 O.aO 4.40 0.00 0.04 O.Op 0.000 • Q5 4.40===Q5 EQUALS BASIN INFLTT=== LACFCD �73D OCEMA FLOW JUNC'FION FORMUIJ�E USED: DY=(Q2*V2-Q1•V1�C45(DELTAI)-(23*V3�`C05(DELTA3i- Q4*V4*COSfDELTA4))/;{A�tA2}�15.11+FRICTION LOS5E5 iIPSTREAl�1: MANNING'S N� 0.0�340; �'RICTION SLOPE = 0.03450 DCIWI3STREAM: MANNING'S N= 0.01300; FRTC�`ION SLOPE = 0.03399 AVERAGED FRICTZON SLOPE IN JUNC�'ION ASSiJMEb AS 0.03397 Ji.Jt3CTI0[d LENGTH = 1.5a FEET FRICTION LOSSES = 0.051 FEET EiJTRAI3CE LOSSES = 0.400 FEE2' JUNCTION E,OSSES = (DY+HV1-HV2j+(ENTRANCE LOSSES) JUNCTION LOSSES =( 0.257)+( Q.Q40) = D.257 ------------------------------------------------------------------------------ NODE 1Q0.15 : HGL =� 236.496>;EGL= < 246.686>;FLOwLINE= < 232.620> ♦�+�rr*wrr+s�rt****�r+�rii�+tr+a**++r*�ws�*�irt*s�+*+*r*rra*wrt*ar*frttt+***r+,r*x**f FLdW PROCE55 FROM FIODE 100.15 TO NODE 100.20 IS CODE = 3 UPSTi2EAM NOD� 1Dfl.20 ELEIIATIDN = 235.55 (FLpW IS SUPERCRITICAL} CALCULATE PIPE-BEND Lt?SSESfOCE�+3A) _ PIPE FLOW = 957.00 CFS PIPE DIAMETER = 60.D0 INCHES CENTRAL ANGLE = 1.6a0 DEGREES MANNiNG'S N= 0.01300 PIPE LENGTH = B.OQ FEET NORMAi� DEPTH{FT} - 1.89 CRITICAL DEPTi-1fFT) � 4.93 UPSTRF�IM CON'I'ROL ASSUMED FLOWDEPTH (F'i') = 4.93 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------ GRADUALLY VARIED FLOW PROFILE COMPiJ'I'BD II3FQRMATION: DISTANCETFROM^'^^ FLOW DEPTHT VELOCITY SPHCTF�CT`� PRESSURE} . p � • r • CONPROLiFT) a.00D a.i�s 0.497 1.047 1 .783 z.�ii 3.849 5.217 6.645 s.000 [FT) 9.932 9.809 9.585 4.561 9.438 4.314 9.191 9.067 3.944 3.s�a iFT/SEC} 23.330 23.564 23.697 24.311 2A.800 25.362 25.997 26.709 27.501 28.D17 EI3ERGY ( FT } 13.389 13.436 13.556 13 .'745 13.994 14.306 14.b92 15.151 15.b95 16.066 MOMEN'�'UM ( POUNDS ) 23647.78 23704.67 23851.�8 29071.90 24361.50 29718.67 25144.41 25641.3� 26213.58 26594.48 ------------------------------------------------------------------------------ NpDE 1D0.20 : HGL =< 240.482>;EGL= < 248.939>;FLOWLINE= < 235.550> iF iF * Yr * 1r * * * * * * �Ir il Yr Y� 1� f * * iF iY ri w f Y� �k * f f �Jr �Jr fr w * k w * * s * * t # � * } } * * * 1� �k i s * * * * * * * * s �F # * w i i. * * f 't + * f 't UPSTREAM PIPE FLOW CONTROL DATA: NODE NL7MBER = 100.20 FLOWLINE ELEVATION = 235.55 ASSUMED UPSTREAM CONTROL HGL = 240.46 FOR DOWNSTAEAM AUN ANALYSIS ------------------------------------------------------------------------------- END pF GRADUALLY VARIED FLOW ATIALYSIS � • ***��.,,,�.,.��*.��.�t�***...f��.�t�****��....�*�*��*f��.*��****��.....*****�.t PIPE-FLpW HYDRAULICS COMPU'I'�R PROGRAM PACKAGE {Reference: LACF'CD,LACRD, AND OCEMA HYDRAULICS CR�T�RION) (c) Copyright 19B2--2002 Advanced Engineering Software (aes} Ver. 8.4 Release Date: O1/O1/2002 License ID 1509 Analysis prepared by: PR03EC'T' DESIGN CONSULT7IN'I'S 701 'B' STREET, SUITE Bd0 SAN DIEGO, CA 92101 519-235-6471 • � *****+v.**rrt**+�w��*r+�s** DESCRIPTION OF STUDY +�*ww�**+t*Y**********+*+* * BAESSI RANCH - iFLTIMATE COI3DITIONS * � SYSTEM 100 - ALICAI3TE/GATEWAY CENTER DRIVE * * 100-YEA�i STORM EVEI3T: UPSTREAM OF CDS UNIT * ##�}iY******#i##Yr�*Y**i'M'M Y�*i��1'Y1t*�F 1�*#i1� i**ir*1�Y�Y*}ii ikiYk *�*�'k'M *i'f i1t**1r*#'F* FILE NAME: P100US.DAT TIME/DATE OF STE]�Y: 12:48 Ol/17/2003 y� tY��lr1r *#**tt1"!'! tt*'k11r**i� # I� � Yr't**yrYriF# # t 1'k** i iF'lri� ** Y�i YY*�r**yr'k'lrlr*# M t Y* t* 4� i*+�kt#!w i� * GRADUAI.LY VARIED FLOW ANALYSIS FQR PIPE SYSTEM i�IODAL POIfIT STATUS TABLE qNote: •*' indicates nodal point data used.) UPSTREAM RUN DOWi3STREAi�7 RUN NODE MODEL PRESSURE PRESSURE+ FT,OW PRESSURE+ NUMBER PRbCESS 4�iEAD ( FT ) I'40MEN7'LFM i POU�TDS j T�EPTH ( FT ) MOMEN'FUM I POClNDS j kdQ.30- 19.12* 34899.59 3.Q9 32831.30 } FRICTIOI3 ��2.00- 12.25* 32561.$0 } ,7Ui�ICTION 102.Qa- 15.79* 32646.54 ) FRYCTION+BEND } HYDRAULIC ,7UMP 102.90- }�1.26 27�53.47 } FRICTION 103.00- 4.$9 Dc 19440.65 } FRICTIOi3+BEND lOS.00- 4.89 Dc 19440.65 } ,7UNCTIOId 105.90- 5.05 19149.67 } FRICTION+BENA 146.00-- 4.89 Dc i9046.36 ) FRICTION 105.10- 4.89 Dc 19046.36 ) FRICTION+BEND 106.20- 4.89}Dc 19fl46.3E } FRICTTON 110.D0- 5.74* 200a�#•89 } ,TUNCTION 110.94- 11.22* 19472.59 } FR�CTION 112.00- 7.57* 150D5.4E } �NCTION 112.90- 7.47* 14663.2`_ } FRICT�ON 113.00- 7.71* 14957.9� } FRICTION+BEND 119.00- 8.Q7* 15901.3� 3.i$ 2.59 2.67* 3.1a* 3.29* 3.21{ 3.26* 3.68* 4.89*Dc 4.89 Dc 3.10 3_98 3.98 3.75 3_61 31852.64 32063.75 30952.07 26265.36 24798.61 24770.40 24427.55 21885.93 190A6.36 19D46.38 14568.52 izlao.oi 11934.99 12313.30 12607.80 . } MPIVHOLE �14.90- 6.92* 13985.05 4.65 Dc 1�483.22 } FRICTIQN 120.00- 9.29* 1b894.36 4.65 �c 1?483.22 ) JUNCTION 12D.90- �0.88 1605d.45 2.16* 15531.93 ) FRICTION 124.QQ- 7.59 19080.85 2.25w i5997.D4 ) FRICTION 124.10- 3.4$ Dc 11518.25 3.13* 12047.45 ] JUNCTION 124.10- 4.13 1�b62.$5 2.95{ �2115.27 ] FRICTION 125.OQ- 3.48*Dc 11279.25 3.48"Dc �I279.25 } ,3UNCT�ON 125.90- 9.1&* 1Q780.19 2.27 9619.53 } FRICTION ) HYDRAULIC JUMP 126.00- 3.44 Dc 7370.95 2.48* 8657.37 } MANHOLE 126.90- 3.49 Dc 7370.45 2.4b* 8917.78 } FRICTION 130.00- 3.44 Dc 7370.95 3.09* 7591.86 } NNCTION 130.90- 5.26 7191.73 2.38* 7470.49 } PFtTCTTON 139.00- 3.41*Dc 611B.01 3.41�Dc 6118.42 ) JUNCTION 139.94- 7.36* 4714.52 1.51 3406.93 ) FRICTION } HYDRAULIC JL7I�P 144.Oa- 2.82 Dc 2222.25 �.76* 2896.12 � ) JUNCTI4N 140.90- 2.75 Dc 2285.77 1.83* 2833.98 ) FRICTiON 150.00- 2.75 Dc 2285.77 2.34* 2377.64 } rSAN7-IOLE ' 7.50.90- 2.75 Dc 2285.77 2.60" 2297.94 } FRICTIOI3 �60.00- 2.75 I]c 2285.77 1.68* 3Qb5.72 } JUNCTION 150.90- 3.15 2�65.31 1.4B* 345b.51 ) FRICTION 170.Q0- 2.69*Dc 2047.9b 2.69*Dc 2047.9b ) ,7UNCTIQN 170.9D- 5.95* 3399.03 2.69 Dc 2047.46 } FRICTTON 175.00- 6.0?* 3452.50 2.69 Dc 2047.96 } ,7UNCT�ON ?.75.90- 9.04' 4764.7$ 2.59 Dc 2047.96 } FRIC?'ION 176.00- 9.17* 4821.39 2.59 Dc 2D47.96 -------------------------------------------_____------------------------------- [y3AXIMUM NUMBER 0�' ENERGY BALANCES USED IN EAC1-i PAQFILE = 25 ------------------------------------------------------------------------------- NOTE: STEADY FLOW HYDRAULIC HEAD-LOSS CQMPUTATIONS BASED ON THE MOST C0135ERVAT�VE FORMUI,AE FRQM 7'HE CURRENT F�RCRD, LACFCD, AND OCEMA DESIGN MANLIALS . �r��r*trwy**y*w��:itiftii*+x***�w*r***x**�**wi�*++*s**r*++r**�rt��**fx+*:,r**�tt>a** FOWNSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = J.�0.30 FLOWLII3E EL�L7ATION = 235.88 • PIPE FLOW = 457.00 CFS PIPE DIAMETER = 60.04 INCHES ASSLTMED DOWNSTREAM CONTRpL HGL = 250.004 FEET r) � ------------------------------------------------------------------------------ NODE 100.30 : HGL =< 250.000>;EGL= < 25$.412>;FLOWLINE= < 235.880> �r�wx**+tkta��titr*ttr�Yr*iy+ri*tt+*++x+*�**xy+***�+�***�*++i+�itr*f*i*rsr�**�� FLOW PROCESS FROM NODE 100.3Q TO NODE 142.40 IS CODE = 1 �PSTREAM NODE 1a2.00 ELEVATION = 23$.44 {FLOW IS UNDER PftESSURE) ---------------�--------------------------------_____----__------------------- CALCULATE FRICTIpN LOSSESILACFCD): PIPE FLOW - 457.00 CFS PIPE DIAthETER = 60.00 INCHES PIPE LENGTH = 22.50 FEET MP.NNII3G'S N= 0_01300 SF=IQ/K)+*2 = (( 957.00}/{ 2604.413})*�2 - p.�3D79 HF=L*SF = ( 22.50)*;0.03079} - 0.643 -----------------------------------�___-------------------------------�___---- 3�70DE 102.00 : HGL =< 250.693>;EGL= < 259.104>,FLOWLINE= < 238.440> .*.�.*��+++f+�+..w:.�.+**.*..�**t+*.**�*.�*****�***+++,.*�+.+++..W.*+**��.+*�.* FLOW PROCESS FRpM A10DE 102.00 'i'O NODE 102.Ofl IS CODE � 5 UPSTREP.M NODE 102.fl0 ELEVATION = 238.44 (FLOW IS UNDER PRESSi3RE) --------------------------------------------------------------------_--__------- CALCULATE JUNCTIOAF LDSSES: PIPE FLOW DIAMETER ANGLE FLOWLIAiE CRITICAL VELOCITY (CFSi {INCHESj (QEGREES) ELEVATION DEPTH(FT.} (FT/SEC1 UPSTREAM 407.94 60.�00 Q.00 238.44 4.89 20.774 DOWiVSTREAM 457.00 60.04 - 236.44 4.43 23.275 i,ATERAL RZ 49.10 30.00 90.00 239.42 2.29 10.003 i�ATERAL #2 0.00 O.Ob 0.00 0.00 0.00 O.00d 45 0.00===Q5 EQUALS BASIN INPUT=== LACFCD AND OCEMA FI,OW JUNCTION F'ORMETLAE iiSED: • DY=(Q2*V2-Q�*V�*COS(DELTAIj-Q3}V3*COS{DELTA3)- Q4*V4*COS{DELTA4)}/((A1+A2)*16.1}+FRIC�FON LQSS£S UPSTREAM: MANNING'S N= 0.01300; FRICTION SLpPE = D.QZ453 D(}WNSTREAM: MPNNING'S N= 4.41300; FRICTIQN SLOPE = O.Q3079 AVERAGED FRTC7`ION SLOi'E IN JUNCTIOAi ASSUMED AS 0.02766 JUNCTIpI3 LENGTH � 2.50 FEET FRICTI013 IASSES = 0.069 FEE'r ENTR.ANCE LOSSES = Q.000 FEET JUNCTIOI3 LOSSES =( IJY+HV1-HV2 )� 1�I�7TR�f`ICE LOSSES ) JUNCTION L055E5 =( 1.780)t{ O.Q00) = 1_780 ------------------------------------------------------------------------------- NODE 102.OQ : HGL =< 254.183�;EG�= < 250.884>;Fi,dWLINE= < 238.444> *'!rf 1#f *i *tf *Y f Y Y ili�A *Y*ti i#t tt* tlrikYrlr*f�h �k i*##* f*i;iF*1�li�i�yr�Yl�1*�Y Y! Y**#*ir*'M #***f*�' FLOW PROCESS FROM NODE 142.04 TO I30DE 102.9a IS CODE = 3 i7PSTRE.�M NODE 102.90 EI,EVATIOI3 = 245.48 (HYDRAULIC JLTMP OCCURS) CALCl3I.ATE PIPE-BE1�D LpSSES{OCEMA} : PIPE FLOW � 4D7.90 CFS PIPE DIAMETER = 60.00 TNCHES CENTR.AL P,NGiE = 30.500 DEGREES MAAINYNG'S N= Q.013a0 PIPE LFNGTH = 64.47 FEET ------------------------------------------------------------------------------- HYDR.AULiC 3UMP: DOWI3STREAM RUN AI3RLYSIS RESU?�T'S NORM.�L 33EPTH ( FT f- 2. 42 CRI'FICAL DEPTH ( FT J= 4. 89 UPS'i'REAM COI3TROL ASSUMED Fi,OWD�PTH ( F`I') = 2. 67 GRADUAI,LY VARIED FLOW PROFILE COP4PUTED I1+�'DRMATION: DISTANCE FRONi FLOW DEPTH VELpCITY SPECIFIC PRESS[7RE+ • CONTROL{FTj (FTj (FT/SEC) ENERGY{gT) MOMENTUMlPOiJNDS) O.D�O• 2.673 36.�83 25.326 30952.07 . 6.7�2 2.663 38.362 25.528 31d86.e9 13.754 2.653 38.543 25.734 31223.�2 21_156 2.b43 38.725 25.943 3136U.76 28.952 2.533 38.909 26.155 31999.83 37.181 2.523 39.095 26.371 31640.36 45.887 2.b13 39.283 26.589 31782.37 55.123 2.503 39.473 26.811 31925.86 b9.470 2.593 39_655 27.026 32063.75 ------------------------------------------------------------------------------ 3-IYD�AULIC JUMP: UPSTREAM RUN ANALYSIS RESULTS DOWNSTREAM CONTROi, ASSi]�IED PRESSURE HEAD(FT) = 15.79 PRES5IJRE FLOW PROFILE CON3P[]`f'ED INFORMATIpN: ------_------------------------------------------------------------------------� DISTANCE FROM PRESSURE VELOCI�`Y SPECIPIC PRESSURE+ CONTROL(FT} HEAI)(FT} (FT/5EC) ENERGYIFTj MOMEI+T'PUM{pOUNDS) 0.000 15.743 20.774 22.444 32b46.54 69.474 11.259 2�.774 17.961 27153.47 ------------------------END OF HYDRAULIC JUMP ANALYSIS--------------_..__.._---- PRESSURE+MOMENTUM BALANCE OCCURS AT 8.27 FEET UPSTREIIM OF NODE 1Q2.00 � DOWI3STREAM �EPTH =i5.157 FEET, UPS'T'REAM CQNJUGATE DEPTH = 2.602 FEE'P � NOIlE 102.40 : HGL =< 246.153>;EGL= < 270.806>rFLOWLINE= < 245.4$0> *r****�r*i�+,�***x�*****+�ii+tw�++*s*�y++***+**xx*w*+wx+s***,r**++*f+rti+txx*�**x* FLOW PROCESS FROM FIOiIE 102.9Q TO NODE 103.00 IS CODE = 1 . UPSTREAT4 NODE �03_04 ELEVATiOId = 260.57 (FLRW IS SUPERCRiTICAL) ------------------------------------------------------------------------------ • CALCULATE FRICTION LOSSES(LACFCD): - PTPE FLOW 407.90 CF5 PIPE DIAMETER = 60.aa INCHES PIPE LEA7GTH = 132.71 FEET MANNING'S N 0.01300 ________________....__-----------------------------___----------------------------_ NO�tMAi.. DEP'I'H ( FT} - 2. 3 9 CRITICAL AEPTI-1 { FT )= 4. 8 9 UP5Ti2EAN3 CONTROL ASS[TMED FLOWDEPTH ( FT) = 3.10 GI�I:DUALLY VARIED FLOW PROFILE COMPUTED I�iF'ORMATION: --------------------------------------------------------------------------___-- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CQNTROL(FT) IFT) IFT/SEC} FNERGY(FT) MOMENTUM{POUNDSj O.ODD 3.102 31.657 18.871 26265.36 4.947 3.074 32.204 19.188 2651b.54 ' 10.202 3.046 32.556 19.516 26774.75 15.746 3.�17 32.922 19.858 27040.20 • 21.761 2.989 33.294 2D.213 . 27313.12 28.1.35 2.961 33.677 20.582 27593.73 34.963 2.933 34.066 20.965 27882.28 42.295 2.904 34.470 21.365 28179.02 50.191 2.876 34.682 21.782 28484_21 58.722 2.848 35.305 22.215 28798.13 67.974 2.819 35.739 22.66b 29121.07 78.048 2.791 36_185 23.135 29453.32 89.474 2.763 36.642 23.624 29795.2a I01.195 2.739 37.112 24.139 30147.04 �19.539 2.706 37.594 24.6b5 34509.19 129.595 2.676 38.D90 25.221 30882.01 132.710 2.673 38.183 25.326 30952.07 -------------------------------------------------------------------------------- • NODE 103.00 : HGL =< 263.b72>;EGL= � 279.441>;FLOWLINE= � 260.57Q> � * � * * * � * * * t * * * * t * t * # � * # 1 # f * + * * * * * * f Y * 4 f * < # } * ! Y f � Y i � � Y f * i * i * * Y Y # Y i � Y # i * * i * i i # * * * FLOW PROCE55 FAOM NODE 103.00 TO NODE 1D5.00 �S CODE = 3 UPSTREAM NODE 105.OQ BLEITATION = 263.53 {FLOW I5 SUPERCRITICA�I.) ------------------------------------------------------------------------------ CALCULR`i`E PIPE-BEND LOSSES(OCEMAf: PIPE FLOW = 407.90 CF5 PIPE DIAME'i'ER = 6fl.D0 INCHES CE3dTRAL AI3GLE = 5.200 DEGREES MPJ3NING' S N= 0. 01300 PX�E LENGTH = 26.D1 FEET ----------_______r------------------------------------------------------------ NORt�4AL i1EPTH{FT) = 2.39 CFtITICAL flEPTH(FT) = 4.89 UPSTRE.�M CON'PROL ASSUMED FLdWDEPTH(FTy = 3.29 GRADI}AI,LY VARIED F'LOW PROPSLE COMPUTED INFORMATION: ---------------------------------�_------------------------------------------- DISTA�ICE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ C OTI'I'ROL ( FT } ( FT } ( FT / SEC } ENERGY ( F"I`? MOMENTLTM { PO[JI+1D51 0.000 3.285 29.$11 17.099 24798.61 9.378 3.250 30.186 17.4Q7 25Q64.38 9.055 3.214 30.571 17.73b 25339.49 14.06D 3.178 30.969 1B.080 25524.29 19.427 3.143 31.378 1B.441 25919.12 25.7.92 3.107 31.801 16.820 26224.34 26.010 3.102 3�.657 16.871 262b5.36 ------------------------------------------------------------------------------ i�ODE 105.00 : HGL =< 266.815>;EGLY < 280.624>;FLOWLINE= � 2b3.530> *�..*+*..��.�**t+�+.***�.**+�t***�*******�**.*��**��****��*+#.�*��.*.t�*+�� FLOW PROCESS FRpM NODE 105.00 TQ NODE 105.90 xS CODE = 5 • UPSTR�M N017E IQ$.90 ELEVA'I'�ON = 263.86 (FLOW I5 SUPERCRITICAL} CAi,CULATE JCiNCTION LQSSES : PIPE FLOW DIAMETER ANGLE Fi�OWLINE CR�TICAL �IELOCITY (CFS) (INCHES) (DEGREES} ELEVATION DEP'iH{FT.j (FT/SEC} UPSTREAM 9Q3.Q0 60.00 O.OD 263.86 4.89 3Q.225 D04+TN5TREAM 907.90 60.00 - 263.53 4.89 29.$21 LATERAL #1 3.30 18.00 90.Op 267.00 O.b9 4.142 L�+TER7�L #2 �. 60 18. 00 90 . 00 267 . 00 0.48 3. 330 Q5 o.ao-==45 EQUALS BASIN INPUT=== LACFCD AND QCEMA FI.�OW JIJNCT10P1 FORMiTL,�E USED: DY=(42"`V2-Q1*VJ.*COS(BELTAI}-Q3*V3`CQ5(DEL'FA3)- Q4*V4*COSIDELTA4))/((A1+A2}*16.1j+FRICTION LOSSES UPSTREAM: MANNING'S N= 0.01344; FRIC'FI4N SLOPE = fl.04325 DOWNS'i'AEAM: MANNING'S N= 0.01344; FRICTION SLOPE = 0.04157 AVERAGED FRICTIQN SLOPE IN JUNCTION ASSUMED AS 0.04241 JUNCT�ON LENGTH = 4.00 FEET FRICTION LOS5E5 = 0.170 FEET ENTRANCE LpSSES = O.OD4 FEET �UNCTION LOSSES = (DY+HV1-HV2}+{ENTFtANCE L�55ESa JUNCTTON LOSSES =( 0.634j+{ 0_000) = 0.634 ------------------------------------------------------------------------------- NODE 1D5.90 : HGL =< 2G7.073>;EGL= < 2$1.258>;FLOWLINE= < 263.860> *i�**�*ta**++Yrrrf*yi*��*t++*r***-,r*+.+*�*++rt�+i�ra�rta�riiittrr*+i+ta*+,��r*si+t*�+� - FLQW PROCESS FROM 2JOI]E 145.9Q TO NODE 106.Ofl IS COI}E = 3 UPSTREPI+3 NODE 106.00 ELEVATIOI3 = 266.28 (FLOW i5 SUPERCRITICAL) ------------------------------------------------------------------------------ CALCULATE PIPE-SE�iD LOSSES(OCEMA}: PIPE FLOW = 403.00 CFS PIPE DIAMETER = 60.Q4 INCHES � CENTFZP,I� ANGLE = 9.550 DEGREES MANNTNG'S N= 4.Q130d PTPE LEI3GTH = 47.42 FEET � --------�---------------------------------------------------_----------------- NORMAE, DEPTHiFT) = 3_D4 CRITICAL DEPTHfFT} 4.89 UPSTREAM CONTROL ASSUMED FLOWDEPTH(FT} - 3.26 ------------------------------------------A----------------------------------- ------------------------------------------------------------------------------ GRP.DUALLY VARIED �LOW PROFxLE COMPUTBD INFORMATION: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CON'I`Rd� ( F'F] ( FT) ( FT/ SEC } ENERGY ( FT } MOMF1VTi3M ( POUNpS ) O.QOD 3.259 29.728 16.990 24427.55 8.214 3.250 29.820 17.067 24492.35 16.824 3.241 29.913 17.144 24557.71 25.865 3.232 30.007 17.223 24623.63 35.376 3.223 30.102 17.302 2469D.13 45.406 3.215 30.197 17.383 24757.19 47.420 3.213 30.215 17.398 247']0.00 __-_--------------------------------------------------------------------------- NODE 106.00 : HGL =� 269.539>;EGL= < 283.270>;FLOWLINE= < 266_284> ***� i� *Yr**! � ir*ttt1� Yr Y 1 iYYi y*4*rt ti ik rt 4 Y 1 Y i Y i Y� Y 1*Y * f?Yr*1 i i 4! Y Y Y Y Mi �*#**i� **#i iy� *'!�*11k# FLOW PROCESS FRQM NODE 106.00 'I'Q NODE Z66.10 IS CODE = 1 UPSTREAM NODE 1a5.1D ELEVA`FION = 276.14 (FLOW IS SUPERCRITZCAL) CALCt3LATE FRiCTYON LOSSES(LACFCF): PIPE PLOW = 4D3.00 CFS PIPE AIAMETER = b0.00 INCHES P�PE LENGTH = 192.90 FEET MANNING'S N- Q.01340 ------------------------------------------------------------------------------ NORMAI, DEPTH{�j - 3.09 CRITICAL DEP�'H{Fi') = 4.89 _--_-_--__------------------------------------------------------------------------ ------------------------------------------------------------------------------ � -_UPSTREAM_CON'FROL-ASSUMED�FLOWDEPTH(FT)-=-----3�6$TT-»_F-LL=====__----`-`�y-`Y GRADUAi,LY VARIED FLOW PROFI�,E CO�7PU`PE13 iTFFQRMATiON: --------------------------------------------_____------------------------------- DISTANCE FAOM FLOW DEPTH VELOCI'I'Y SPECZFIC PRESSURE+ CONTRO�, ( FT ) ( FT ) ( FT / SEC ) EIQERGY ( FT ) t+30I�ENTUM { pptlrTDS ) 0.000 3.684 25.961 14.171 21885.93 6.268 3.656 26.174 14.302 2201�_73 12.921 3.632 26.371 14.437 22240.91 19.995 3.606 26.572 14.577 22273.55 27.529 3.580 26.777 14.721 22409.71 35.569 3.554 26.987 14.871 22549.47 99.168 3.52B 27.202 15.025 22692.9D 53.388 3.503 27.42� �5.1.85 22840.06 63.301 3.477 27.649 15.350 22991.1� 73.943 3.451 27.872 15.522 23145.09 85.565 3.425 28.106 15.699 23304.99 98.192 3.399 28.344 15.882 23468.04 1.11.873 3.373 28.587 16.071 23635_28 126.946 3.347 28.836 15.267 23806.81 143.597 3.321 29.D90 Zb.470 23962.74 162.130 3.296 29.349 Ifi.679 29163.17 182.945 3.270 29.614 16.896 29398.21 192.900 3.259 29.726 16.994 24427.55 ------------------------------------------------------------------------------ NODE 1Q6.10 : HGi, _< 279.824>;EGL= < 294.311>;FLOWLIIdE= < 276.140> *t*t*�r*rr**at++ttfai�+x+r++rt*++�**++++++i�++++t�:i.�i.a+t+*,r,r��*�*��*+**��w�*+x,t+* FLOW PROCESS FROM NOAE 106.1a TO NODE 1a6.20 IS CODE = 3 UPSTREAM NODE 106.24 ELEVAi'�QN = 2$1.44 (FLOW IS SUPERCRITICALJ � --------------------------------------------------------------------------- CALCULATE PIPE-BEND LOSSES(OCEMA): � P7PE FLOW = 403.00 CF5 PIPE DIAME�ER = 60.DQ INCHES CENTRAL ANGLE = 19.100 DEGREES MA2�NING'S N= 0_4�30D PIPE LENGTH = 103_88 FEET NORMAI, DEPTH(FT} = 3.04 CRITICAL DEPTH(FTJ = 9.89 'UPSTREAM CONTROL ASSUMED FLOWDEPTH{FT) = 4.$9 G�DUALLY VARIFD PLpW PROFILE CdMPiJi'ED INF'pRMATION: FISTANCE FROM FiAW DEPTH VELOCITY SPECIFIC PRESS[3RE+ CONTRpL ( FT ) ( FT ) ( F�' 1 SEC ? ENERGY ( FT ) M0�]II3Ti3i+� ( POiJi+IDS } 0.000 4.889 2D.b34 11.549 19046.36 0.389 4.815 20.767 11.515 19D60.52 �.465 4.741 24.931 11.548 19099.71 3.154 4.657 21.123 11.599 19160.93 5.933 4.593 21.340 11.66$ 19242.62 8.3Q3 4.519 21.580 11.755 19343.90 11.788 4.445 21.844 11.$59 19469.37 15.924 4.371 22.131 �1.981 19603.89 20.765 4.297 22.441 �2.122 19762.59 26.379 4.223 22.775 12.282 19990.74 32.857 4.149 23.132 12.463 24138.79 40.311 4.075 23.514 �2.665 20357.32 4B.880 4.001 23.921 12.892 20597.05 56.743 3.927 29.355 13.�43 20858.81 70.128 3.853 24.816 13.921 21143.59 83.332 3.779 25.307 13.729 21452.46 98.747 3.�05 25.828 14.069 21786.69 . --------1.03_88�-----____..3^684-----25_981-----»--J14'�71---------21885_93__..__ NODE 1a6.2D : HGz� _< 286.329>;EGL= < 292.944�;FLOwLTNE= < 281.440> x***w�w+++*w*++**+*+++r++*+ai�xx+�**W*+***+**+***+.*,rww*�**�*xx**+wi.+**wt+*++r**x FLOW PROCESS FROM NODE 106.2� TO NODE 110.00 I5 CQDE = 1 UPSTREAM NODE 110.00 ELEVATION = 283.85 (FLOW UNSEALS IN RL�ACH] CALCiTi�ATE FRTCTTpN LpSSES;i,ACFCD) : PIPE FLOW = 403.OD CFS PIPE �IAME'FER = 6fl.d0 INCHES PIPE LENGTH = 133.86 FEET MANN�NG'S N= 0.01300 __=> NORMAL PIPE�'LOW IS PAESSi7RE FLOW • N4RMAL DEPTH(FT) = 5.00 CRITICAL DEPTH(FT) = 4.89 �HDC3WN5TREAM CONTROL ASSiJMED FLOWDEPTHiFT� = 4.B9 Gi�ADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: -------__�----------------------------___-------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSUAE+ CONTROL(FT) (F?`1 iFT/SECf ENERGY(FT) MOMENTUM(PdUNDS) 0.000 9.889 20.634 11.504 19Q46.36 D.014 9.893 20.627 1].5d4 19046.43 O.D55 9.898 2D.620 11.504 19046.58 0.123 4.902 20.514 11.544 19045.87 0.218 9.906 2Q.607 11.545 19D47.27 0.340 9.911 20.6a1 11.505 19447.8� 0.489 9.915 20.595 11.5ab 19d48.45 0.664 9.920 20.589 11.506 19049.22 0.667 9.924 20.583 11.547 1905d.13 • 1.095 9.929 20.577 11.50$ 1905?.27 1.350 9.933 2p.572 11.549 19052.39 r1 L_.J l � i 20.567 20.562 20.557 20.552 2Q.548 20.543 20.539 20.535 20.532 20.529 20.526 20_523 20.52i 2�.519 20.518 11.51D 11.51I 11.512 11.514 11.515 11.517 11.519 11.521 11.523 11..526 11.528 11.531 11.534 11.537 11.541 19053.66 19055.12 19056.74 19058.51 1906Q.45 19062.56 19054.8fi �9067.34 19074.Q3 i9072.94 I9p76.�0 19479.53 19083.28 19487.91 19492.12 133.860 5.745 20.525 12.286 20004.87 -------------------------------�---------------------------------------------- 730DE 110.00 : HGL =< 289.595>;EGL= � 296.135>;FLOWLINE= < 263.�850� 1.531 9.938 1.939 4.942 2.272 9.947 2.632 4.951 3.018 9.955 3.43d 9.9b0 3.869 4.9fi4 9.335 4.9b9 9.827 4.973 5.348 4.978 5.897 4.982 b.975 4.987 7.Q87 4.99t 7.735 4.99b 8.434 5.OD0 ___> FLOW IS UNDER PRE$Si7RE �k111i1iiYr*i i*�kt�kY*YYYtYtti ***irk�F�/riFY�iFffwY�itM*�Fff*�k'k4tlfik+fitf lffif4lti�k�kiYr�rYrY�Y� # FLOW PROCESS FROM NODE iio.aa TO i30DE ll0.90 �S CObE = 5 i3PSTREAM AIpDE 110.90 ELEVATIOI3 = 28g.18 {FLOW xS UNDER PRESSURE) CALCiJT�ATE JUNCT�ON LpSSES: P�PE FLOW DZAME'i'ER AAIGLE F�,OWLINE CRi'I'�CAL V�LOCI`1'Y (CFS) {z�ICHES) (DEGREES) ELEVATION DEPTH{F'F.J (FT/SECi UPSTREAM 298.4D 60.Q0 4.Dfl 284.1$ 4.66 15.197 DOWNSTREAM 403.00 60.0� - 2$3.85 4.$9 20.525 LATERAL #3 82.20 3b.4� 9fl.00 286.18 2.79 11.629 LATERAL �!2 22.40 24.44 45.00 286.85 1.69 7.130 Q5 0.00===Q5 EQUALS BASIN INPUT=== LACFCD AND OCEMA FLOW �UA3CTION FORi+1ULAE USED: DY=f4z*V2-Q1*V1*COSIDELTAI}-Q3 V3�C05(DELTA3)- ' Q4*V4*COS(DELTA4}j/((A1+A2)*16.1}+FRICTION LOSSES UPSTRF�M: MP.NNING'S N= O.Q7.3Q0; FRICTION SLOPE = 0.01313 DOWNSTRFF.M: MANNiNG'S N= 0.013a0; FRTCTTON SLOPE = 0.02394 AVERAGED FRICTION SLOPE Ii3 JCINCTION ASSUMED AS 0.01853 JUNCTION LENGTH = 4.00 FEET FRICT'ION L055ES = 0.074 FEET ENTRANCE LOSSES = 0.000 �'EET JUNC7'FON LC}SSES = (DY+HVl-iiV2)�(ENTRAATCE LOSSES) JUNC'FION LA55E5 = f 2.8501+( O.00Of = 2.850 NODE 1�0.94 : HGL =< 295.4dD>;EGL= � 298.987>;FLOWLINE= < 284.180� �.**.**.�*+.**�t�:k*.***�*�.+��**+..tit�*.*.***.�.***..*�..*�.�*�.....*.+++*+.*. Fi,OW PROCESS FROM NODE 1�4.90 TO NODE 112.D0 IS CODE = 1 UPSTFtF.AM NODE 112.a0 ELEVATTO�i = 289.52 IFLOW IS UNDER PRESSURE) ----------------------------------------_.._____--------------------------------- CAI,CULATE FRICTION LOSSES{LACFCDj: PIPE FLpW = 298.4D CFS PIPE DIAMETER = 64.00 INCHES PIPE LENGTH = 129.05 FEET MANI3ING'S N= 0.0�304 SF=(Q/K)**2 = S( 298.90)/( 2609.43311**2 = 0.42313 HF=L*5F = ( 129.45J*f0.01313? = 1.694 -----------------------------------------------..____---------__---------------- NODE 112.00 : HGL =� 297.094>;EGL= < 300.68�>;FLOWLINE- < 269.520> *.*�*�*.*,�**,,,..�.�...*�+t.+��w+�.*.**.>�:**.**.****..*,,..*+**.*,,.�+k*.��.. FLOW PROCESS FRbM NODE 112.00 'I'0 NODE 112.40 IS CODE = 5 UPSTREANi iQODE 112.90 ELE'�IATION = 284.85 {FLOW IS LTNDER PRESSUREj � --------------------------------------------------------------------------- CALCULATE J43A3CTION LOS5E5: PIPE FLpW D�AMETER ANGLE F�OWLINE CRITICAL VELOCITY (CFS} (�NCf-IESi (DEGREES) ELEVATION DEPTH(FT.) iFT/SEC) �iPSTREAM 294.70 60.00 0_Oa 289.85 4.65 15.009 bOWTISTREAM 248.40 b0.00 - 289.52 4.66 15.197 LATEKAL #1 2.1Q 18.OD 90.00 293.35 0.55 � 1.188 LATERAL #2 1.60 18.00 60.00 293.35 0.48 0.9fl5 Q5 0.00===Q5 EQIIAZ,S B.�SIi�i FIdPiTF=== LACFCD AND OCEI�A FLOW JUIVCTION FORMULAE US�D: DY=(Q2*V2-Q1*Vl*C05(DELTAlj-4�''V3wC05(DELTA3}- Q4*V9*COSIDELTA41i/((A1+A2)*Z6.1}+FRICTION i�05SES i7PS'TREAM: MANNING' S• N = D. 4�300 ; FFtICTIO�I Si3OPE = 0. Q128Q DOWNSTREAM: MAI�NING'S N= 0.01304; FKICTION SLOPE = O.D1313 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMEb AS 4.01296 JUNCTION LENGTH = 4.00 PE�T FRICTYON Lt}5SE5 = 0.052 FEET ENTRANCE Lt?SSES = D.DOp FEET ,TUNCTYOIV L055ES = (DY+HVI-I-LV2}+{FNTRANCE LOSSES} ' ,7iTNCTIOPI LOSSES = ( 4.139)+( O.Q40} = 0.�39 ----__-_------------------------------------------------------------------------ NOI�E 112.90 : HGL =� 297.322�;EG�.= < 300.82D>;FLOWLINE= < 289.SSU> *�**1�YcY�il YrY�Y#i�i�f i�#}�{*iiii*f1 YYY*t�iF*#�k1 #�M1i*#}}+#Y�i Y4�kiy�*YitiiYt#�tY�**kYrfYr*Y�* FLOW PROCESS FROM NOD� 1�2.90 TO NODE i13.0� IS CODE = 1 UPSTREAM NODE �13.ao ELEVATIOI3 = 290.69 (FLOW IS [7NDER P3tES5URE) -----------------------------------------------------------------_-_-_---------- CALCCTL�TE FRICTION LOSSES{LACFCD): PIPE FLOW = 294.70 CF5 PTPE DIAME'FER = 60.00 Ii�7CHES • PTPE LETFGTH = $4.39 FEET MANNENG'S N= 0.01300 SF-fQ/K1'�2 = [f 294.701/f 2604.464}}**2 = 0.01280 HF=L*SF = ( 84.391*10.01280} = Z.DSQ NODE 113.00 : HGi, _< 298.402>;EGL= < 34i.9D0>;�'LOWLIidE= � 290.690> �}�} Y 1� *#i� i*f� **� �'M'M'k k* 1r �'k'k iF k ikk iF �h Yr*}*1Y�*'t**t*#*ir *****�M iF f YrYrYc*�kYr**}**** **'t*i Y* k R**1� FLOW PROCESS FROM NODE 113.00 TO NODE 1Z4.00 �5 CODE = 3 UPSTREAi�4330DE 114.00 ELEVATION = 291.21 {FLOW IS UNDER PRESSURE} ------------------------------------------------------------------------------ CALC�LATE PIPE-BFND LOSSES{pCE3�SAj; PIPE FLOW = 294.70 CFS PIPE DIAi+�ETER = 60.00 INCHES CENTRAL A�iGLE = 6.D50 DEGREES MPNNTNG'S N= 0.01300 PIPE LENGTH = 51.i7 FEET BF�ID COEFFICIE?�TT(KB) = Q.06462 FLOW VELOCITX = 15.01 FEET/SEC. VELOCI�'lC HEAT3 = 3.498 FEET HB=KB*IVELOCITY HEAD1 =( 0.065)*( 3.498) = 0.227 SF=(Q/K�**2 = I( 294.70)/( 2604.427}}�*2 = 0_01280 HF=L*SF = ( 51.17]*f0.012601 = 0.655 7'O'I`AL HEAII LOSSES = HS + i-IF =( 0. 227 )+( 0. 555 )= 0. 882 `�NaDE 114.00 : HGL =< 299.284>;�GL= < 342.782>;FLOWLINE= < 291.210> +x**x+*t*+++*i.*++��ri+�*��i�++x�t*t+*+,tw�**x��++x*i.t�+��*�*�rw�rt+sx*at,t+r�,rx�+x�+ FLdW PROCESS FRQM NOJ.?E �14.00 TO NODE Z14.90 IS CObE = 2 UPSTREAM NdDE 1�4.90 EI.�EVATION = 292.54 {FLOW IS UNDER PRESSEJRE? CALCi7LATE MANHOLE I,OSSES;LACFCDj : PIPE FI.,QW - 294.70 CFS P�P� DIAI+3ETER = 60.00 INCHES FLOW VEL4CITX = 15.41 FEE'i'/SEC. VELOCITY HEAIJ = 3.498 FEET HMN = .05'(VELOCITY HEAD) _ .05*[ 3.498) = 0.175 • ----------------------------------------_--------------------------__----------- NODE 114.90 : HGL =< 299.459>;EGL= < 302.957>;FLOWLINE= � 292.54D> • 1 i * * t * * * i t * * * * * # � * * * * i * * � * k � * i i � i ? M * f i + + f i i i Y Y f * * * k * 1 � Y ti + Y � � Y f Y Y � * * t w * � f k w k rt * M FLQW PROCESS FROM NODE 1Z4.94 TO NODE 120.00 ZS CODE = 1 UPSTREAM NODE �20.00 EiEVATION = 296.48 (FLOW IS UNDER PRESSUREf ------------------------------------------------------------------------------ CALCULA'9'E FRICTION L055E5(LACFCD): PIPE FLOW = 294.70 CFS PIPE DIAMETER = 60.OD INCHES PiPE LENG'iH = 493.12 FEEi' MANNING'S 13 = 0.01300 SF={Q/K}**2 = ff 294.70}/{ 26D4.437})**2 = 0.01280 HF=L*SF = { 493.12}*(0.012801 = 6.314 ------------------------------__------------------------------------------------ NODE 120.00 : HGL =< 305.773>;EGL= < 369.271>;FLOWLINE= < 296.48D> �*+++++,�**+«+++r�**+*******++t�*�+****�**��+i*****+****�++�+++r*�r�*******+*..,. FLOW PROCESS FRqM NODE 120_00 TO NODE 120.9Q IS CQDE = 5 UPSTREAM NODE 120.90 ELEVATION = 297.98 (FLOW I5 UNDER PRESSURE) (I30TE: POSSIBLE 3UMP IN OR UPSTREAM OF STRUC�'URE} --------------------------------------------------------------------------�--- CAL,CULATE JUNCTION LQSSES: PIPE FLOW DIA�fETER ANGLE FLpWE,ENE CRITICAL VELOCI'FY (CF5? {ENCHES) iDEGREES} EI,EVATTON DEPTH(FT.} (FT/5EC) UPSTR� 229.iD 42.00 6D.00 297.98 3.46 36.404 DOWt�STRE.AM 294.70 6D.00 - 296.98 4.65 15.009 LATERAL �1 '65.6Q 36.D0 60.00 298.98 2.59 9.281 LATERAL #2 Q.OQ 0.00 0.00 4.00 0.00 0.000 Q5 a.aa==-�s EQLiALS BASIN INPU'P=== LACFCD AND OCEM71 FLOW JUNCTIOI3 FORMUi�AE USED: DY=fQ2*V2-Q1*Vl*COS4DEL`I'A1)-Q3"V3*COSlDEE.,TA3}- . • Q4�V4*COS(DELTA4?)/ilA1+A2f"'16.1)+FRICTTON LOSSES UPSTREAM: MANNING'S N= 0.013D0; FRICTION SLOPE = p.�0289 Z70WNSTREAM: MANNTNG'S N- 0.01300; FRICTION SLOPE D.�128D AVERAGED FRICTION SLOPE IN JUNCTIOI3 ASSUMED AS 0.05784 JUI3CTION LF33GTH = 4.00 FEET FRICTION L055ES = Q.231 FEET ENTRANCE LOSSES = 4.000 FEET Ji_TI3CTION L05SES = (DY+HVl-HV2 ) + (FN'I'RANCE LOSSES? �TT.Ti�FCTION LOSSES = (1�.45�}+( p.000i = 11.461 ------------------------------------------------------------------------------ NpDE 120.90 : HGL =< 340.158>;EGL= < 32D.732>;FLOWLINE= < 297.960> +�xww,�+�+*f*�+*�**�*t*W*-r�**+f*y+trt�*++�*++�***x�+**x*+�fi*+*t��*++i.�***t��*rr* FLOW PROCESS FROM NQD� 12D.90 TO tdODE 124_00 IS CODE = 1 UPSTRF}F�M idODE 124.Oa SLEVATION = 303.41 (FLOW IS SUPERCRITICAL) ------------------------------------------------------------------------------ CALCULATE FRICTION �,OSSES(i�ACFCD�: PIPE FLOW = 229_10 CPS PIPE DIAMETER = 42.04 INCHES PIPE LENGTH = 41.45 FEE'I' MANNING'S N= 0.01300 ----------------------------------------------------------------------------.._ NQRMAL DEP3`H f FT) = 2. O1 CRTTICAL DEPTH i F`d'? = 3. 48 yUPSTREAM CONTROL A55UMED FI,OWDEPTH(FT) = 2.25 GRADUALLY VARIED FLOW PROF�I,E COMPU3'ED INFORMA`PION: ------------------------------------------------------------------------------- DTSTANCE FROM FLOW DEPTf-1 VELOCITY SPECTFIC PRE55URE+ CONTROL ! FT ) ( FT ) ( FT / SEC 1 �NERGX { �"Z' ) MpM�1Ti7M ( POLTNDS ) 0.006 2.245 35.124 21.414 15497.09 4.633 2.236 35.293 21.589 16068.27 9.908 2.227 35.464 21.'768 16140.35 . 15.248 2.217 35.636 21.949 16213.33 20.678 2.208 35.811 22.134 16267_38 C J • C � 25.826 33.125 39.814 41.45Q 2.199 2 .190 2.lBfl 2.178 35.986 3b.166 36_347 36.389 22.322 16361.94 22.513 16437.61 22.707 16514.2D 22.752 16531.93 ------------------------------------------------------------------------------- NODE 124.OD : HGL =� 305.655>;EGL= � 324.824>;FLOWLINE= < 303.410> f ti**Yrf#�k#i�i'k'kY�Frt�i�Y i 1*tir*�kYriYr** i�#i�kl�kY�*#Yr�k�lrYrYriY# *Y��Mk i iFiFi��k###*Y4Yrkft**Yr Yr�kiF f 4 f*#* FLOW PROCESS FROM NODE 124.00 Tp NpDE 124.10 IS CODE = i UPSTREAM �IODE i24.1fl ,ELEVATION = 322.D0 {FLOW IS SUPERCRITICAL} CALCUi.ATE FRICTION LOSSESILACFCD): PEPE FLOW = 229.10 CFS PiPE DIAMETER = 42.D0 INCHES PYPE LENGTH = 141.3D FEET MANNING'S N= 0.01300 -------------------------- - NORMAL D£PTIi{FT} 2.0� CRITZCAL DEPTH{FT) = 3.48 i7PSTRF.AMRCON�'RQL A55UMED FLOWDEP`I'H S FT 1= 3. 13 GRADUALLY VARIED FLQW PROFILE COMPUTED INFORI�4ATION: -------------------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PFtESSURE+ CONTROL(FT} (FT) (FT/SEC) ENERGYSFTi MOMENTLTM(POUNDS) 4.000 3.126 25.255 13.436 12047.45 2.056 3.081 25.535 13.212 12146.12 4.347 3.036 25.833 13.A05 12253.86 6.890 2.992 26.152 13.618 12370.76 9.705 2.997 26.49fl 13.850 12496.96 12.B16 2.9D3 26.850 19.104 12632.63 16.252 2.858 27.230 14.379 12778.03 2D.048 2.813 27.632 14.677 12933.44 24.247 2.769 28.057 15.000 13D99.20 2g,gg7 2.729 28.505 15.399 13275.69 34.060 2.679 28.978 15.727 139b3.35 39.810 2.635 29.476 16.134 13662.66 46.236 2.590 30.D00 16.574 13879.14 53.453 2.546 30.553 17.049 Z4098.39 61.6Q4 2_501 31.134 17.562 14336.04 7a.875 2.456 3�.747 16.116 Z4567.$0 81.510 2.412 32.392 18.715 14854.45 93.894 2.367 33.072 19.361 15136.86 108.343 2.323 33.7$S 20.D61 15435.92 Z25.593 2.278 34.593 20.818 15752.67 I91.300 2.245 35.129 21.414 15997.04 NODE�T 124 10 HGL =� 325 126>;EGL= < 335.036>;FLOWLINE= � 322.OD0� «..,.**«*++t+{+fv...�+..t,t***.it**�*+*..*.+.�*:**�*�*..�**+�..+.�3t++�.****��+� FLOW PROCESS FROM NODE 124.1Q TO NODE 124.10 IS CODE = 5 iJPSTREAM NODE 129.10 ELEVATION = 322.00 (FIAW IS SUPERCRITICAL) CALCULATE JUNCTION LOSSES: PIPE FLOW DIAM�TER AI3GLE FLOWLINE C3tITICAL VELOCI`I'Y (CFSf fINCHESj (DEGREES} ELEVA'FION DEPTH(FT.) (FT/SECj UPSTREAM 225.40 92.Q0 0.04 322.40 3.48 26.056 DOWNSTREAM 229.1p 92.QQ - 322_00 3.48 25.264 LATERAL �1 3.70 18.64 90.00 322.57 a.73 2.094 LATERAL #�2 0.00 O.QO �.00 4.OD Q.00 0.000 ¢5 0.00===Q5 EQURiS SASIN INPU'F=== LACFCD ANd OCEMA FLOW JUNCTION FORMUl.AE �JSED: . DY=(Q2�V2-Q�'V1*C05(DELTAlj-Q3*V3'COSiDELTA31- Q4*V4'CQS(D�LTA4))/(lA1+A2)*16.1}+FRICTION L055ES UPSTAEAM: MANNING'S N= Q.01300; FRICTION SLOPE = 0.04791 DOWNSTREAM: M.�NNING'S N= Q.4�300; FRICTION SLOP� = 0.09595 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS 0.04694 JLFldCTION LENGTH = Z. 50 FEET FRIC'I'ION LOSSES = 0.070 FEET ENTAANCE LpSSES = 0.000 FEET 3UNCTION IASSES = IDY+HV1-HV2}+(ENTRANCE LQSSES) ,7L7I3CTION T�(}SSES = I �.456j+( 0.000} = 0.956 ---------------------------------------- NODE 124.10 : HGL =� 324.949>;EGL= < 335.492�,FLpWLINE= < 322.000> *'k� Y Y f**ik'li i�f # f## Y� f* ii** *!r* * ifl� 4*****yrY� **# t##�k t t�k�k'k'k 1� *Y� k'/�'M **f ��4 * i*�F *Yr*i�f'� *f tt F'LOW PAOCESS FRQM NODE 129.10 TO NODE 125.D0 I5 CODE = 1 UPS'I`REAM NODE 125.00 ELEVATIdN = 32A.28 (FLOW IS SIiPERCRITICAL) CALCUT�.�`PE FRICTION LOSSES(LACFCDI : PIPE FLOW = 225.40 CFS PIPE DIAMETE�2 = 42.Q0 INCFfES PIPE LENG'i'H = 17 .$1 �'EE'P MANNYNG' S N = 0.0�300 -------------------------------------- NORMAI� DEPTH(F'F') = 2.01 CATTICAL DEPTH(FTj = 3.48 _�-__- UPSTAE7�3 CONTROL ASSUMED FE,OWDEPTH I FT} = 3. 48 GRADUALLY VARIED FLOW PROFILE COMPUTED I�IFORMATTpN: -------------------------------- DI5'i'ANCE FROM FLOW DEPTH VELOCZ'1'Y SPECIFIC PRESSi7RE+ CONTROL {�'I' ) ( F"i' 1_ ( FT/ SEC 1 ENERGY l FT ) MOMIIVTUM ( POUIdEE?S } O.DDD 3.477 23.941 12.015 11279.25 • 0.352 3.418 23.5b2 12.044 �1296.71 1.214 3.360 23.74D 12.117 �1339.7q 2.474 3.3Q� 23.963 12.223 11902.50 4.096 3.242 24.225 12.360 114$2.57 6.072 3.183 24.523 12.527 11578.77 8.412 3.124 24.855 12.723 1].690.48 11.134 3.Ofi6 25_221 12.9A9 11817.48 14.271 3.007 25.622 13.207 11959.81 17.810 2.949 25.050 13.492 12115.27 ---------------------------------------------- NODE 125.OQ : HGL =< 327.757>;EGL= < 336.295>;FLOWLINE= � 324.280> ***�..�+***�*�****+�+++.****.«***+++w*+***�*+.��*�*+++.**,.*,,�*�++�..+**+�++r+* FLOW PROCESS FitOM NODE 125.a0 TO NODE 125.90 IS CODE = 5 LiPSTREAM NODE 125 . 94 Ei,EVAT1013 = 324 . 61 ( FLOW LTNSEAF�S TN REACH j CAI,CULATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLxNE CAITICAL VELOCITY fCFS? fiNCHES) (DEGREES} ELEVATION 1]EP`FHSFT.) (FT/SEC) UPSTREAM �77.34 42.00 0.00 324.61 3.44 18.428 DOWDISTREAM 225.40 42.04 - 324.28 3.48 23.448 LATERAL �41 99.80 30.00 60.00 325.61 2.22 4.�27 LATERAL #2 3.30 18.00 90.00 326.61 a.b4 1.867 Q5 0.00===(Z5 EQiJALS flASIN ENPLTP=== LACFCD ANA OCE�SA FLOW JUNCTTON FORMULAE USED: DY=(Q2*V2-Q7*V1�CQ5IDELTAI)-Q3*V3"`C05{DEL'T'A3]- Q4*V4*COSSDELTA4j}/((A1+A2)*16.1)+FRICT�ON L05SE5 UPSTFZEAM: MPNNING'S N= 0.01300; FRICTION SLOPE = 0.03105 DOWNSTR�AM: MANNING'S N= 0.013D0; FRICTION SLOPE = 0.04692 • AVERRGED FRICTION SLOPE IN JUNCTIOI3 ASSUMED AS d.03894 JUNCTION LENG�`H = 4_QO FEET • FRICTION LOSSES = D.156 FEET ENTRA�CE LOSSES = �.000 FEET �UNCTION LOSSES = (AY+HV1-HV2}+{�NTRANCE LOSSES) JUNCTI�iV LOSSES =( 2.748)+{ 0.000) = 2.�48 ---------------------------------------- NODE 125.90 : HGL =� 333.770>;�GL= < 339.043>;FLdWLINE= < 324.6ifl> *�+�*,.**�f�+*�w.t..�**.****«*****+�*.**��++�.t,***.*.****«**++��**�*,�***+w�*. FLOW PROCESS FROM IJODE �25.94 TQ NQDE 126.00 IS CODE = 1 UPSTREAM NODE 126.00 ELEVATION = 342.75 (HYDRA[3LIC JUMP OCC[3RS) ^^CAi,CULATE FRIC'I'�ON LOSSES(LACFCD}; PIPE FLOW = �77.30 CFS PIPE DIAMETER = 92.00 INCHES PIPE LENG'I'H = 32A.00 FEET MANNING'S N= 0.01300 HYDRAEJLIC^+7UMP: DOWNSTREAM RUN ANALYSIS RESUI,TS -------------------------------------- _ NORl+U�L DEPTH(F'I') = 2.25 CRITICAL DEPTHfFT} 3.44 UPSTREAM CONTROL�ASSLFMED FLOWDEP�'H(FT? = 2.98 GRADUALLY VARIED FLOW`PROFILE COMPUTETI INFOR2�IATION: DESTANCE'FROM FLOW DEPTH VELOCITY SPECIFIC PAESSURE+ CONTRbLIFT) (FT) (FT/SECj ENERGYIFT} MpMENTUMiPOUNDS) 0.4Q0 2.480 29.3]8 11.668 $657.37 5_p5g 2.971 29.416 11.733 B886.83 10.36b 2.96� 29.515 11.799 8916.67 15.958 2.952 24.b15 11.866 8946.86 21.856 2.493 24.716 11.935 8977.48 � 28.091 2.434 24.838 12.004 9QQ8.47 34.698 2.425 24.921 f2.Q75 9039.86 43.716 2.916 25.025 12.146 9471.64 99.193 2.406 25.131 12.2�9 9103.82 57.185 2.397 25.237 12.299 9136.42 65.759 2.388 25.345 12.369 9169.42 74.995 2.379 25.454 12.446 4202.84 84.992 2.370 25.564 12.524 9236_66 95.872 2.36� 2�_675 12.603 9270.96 107.794 2.353 25.788 12.684 93Q5.66 120.944 2.342 25.941 12.766 9340.8a 135.595 2.333 26.016 12.850 9375.38 152.D47 2_324 26.].32 12_935 94Z2.91 170.946 2.3J.5 26.2�4 13.021 9448.89 192.B69 2.306 26.368 13.109 9985.83 218.994 2.296 26.488 Z3.198 9523.24 251.207 2.267 26.610 13.289 9551.12 293.049 2.278 26.732 13.382 9599.47 324.D00 2.273 26.797 13.43D 4619.63 }iYDRAULIC J173�3P: UPSTRF.A1�4 RL3N ANALYSIS RESULTS _==--__-- --------------- -___ DOWNSTREAM CONTROL ASSUMED PRESSi.TF2E HEAD f F'I'? = 9. 16 PF2ESSURE Fi,OW PROFILE COMPUTED INFORMATION: 'DIS�'ANCE FROM PRESSURE VELOC�TY SPECIFIC PRESSU3�f CON'I'ROL ( FT ) HEAD { FT J ; FT/ SEC ) ENERGY ( F'T } i+10�'1�N'F'UM { POUNDS } D.d00 9.I60 16.428 14.433 i0786.i4 226.999 3.544 16_928 8.773 7382.33 i ----------------------------=-----��______=_______________=_=___�_______==__- ASStJMED DOWNS'I'REANS PRESSURE HEAD I F'T) = 3. 54 ________________��_�___________________________________=====Tv�=-==_________-_ GRADUAL.I.�Y VARIED FLOW PROFILE COMPU`1'ED I�QRMA'I'ION: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ COAi'I'ROI.� f F'T ) ( FT j ( FT / SEC } ENERGY ( FT j MOMENTUM { POUi3DS 1 226.999 3.5Q0 18.422 8.773 7382.33 227.480 3.498 18.423 8.771 7381.09 227.150 3.495 18.424 8.769 7380.02 227.212 3.993 18.425 8.768 7379.D5 227.269 3.491 18.427 8.76b 7378.16 227.3�21 3.4$9 1$_429 8.765 7377.34 227.368 3.4&6 19.431 8.764 737fi.58 227.412 3.483 18.433 8.763 7375.86 227.452 3.981 18.435 8.761 7375.24 227.489 3.479 18.437 8.760 7374.64 227.523 3.97b 1$.440 8.76a 7379.1D 227.554 3.974 18.442 8.759 7373.59 227.582 3.472 18.445 8.758 7373.13 227.6DB 3.969 1.8.448 8.757 7372.72 227.631 3.967 18.451 8.757 7372.34 227.652 3.465 18.454 8.756 7372.00 227.670 3.462 18.458 8.756 737I.69 227.687 3.460 18.461 8.755 7371.42 227.701 3.457 18.464 8.755 7371.19 227.713 3.455 18.468 $.754 7370.99 227.723 3.453 18.472 8.754 7370.82 227.731 3.k50 18.475 8.754 7370.69 227.737 3.448 18.479 8.754 7370.58 227.742 3.446 19.483 8.754 7370.51 227.744 3.443 18.487 8.753 737D.46 � � 227.745 3.441 18.491 8.753 7370.45 329.00fl 3.441 18.491 B.753 7374.45 ------------------------END OF HYDRAUL,IC JUMP ANALYSIS------------------------ I PRESSURE�MOMEN�'UM BALANCE OCCURS AT $2.1$ FEET UPSTREANF OF NODE 125.90 � DOWNSTRF�M DEPTH = 7.111 FEET, iJPSTREAM CON�3L]GATE DEPTH = 2.290 FEET � NOIIE �26.04 : HGL =< 345.230>;EGL- � 354.416>;F'LpWLI3+TE= � 3�2.75D> ******�*w..w*...**�+***+*.++.r.***.:.,r�*x****++,rr*�+i�.rr.*.*w*.*w��*.*.**t+*��r� FLOW PROCESS FROM NODE 126.00 TO NODE 126.90 IS CODE = 2 UPS'd`REAM NODE 126.90 ELEVATIOA3 = 343.08 (FLOW I5 SUPERCRIT�CAL) ------------------------------------------------------------------------------ CALCULATE MANHOLE IASSESfLACFCD}_ PIPE FLOW = 177.30 CFS PIPE DIAMETER = 42.00 INCHES AVERAGED VELOCITY HEAD = 9.265 FEET HrIId =.05"{AVERAGED VELOCTTY HEAD} _.05*f 9.265} = 0.463 NQAE 126.90 : HGL =< 395.54��;EGL- < 354.682>;FLpwL,zNE- < 343.080> �****,,.........*�***.**�.*.*�...***.�..*�*..,,.*...*****x*...******�*..,.*****�.t FLOW PROCESS FROM NODE 325.90 '�'O NODE �34.00 IS CODE = 1 UPSTREAM NODE 130.00 ELEVA'iION = 355.59 (FLOW FS SUPERCRITICAL} CAl�CTJLATE FRIC`PION LOSSES (LACFCDJ : PFPE FLOW - 177.30 CFS PIPE DIAMETER � 42,00 INCHES PIPE LENGTH = 263.67 FEET M.�NNING'S I3 - 0.01300 ------------------------------------------------------------------------------ NQRMAL DEP'I'H{F'T) = 2.38 CRITICAL DEPTH(FT) = 3.49 ------------------------------------------------------------------------------ � UPSTRF.AM C4NTROL ASSUMED FLOWDEPTH(FT} - 3.09 . GR�UALLY VART�U FLOW PR4FILE COMPUTED INFORMATIQN: DISTANCE FROM F�OW DEPTH 17�LOCITY SPECIFIC PRESSURE+ CdNTRQL ( FT } ( P�' j { F'P / SEC } ENERGY ( FT ) 2+1pMF.�I'I'i7M ( POUNDS } D.000 3.Q8b ]9.736 9.138 7591.86 3.028 3.Q58 �9.879 9.196 7625.33 6.334 3.Q34 20.028 9.262� 7661.03 9.939 3.061 20.184 9.331 7696.97 13.868 2.973 20.346 9.405 7739.17 18.i50 2.945 20.514 9.483 7761.67 22.819 2.917 2D.688 9.567 7826.50 27.915 2.889 20.869 9.656 7B73.69 33.985 2.860 21.057 9.75Q 7923.27 39.585 2.832 21.251 9.849 7975.31 46.284 2.804 21.452 9.954 8029.85 53.663 2.776 21.661 10.066 808b.94 61.823 2.747 21.876 10.183 8146.64 70.890 2.719 22.099 10.347 8209.02 8i.421 2.691 22.329 10.438 8279.15 92.422 2.663 22.567 10.576 8342.09 105.361 2.635 22.813 1D.721 84�2.92 Z20.204 2.5D6 23.Ob8 10.874 8486.74 i37.463 2.578 23.331 1�.036 85b3.62 157.888 2.550 23.602 11.205 8643.66 182.645 2.522 23.883 ii_389 8726.95 213.6$5 2.494 24.173 1�.572 8813.fi� 254.668 2.465 24.472 11.771 89Q3.75 263.670 2.461 29.519 11.802 8917.78 ------------------------------------------�__-_------------------------------- AFODE 130.00 : HGL =� 358.776>;EGL= � 369.828>;F'LOWLENE= < 355.690> . +*+****+*+�tf*+**+,**++.**t************„**..*,..,***++*+t*****t*:*.+*+.*.**+�+** FLOW PROCESS �'RQM NODE 130.Q4 TO NODE 130.90 IS CODE = 5 UPSTREAM NODE 130.90 ELEVATIdN = 356.02 (FLOW IS SUPERCRTTTCAL) CALCULATE ,7LiTTC`�'ION L05SES : PIPE FLOW DIAI�E'PER A�7GLE FLOWI�zNE CRITICAL VELOCITY [CF5} (I�iCHES1 (DEGREES) ELEVATION DEPTH(FT.a (F"P/SECj UPSTREAM 158.90 42.00 O.DO 355.02 3.41 22.778 DOWNSTREAM 177.30 42.00 - 355.b9 3.44 19.742 F�ATERAL #1 18.44 36.00 60.OQ 356.52 1.37 3.538 LATERAL �2 O.Qp a_00 4.00 4.04 0.00 0.040 Q5 0.60===Q5 EQURLS BASIN INPUT=== LACFCD AND pCEF�La, F�,OW �UNCTION FORMUi�AE USED: DY=(Q2`V2-Q1*V1*C05(DELTAl)-Q3*V3*CQS(DELTA3)- Q4�V4*COS(DELTA4f}/(�Al+A2]*16.1}+FRICTIpN LOSSES l3PSTREAM: MANNII3G'S N= 0.01300; FRICTIpN SLOPE = 0_03832 DOWNSTRFAM: MANNI[3G'S N= 0.01300; FRTCT70N SLOPE = 0.42788 AVERAGED FRICTION SLOPE IN �7I]�iCTIOAi ASSUMED AS 4.033Z4 ,7CJ�7CTION LENGTH = 4 . QO FEET FRICTION LOSSES = 4.132 FEET EN'i'RANCE LOSSES = D.{]00 FEET JiJI3CTI0i�7 LOSSES =(DY+HV1-HV2 J+{ EN`i'RANCE LOSSES) JUNCTTON LOS5ES =( 1.631]+{ Q.000) = 1.63� --------------------------------------------------------------------------------- NODE 136.90 :�GL =< 359.4�3>;�GL= < 366.459>;�LOwLINE= < 356.020> .,*t��**,�,.t�.��t.*.�**,,**.w*�.*�*.�*.*�*��+��.�t.xti*��t**t*��t*.,..*�.+**�� FLpW PROCESS FR03�f �iODE 130.90 TO NODE 139.00 IS COD� = 1 � --UPSTRFrA�] NODE 139.00 ELEVATION = 362.33 (FLOW IS Si7PERCRI'I'ICAL) ------------------------------------------_____------------------------- � CALCLII�ATE FRICTION LOSSES(LACFCD}: PIPE FLOW 158.90 CFS PIPE DIAMETER = 42.00 INCHES PIPE LENGTH = 116.B3 FEET MPNN�NG'S N= 0.01300 NORMT�L DEPTH ( FT} - 2. 12 CRITICAL DEP`I'H (FT) = 3. 91 ------------------ i3PSTREAM CONTROL ASSUMED FLOWDEPTH(FT} = 3.41 -------------------- GRADUALLY VA1xIID FLOW PROFILE COMPUTED INFdRMATI0IV: ------------------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC P13ESSU}t�+ COI3'I'ROL { FT ) ( FT ] ( FT / SEC i ENERGY f F"I` ) MOMENTUM { POL7ND5 ) 0.000 3.448 16.631 7.7Q5 5118.02 4.236 3.356 16.745 7.713 6122.54 • O.B70 3.304 16.883 7.733 6134.64 1.86$ 3.253 17.p43 7.766 6153.55 3.22D 3.2p1 17.222 7.809 6178.B6 4.929 3.149 17.420 7.864 6210.33 7.013 3.Q98 17.b37 7.931 6247.86 9.491 3.046 17.872 8.009 6291.44 ` 12.40Q 2.994 i8.126 8.099 6341.12 15.784 2.943 i8.398 8.202 6397.40 19.697 2.641 18.690 8.316 6454.25 24.2Q8 2.639 19.Oa1 8.449 6528.04 29.444 2.7$8 19.334 8.595 5603.62 35.395 2.736 19.687 8.756 6fi$6.27 92.321 2.689 20.063 8.938 b77b.29 50.365 2.533 20.463 9.138 5879.D6 59.768 2.581 20.BB7 9.359 b979.96 70.Bb1 2.529 21.337 9.603 7499.46 • 84.107 2_978 21.816 9.872 7218.04 1.OD.188 2.426 22.323 10.159 7351.27 116.830 2.383 22.77i 10.939 7470.09 ------------------------------------------------------------------__-----__--___ NODE 139.Oa : HGL =< 365.738>;EGL= < 370.035>;FLOWLTNE= < 362.330> Y Yif#i#i ti Y YiF#+*}#*YriFYr�k�k***i� ***� f* f�*i *ttYi �k Y YY 1* f 1f#**yr*!Yr*YrYr�/r*YrYrYrYrYi k Yrk YrYrYr*�F FLOW PROCESS FR4M NODE 139.00 �'Q NODE �39.90 TS CODE = 5 UPST1tEAM NODE 139.90 ELEVATION = 3fi2.83 (FLOW LTN5EAL5 IN REACH} ______..-----------------------------------------_--_----------------------------- CALC[JiJ�TE JUNCTION LOSSES: PIPE FLOW D�AME'T'ER ANGLE FLpWLINE CRITICAL VELDCITY (CF$) jTNCHESy (DEGREBS) ELEVATIOi3 DEPTH(FT.) {�/SEC) UPSTREAM $�.70 42.00 O.Op 362.B3 2.82 8.492 DOWNSTREAM 158.90 42.00 - 362.33 3.91 1.6.633 LATERAL #1 77.20 36.D� 95.00 352.83 2.79 10.922 LATERAL #2 0.00 0.00 �.40 0.00 �.00 O.00Q QS 0.00===Q5 EQUAi,S BASIN INPU'i'=== LACFCD AND OCEMA FLOW JUNCTION FORMULAE [35ED: DY={�Z*V2-QZ*V1*COSIDEE,TA1]-Q3*V3*COS[DEL'I'A3J- Q4*V4*CQS{DELTA9))1({A1+A2)*16.1)+FRICTIDI3 LOSSES iJPSTRFAi�i: MANNING'S N= 0.01300; FRICTIOiV SLOPE = O.OD659 DOWI35TREAM: �SANNFNG'S i+7 = O.fl130D; FRiCTION SLOPE = 0.02209 AVERAGED FRxCTION SE,OPE I23 JUNCTION ASSUMED AS 0.41439 JUNCTIQN LENGTH = 5.4D FEET FAICTZON LOSSES = 0.072 FEET F�ITRANCE L055E5 = 0.000 FEET JUNCTION LOSSES = (DYkHV1-HV2J+(ENTRANCE LOSSES) JUNC'FION Ld55ES ={ g,278?+S 4.04D) = 1.278 ------------------------------------------------------------------------------ � E30DE 139.90 : HGL =< 370.194>,EGL= < 371.313>;FLOWLINE= < 362.$30> � * * * # * * Y M i i f # # * k * * * * f * f � k * * * * * � * * * * * * * k * # k 1 * i * f ? * 1 k * * * f * * * * * * * # * * � * # * * * * � � * # f * * FLOW PROCESS FROM NODE �39.90 TO NODE 140.00 IS CODE = 1 UPSTREAM NODE 140.00 ELEVATIOI3 = 3fi8.00 (HYDRAUI.xC �i7MP OCCURS) CALCI3LATE FRICTION i3OSSES {F,p.CFCD} : PIPE FLOW = 81.70 CFS PIPE DIAMETER = 42.Q0 INCHES PIPE LEI�iGTH � 91.28 FEET MANNING'S N= 0.01300 ------------------------------------------------------------------------------ HYDRAETLIC JUMP: DOWNSTREAM RUTi ANALYSIS RESULTS NORMAL DEPTH{�"Z'} - 1.41 CRiTTCAL BEPTH{FT) = 2.82 UPSTREAM CONTFtOL ASSUMED FLOWDEPTH(FT} = 1.76 ---------------------------------------------___------------------------------- ------------------------------------------------------------------------------ GRADUALLY VARIED Fi,OW PRQFILE COMPUTED INFORt9ATIdN: D�STANCE FFtOM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CQNTROL ( FT j { FT f ( FT / SEC } Ei�IERGY ( F"I' ) i�70MENTL7A7 ( POUI+FDS ) D.000 �.758 16.875 6.183 2698.12 2.529 �.744 17.097 6.2bQ 2921.17 5.215 �.730 17.223 6.339 2944.62 8.Q73 �.717 17.402 6.422 2969.09 3�.119 i.703 17.585 6.507 2993.99 19.372 1.689 17.772 6.596 3019.54 �7.854 1.675 17.963 6.688 3D45.77 2�.592 1.661 18.157 6.783 3072.68 25.614 1.647 18.356 6.882 31D0.30 29.957 1.633 18.5b4 6.985 3128.64 39.662 1.619 18.757 7.fl91 3157.73 • 39.7B2 1.605 3$.980 7.202 3167.58 45.378 1.59� i9.i97 7.317 3218.22 51.529 1.577 19.4�8 7�.436 3249.68 58.332 1.563 19.645 7.560 3261.97 65.913 1.599 19.&77 7.688 3315.12 7A.439 1.535 20.115 7.822 3349.J5 . 84.134 1.521 2Q.358 7.960 3384.10 91.280 1.5�2 2Q.516 8.052 3406.93 ------------------------------------------------------------------------------ HYDRA[FLIC JUMP: iTPSTREAM RUN ANALYSIS RESULTS ---___----------------------------------------___-----------------------------_-- ------------------------------------------------------------------------------ DOWNSTREAM COI�!'ROL ASSUMED PRESSURE HEAD(F'4'} = 7.36 ------------------------------------------------------------------------------ -------------------------------_---------------------------�___�____----------- PRESSURE FE,OW PROFILE COMPUTED TNFORMATION: DISTANCE Fi20M PRESSURE VELOCTTY SPECIFIC PRESSURE+ CaNTitOL(FT) HEAD(FTj (FT/SSCj E1dERGY(FT) MOMENTUM(POUNDS} d.D00 7.364 8.492 8.463 4719.52 77.202 3.500 8.492 4.620 2395.08 ASSLT2�ED DOWNSTREAM PRESSLFRE HEAD { F'�'} - 3. 50 ------------------------------------------------------------------------------- ---------------------------------------------------------------__----___--------- GRADUALLY VA3t�ED FLOW PROFILE COMPUTEI3 INFO}+MA7'ION: ------------------------------------------�_--_------__------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL{FTj (FT) (FT/SECJ ENERGY(FT) MOMFN'I'l]M(POUNDS) 77.202 3.500 8.489 4.520 2395.08 77.693 3.973 6.499 4.�95 2380.34 78.135 3.446 6.517 4.573 2366.92 78.549 3.419 8.540 9.552 2354.36 � 78.939 3.391 B.56B 9.532 2342.58 � 79.308 3.364 $.599 4.513 2331.44 79.658 3.337 8.634 4.495 232D.90 79.990 3.310 8.672 4.478 2310.95 SQ.305 3.283 $.714 4.462 2301.54 84_603 3.256 8.758 4.447 2292.fi8 SQ.885 3.228 8.805 4.433 2264.34 Si.151 3.201 8.854 4.419 2276.53 81.401 3.174 8.907 4.407 2269.23 81.635 3.147 8.962 4.395 2262.44 81.B52 3.12D 9.019. 4.384 2256.17 82.054 3.093 9.079 4.373 2250.4i 82.239 3.065 9.142 4.364 2245.�7 82.406 3.438 9.2D8 4.356 2240.95 82.557 3.011 � 9.276 4.346 2236.26 82.6B4 2.984 9.347 4.341 2232.50 82.803 2.957 9.420 4.336 2229.4$ 82.$98 2.93D 9.496 4.331 2226.90 82.973 2.902 9.575 4.327 2224.89 83.028 2.875 9.657 4.324 2223.43 83.061 2.848 9.741 4.323 2222.55 83.073 2.$21 9.629 4.322 2222.25 91.280 2.821 9.629 4.322 2222.25 ------------------------END OF HYDRAULIC JUMP ANALYSIS------------------------ � PRESSURE+MOMENTUM BALANCE OCCURS AT 5D.58 FEET UPSTREAM OF NODE 139.90 I I DOWI3STREAM DEPTH = 4.g2$ FEET, UPSTREAM CONJUGATE DEPTH = 1.603 FEET NODE 140.44 : HGL =� 369.75$>;EGL- < 379.183>;��OWLINE= < 36B.00Q> �+****�*�.��***.**�*.«+*�*..*.�*�+.**.*��*.�xx,..**..**..��*«.*�**��.�*****.*� FLOW PROCE55 FAOM NODE 140.00 TO NDDE i90.94 IS CODE = 5 . --UPSTItF� NODE 140.90 ELEVATiQN = 35$.33 (FLDW I5 SUPERCRITICAi�) CALCULATE JUNCTION LOSSES: � PIPE FLOW I�IAMETER ANGLE FLOWF�INE CRIT�CAL VELOCI'I'Y (CFS} (INCHESJ (DEGREES) ELHVATION DEPTH(FT.) (F�'/SECi UPSTREAM 77.9fl 36.OQ Q.00 36$.33 2.75 �7.302 DOW3ISTREAM 81.70 42.44 - 3G8.00 2.82 �5.881 LATERAL #1 1.90 18.00 90.D0 3b9.83 Q.52 3.5D0 LATE]�P.L #2 1.90 1$.44 90.00 3fi9.63 D.52 3.500 Q5 O.flD===Q5 EQUALS BASIN INPU'F=== LACFCD AND OCET+3A FLpW JUNC'I`�ON FORMUI,I�E USED: DY=(Q2*V2-Q1*V1'C05{�ELTAij-Q3*V3*COS{DELTA3)- . Q9*V4*COS(DELTA4})/{{A1+A2)*16.1)+FRICTION L05SE5 UPS'd'REAM: I�ANNING'S N= 0.01300; FRICTION SLOPE = O.Q2897 • DCiWNSTREAi4: MANNTNG'S N= Q.01300; FRICTIOAi SLOPE = 0.02595 AVERAGED FRICTION SLQPE IN JiJNCTTON A$SUMED AS 0.02745 ,7iJNCT10N LENGTH = 4.00 FEET PKICTION LOSSES = 4.114 FEET ENTRAPiCE LOSSES = 0.04Q FEET JUNCTION LOS5E5 = (DY+HV1-HV2�+[EN'PRANCE LOSSES} ,3LTNCTION L05SES = ( D_621)+[ O.00O) = 0.621 NODE 194.9D : HGL =< 37D.155>;EGL= � 379.804>;F�,pvJLTNE= < 368.330> }f# 1# i k f f M****Yr****� iY *** �c 1� * i k Yr * iF **?Yr*Yri� ik Y� * Y�Y1rYr * iF #*Yr k******ititYri ******ik Y i* i#44 FLOW PROCESS FROM fVODE 140.94 TO NODE 150.40 IS CODE = 1 UPSTREAM NODE 150.00 ELEVATION = 377.39 (FLOW TS SUPERCRITICAL) CALCU�ATE FRICTTON LOSSES(LACFCD): PZPE FI,OW = 77_90 CFS PIPE DTAMET�it = 36_00 INCHES � PIPE LENGTH = 295.45 FEET MANNING'S ?�i = O.Q1300 � ------------------------------------------------------------------------------ NORMAL DEPT�{FT) _ ----1_80_ --___CRITICAL DEPTHfFT) _ _____2_75___ UPSTREAM C�NTROL ASSUMED FLOWDEP'I'H(FT} � 2.34 ------------------------------------------------------------------------------- ------------------------------------------------------------------------------ G�ABUAi.,I.�Y VARIED FLOW PROFI3.,E COMPUTEd II3FOAMATION: DISTANCE FFOM FLOW i}EPTH VELOCIi'Y SPECIFIC PRESSURE+ CONTRpL(FT) (FT) GFT/SEC) �]ERGY(FT} MOMENTUM(POUNDS) O.00D 2.341 13.1b2 5.032 2377.64 1.887 2.319 13.282 5.060 2387.94 3.948 2.298 13.40b 5.094 2398.85 . 6.199 2.276 13.534 5.122 2910.40 8.659 2.255 13.66b 5.156 2�122.59 11.347 2.233 13.BQ1 5.143 2435.45 14.2B8 2.212 13.941 5.231 2498.99 17.510 2.190 14.084 5.272 2953.22 21.046 2.169 14.232 5.316 2478.17 24.935 2.147 14.384 5.3fi2 2493.85 29.222 2.126 14.541 5.411 2510.29 33.965 2.104 14.702 5.463 2527.51 39.232 2.083 14.868 5.538 254�.52 45.108 2.D51 �5.039 5.576 2564.36 51.742 2.040 15.215 5.637 2589.05 59.153 2.01$ 15.396 5.742 2644.6Z 67.594 1.997 15.583 5.770 2626.D7 77.422 L 976 i5.775 5.842 264$.45 88.836 1.959 �5.973 5.91B 267i.8i 102.395 1.933 16.Z78 5.999 2696.15 1�8.&91. 1.911 16.3$$ 6.a84 2721.52 � 139.648 1.890 16.605 6.174 2747.94 167.149 1.868 16.829 6.266 2775.47 2Q6.978 1.847 17.059 6.368 26Q4.13 277.046 1.825 17.297 6.474 2633.98 295.050 1.825 17.297 6.479 2633.98 -------------------_----------------------------------------------------------- 3�10DE 150.00 : HGL =< 379.531>;EGL= < 382.222>;FLOWLINE= � 377.190> # # # # # # *f i iy.r y� * y� * Y� Yr Yr * **tt*i***tYrYc k �k * *t*tYi *ti*i*Yi #i Y 14i �L Yi+# �##*y.}i�.i*}#tyrl�iiY�• FLOW PROCE55 FROM NODE 150.00 'i'O NODE 150.9D FS CQbE = 2 UPSTRF.'AM NODE 150.94 ELEVA�`ION = 377.52 iFLQW IS SUPERCRI�'�CALf -------------------------------------------------_--__-_--_--_-------------------- CRLCULATE MANH�LE LOSSES�LACFCD): PIPE FLOW = 77.90 CFS PIPE bIAMETER = 3$.00 IFiCHES AVERAGED VELOCITY HEAD = 2.459 FEE'I' IIi�IN =. 05* (AVERAGED VELOCTTY xEP.D) _.4S* ( 2.459) = 0.123 ------------------------------------------------------------------------------ NODE 150.90 : HGI. _< 380.119>;EGL= � 382.345>;FLOWLII3E= < 377.520� if My�i#*�k t #} f+# f y� *1*?*******Yrtii *�*�*k # *Yr�t *yr ***#Yr**Yj�Y�Y**iF* �+lt�;�##f}i *1�**4�Y4f i FLQW PROCESS FROM NODE 150.90 TO 3VODE 160.00 IS CODE = 1 UPSTRFAM NODE 160.04 ELEVATION = 381.78 (FLOW IS SUPERCRITICAi,) --------------------------__--______--__�_�---___------------------------------ CALCUf,ATE FRIC`T'TON LOSBESILACFCD) : PIPE FLOW = 77.90 CF5 PIPE DIAMETER = 36.00 TNCHES PTPE LENGTH = 355.34 FEET MANNING'S N= O.Q1300 NORMAL DEPTH{FT) = 2.71 & 2.91 CRZTECAL DEPTH(FT) = 2.75 NOTE: SUGGES'I' COI�3SIDERATzON OF WAVE ACTION, UNCERTA�NTY, ETC. ---------------------------------------------_____--_---_----------------------- ------------------------------------------------------------------------------ � UI'S`iREAhf CONTROL ASSUMED FLOWDEPTi�i ( FT )= 1. 6 B � GRAI]UAI,LY VARIED FLOW PROFTLE COMPUTED Ii�iF'ORMATIONA4________________________ -------------�___------------------------------------------------------------- DISTANCE FRQM FLOW DEPTH VELOCITY SPECIFIC PRESSUR�+ CONTROL{FT] (FTj {FT/SEC1 ENERGXIFT) MOTSENTUM(POUNDS} Q.ODO 1.682 �9.D92 7.345 3066.72 �2.779 1.723 18.539 7.Ob3 2993.76 23.675 1.764 18.019 6.849 2926.13 35.702 1.805 17.530 6.579 2863.46 97.876 1.646 17.069 6.373 2805.39 6Q.215 1.887 16.635 6.186 2751.61 72.738 1.928 16.225 b.D18 2701.B5 85.468 1.969 7.5.638 5.866 2655.85 98.431 2.D10 15.473 5.729 2613.38 111.657 2.051 15.128 5.b06 2574.23 125.1B0 2.09i 14.601 5.495 2536.22 139.042 2.132 14.492 5.396 2505.16 153.290 2.173 14.200 5.306 2474.90 16'7.982 2.214 13.923 5.226 2447.30 163.168 2.255 13.662 5.155 2422.23 198.995 2.296 13.414 5.092 2399.57 215.512 2.337 13.180 5.036 2379.21 232.879 2.37$ 12.959 4.988 2361.05 251.282 2.419 12.75? 4.945 2345.03 270.977 2.46D 12.559 4.909 2331.03 292.339 2.501 12.364 4.878 2319.Q2 315.929 2.542 12.194 4.852 2308.91 342.759 2.583 12.031 4.832 23D0.57 355.34d 2.599 17.970 4.825 2297.94 ------------------------------------------------------------------------------ � NQDE ZSD.OQ : HGL =� 383.462>;EGi,= < 389.126>;FLOWLINE= a 381.780> ****+i.*t+***x+xkw�***++**�+t*x***t+ss***++ta+�t*t*+yti:+�y�f*+�+irW++*�t*��v.��st FLOW PROCE55 FROM I30DE 160.00 Td NODE �50_90 IS CODE = 5 UPSTREAM NODE 160_90 ELEVATION = 382.11 (FLOW IS SUPERCRI'i'iCA�) CALCUiATE JEii�3CTIQN LOSSES : PIPE FLQW 17IAMETER ANGLE Fi,OWl�ZNE CRITICAL VELOCITY (CFS) (INCHESj (DEGREES} ELEVATION DEPTH(FT.} (FT/SEC) UPSTREAM 72.40 36.00 0.00 382.11 2.69 20.813 llOWNSTREP.�I 77.9a 36.Q0 - 381.78 2.75 19.098 LATERAL #}� 2_75 �8.4D 90.OQ 383.5Z 0.63 3.911 LATERAL �2 2.75 18.00 90.OQ 383.51 0.63 3.911 - Q5 0.00===Q5 EQUALS BASIN INPUT=== LACPCD AND OCEMA FLOW JUNCTIOi�i FORM[TIsAE USED: DY=(Q2*V2-Q1*V1*COS(DELTAI)-Q3*V3*CQS(DELTA3}- Q4*V4*COS(DELTA41}/(fA1+A2}*1fi.11+PRTCT10N LOSSES UPSTREAM: MJ�iAiING'S N= fl.01304; FRTCTION SLOPE = �.44918 � DOWNSTREA2+1: N3ANNING' S rr = o_ o�3aa; FRICTION SLOPE = D.03738 AVERAGED FRICTION SLOPE IN�JLTNCTIbN ASSEJMED AS 0.0432$ Ji3NCTI0N LENGTH = 9.00 FEET FRICT�ON I,�55E5 = 0_173 FEET ENTRP.NCE LOSSES = 0.440 FEE'F JLiNCTION L05SE5 = {DY+HV1-H�2)+(ENI'iZ�NCE LpSSBS} JUNCT�ON L4SSES = ( 1.1921+( 0.000} - �.�92 --------__-------------------------------------------------------------------- NODE 160.90 : HGL =< 383.591>;EGL= < 390.3�$>;FLOWLTNE= < 382.110> �*****�..�**,.t***�...��.�w+�t��,�*�...t�*.,x*«��*,..�,**.**.**.�*****�**w�x*** FLOW PROCESS FROM NODE 16D.90 Tp NpDE 170.OQ IS CODE = 1 • UPSTREAM NODE 170.00 ELEVA3`T4N = 394.39 (FiAW IS SUPERCRITICAL} � --------------------�---- CALCETLATE FRICTION LOSSESiLACFCDI= P�PE FLOW = 72.40 CFS PIPE DIAMETER = 36.40 INCHES PIPE LENGTH = 221.91 FEET MA�INING'S N= 0.01300 NflRMAL DEPTH(FTj = 1.43 CRITICAL DEPTH{FT) = 2.69 UPSTREAM CON'I'ROL ASSUM�D FI.,OWDEPTI3{FT) = 2.69 GRADI3ALLY VARIED FLOW PFtOFIiE COMPLTFED IIJFORASATION: DISTANCE PROM FLOW DEPTH VEI,OCITY SPECTFIC PRESSURE+ CONTROI.� ( FT f ( FT j ( FT / S�C ) F13ERGY ( FT } �pMINT� { p(}��S } 0.000 2.668 1D.836 4.5i3 2Q97.96 O.D64 2.638 10.492 4.516 2Q49.Z4 0.260 2.588 11.164 4.529 2Q52.70 , , 0.596 2.538 1�_35a 4.539 2058.68 1.084 2.467 11.552 4.551 2Q67.�4 1.738 2.437 1.1.769 4.589 2678.27 2.574 2.367 12.d03 4.625 2091.86 3.614 2.336 12.254 4.6G9 21Q8.35 4.882 2.286 12.523 4.723 2�27.76 6.410 2_236 12.811 4.786 2154.27 8.235 2.186 13.119 4.85Q 217b.03 10.402 2.135 13_449 4.996 22Q5.27 12.968 2.085 13.803 5.09$ 2238.2Q 16.OQ4 2.035 14.181 5.159 2275.07 19.fiO3 1.984 14.587 5.29Q 2316.18 23.880 1.934 ].5.a21 5.440 2361.84 28.993 1.684 15_486 5.611 2412.42 . 35.�55 1.834 15.989 5.806 2468.34 92.b66 1.783 16.528 6.428 2529.97 51.957 1.733 17.108 6.281 2597.92 63.745 1.683 17.734 6.569 2672.76 - 79.152 1.632 16.411 6.899 2755.15 14Q.353 1.582 19.143 7.276 284$.B7 132.217 1.532 19.938 7.709 2945.79 190.372 1.482 20.802 8.205 3055.94 221.910 Z.481 20.807 8.206 . 3056.51 ------------------------------------------------------------------------------ NODE 170.00 : HGL =< 397.078>;EGL= < 398.903>;FLOWLINE= < 394.390> r****+**tr+++y*ttt*t+r**r*artt**+t+*ai*+ar*+*t*rw�++**r�rtti**r****eiy+ty***+*• FLOW PROCE55 FRQM NQBE 17d.Q0 'I'0 NODE 170.90 IS CODE = 5 UPSTREAM 130DE 17d.90 EiEVATION = 399.'72 ;FLOW [,7NSEALS IN REACH) CALCULATE JUNC'd`ION LOSSES: PIPE FLOW DIAk1E"PER ANGL� FLOWLINE CRITICAL VEI,OCTTY (CF5) (IA}CHESj {p�GREES► F,�,EVATION DEPTH(F�'. ) (FT/SEC) UPSTREAM 72.40 36.OQ 90.00 394.72 2.69 10_292 DOWNSTREAM 72.40 36.OQ - 394.39 2.69 14.839 LATERFiL #1 0.04 0.00 0.00 0.00 0.00 a.000 LATERAi� #2 O.QO 0.00 0.00 O.DO O.DO O.QaO Q5 0. 00===45 �4�7�5 BASI�I rI3pU'�'==_ LACFCD AND OCEMA FLOW JUNCTION FORMULAE USED: DY=lQ2*V2-R1*V1*COS{y}ELTA�J-Q3*V3*COSfDELTA3)- Q9�V4"C05IDELTA4)]/{(A1+A2}*16.1}+FRICTION L05SE5 UPSTREAM: MF�iNING'S N= Q.01300; PR�CTIpN SLpPE = 0.0�.378 DOWNSTREAM: MANNING'S N= a.ai3ao; FRiCTTQN SLOPE = O.Olfl41 • AVERAGED FRICTION SLOPE IN JUNCT�ON ASSUMED AS Q.0117.0 � JUNC'i'ION LENGTI-3 = 4.00 FEE'I` FRICTION L055E5 = 0.044 FEE�' ENTRANCE LQSSES = 0.6Q0 FEET JUNCTIDN LOSSES = IDY+HV1-HV2]+(ENTRANCE LOSSES} JUNCTIdN E,(755ES =( 3.394j+{ 0.000} - 3.394 NODE 170.94 : HGL =< aaa.66s>;EGL= � 4Q2.297�;FLdWLINE= < 394.720> x+*�+�*****+tytt+*t��:r.ii***f**+..t*x**�tx+�.****...*.r.wfrr..ifr+r*x.rt.i+*. FLOW PROCESS FROM i�IODE 170.90 TO N4D� 175.00 IS C4DE = 1 UPSTFtEAM NODE 175.00 ELEVATION = 395.40 {FLOW I5 LTNDER PRE55UREJ ------------------------------------------------------------------------------ CALCUL.ATE FRICTIOid LOSSES(LACFCD?: PIPE FLOW = 72.40 C�'S PTPE I7IAMETER = 35.40 INCHES pTPE LENGTH = 68 . 00 FEET M.�NrII13G' S N = 0. 0�300 SF=l4/K)'`*2 = If 72.40j/! 65b.979)}**z = O.aI178 HF=L*5F = { 66.001*f0.61178} = 0.801 -----------------------------------------------------------------�_----------- NODE 175.Q0 : HGL =< 4a1.459>;EGL= < 403.098>;FLdWLINE= < 395.4Q0> **:r�rrar,�*r�rt�+r+*��+*+**+**i.*t.+++t+��+�r+s*i+�ry***t+ti,*+y*xx*�,r+x+*++��*w*r♦ FLOW PRpCESS FROM NODE 175.Q4 TO NObE 175.90 IS CdDE = 5 UPSTRF.AM NODE 175.90 ELEVATION = 395.73 (FIAW IS LJNDER PRESSURE} ------------------------------------------------------------------------------ CALCLFL�ATE JUNCTION L05SE5: PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCITY {CFS} (INC1iES) {DEGREES) ELEVA�'IQN DEPTH{F�'.? {F'T/SEC) UPSTREAM 72.90 36.00 90.04 395.73 2.b9 10.242 DOWNSTRF�:M 72.9Q 36.OQ - 395.40 2.69 10.243 LATER.AL #1 O.OQ O.Q4 0.00 Q.DO O.OQ O.ODa L�ATERAL #2 0.40 D.aO 0.04 0.00 O.QO O.ODO � Q5 0.0�===QS E4UAL5 BASIN INPLT'�'==_ LACFCD AND OCEMA FLOW JUNCTION FOF2MULAE USED: DY=(Q2*V2-Q1*V1*COS(DELTAII-Q3*V3'C05fDELTA31- - Q4*V4*C�S{DEi,TA4))/{(A1+A2)*16.1j+FRICTFQN LOSSES - C3PSTREAM: MANNTNG'S N= 0.01300; FRICTIpN SLOPE � 0.01178 DOWNSTREANS: MANNING'S N= 0.01300; FR�CmION SLOPE = 0.01178 AVERAGEI? FRICT�ON SLOPE �23 J[7�+7CTTON ASSUM�i? AS 0.017.7B ,TCTNCTIQN LENGTH = 4.OQ FEET FRICTION L05SES = 0.047 FEET ENTRANC� LOSSES = 0.000 FEET J[i3�JCTION LASSES = (DY+HVl-HV2)+(ENTRANC� LOSSESy JUi�ICTION LOSSES =( 3.3Q5j+{ 0.000) = 3.305 ------------------------------------------------------------------------------ NODE 175.9a : HGL =< 904.775>;EGL= < 406.404>;FLOWLIA3E= < 395.73D> *�*t++x****+*x*t*ww**w�r*�r*r�rt+tti*+*y****x*t�*+*xr+�t+tir�r�r*+i.+{�r*r,�y�y+t*�+* FI,OW PROCE55 FROM NODB 175.90 TO NODE 176.00 �S COD� = 1 iJPS'3'REAM NODE i76.00 Ei�EVAT10N = 396.45 {FLOW IS UNDER PRESSURE} CALCULA�'E FRTCTION LOSSES(LACFCDI: PTPE FLOW = 72.90 CFS PIPE DIAMETER = 36.Q0 INCHES PIPE LENGTH = 72.Q0 FEET MANNING'S N= 0.01300 SF=(Q/Kj*i2 = ({ 72.401/( 666.984})�*� = 0.01178 HF=L'SF = { 72.00)*(0.01178) = 0.848 NDDE 176.00 : HGL =< 9D5.623>;EGL= < 407.252>;FLOWLINE= c 395.450> ***** *Yc*# Y�k 1*4YrrtY #YrYrYrYrYY41�* i**kYr *1 t*i � *YtY**�*ii *i * * i�kk# �k�kiF+}4iF+�k�k �k �iif i iM Y� t*t* ** UPSTREAM PIPE FLOW CONTi2QL DATA: NpDE NLJMBER = i76.00 PLUWLIi�IE ELEVA'PION = 396.45 • ASSUMED UPSTREAM CONTROI, HGL = 399.14 F'OR IIpWNSTREAM RLTN ANAi,YSIS � +ik �t **i �h�F /� �F Y��t� }'tt�'�* *� **iY �M ri 1 #i+�k i� *�F1r * *�FY�}yr+�1** *�F �k#YiF iF Y�*i+i #k f Y*Y� **�kk } YrY�i�`�ti *w* PTPE-FLOW HYDRAULICS COMPUTER PROGRI�M PACKAGE {Reference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION} ic) Copyright 1982-2002 Advanced Engineering Software (aesl Ver. 8.a Re�ease Date: O1/0�/2002 License I� 15Q9 Analysis prepared by: PROJECT DE5IGI3 CONSULTAN'i'S 701 'B' STAEET, SUITE BDO SAN DIEGd, CA 42�41 619-235-6471 . C � ,r***�*t**+*'********�`�+*** DESCRIPTION OF S'TUT)Y **++*��++**+*****+w++*�++• * SftESSi RANCH - MASS GRADENG STORM DRAIN * * ALICAT3TE RpAD - SYSTEki 101 {ALICANTE ROAD STATION 103+00 TO �05}50) * " 104-YEAR UL'I'IMATE CONDITION STORM EVE�IT * ♦ 4 Y� Y 1t *YrYrYr}*irit Y1Y'tfY****Yi Yr# i� # tk t* Y f*�Ir *YrM*#1 i�k***Yr�M 1F * iF **##*+11 i**t*�k ik tkM' ****'f Y FILE NAME: 101.DAT TIi+IE/DATE OF STUDY: 12:52 O1/].7/2003 �k*�r*iA'**1 # � Y # f* *i*Yr* h * * i* 4 yr rt tY***'kY� iY#'f t 1 f***ri �h # # i *'k't't1'YY �c * � �1r * } ** **#tt**1; * Yr*ri k * GRADUAI,LY VARIED FLOW ANALYSIS FOR PIPE SYSTEM f30DAL POINT STATUS TABLE (Note: "'" indicates nodal point data used_} UPSTREAM RUN DC}WP7STREAM RUN NODE t�30DEL PRESSURE PAESSl3RE+ FI.OW PRESSURE+ NCTMBER PROCESS HSP.D ( F'T ) MOMENT[JA7 i POUNDS ) DEPTH � FT ) �'fOi+3E3�ITEJM l POU�FDS i 101 OQ- 3.51* 334.40 4.b3 85.91 FRICTION 2.57* 241.58 FAICTFON+HEND 2.22* 191.87 FR�C7'ION } HYDRAULIC �[JMP 0.88"Dc 74.13 JUNCTION 1.23* 55.97 FRICTION } HYDRAULIC JUMP 0.66*Dc 36.26 0.63 0.64 0.68�17c 0.47 O.b6*Dc 85.55 85.�2 74.13 42.55 36.26 } CATCH BASIN ioi.5a- a.96* 19.47 0.�� aC iz.a� ------------------------ MA?CTMIJM NLTi+iBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 ---------------�------ NOTEf STEADY Fi�QW HYDi�AULIC HE.AD-T_�OSS COMPUTATIOt3S BASED ON Ti3E MOST COPiSERVA'd'IVE FORMULAE FRbM `I`HE CURRFNT LACRD, LACFCD, P.�ID OCEMA DESIGN MANUALS. �.1#t�'F'M k �k Yr **#�##�'1iF't * Y ** * * �k* **}� ** 4 �k * M***#tt�'k'k't * t***Yr*f i� Yr*** *t'�'k4 # # * �r**i�# t **� * DOWNST}ZEAM PIPE FLOW CONTROL AATA: i�iODE NUMHE�2 = 141 . DO FLAWLINE ELEVATION = 234 . 11 PIPE FLOW = 5.24 CF'S PIPE DIAMETEA = 18.00 INCHES A5S17t�48� DC)WNSTREAM CONTROL HGL = 237.620 FEET NODE 101 4D4� HGL =� 237.620>;EGL= <T 237.754>;FLOWi�INE� � 234.110> _ ) 101.1d- ? 101.20- } 101.30- } 101.40- } i0i.50- *.*++��.t++..*.***.,,**+�.+.*�+...>�..:«.*+..***f++�,+.+..,*�*.+***+++�.��» .�+ FLOW PRpCESS FROM NODE 1D1.44 TO NODE 101.10 IS C4�E = 1 UPSTREAM I�ODE 101.10 ELEVATIpAi = 235.06 {FLOW IS LTNDER PRESSURE} � CAI�CULATE FRICTION LOSSES(LACFCDI: PIPE FL4W 5.20 CFS PIPE DIAMETER = 16.00 INCHES PIPE LENGTH = 53.81 FEET MANNING'S N- 0.01300 SF=IQ/K}**2 = {( 5.241/f 105.043i)*"2 = 0.00245 HF=L*SF = i 53.811*{fl.00245} � 0.132 J�ODE 101 10 ^'HGL =< 237 752>,EGL= <T 23�.886>;FLOWLINE= < 235.480> +t+w*t*+rw��++***+*t*r+�*+*aa��++�+w*+++�*+*rsw*+�f+++**rw+*�x+**afrr��rt*k**� FLOW PROCE55 FROM NODE 1D1.10 TO NODE• 161.24 I5 CODE = 3 UPSTREAM NOBE 14I.2D ELEVATTQN = 235.63 [FLOW IS UI3DER PRESSUAE) CALCULATE PIPE-BEND LQSSES {pCgt�3P,} : PIPE FLOW = 5.20 CFS PTPE DIAi�7ETER = 1$.00 IiQCHES CEN'T'RAL AI'IGLE = 45.000 DEGREES I�7INNING'S N= a.0130Q PIPE LENGTH = 30.79 FEET BEND CQEFFICIENT(KB} = 0.17678 FLOW VELOCITY = 2.94 FEET/SEC. VELOCI'i'Y HEAD = D.134 FEET IiB=KB*(VELpCITY HEAi)) _{ 0.1771*( 0.134} = D.024 SF=(Q/K}}*2 = {( 5.20)/( 1a5.0491}**2 = 0.00245 HF=L*5F = ( 30.791*(O.Q0245? = 0.075 TOTAE,3-IEAD LOSSES = HB + HF =( 0.024)+{ 0.0751 = 0.099 ------------------------------------------- NODE 101.20 : HGL =< 237.851>;EGL= < 237.986>;FI,OWLINE= < 235.630> YrYr**'k * 1�*`ky'Y#*�r*YrYriF'!r**i W #i**t# �'k ***i 1tt t * # * f r�f f'111* # * ��k hYrit**# i�+Y*Yii� * �Ir**?#*4Yt FLOW P�QCESS FROM NODE 101.2Q TO 130DE 1Q1.3d i5 C4DE = 1 UPSTRE.AM NODE aai.3a ELEVATTON = 238.80 IHYDRAULIC JUMP OCCURS) � CALCULATE FRICTION LOSSESLLACFCD}: . PIPE FLOW 5.2D CFS PIPE DIAMETER = 18.00 INCHES PIPE LEi�iGTH 175.$8 FEET ----__-__MP.PiD]I�]G_5 N = fl.01300 ------------ HYDRAULIC JiJi+IP : DOWNSTREF� RUN ANALYSIS AESULTS -- -------------------------------------- - NOFtMAF� DEPTH(FT) = 0.63 CRITICAL DEPTH{FTj 0.88 UPSTREAM CONT3tOi� ASSUMSD FLOWDEPTH ( FTi = fl- 88 ----------------------------- GRADUALI.Y VARIED FLOW PROFILE COMPUTED INFORMATION: ------------------------------------ DISTANCE FRDM FLOW DEPTH VEI�OCITX SPECIFIC PRESSURE+ C013TROL ( FT } ( FT j ( FT / SEC ) ENERGY ( FT ) MOM�TTUM i POUTFDS J 0.00� 0.678 4.837 1.2A2 74.13 0.016 O.Bb8 4.949 I.242 79.15 0.075 0.858 4.973 �.242 74-19 0.173 0.848 5.094 1.294 74.27 0.319 0.83$ 5.117 1.295 'i4.37 0.515 0.829 5.193 1.247 74.51 0.769 0.819 5.270 1.250 74.b8 1.086 0.809 5.351 1.259 74.$8 1.475 a.799 5.439 ' 1.258 75.12 1.944 0.789 5.519 1.262 75.40 2.5Q5 d.779 5.607 1.268 75.71 3.171 0.769 5.699 1.274 76.06 3.958 �.759 5.793 1.281 7fi.45 9.SSb 0_749 5.890 1_288 7b.89 5.g81 0.739 5.991 1.297 77.36 7.275 0.729 5.495 1.307 '17.88 8.812 0.720 b.204 �.318 76.95 • 1p.650 0.710 6.315 1.329 74.Ob 12.871 0.700 6.431 1.392 79•73 � 15.596 0.690 6.551 1.357 8D.94 19.010 0.68d 6.67& 1.372 81.21 23.427 D.570 6.605 1.39Q 82.fl4 29.432 Q.6b0 6.939 1.4d8 82.42 38.342 0.650 7.076 1.429 83..87 59.38D 0.640 7.223 1.451 84•87 175.880 0.639 7.243 1.454 85.02 HYDRAULIC JUMP: UPSTREAM RUN AIQP.LYSIS RESUL'PS DOWNS'FREA�i CONFROL4ASSUMED PRESS[3RE HEAD {F`Pi = 2• ZZ PRESSURE FLOW PROFILE COMPUTED INFORMA'3'ION: DISTAi3CE FROM `+ ^ PRESSURE VELOCITY SPECIFIC PRESSURE+ CON'I'120L { F'T ) 4-IEAD ( FT j S FT / S�C } ENERGY ( FT } MOMENTt3M { POUNDS j o.aao 2.zzi 2.943 2.356 is�.s� 46.303 1.54Q 2.943 1.634 112.36 ~ASSUMED DOWNSTREAM PRESSURE'HEAD(FTf = 1.50 -----------W--------- GRADUALLY VARIEA FLOW PROFILE COMPUTED iN�'ORMATION: ----------------------------- DISTAFICE FROM FLC?W DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL { FT ) ( FT f ( FT / S EC } ENERGY ( FT } MOi+]EhITLTM ( POUNDS f 4fi.303 1.5D0 2.942 1.634 112.36 47.825 1.475 2.952 1.611 149.72 49.282 1.450 2.972 1.567 107.19 50.699 1.425 2.997 1.565 109.75 52.Q84 1.40a 3.028 1.543 102.37 • 53.44� 1.375 3.453 1.521 100.08 54.770 1.35i 3.142 1.500 97.85 56.074 I.32b 3.145 1.480 95.71 57.352 1.301 3.193 �.459 93.64 58.603 1.276 3.295 �.440 91.65 59.826 L 251 3.301 1.420 89•75 61.019 1.226 3.361 1.402 87.94 62.181 1.201 3_426 1.364 86.22 63.309 1.177 3.496 1.366 84.59 64.400 1.152 3.571 1.350 83.D5 65.449 1.127 3.651 1.334 81.62 66.452 1.102 3.736 1.319 Bfl.30 67.944 1.077 3.828 1.305 79•Q9 68.297 1.052 3.926 1.292 77.99 69.123 1.027 4.03Q 1.280 77.42 69.673 3_002 4.192 1.269 76.18 70.533 Q.978 4.262 L 260 75.97 71.089 a.953 4.39� �.252 74.9Q 71.522 0.928 4.529 �.247 74.48 7]..806 0.903 4.67$ 1.243 74.22 71.909 0.87B 4.837 1.242 74.13 175.B60 0.678 4.837 1.242 74.13 ---___-----------------END OF HYDRAULIC JUNSP AI3ALYSTS------------------------ � PRESSURE+MOMENTUM BALANCE OCCURS AT 63.06 FEET iiPS'I'REAM OF NODE 101.20 € 1 D04�7NSTREAM DEP�H = 1. 182 FEET, �7PSTREA3'1 CONJ43GATE DEP'f'H = 0. fi90 FEET i NODE I01 30 +'HGL =� 239`578>;EGL= < 240.042>;FLOWLINE= < 238.800> �*y,�,yy,**a+fsa+�:+*xt++*+�**ttt*�,r*++*+�+*y**t:**k:a*raks**s�+w+t:+�s+*++t�*+*+* � FLOW PROCESS FROM NODE 101.30 TO NQDE 101.4D IS CODE = 5 UPSTRE.n.M NODE 101.40 ELEVATION = 239.47 (FLOW IS SUBCRITICAL) � ------------------------------------------------------------------------------ CALCULATE ,7UNCTION L055ES: P�PE FLOW DIAMETER ANGLE Fi�OWi�INE CAITICAi, VELOCITY (CFS) (INCHES) {DEGREES) ELEVATIQN DEPTH(FT.) (FT/5EC) UPSTREP� 3.00 18_00 90.OQ 239.07 Q.66 1.929 DOWNSTREAi�7 5.2D 1$.40 - 23B.80 0.88 4.639 LATERAL #1 2.2D �5.00 90.04 239.07 0.5b 1.939 LATERAL #2 0.60 O.DO 0.04 0.00 0.00 0.000 Q5 4.00===Q5 EQUP,I,S SASIN INPUT=== i,ACFCD AND OCEMA FLOW JUNCTION FORMULAE USED: DY=lQ2*V2--Q1*V1*COS(DELTAI)-Q3*V3*COS(DELTA3)- Q4*V4*COSIDELTA4}}/((A1+A2)"16.1)+FRICTION LOSSES UPSTREAM: MPNPIING'S N= 0.0130D; F'RICTYON SLOPE = O.D0081 AOWNS`d`REP.rS: MA4�iNIFFG'S N= 0.01340; FAICTION SLOPE = 0.00586 AVERAGED FRICTION SLOPE IN J[7NCTION ASSUMED AS 0.04334 JUNCTION LENGTH = 4.00 FEET FRICTION LGSSES = 0.013 FEET ENTRANCE LOSSES = 0.040 FEET JUNCTION LOSSES = (DY+HV1-HV2?+{EI�ITRANCE LOSSES) JUNCTION LC}SSES = i 0.320}+{ 0_000) = 4.320 --------------------------------- NaDE 101.40 : HGL =< 240.304>;EGL= < 24fl.361>;FLOWLINE= � 239.070> * ik* **fi**Y i�k t***'k * iF k k ik Y� *�k *i�*'k'k1'Y�rt*****}**#*Y�*i 1�R1�Yr***t*�riFik'kri ii *i� *# i t Y Yi**'kk'lriF FLOW PRpCESS FROM NODE 101.4D TO NODE 1D1.50 I5 CODE = 1 UPSTRF.AM NDDE 101.50 ELEVATION = 239.70 SI-iYDRAULIC JUN3P OCCUAS) -----------------------------------_-------------------------------------�------ CALCUL�ATE FRICTIOTF LOSSES(LACPCD) : PIPE FLOW = 3.04 CFS PTPE DIAMETER =�.8.40 ENCIiES PIPE LENGTH = 31.25 FEET __----�^-MA�NFNG'S N= Q.D13Q0 � -------------------------------- --------______-------------- HYDRAULIC �UMP: DOWNSTREAM RUN ANALYSIS RESULTS ---------------------------- - NORt�SAL DEPTHSFT) = 0.4b CRITICAL DEPTH{FT) = 0.66 UPSTRF..AM CONTROi, A55UMED FLOWDEPTH(FT} = 0.66 ------------------------------ GRADUALLY VAATEI7 FLQW PROFILE COMPU'TED iNFORMATIOI+i: -----------------------------------------------------------__------------___--- DI5TA23CE FF20M FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL ( F`F ) ( FT } ( FT / SEC � ENERGY ( FT ) MOM�TFTUM ( FOLTNAS ) 0.44� 0.658 4.017 0.909 36.26 0.0�3 0.650 4.083 0.909 3b.26 0.054 0.642 4.151 4.914 36.29 0.325 0.634 4.221 b.911 36.34 0.23q 0.626 4.293 0.912 36.40 0.372 0.618 4.36B 0.914 36.49 D.556 0.61D 4.445 4.917 36.59 0.786 0.602 4.525 4.92p 36.72 1_fi66 D.594 4.608 4.924 36.87 1.4D9 D.586 4.693 4.928 37.�4 1_817 0.578 4.781 Q.933 37_23 2.301 0.569 4.873 0.93$ 37.45 2.874 0.561 9.968 4.945 37.70 3.55� 0_553 5.066 Q.952 37_97 4.349 0.545 5.168 4.96Q 38.27 5.294 0.537 �.274 4.969 38_59 6_417 0.529 5.384 0.979 38.95 7.762 0.52� 5.498 0.991 39.33 � 9.368 Q.513 5.617 1.003 39.75 11.385 0.505 5.741 1.017 40.20 � 13.890 4.497 5.8b9 1.032 40.69 17.133 fl.989 6_003 1.049 41.21 2 L 547 0_481 6.193 1.057 41.76 28.101 0.472 6.268 1.087 42.36 31.250 0_470 6.32B 1.D92 42.55 HYDRAULIC JUMP: UPSTREAM RUN ANALYSTS RESULTS DOWNSTREA34 CONTROL ASSUMEDTFLOWDEPTH(FTj = 1.23 GRA�UALLY VARIED FLOW PROFILE COMPUTED ENFORr3ATION: DISTANCE�FROPt FL,OW DEPTH �IELOCiTY SPECiFiC PRESSURE+ CONTROL{FT) IFTi IFT/SEC} �RGYfFT} MOMEN'I'CTM(POUNDS} 0.000 1.233 1.929 1.291 65.97 1_084 1.210 7.963 1.270 53.95 2.36D 1.187 1.999 1.250 b1.99 3.228 1_164 2.Q37 1.229 60.08 4.288 �.�41 2.478 1.209 58.23 5.338 1.��$ 2.122 1.188 56.93 6_377 1.095 2.169 1_169 54.70 7.405 1.072 2.218 1.149 53.02 $.421 1.049 2.271 1.130 51.41 9.423 1.026 2.327 1.111 49.86 10.409 1.D03 2.367 1.092 48.38 11_378 0.980 2.451 1.074 46.96 12.327 0.957 2.519 1.056 45.64 13.254 D.934 2.591 1.039 94.37 14.156 0.911 2.668 1.022 43.19 15.034 4.888 2.751 1.006 42.08 � 15_671 4.865 2.844 0.991 41.Q5 16.674 0.892 2.935 D.976 4p.11 17.439 0.8�9 3.037 a.963 39.26 18.142 0.796 3.14b 4.950 3B.51 �8.790 0.773 3.259 4.939 37.85 19.366 0.750 3.392 4.929 37.30 19.855 0.727 3.529 0.921 36.86 20.240 0.7�4 3.679 0.915 '36.53 24.496 D.681 3.841 0.911 36.32 20_591 0.656 4.017 0.909 36.26 31.250 0.658 4.017 0.909 36.26 ------------------------�ND OF HYDRAL7LIC JUMP ANALYSIS------------------------ � PRESSURE+MOMFNTUM BALP.NCE OCCURS AT 15.99 FEET UPSTREAM OF 130DE 101.40 � DOWAiSTREAM DEP'i'li = a.862 FEET, UPSTREAM CONJUGATE DEPTH = D.443 FEET ----------------------------------- NODE 101.50 : HGL =< 240.35$>;EGL= < 240.609>;FLOWLTAIE= � 239.70Q> �**..*f*.+��..+....++t�*****.++.+**.***.++t�+..�***+**.�,..,�,.»w�*.�+..�++>.*+�. FLOW PROCESS FROM NODE 10�.50 7'Q NODE 101.50 IS C4DE = 8 17PSTREP,i�i NODE 101.50 ELEVA'I'ION = 239.7Q (FLOW I5 SUBCRiTICALI y CALCULATE CATCH BASIfd F.N'PRP.NCE LOSSES (F�ACFCD) : PIPE FLOW = 3.00 CFS PIPE DII�ETER = 78.00 TNCHES FLQW VELOCTTY = 4.02 FEET/SEC. VELOCTTY HEAD = 4.251 FEET CATCH BASIN ENERGY LOSS =.2*fVELOC�TY HEAD1 =.2*{ 0.251) = 0_45a ----------------------------------- NODE 1�1.50 : HGL =< 290.659>;EGL= < 24D.659>;FLOWLINE= < 239.704> *****.*�ttt+t+,t*��*.***��.**��*�**+*+w.«**..*�*�**.*.*�+�****�++k+�..+�+*� ' UPSTREAM PIPE FLOW CONTROL DATA: �• NODE NUM$�R = 101.50 FLOWL,ZNE ELEVATION = 239_70 � A55UMED CIPSTREAM CON'F'ROL i3GL = 290.36 FOR iJOWNSTRF:AM RUN ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS �� .� � / � +x++�*t*er**+*�ttt*�.+-rt**i+++t�s***++*+w*+xrw�r�rt+*+++*�++*�+*�e+*+i+�rx*t+*�* PIPE-FLOW HYDRAUi�ICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACR1?, AND OCEMA HYDRAULfCS CRI`�ERION� (c} Copyr3ght 1982-2002 Advanced Engineering Software (aes) Ver. 8.0 Release Date: 01/01/2002 License ID 1549 Analysis prepared by: PRdJECT DESIGN CONSULTANTS 70� 'B' STA�ET, SUIi`E 80d SAN DIEGO, CA 9210� 619-235-6471 +w��r++*+r�x**++++++*r*y:t DESC3ixi�'IQ� �F $`I'�T�i ++*+t*+t*y***si*+�t,t+w*,t,rt * BRESSI RAidCH - ULTIMATE CO3dDITIONS "` * ALICANTE - SYSTEM 102 (PLANNING AREA 10 CONi�iECTION� " * 100-YEAA STORM EVENT ' i+*+*+**i.t�+r**it*++r+**x**+{*yyrt*++vr+***i.�,r�+�iy+*+��*a*��xxx*t�+�+wr**++ FILE NAME: 202.DAT TIME/DATE OF S'I'UIIY: 13:15 O1/17l2Q03 ***+*+.��**�***.****+�*�****+*****�.+�,.t«**+�«*****x*+�+*��:++*��*+*******+�� GRADUALLY VARIED FLOW ANALYSIS FOR PiPE SYS'1'EM 130DAL POIN'I' STA'PU5 TABLE {Note: "*' indicates nodal point data usec3.) UPSTREAM RUN DC3WNSTREAM RiJ�3 N�dE MODEL PRESSURE PRESSURE+ FLdW PRESSURE+ 3J[IMBEft PRpCESS HEAD ( FT ) [�fOMFI3'!'UM I�L7�DS � DEPTH { F'T ) MOMENTL7�7 ( POLTNDS ) � 102.00- 19.50* 5041.56 0.88 3150.97 ) FRICTION } HYDRAULIC JUMP 102.21- 4.�5 1875.14 0.83* 3512.68 ) MANFiQLE 102.22- 3.9I J.798.64 0.80* 3572.36 ) FRIC�`ION 102.94-- 2.30 17c 1343.83 1.00* 2665.45 } �INC�ION 102.91- 2.77 1417_29 0.89* 3022.�7 } FRIC`I'ION 102.5�- 2.29 Dc 1311.28 1.69* 1486.57 } MAN730LE 1D2.51- 2.29 Dc 1311.28 1.76� 1444.59 } FRICTION �02.60- 2.29'Dc �311.28 2.29*Dc 1311.28 } CAT'CH BASIN �02.60- 4.31* 938.67 2.29 Dc 318.94 MAXIMUM NOMBER OF EidERGY BALANCES USED IN EACH PROFILE = 25 NQTE STEADX FLQW HYDRAULIC HF.AD--L055 COMPt3TATI0NS HASED Obi THE MOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, AND OCENdA DESIGN MP.NUALS. **++t�+�+�+�*,ry*+x�*t*+****�+��****fi��*�xi.*�r*�w��y+y�*x**a+��xwta++**�r+***k+�r DOWNSTRFAM PTPE FLOW CdNTROL DATA: NdDE NUA3BER = 1�2.00 FLOWLINE ELEVATIOI3 = 239.60 PIPE Fi�OW = 49.40 CFS PIPE DIAMETER = 30.OQ SNCHES ASSUMED DOWNSTREAM CONTAOL HGL = 254.100 �EET -------------------------------------------------------------------__---------- . NODE 162.a0 : HGL =< 254.14D�;EGL= < 255.705>;FLOWLINE= < 234.600> � * i * Y i * * * * * * * * * } } f * t i ! f ti i * * * � * * * * i i } f 1 * * * * * * � # i 4 Y * t * * * � * � * * * � i # f * t + * Y * * rt t # k * * # t FLOW PROCESS FRO� NODE 102.04 �O NpDE 102.21 IS CODE = 1 UPSTREAM NODE 102.21 ELEVATiON � 250.89 (HYDRAULIC JEiMP OCCURS} CAT.CiTLATE FRICTION L4SSES SLACFCD) : � PIPE FI.�OW = 99.90 CFS PIPE 17IAME'PER = 30.00 INCHES PIPE LENGTH = 64.3b FEET MI�FNING'S N- 0.01300 HYDRAULIC 3i�7P: DOWAISTREAM RUN ANAI,YSiS RESULTS -------------------{----------__----- - NORMP.L DEPTH{FT} 0.92 CR�'I'ICAL DEPTH(FT) = 2.34 ==-------------------------------__�_ _ UPSTREAM CONTROL ASSUMEI7 FLOWDEPTH I F'I'1 0. 81 ------------------------- GRAI]UAI,LY VARIED FLOW PROFILE COT+IPUTED I13F'ORMI�TION: ----------------------------------- DiSTANCE FROl�7 FLOW DEPTH 17ELOCITY SPECIFIC PRESSURE+ CONT42dL S F"I' ) I FT } { FT / SEC ) ENERGY ( FT } MOMEN'I'UM l POUNDS ) 0.004 0.813 3b.013 20.965 3512.6$ 2.79Q 0.818 35.746 20.674 3487.44 5.b78 0.822 35.AB7 2a.389 3462.54 8.674 a.826 35.229 20.110 3437.98 11.788 0.831 34.975 39_837 3413.75 15.032 0.835 34.723 i9.569 3389.SA 18.418 0.840 34.476 19.347 3366.25 21.963 0.844 34.231 19.D50 3342.98 25.685 0.848 33.4$9 18.798 3320.01 29.605 0.853 33.75Z 18.552 � 3297.39 33.749 0.857 33.515 18.310 3274.97 38.�49 D.861 33.283 18.073 3252.89 � 92.893 a.866 33.053 J.7.841 3231.09 47.877 0.870 32.627 17.b13 3209.58 53.312 0.875 32.603 17.39D 3188.34 59_223 0.879 32.382 17.171 3167.36 � 64.360 0.882 32.209 17.441 315Q.97 HYDRAULIC .TUMP: EIPSTREA3+9 RUN ANALXSIS RESULTS DOwNSTREAM CONTROL ASSUMED PRE55URE^HEAD{FT) = 14.50 PRESSUitE FLOW PROFIf,E COMPiJ'I'ED INFORMAT�ON: ------------------------------- - DISTANCE FRQM PRESSURE VELOCITY SPEC3FIC PRE5S13RE+ CONTROL(FT) HEAD(FT) (FT/SEC] ENERGY{FT) MQMENTUM(PO[JNDS) Q.000 i9.500 10.166 I5.105 5441_56 64.3b0 4.�63 10.166 5.767 1875.14 ------------------------ENF3 OF HYT7RAULIC JiJMP AidALYSIS------------------------- I PKESSURE+MOMENTUM BALANCE OCCURS AT 35_38 FE�T UPS'I'REAN3 OF NpDE 102.00 � . I DOWNSTREP,M DEPTF-I = 8.817 FEET, UPSTREAE�S CONJUGATE DEPTH = 0.852 FEET � -------------------------------------�-------- NODE 1D2.21 : HGL =� 251.703>;EGI�= < 271.655>;FLOWLINE= < 25b.89Q> f+r**r+��,r*�*tt��+t++++i++***+i.�rr*w*+***��+rrar*+t*+*�w*x+*a+t*+tt*�*x+aw**** FLOW PRaCESS FROM t+3017E 142.2� 'X'a NOBE 102.22 IS CODE = 2 UPSTREAl+3 NODE 102.22 ELEVATION = 251.22 (FLOW IS SUPERCRTTICAL} CAL�CULATE thANHOLE LOSSES(LACFCD}_ • PIPE FLOW = 49_90 CFS PIPE DIAMETER = 30.40 INCHES AVERAGED ITEI,OCITX HEAD = 20.50$ FEET � HMM��II = .05* {AVERAGEA 1IELOCITY HEA3�} _ .05* (2D.505) = 1.025 � ----____------------------------------------------------------------------------ �+ � • NODE 1D2.22 : HGL =< 252.023>;EGL� < 272•8B1>:FLOWLINE= < 251.224> *rt+r+*+*++ry�*+*ra�xrr**a+�+*>+**t�+r****�sti�wx+�>++**+++*+tx****r***+++*t** FLOW PROCESS FROM NODE 1Q2.22 �0 N�DE 102.44 IS CODE = 1 UPSTREAM NODE 102.40 ELEVATION = 268.24 {Fi.OW IS SUPERCRITICALi y'CALCULATE FAICT�QN �OSSESILACFCDi: � PIPE FLOW - 49.90 CF5 PIPE DIAME�ER = 30.d0 INCHES PIPE LENG�H = 35. 45 FEET MP.I3riING' S N= a. ai3oo ------------------------------------------, NORMAI., DEPTH(FTj = 4.71 CRITICAL bEPTH(FT} = 2.30 --==---------------------------------- UPS`i'RF.AM CONTROL ASSLTM�D FLOWDEPTH(FT) = 1.00 ---------------------------------- G13ADl3ALLY VAAIED FI�OW PROFILE COMPUT�D INFORMATI013: ---------------------------------------- DISTAi+]CE FROM FLAW DEPTH VELOC�i'Y SPECxPIC PRESS[iRE+ CON£ROL ( F�' ) 4 F'3' 1 { F'T I SEC } ENERGX ( F'�' i MOMENTUM i POlTNDS ) 0.400 1.009 27.067 12_387 2666.45 1.414 0.992 27.498 12.740 2706.78 2.094 D.980 27.941 13.111 279$-39 3.248 0.968 28.399 13.500 2791•34 9.489 0.957 28.871 13.907 2835.67 5.809 0.9A5 29.357 14.336 2881.4b 7.234 Q.933 29.859 14.765 2928.75 8.771 D.921 30.377 15.256 297�.63 1�.932 0.910 30.911 15.756 3028.15 12.235 0.898 31.464 1&.279 3080.40 24.199 fl.886 32.034 16.83a 3134.45 16.34b 0.874 32.624 17.411 3�90.38 18.706 0.862 33.234 18.024 3248.29 21:315 0.851 33.866 18.670 3308.27 24.216 0.839 34.519 19.353 337D.92 27.468 0.827 35_196 2Q.Q75 3434.84 31.�46 �.8i5 35.698 20.838 35Q1.65 35.354 0.603 36�.625 21.645 3570.98 35.954 0_803 36.639 21.66� 3572.36 ------------------------ NQDE 4�02 40 HGL =< 269.244>;EGL= < 280.627>;FLOWLTNE= � 268.240> *�Y* **Y�'k'k # f�'tti * Y!#Y� * **Yr**#f �YYr##�k * i� # � *'k * * *'X* *# � Y!***Yr'kiFiM'h **i�#'k'� t *ir'k*Yr*i iFi� **'k'k FLOW PROCESS FRONI NOD� 102.40 TO NODE 102.4� IS CODE = 5 UPSTREAM NODE 102.41 ELEVATION = 268.57 (FLOW IS SUPERCRIT�CAL? CALCUL7ITE JUI3CTEQN LOS5E5: PIPE FLOW DIAMETER ANGLE FLOWLiNE CAiTICAL VELOCZTY {CFSi [INCHES} (DEGREES} ELE17A'TTON DEPTHLFT.? (FT/SEC) UPSTREAM 49.10 30.D0 Q.aO 268.57 2.29 31.3&3 DOWNSTREAM 49.90 30.Oa - 268.24 2.3D 27.fl75 i,AfiERAL #1 4_00 0.00 4.46 D.00 0.00 0.000 LATERAL #2 4.OD 0.04 0.4Q 0.00 0.00 O.ODO Q5 0.80===45 EQUALS BASIN INP[J'I'�== LACFC➢ AND OCEMA FLpW JUNCTION FORMULAE USED: DY=fQ2*V2-Q1*V3*COSf�ELi'A11-Q3*V3*COSfAELTA31- 44*V4rCOS{pELTA4})/({A�+A2)*16.1�+FRICTION LOSSES UPSTREAM: M.�NNING'S N= 0.01300; FRIC'i`ION SLOPE = Q DpW?�]STREAM: MANNING'S N= 0.0130D; FRICTION SLOPE = D AVEI�AGED FFtICTION SLOPE I[d JEJNCTION ASSU2�FED AS 0.1fi189 JUNCTION LENGTH = 2_94 FEET FRICTION LQSSES = D.395 FEET ENTRANCE L055E5 = I9525 1285� 2.27�7 FEET • JUNCTION LOSSES = (DY+HV1-HV2}+(ENTRANCE i�OSSESI JUNC'�`ION LOSSES =( 1.849)+( 2.277) = 9.126 ------_�------------------------ NODE 102 41 : HGL =� 259-453>;EGL= < 284•752>;FLbWLZNE= < 268.570> ��.*****:+*�***�*+�+...*>***�,��+,.�++:�+�*++�:*+.*..��++.,�*�3*.****+*�**�+��.* FLOW PROCESS FROM NODE 102.41 TO NODE 102.54 IS CODE = 1 UPS'I'REAM N017E 102.50 ELEVATION = 2$6.30 {FLOW I5 SUPERCRITICALI CALCULATE FRICTIOt�I LpSSESiLACFCD}: PIPE FLOW = 49.10 CF5 PIPE DIAMETER = 30.00 INCHES PIPE LENGTH = 54.00 FEET MANNING'S N= fl.01300 -------------------Y------------------------- _ NO}2MAL DEPTH{FT} 0.78 CR�TTCAL DEPTH(F'T) 2•29 TUPSTRE.�,M'CONTROL ASSUMED FLbWAEPTH(FT) = 1.69 GRADUALLY VARIED FLOW PROFILE COMPUTED iNFORMATION: --------------------------------------- DISTANCE FROM FLOW DEPTI-i VELOCFTY SPECIF�C PRESSURE+ CONTROL l FT ) ( FT ) ( FT / SEC ) ENERGY ( FT ) N30MEi3'I'iTM ( POi3NDS j 0.000 1.69Q 13.900 4.692 1466.57 0.378 1.653 14.247 4.B07 151�.65 O.SQ2 1.617 19.616 4.936 1539.Q3 1.27g 1.580 15.009• 5.080 3568.82 1.815 1.544 15.425 5.241 1601.21 Z,q�9 1.507 15.871 5.421 1636.40 3.D98 1.47� 16.346 5.522 1674.60 3.864 1.434 16.852 5.847 1716.D5 4.730 1.397 17.393 6.098 1761.02 • 5.7�2 1.361 �7.973 6.360 i809.$2 6.829 1.324 i8.599 6.696 1852.79 8.104 1.288 19.2b4 7.Q51 1920.31 9.566 1.251 19.977 7.952 1982.62 13.252 1.215 20.749 7.909 205D.61 13.208 L 178 21.583 8.416 2124.85 15.496 1.141 22.484 8.996 2205.59 18.195 �.105 23.462 9.656 2293.77 21.417 1.068 24.525 �0.914 2390.26 25.318 1.432 25.583 11.281 2496.05 3Q_127 fl.995 26.950 12.280 2612.31 3b.205 0.958 28.338 13.43b 27A0_4Q 44.155 0.922 29.666 14.781 28&1.94 54.d00 D.889 31_373 16.182 3022.I7 -------------------------------------------------- t�70DE 102.50 : HGL =< 267.940>;EGL= < 290.992>:FLOwLINE= < 286.300> ,r�**i.�rtt**�+x+��iw**++*++i.r*r*r+**�ti�*rx��t+r*rr*x*t*�r*****r**�*�*y+*wi.i�t�r* FLOW PROCESS FROM NODE 102.50 TO 130DE 102.51 IS CODE = 2 UPS7'REAM NODE 102.51 ELEVATI01� = 286.63 (FLOW IS SUPERCRITICAi�) CALCUI.ATE MA3�FHOLE I.�OSSES (LACFCD} : PIPE FLOW = 49.�a CFS PIPE DIAME'FER = 30_00 IE3CHE5 AVERAGED VELOCITY HEAD = 2.674 FEE'i` HNII3 =. 05* {AVER.AGED VELOCITY HEA3]} _.45* { 2. 874? = a.144 --------------------------------------�-------------- NODE 102.51 : HGL =< 288.390�;EGL= < 291.136>;FLOWLZNE= < 286.630> «**��t*�***�*�+�,.*.*�*+*t«*++**,.*+�*>.�*++**+.t�+*��.�*t*�**++��wr*.**��**�*. � FLOW PROCESS FROM NQDE 102.51 TO NODE 102.b0 IS C017E = 1 UPSTREAM NODE 102.50 ELEVATIQN = 287.93 (Fi,OW IS SCiPERCRITICAL) • • �YCALCiJLATE FRICTION LQSSES(LACFCDJ: PIPE �Low = 49.1a CFS PIPE DIAMETER = 30.00 INCHES PIPE LENGT`H = 16 . Q� FEE'i` MP.d3fIiNG' S N = 0. 01300 -------------------------------------- NORMAL DEPTH[FT) = 1.30 CRITICAL DEPTH(FT) = 2.29 'UPS'i'REAN3 CdNTROL ASSUMEDJFLOWDEPTHiF'I'} � 2.29 ------------------------- GRADUALLY VARIED FLOW PROFILE COMPUTED INFOHMA'I'ION: DISTAI3CE FROM�Y FLOW DEPTH VELOCITX SPECIFIC PRESSUR�+ CONTROL ( FT } ( FT } ( FT / SEC 1 ENERGY ( FT ) I'�SOM�7Ti7M { POi7NIlS 1 D.D00 2.268 1d.425 3.977 131Z.28 0.063 2.248 J.0.554 3.979 131i.97 0.25� 2.209 14.695 3.986 1314.03 0_580 2.169 10.649 3.998 1317.45 1.047 2.13a 11.016 9.015 1322.26 1.fi58 2.093 11.195 9.a38 1328.48 2.457 2.051 11.389 4.066 1336.16 3.430 2.012 11.596 4.341 . 1345.36 4.610 1.972 11.817 4.142 �35b.12 6.022 1.933 12.054 4.190 �36$.52 7.697 1.893 �2.306 4.245 1382.64 9.57A 1.854 12.576 4.311 1398.56 12_4a2 1.814 32.863 4.385 1416.44 14.741 �.775 13.169 9.470 1436.27 i6.044 1.764 13.294 4.5D6 1444.59 --------------------------------------------_ _ NODE 142.60 : HGL =� 284.718>;EGL= < 291.407>;FLOWLINE- < 287.43D> Y# f1r* **}}i 24*i Y1r *t'kik yr f**i�}#*f }�ryr*Yr*1r*�'1 Y' **iYr*kY� 1� *#Y�'t4YYii i!**�F Yri }}} y** i*Yr*#t'hY FLOW PRaCBSS FROt�S NdDE 102 . 60 `I`O NODE 102 . fi0 IS CODE = 8 UPSTftEP.M NODE 1D2.6D ELEVAT�ON = 287.43 (FLOW UNSEALS IN REACH) +CALCUI�ATE CATCH BASIN ENTRANCE L05SE5(LACFCD): PIPE FLOW = 49.10 CF5 PIPE DIAMETER = 30.OD INCHES FL�W VELOCITY = J.0.43 FEET/SEC. VELOCTTY HE.AD = 1.689 FEET CATCH BASIN ENERGY LpSS =.2*(VELOCITY HEAD} _.2*( 1.6891 = 0_338 ------------------------------------------------ NODE 102.b0 : HGL =< 291.745>;EGL= < 29i.745>,FLOWLINE= < 287.430> ♦*******} # t�'t4! # t*t �r ***f **#tttt******# �'t+i YtYi 1� 1� Y�' ****ii! 1 Y Yr Y�k* * i� k* 4 Y� # t+Yc #***f}W* UPSTRFAM YIPE FLOW CONTROL DATA: NOBE I3UMBER = 102.60 FLOWLINE ELEVATION = 287.43 ASSUMED UPSTREAM CON'i'ROL HGL = 289 • 72 FOR DOWNSTRF�.N3 RUFI Af�iALYSIS ---------------___ END QF GRADUALLX VARIED FLUW ANALYSIS • r r rt* f* 1*�/* f? k##+ f y f W rt Y* t**** f* k* 1* f M+ f f* V Y k W#* t Y** W* Y 4 Y t**� f#**�* f fi M�* f i�� Y t* . PIPE-FLOW HYDRAULICS COMPiTI'ER PROGRAM PACKAGE iReference: LACFCD, i�ACRD, AND OCEMA HXDR.Ai7LICS CRITER�ON) {c) Cbpyright 1982-2601 Advanced Engineering Software {aesj Ver. B.0 Release Date: 03/O1/20�1 Lacense ID 1509 Analysis prepared by: PROJECTDESIGN CONSUI,TANTS 701 'B' STREET, SUITE B00 SAN DIEGd, CA 921D1 619-234-0349 � .*...*...,*.,+*+.+*+.**�+*,.,. DESCRIPTIaN OF STC1bY �*.*...,�**++*�..,x.**+**�.w. * BF�SSI RANCH - ULTIMATE CONDTTIONS * * SYSTE33 lOD - LATERAL 130 (PA-2 I�T ALICAN'I'E/TOWN GARDEN RpAD) " * �OD-YEAR ' tirrr�r**rwr*r*:w******+++wxri.,rrrtY**rxwx��w+xr*++*+x**x**+**+w+r**tixeti+*+*x F�LE NAME: L1�O.DAT T�ME/DA'£E OF STUDY: 15:14 10/24/2Q02 Yr YYrYY�Y*�*tY�yr**k*k*Yr* * i*1�f 1'Y�*fY� *i*�rY� YrYrf Y�* *kYrri �k**i*f *Yr***Y�1k 1*1 Y#** tkY�* Yrrt Yr *�i�i�Y�� GRAI)UA�,LY VARIED FLOW ANALYSIS FOit PIPE 5Y5TEM 130DAL POINP STATU5 TA�LE SNote: '*' indicates nodal point data used.l UPSTREAM RLTN AOWNSTREAM AUN NODE MODEL PRESSUFtE PRESST3AE+ FLAW PRESSURE+ NUMBER PROCESS HEAD ( FT ) [SOMENTUM ( POi7NI?S } DEPTH ( FT j MOl�SENTUM ( POCR3DS ) 11D.10- 8.65* 16fi9.93 0.93 844.86 833.60 110.20- 4.95* 773.63. �.75 Ac 148.24 ---------- - MP.XIMU2+I NUMBER OF ENERGY BAL.�NCES USED II3 EACH PROFILE = 25 -----------------------------------------------------------------------------__ NQTE: STEADX FLOW HYDRAi3LiC HEAD--LOSS CONfPUTATTONS $ASED OId THE �SOST CQNSEitVATIVE F'ORMUI�iE FROM THE CURRFNT LACRD,LACFCD, ANA OCEMA DESIGN MANUP.�S. ♦s*rtx*�tr*y,rri.rrr*x***wr**wry+*f�+*r�rr***r*wttif*r*rfx+a�r*r*i.wa++,rr**+t+x*wk� DOWNSTREAri P�PE F�,OW CONTROL DATA: NpDE NU[�ER = 110.1� F'LOWLINE ELEVAT�ON = 286.85 PIPE FLOW = 24.5D CFS PIPE D�P.METER = 24.00 INCHES ASSTJ�iE17 DOVTt3STREAM COSI'i'ROL HGL = 295.5D0 FEET ------------------------____------ NODE 110.10 : HGL =� 295.500>;EGL= � 296.444>;F�OWLINE= < 286.850> } FRiCTIQN 110.15- 8.15* • ) FRICTIQN+BEND 110.20- 3.8�* } Cp'x'CH SP.Si13 ��z.s� 921.92 0.94 1.75 Dc 547.51 *w,rw**�x*,r�*ya�w*�tri.tY+******r*�**w*ii.+t++r*+iv,r+y.t+***�ti**x*+*x,r**+tk+rw+w** FLOW Pi�OCE55 FROM NOAE 110.10 TO NQDE 110.15 IS CODE = 1 UPSTREAi�i NODE 110.15 EL,EVATION = 287.44 (FLOW IS UNDER PgESBLFRE} CALCLiLATE FRICTION LOSSESILACFCD): PIPE FLOW = 24.50 CFS PTPE bIAMET�R = 24.00 INCHES PTPE LENG'�`H = 8_ 04 FEET I�5.n13NING`5 N = 0. D1300 SF=(Q/K)**2 = I( 24.501/( 226.21ZJ}**2 = D.D�.173 HF=L*SF = ( 8.00}*{0.01173) = O.a94 ____..-------------------------- NODE 110.i5 : HG� �< 295.594>;EGL= < 296.538>;FLOwL2NE= < 287.440> s.Wr*+*******:***x►,rw**wx**fr�+*�wst****++�*w**ttt+>+ka***wrte*++rrrt�:**�*�+i.+ • FLOW PROCESS FRpM NODE 110.15 TO NODE 110.20 IS CODE = 3 UPST?REA2+F NODE 1�0.20 ELEVATION = 292.77 (FLOW IS UIdAER PRESSURE) CALCiTLATE PIPE-B£?JD LOSSES(�CE�IA) : P�PE FLOW = 24.50 CF5 PIPE DIAsiETER = 24.04 INCHES CENTRAL ADIG�E = 34.340 DEGREES MANNING'S N= D.Di300 . PIPE LENGTH = 72.00 FEET BEND COEFF'ICiENfiIKB1 = 0.15434 FLpW VEL,OCITY = 7.80 FE£T/SEC. VELOCITY HEAi} = 0.944 FEET HB=KB�(VELOCITY HF_AI)) _{ 0.154}x( 0.944j = 0.�46 , SF=IQ/K)*�2 = fi 24.50}/( 226.223?)**2 = 0.01173 J HF=L*SF = ( 72.0�)"[O.OZ173) = 0.844 TOTAI, HEAD LOSSES = HB + HF =( 0.146)+( 0.844) = Q.990 NODE 110.20 : HGL =< 296.589>;EGL= < 297.528>;FLOWLINE= < 292.770> **.*.+**�.*+*++�..,,*.*x*.***�***+*+�*+**��++**+***t+�.*�*.*.*+++***«��.*,�.�:.� FLOW PROCE55 FROM NODE 11D.20 TO NODE 110.20 IS CODE = 8 UPST'REAM NODE 110.2� ELEVATION = 292.77 {FLOW IS UIdDER PftESSURE} CALCUI.ATE CATCH BAS�I3 ENTRANCE LOSSESfLACFCD}: PIPE FLOw = 24.5D CFS PIPE DIAMETER = 24.00 INCHES FLOW ITELOCITY = 7. BD FEET/SEC. VEL�C)CITY HEAI] = 0.944 FEET CA'i'CH SASIN ENERGY LOSS =.2'{}�LOCITY HEAD} _.2�{ 0.944} - 0.189 ------------------------------------------------------------------------------ NODE �1a.24 : HGI.� _< 297.7i7>:EGL= < 297.717>;FLOWLINE= < 292.77�> x*�*rxit+x**trf+++r*�*+x+*wx*+*w*+**x+xfw*.++�+awrt*r+**r►wt*+t�l�1*fiYYi1Y*Y1♦ LiPSTREAM PIPE FI,OW CONTROL DATA: NODE NL7M$ER = 110.20 FLOWI,INE ELEVATION = 292.77 ASSLTMED UPSTREAI� CONTROL HGL = 294.52 FOR DOWNSTREAM RUN AidALYSIS --------------------------------------------- END OF GRADUAi�LY VARIED FLOW ANALYSIS � L J • *sxw+rYrex*r*�xwrx**w++�:rxrww��rw�w�xxwx�www***rxrf*rxrfi*�rrtr�t�rrt+ryx*x*�*�x � PiPE-FLOW HYARAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRAUL,ICS CRITERION} fc) Copyright i962-20Q1 Advanced Engineering Software (aes) Ver. 8.0 Release Date: 0]/4]./2001 License I� �509 Analysis prepared by: PR0,7ECTDESIGN CONSULTANTS 701 'B' STREET, Sl7ITE 80Q SAN DIEGO, CA 92101 b19-234-0349 +....*.x...*...».*++....** g?ESCRIPTIO�I OF STUDY *•"'*•+*+*�.�++*v....*t+�*.. * BRESSI RANCH - iFLT2P4ATE CONAITIONS * * ALICANTE - SYSTEM 102 fPL.�PTNING AREA i0 CONNECTION) * * 100-YEAR S'FORM EVENT "' Y* 1 tYYY 1 Y YYYY!* f t*Yf * W R ri Yr f*Y�Y� i� Y�*'Y *T �i *Y t* W*Y *Y *f Y f*#YrlYYi YlYrYrt �IrYr*YrY� f Yr ***i tM FILE NAME: 102.DAT TI2+IE/DATE OF STLTAY: 07:4$ 10/24/2002 tia+yw+*++i+**+++�ww*xx++*�+++*�+rrt*a+tiy++rx*r**ita+*�*�*w�w*s*+wf+�.w.r*x*+x**+ GRADUALLY VARIED FLpW ANALYSTS FpFt PiPE SYSTEM I30DAL 1'OINT STATUS TASLE (ldote: "+" indicates noda� point data used.l UPSTREAid RUN DC3WNS�'REAM RUN NOAE MODEL PRESSURE PRE55URE+ Fi,OW PRESSURE+ NUMBER PROCESS HEAD ( FT ) MOMENR''UM { pOUNi?5 } DEPTH 1 FT } MpM�N'1'LT�I { POCri1D5 ) 102.00- 14.50' S0Q3.56 p.88 3148.50 ) FRICTTON } HXARAiTLIC JUMP z42.21- 4.16 1875.�4 D.81* 35D5.28 � , �SA23H�LE 142.22- 3.91 1798.54 0.80* 3564.71 ) FRIC�ION . 102.40- 2.34 Dc 1343.83 1.01* 2647.21 } ,7LTNCTION 1D2.41- 2.77 1417.29 0.89* 2999.31 } F'RICTIQN 1Q2.50- 2.29 Dc J.311.28 1.52* 1626.64 } MANHOLE 1D2.51- 2.29 Dc 13].1.28 ]..55* 1598.82 } ��CTION 1D2.60- 2.29�Dc 1311.28 2.29*Dc 1311.28 } ��] gASIN 1D2.60- 4.31* 938.67 2.29 Ac 318.94 MA}CIMUM NUMBER OF ENERGY SAL�PNCES USED IN EACH PROFILE = 25 NOTE: STEADY FiOW HYIIRALiLTC HEAL1-LOSS COMPUTAT�ONS SASED ON THE MOST CO�ISERVATIVE FORMULAE FROi�i Tf�E CURRENT LACRD, LACFCD, AND OCRMA DESIGN MANiJALS . ****x�x*w*�ww�srtx�*x*+*rtr+wr*++r+.***+.*k**++**x*+*r*w**�xwx+*rWr�rwrttt+.t+*�*++s bOWNSTRE.�h1 PIPE FL,OW CONTROL DA'I'A: DiODE NLFMBER = 102.00 FLOWL�NE ELEVATIQN = 239.60 , PIPE �'LOW = 49.90 CFS PIPE DIAt�ETER = 30.OD INCHES ASSUMED DOWIJST}tEAM CON'I'ROL HGL = 254 .�D4 FEET ------------------------------------------------------------------------------ NODE 102.00 : HGL =< 254.].DO>;EGi� � 255.7p5>;�'LpWLINE� � 239.60D> t*itk Yr Yr } Vr f Yr ir Vrk+*Yr1rYr k*�# * t*I�fY�FY f Yr #Yr�lr rt�i #it*Y� Yr*Yr *Y� *}YrYc*YrM*Y� Yr*+FyrYr k*#*i�f *� M*rt f*�kkYrYr♦ F"LpW PROCESS FRDI+3 NODE 102.00 TO NODE 102.21 IS CQDE = 1 UPSTAEAM NODE 1a2.21 EL�LTATIDN = 250.89 (HYDRAULIC J[3MP OCCURSi � ---__------___------------------------------_______----______-__----------__-__ CALCULATE FRICTiON LOSSE5SLACFCi�): PIPE FLOW = 49.9D CFS PIPE A�AMETER = 30.00 INCHES PIPE LENGTH = 64.36 FEET MANN2NG'S 13 = 0.01300 HYI7RAULIC JUMP: DOWNSTREAM AUN ANALYSIS RESLjLTS � ------------------------------------------------------------------------------ __NORMP.L-!]�PTHIFT}===-==-=0=92^====_=====CRITICAL-DEPTHIFT�=======-2-3�=`�Y-�= U1'STREAM CONTROL ASSUMED FF�OWDEPTH(FT) = D.81 GRADUALLY VARIED FLOW PROF�LE COMPi7'T'�D INFOAMATION: ----------------------------------------------------------__-______------------ pISTANCE FRpM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL { FT } ( F'I' } ( FT / SEC � ENERGX ( F'F 1 MOidENTiFM ( POU�S } 0.000 0.815 35.936 20.879 35Q5.28 2.784 0.819 35.fi75 20.594 3480.43 5.667 0.823 35.418 20.314 3455.91 B.b58 O.B28 35.1fi4 2D.039 3433.73 11.767 0.832 34.9i3 �9.772 3407.86 15.005 0.636 34.665 I9.507 3389.34 i8.386 fl.841 34.42� 19.250 3361.dfi 21.925 D.845 34.184 18.997 3338.12 25.642 O.B49 33.942 1E.749 3315.46 29.557 0.$53 33.707 16.506 3293.14 33.696 D.858 33.474 18.268 3271.OB 3$.09� D.862 33.245 16.035 3249.3D A2.779 0.865 33.419 17.806 3227.81 47.806 0.87Z 32.795 �7.582 3206.59 53.238 0.875 32.574 17.362 31B5.64 ' 59.�44 4.879 32.356 I7.146 � 3164.95 64.36D 4.883 32.182 16.475 3146.5D HYDRAiFL�C JUMP : UPSTREAM RUN ADIALYS�S RE5[7LTS ------------------------------------------ _ DOWNSTREAM CONTROL ASSUMED PRE55URE HEAD(FT) 14.5D PRESSURE FLOW PROFILE COMPUTED INFORMAT�ON: • ------------------------------------------------------------------------------- DISTANCE FROM PRESSURE VELOC�TY SPECIFIC PRESSURE� CONTROL ( FT i fiEP.D ( FT ) ( PT /$EC i ENERGY ( FT j MOMEN'T'iIM ( POUNDS ) fl.D00 �4.5D4 10.166 16.105 5041.5fi 64.36D 4.163 14.1b6 5.767 1875.14 ----------__.._____------END OF HYDI2AULIC JUDSP ANALYSIS----_.._-----------W----- � PRESSiTRE+MOMENTtJM BALANCE OCCiFRS A�` 35.46 FEET DPSTRE.�M OF NODE i02.00 I DOWNSTREA�I DEPTH = B. 844 FEET, UPS7'RE.�hl CONJUGATE DEP'I'x = 0. 853 FEE'F -----------------------�------------------- NODE 102.21 : HGL =< 251.705>;EGL= < 271.769>;FLOWLINE= < 250.69D> •*ytxrs*t+ww**rw*+x**ta++r+t*rrw*+w**+wr+t�++f+a**.**rf*t++**xs*+*+rtitrf*w**+� �'LOW PROCESS FROM NODE 1Q2.21 'i'0 NODE 142.22 IS CODE = 2 i3P5TREAM NODE 102.22 ELEVATION = 251.22 {FLOW IS SUPERCRTTiCALi CALCULATE MANHOLE LOSSES{L,ACFCD}: PIPE FLOW = 49.9D CF5 PIPE DIAMETER = 34.Q0 INCHES AVERAGED VELOCITY HEAD = 2D.4�6 FE�`I' HMN = .05"fAVERAGED VELOCITX I-IEAD) _ .05*(2D.416} = 1.021 ------------------------------------------------------------------------------- NODE 102.22 : HGL =< 252.R24>;EGL= < 272_791>;FLOWLINE= < 251.22D> 'h *+* *f W***Y� ** tYr* *Yr*f t Y� * f h} y�ui# YrY Yr**Yr*YrY f# ri f iF f YrYr *i*'kttt *f 1**YYrY* Ii M iFYr *'k+#YYi **�tYrYr i� FLOW PROCESS FROhS NOBE 1D2.22 T6 b30bB 102.40 I5 CODE = 1 UPSTR�AM NOI�E 102.40 Ei,EVATI0I3 = 26$.24 (F3,UW IS 5i7PERCRITICAL? CAI,CiTLATE FRICTTpN LQS5E5{LACFCDi: PIPE Fi,OW = 49.90 CF5 P�PE DIAMETER = 30.OD TNCHES PTPE LENGTH = 35.45 FEET M.�NNING'S N= 4.41300 ------------------------------------------------------------------------------ • --NORi+L�L-DEQ'I'H (FT� ^�-----_0-71"-"^-----CRITICAL-DEP'iH {�'T) -=-y_---2-30---Y'-- LTPS'T'REP.M COI3TROL ASSUMED Fi,OWDEPTH ( FT }= 1. O1 GRADUALLY VARIEA �'LOW PROFILE COMPUTED I�1F'ORI+fATION: � DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT} {FTJ SFT/SEC) ENERGYIFT) MQMENTI3M(POL7NDSj ' O.ODO 1.010 26.86� 12.22D 2647.21 1.DR3 0.996 27.244 12.573 2687.72 2.072 U.986 27.740 12.942 2729.54 3.215 0.474 28.201 13.330 2772.72 4.439 a.952 28.675 13.738 2$17.32 ' 5.752 D.949 29.165 19.166 2863.44 7.165 0.937 29.571 1G.6J.6 2911.02 8.689 0.925 30.193 15.089 296fl.26 14.336 0.913 30.732 15.58$ 3011.19 12.128 D.9D1 31.289 16.113 3a63.68 �4.078 0.889 31.B65 1.6.666 3�18.QZ �b.212 D.877 32.461 17.250 3174.9D 38.55B 0.865 33.07$ � �7.865 3233.40 � 21.i51 0.853 33.71b 38.51b 3294.02 24.037 D.84i 34.377 19.203 3356.H8 27.274 0.829 35.062 19.93a 3422.D7 34.937 0.817 35.773 2U.700 34$9.73 35.129 0.805 36.509 23.516 3559.98 35.450 0.8D4 36.559 2].571 3S6A.7� ------------------------------------------------------------------------------- NODE 102.40 : HGL =< 269.254>;EGL= < 280.4fi0>;FLOWLINE= < 268.240> YcYi** Yr iF* *1rYr f t* *M* i#'��1Yi f*Y f�*i1rM f YrYrYr fi Y�* fYrR*i1 *Yc* k*# *i** i� iiktik�*t# i tY�kt 1'frYrY� ►1rk #Yr FF�OW PROCE55 FROi�i NQDE 102.40 'FD NODE 102.41 IS CODE = 5 UPSTREAM NOAE 102.41 ELEVATION = 268.57 (FLUW TS SUPERCRIi'ICAL) ------------------------------------------------------------------------------ CALCULATE JUNCTION LASSES: PTPE FLUW DIAt+�Ei`ER ANGLE FLOWLINE CRITICAE, VELOCTTY (CFS) {INCHES} (DEGREESi ELEVA�`ION DEPi`H{�'T.} (FT/5EC1 � UPSTRE.�M 49.10 30.4D 0_OU 2fiB.57 2.29 3}..J.38 DOWNSTREAM 49.90 3D.40 268.24 2.30 25.869 LATERAL #1 O.OQ 0.00 Q.DO 0.00 O.DO 0.000 LATERP.L #2 O.DO 0.40 O.DO 0.00 0.04 O.ODO Q5 0.80===Q5 EQUALS BASIN I3dPUT=== � LACFCD AND OCEMA FLOW JUNCTION FORMULAE USED: DX=(Q2*V2-Q1*V1*COSfDELTAl}-Q3*V3*COS(AELTA3)- Q4*V4�C05(DELTA4J}/((A1+A2)*16.li+FRICTIdN L05SES UPS'I'i3E.AM: MP,FdNING'S 13 = O.Oi30D; FRICTION SI.�OPE = 4.39�07 DOWNSTREP.I�F: MP.idNING'S N= O.Oi30D; FFtICT'ION SLOPE = 4.325$6 AVEFtAGED �RZCTION SLOPE IN Ji3NCTI0N A55UMED AS 0.15846 NNCTTQN i�ENGTH = 2.44 FEET FRICTION i,05SES = D.387 FEET ENTRANCE LOSSES = 2.242 FEET JUNCTION L,OSSES = {DY+HV1-HV2j+(ENTRAi�ICE LOSSES} ,7LTNCTION I,OSSES = { k. 817 ) +; 2 . 242 } = 4 . 059 "N�DE Y`�02 41':'HGL =�< 269.454>,EGL= < 284.519>;FLOWf,INE= < 266.570> **.*.......*ti.*i+*fr*w*�.�*r�f**w,r�r..w.W*..t..t.rt*t+.++.****.w«..w.*f*+,r*+.+* FLOW PROCESS FROM NODE 102.43 TO NODE ].02.50 IS COAE = 1 UPST'REAM NOD£ 102.50 ELEVATTpN = 285.53 [FLAW I5 SUPERCRITICAL) ------------------------------------------------------------------------------ CAT�CLFLATE FRICTION L055E5(LACFCD}: PiPE FLpW = 49.ID CFS PIPE D�AMETER = 30.00 INCHES P�PE LENGTH = 54.00 FEET MANNING'S N= 4.41300 -------------------- NdRMAL DEP'i'H(FT} 0.78 CRiTICAi� D£PTH(FT} = 2.29 UPSTREAM CONTRpL A55UMED^FLOWAEPTHIFT) = 1.52 � __GRAI}UALLY VARIED FLOW PROFILE CO�FPCTFEA �I3FQR�SATIOI�i: DISTAA}CE FRONi FLOW DEgTH VELOCITY SPECIFIC PRESSUFZE+ CONTROL { FT J ( FT i { FT /$EC } ENERGY (�'T ) MOMENTUM { POL7AIDS i D.DO� 1.517 15.749 5.371 1626.64 D.547 1.488 16.12p 5.525 k65b.32 � 1.149 1.458 16.511 5.694 �fi68.01 1.8Z2 �.429 16.922 5.679 1721.$5 2.545 �.440 17.357 6.081 1757.97 3.355 �.371 17.835 6.342 1745.52 4.253 1.34i �8.300 fi.545 1837.69 5.25Q 1.312 18.813 6.81� 1881.65 6.362 1.263 19.356 7.1D4 1928.54 7.603 1.253 19.932 7.426 1478.86 8.996 1.224 20.543 7.7B1 2032.58 10.564 1.195 21.192 8.373 2D90.0$ 12.338 1.�65 21.883 8.6D6 2151.67 14.357 1.136 22.619 9.086 22i7.71 16.658 1.�07 23.405 9.618 2288.61 19.335 � 1.D78 24.245 10.2�1 2364.74 22.442 �.048 25.144 10.B72 2445.76 26.102 �.�i9 26.149 �1.61I 2535.Q9 3D.474 0.490 27.14fi i2.440 2530.42 35.794 D.960 28.2fi3 �3.372 2733.4B 42.427 0.93i 29.469 14.424 2845.�0 54.986 0.902 3D.773 15.515 2966.25 54.DDD 0.894 31.128 15.949 2499.3� ------------------------------------------------------------------------------ �ODE 102.50 : HGL =< 287.D47>;EGL= < 29D.901>;FLOWLZNE= < 285•530> r**+*****w*��***f++r*rr:f+�*+*rt*r+wa***++**x*fr+w�+++tf**yrt*t*�**wx�++ta�►wr�* FLOW PROCESS FROM NOAE �02.50 TO NODE 142.51 IS CODE = 2 UPSTREP.1� NODE 102.51 ELEVATIdN = 285.86 (FLAW IS SUPERCRITICAL) ----------------------------------------------------------------------------- CALCUI,ATE MANi30i,E LOSSES (L�ACFCDJ : PIPE FLpW = 49.i4 CFS PIPE DIAMET£R = 30.00 INCHES � AVERAGED VELOCITY HEAD = 3.758 F£E�' � E-iNIN =.05*i��1�AGED VELOCITY HFAD) _-D5*( 3.766) = 0.38$ ------------------------------._ NODE 102.51 : HGL =< 287.406>;EGL= � 29i.089>:FLOWLfNE= < 285.864> s*r*rrt*+x***++t***ww*+*�fxt+rr*rt+**tt+rtt*f�f*tr**+.*,r*��wa*,t**r*rrrrttx*�w*�i.*+ FLOW PROCES$ FRQM NODE 1D2.53. TO i�10DE 102.60 I5 CODE = 1 UPSTREAM NODE 102.60 ELEVATION = 2$7.4b i�'LOW IS SUPERCRITICAL) -----------------------------------------____-___---------------------____------ CALCC'filATE FRICTION LOSSES(LACFCD�: PIPE FLOW - 49.10 CFS PIPE DIAMETER = 3D.OD TNC�3E5 PTPE LENGTH = 16. 00 FEET t+iF�TNTNG' S N - 0.0130Q ------------------------------------------------------------------------------- NORMAL DEPTH(FT1 = 1.D7 CRITICAL DEPTHIFTj = 2.29 _________________�� « _ «__�____-______=�=__=___��__,�_��T=====__==_=�==�T�_ UPSTREAM CONTROL ASSUMED FLOWDEPT'H{�a - 2.2g -----------------��-��__-_____==_==_=_=___==_==��_ « ��__��_______=__=��__ GRADiJALLY VARIED FLOW PROFILE COMPUTED iNFOFtMATiON: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFTC PRESSURE+ . C4I3TROLiF'T) (FT) ;FT/SEC� ENERGY(FT) MO�M(POUNDSi �.D00 2.288 10.k26 3.977 131�.28 0.041 2.234 14.587 3.9B0 1312.34 4.158 2.190 10.76'7 3.991 1315.49 0.383 2.141 10.967 4.010 1320.75 0.693 2.092 1�.i87 • 4.037 1328.17 i.149 2.043 1i.928 4.473 1337.83 �.640 1.995 11.690 4.118 1349.82 2.300 1.946 11.4'74 4.174 1354.27 3.107 1.897 12.283 4.241 1381.31 4.D81 1.846 '12.618 4.322 t4U1.12 5.247 1.799 12.9$0 4.4�7 1423.B9 � fi.638 1.75� 13.372 4.528 i449.84 8.293 1.701 13.796 4.659 1479.22 J.0.261 1.553 14.256 4.81D 15Z2.33 12.607 1.604 14.755 4.985 1549.49 15.413 i.555 15.297 5 14k 1591.1D 16.00a 1.546 25.396 5.229 1598.82 � --------------------------------------------------------___---------- NODE ��2.60 : HGL = < 289.748>;EGL= < 291.43�>;FLOWi�INE= < 287.460> ' •wrx++x*+x+++*�xw*+r�+*aw�+k*�r+++*+*t**+x*�*Rr****r*�x*wk+*tt*+tr*rt+*�*x+++a+ FLOW PROCESS FROM NODE 102.60 TO NOAE 102.60 IS CODE _$ UPSTREAM NODE la2.b0 ELEI7ATION = 287.45 {FL(?W IS AT CRITICAi� DE�i'H) '^CALCUI,ATE CATCH BASIN ENTRANCE LQS5E5(TIACFCD): PIPE FLOW = 99.�0 CFS PIPE DIAMETER = 30.00 INCHES FLOW VEI,OCITY = 10.43 FEET/S£C. VEI.00ITY HEAD = 1.689 FEET CATCH BASIN ENERGX LOSS =.2*(VELOCI'I'1' HEAD) _.2'{ 1.669i = D.338 ------------------------------------------------------------------------------ NODE 102.60 : FiGL =< 291.775>;EGL= < 291.775>;FLOWE�INE= < 287.4fi0> f Yr* Yr*�k **ttk4 f Yr* ri Y�# k Y*1� � Yr�klMM*Yr#Yc*### Ir*t!**y f 1*►Yr�k i Y YrYr * i* *}iFYrYrYrY�'kf f Yr!*Yrt*t1rlrYr*R!r UPSTREAM PTPE FLOW CONTRpL DATA: NOD£ NUf�1BER = 142.fiD FLOWLTNE ELEVATION = 287.4fi ASSI]MF� UPSTREAM CON'I`ROL HGL = 289.75 F'OR DOWNSTR�AM RLFN ANALYSIS ___—_---___��_��____--_---�«______________________��_�_______===��__ FS3D OF GRADUALLY VARIED FLOW A3�IALXSIS � � � � � ` /� {� L j�{1 f �I� � ....�*..R.k.�*�t.,�.*..��*�..*.»*..*.+,�*+..f.++.+�....**x�,�.�.,..*w*....:.��., Analysis prepared by: PR0,7ECTDESIGN CONSLFLTP.NTS 70� 'B' STREET, 5UITE 8D0 SAN biEGO, CA 92101 619-234-0349 s *+*r*+r.:r*wx*ffsr***++x** bESCRTP`i'ION OF $T�Y *r**trtir*x+*�f�+�***wxww*+ * HRESSI RANCH - L7LTIMATE CONDI'FIONS * * SYSTEM 100 - LATERAL 2{AL?Cp,N'!'E ROAD STA 108+00 RT) S�. 15 r�►�: yCx3�-SC'� * � 0 0 -YEAR S�'UURt+S EVENT " 4iY�fti�Y4**WYf*r*x**�x***�+*++s+*++*tir�*y�trt*.*�r*�rti�t*tfw:�+*ws*��*+**�rr FTL� NAME: 100-2.DAT T�ME/DATE OF STiTDY: D9:44 09/3D/2002 :a****ww****x*+.**+.**�xxx+xrrt�rtryrttt+a*:x+**frt�*rr�x++*ww*x++**x*xr:�*yr+t*x ldODE PIiJMS�R 105.10- ] 1D5.2D- } 105.20- PIPE-FLOW HXARAULICS COMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRi1, AidD OCEMA HYUR.AiTL.ICS CRITERION) (c] Copyright 1982-2001 Advanced Engineering Software {aesj Ver. 8.0 ReZease Date: O1/O1/2401 License ID i509 GR.AD[iALLY VARIED FLOW ANALYSIS FpR PIPE SYSTEi�f NpDAL POTI3T STATTJS TABLE (Note: "*' indicates nodal point data used.) UPS'I'REAM RUN DOWNSTREP.�i RUN MOPEL PRESSURE PRE55URE+ FLOW PRE55URE+ PROCESS HEAD ( FT) MOMF�N'PiJM { POUNDS 1 DEPTH ( FT} MOMENi`i3M I POUNDS} �.93 Dc 85.62 0.45* 151.4$ FRICTION CATCH HA$Tbi 0.93*Dc i.�a* 85.52 Q.93*Dc 48.2B 0.93 Dc 85.62 28.94 ----------------------------------------------------------------___------------ MAXIMUM NUMBER OF ENEAGY SALANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEAllY FLOW HYDFtAULIC HE.�-LOSS COMPU'I'ATI013S BAS�D QN 'I`H£ MOST CONSERVATIVE FORMUI,AE FROt+S'F'HE CURRENT %ACRD,iACFCD, AND OCEMA DESTGN bIAN[]ALS . Yc t**lrik f�Ftr1 Y�* *k f* f Yr k YrYr* k 4*�+t1tK't *'t'k'1'!! *tk f Y� ir*****Y�Yr tt* # i*Yc+*ikMYr*YrY� k* t i�*#tY MY Yr t*** DOWtdS'T'REAM �IPE FLOW CONFROL DATA: NODE NUMBER = 105.14 FiOWLINE ELEVATIQN = 267.Q0 PIPE FLpW = 5.84 CF5 PIPE I)IAiIETER = 18.00 INCHES ASSIIMED DOWidSTREA3�3 CONTROL HGL = 267.070 FEET *NOTE: ASSUMED DOW3�TSTREAM CONTROL LIEPTH( 0.07 FT.} I5 LE55 THA3�T CRITZCAL DEPTH { 0. 93 F7'. ) -__> CRITICAL DEPTH IS ASSUMED AS DOWNSTREAM COidTROL DEPTH FOR UPS'IRE.�M RUN ANALYSIS ----------------------------------ti ----------------------------------------- NODE 1D$.1Q : HGL =< 267.454 ;EGL= < 27D.481>;FLOWLINE= � 257.400>.,� Y tYrYi **Yr*�k Yr *Yr*Yr*Yrf#�IrMYrtiFk R* *?ik Y�!'k 1� t i�Y Y>*t*Yri+Y f k fY-Yr 4Y♦r YYrflYYrt*�lr*� Yr1rk Yr 1�# *# �i f! tY PLOW PROCESS FROM NODE 105.1D TO NODE 105.20 IS CODE = 1 UPSTitEAM NODE �05.20 ELEVATION = 270.32�{FLOW �S SUP�'RCRITICAL} ------------------------------------------------------------------------------ • • CALCULATE FRICTION L055ES(LACFFD): PIPE FLOW - 5.8d CF S� P�PE DIAMETER = 18.Da INCHES PIPE LENGTH = 30.2i FEET MP.NNING'S N= 0.0�30d NbRMAL DEPi'HIFT) = U.41 CRITICAL DEPTHiFT) = D.93 UPSTREAM CONTROL ASSLIMED FLOWDEP�'H(FT) = 0.93 ---------------=�=_� « ��____=_=======___=__=_____________________-______=====_ GRALIUALLY VARiED FLOW PROFILE COMPUTED INFORMATION: DISTANCE FRQM PLOW DEPTH VEiOCITY SPECIFIC PRESSi7RE+ CON�'i�OL { FT ) ( FT ) ( FT / SEC j ENERGY { � } MOMENTLJP3 [ POUNDS ) O.OflO 0.929 5.441 1.324 65.62 D.009 0.9D9 5.177 1.325 65.59 D.037 0.888 5.321 1.328 85.89 0.065 Q.868 5.474 1.333 85.22 0.159 0.847 5.637 1.341 85.71 D.260 4.825 5.B1D 1.351 87.36 0.393 0.8D6 5.995 1.354 $8.17 0.56� 0.785 6.193 1.3$1 89.17 D.77i 0.765 6.4p4 1.442 90.35 1.424 0.744 6.63� 1.427 91.77 1.343 0.723 6.874 1.457 93.34 1.723 0.703 7.135 1.494 95.26 2.181 0.682 7.416 1.537 97.40 2.733 �.561 7.720 1.587 99.83 3.399 0.641 B.D48 1.647 1D2.56 4.245 0.620 8.404 1.718 i05.57 • 5.184 0.600 8.791 1.800 1Q9.i6 6.385 0.5'79 9.213 1.898 i13.b7 7.B73 D.558 9.674 2.413 ]17.47 9.748 D.538 �10.�80 2.�48 122.4D 12.153 0.517 10.737 2.308 127.95 15.376 0.497 11.352 2.499 134.19 14.873 a.476 12.034 2.726 141.21 26.749 4.455 12.793 2.498 144.15 3D.210 4.450 13.014� 3.081 151.48 ----------------------------------------------- ----------------------------- - I30DE 105.24 : HGi, _< 273.249�EGL= < 271.644>;FLOWLTNE= � 27�.320 **++**xr****xx+w****+*w+�w�r*x*wt+**w*r*xxr��r*++x�*w++x++wxr*+W+*rrrx*+sx*�+** FLOW PROCE55 FR03� NODE 105.20 TO NODE 1�5.20 IS CODE = 8 UPSTR.E.AM NODE 105.20 ELEVATIQN = 27p.32 fFLOW IS AT CRITICAL DEPTHI __----------------------------------------------------------------------------- CALCULATE CA�`CH SASIN ENTR�NCE LOSSES(LACFCD): PTPE FL04d = 5.8D CF5 PTPE DIAMETER = 18.00 INCHES FLOW VELOCITY = 5.Q4 FEET/SEC. VEiOCITY HEAA = 0.395 FEET CATCH BASIN ENERGY L055 =.2*IVELOCITY HEAi)) _.2'�{ 0.395) = 0.079 ------------------------------------------------------------------------------- i30DE 1D5.24 : HG� _< 27�.723� EGL= < 271.723>;FLOY�I�dE= � 270.320> *y��t*+ts*x****+�+++rxrt***+�+**+�+x*�rr:***+iw+w*t++�wrrr*a*+r*w�****+*+�+*+++**r iJPSTR�P,�1 PIPE FLOW CONTROL DATA: T30DE NUMBER = 105.2D FLdWF,TNE ELEVATION = 270.32 ASSUMED UPSTREAM CON'i'ROL HGL = 271.25 FOR DOWNSTREAM RUfI AidALYSTS _____________________��___-___________________=_____=======��_______=== . ' . � Y�wi� t i� xY�t1 Y�Yrt t�k+Y�t f*'kt ��t YrYrx Yr>Y� �iFi1 kY fi* Y� f* i�+fwi #y! **# **f f Y� 1!* Yr*tt�t Y�i �i Y*ZR f! Yr �Y fF Analysis prepared by: PROJECTDESIGN CONSULTAN'PS 701 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 619-234-D349 � �>*witi*x*i*:w*�>+ra*xw+swx DESCRIPTION OF STI.TDY '*:r**r�rt*w+�*+r�r+*x**++ * BRESSE R�NCH - []LTIMA�E CONi}ITIONS "` �* 5Y5TEM lOD - LATERAL 3(ALTCAN'i'E fiOAD STA 1D8+00 LT} S�H'T, i5� I�t�G 't`fU�'�C.-{ * lOQ-XFAR STORM EVEN'I' � ri****rt**�r*tr*rtt*+**t,r*w*+**a��rr*+�*r�*y*��t*+**rt**ryx***t**�+.+�*+*+*++ FILE ?�IAME: 1D0-3.DAT TIME/AA'T'E OF STUDY: 04:45 09/3D/2402 i�r **i **�FtFikM�/rYr�kkYr * Yr1� f YrYrY�# Yr#1r#4Y�f YY f i#*t*tYiktY* YrM*lYrYrlrM*1rYr* 1rM*M'w'ki** # ii�f �*** *Y* NOAE AT[.T[+IBER 145.50- } 105.60- } 105.50- PIPE-F�,OW HYDRAl3LICS COMPUTER PROGRAM PACKAGE (Reference: LAC�'CD.LACRD, AND OCEMA HYDRAULICS CRITERiON) (c1 Copyright 1982-2001 Advanced Engineering Software (aesl Ver. 8.D Release Date: 0�/D1/20D1 License ID 1509 GRAFIUALLY VARIED FLOW ANP.LYST$ FOR PIPE SYSTEt+I NODAL POINT STATUS TABLE (Note: "*' indi�ates nodal paint data used.) UPS�`REAM RUN DOWNSTREAl4 Ri1N MOAEL PRESSUA£ PRE55URE+ FLpW PRESSURE+ P}tOCES S HEAD ( F'I` j MONiENT[7IS ( POUNDS ) DEPTH { FT ) MOMENTUM ( POLTNDS ) �.64 Dc 33.17 0.33* 55.06 FRTCTTON CATCH BASTN D.64*Dc 0.92* 33.17 0.64*Dc 17.78 0.64 Dc 33.17 i1.83 ---------------------------------------------------------------------_--------- MAXI�f[JM 1dCTMBER QF ENERGY BALP.NCES USED IN EACH PROFILE = 25 -----------------------_------------------------------------------------------- NOTE: STEADY FLOW HYDRA[3LIC HEAD-L05S COi�SPUTA'T'IOt35 BASED ON 'iHE MQST CONSERVATNE FOR�3iiLAE FROM TF3E CURRENT LACRD, i�ACFCD, AND OCEMA DESTGN MANi7ALS . +*****,,...,...,.*,..*�***,.+.�.��:�*+.:�*.�+****.*,.+**«*..+*.**+«***.**+�.*w.,.ti:**.* DOWNS'PREAM PIPE FLOW CONTROL DATA: NODE NUMSER = 105.50 FLOWLINE ELEVATION = 267.Q0 PIPE FF�OW = 2.80 CFS� PIPE DIAMETER = 18.Q0 �NCHES ASS[3MED DOWNSTA� CON'I'RpL HGL = 267.470 FEET *NOTE: ASSCJMED �JOWAISTREAM CONTROL DEPTH( 0.07 FT.} IS LESS 'i`HAA1 CRZTICAL DEPTEi ( 0. 54 FT. ) _==> CRITICA� DEPTH 2S AS5[7i�fED AS DOWI35'FRF.AM CONTROL DEPTH FQR UPSTREAT4 RU23 AI3ALYSi5 ------------------------------------------------------------------------------ NODE 105.50 : HGL =� 25�.33C1� EGL= < 268.791>;FLOkT�,INE- < 267.04D> ****w*x��+*�*w+*+**w*+wy+r*+w��rs�r*:**�*v*rw�,�+*r*rt*w:w****+****+*xfi+�.r***+ FLOW P32pCESS FRpNf ATODE 105.54 TO NODE 105.6D I5 CODE = 1 UPSTREAM NODE 1�5.60 ELEVAT�Oid = 25B.07�(FLOW I5 SLiPERCRITICA�i ------------------------------------------------------------------------------ C J • CAI,CULATB FRICTION �OSSES{�CFCD}: PIPE FLOW = 2.80 CFS PIPE DIAMETER = 18.60 INCHES PFPE LENGTH = 9.2� FEET MP.I3NING'S'N - 0.0�300 i ------------------------------------------------------------------------------ NORrSAL AEPTH(FT} = Q.2q CRITICAIa DEPTHIFT) = 0.64 ------------------------------------------------------------------------------ UPSTREAM CONTROL ASSUMED FLOWDEPTHfFT} = D.64 _________________________________________�=__=___=___________=_=_______==_=_�= GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: • DIS'1'ANCE FROM FLOW DEPTH VELOCITY 5P£C�FIC PRE55URE+ CONTROL(FT) (FTj (FT/SEC� �NERGY(FT} MOMENTUM�POUNDS) O.�OD 0.635 3.931 4.875 33.17 0.003 0.619 4.067 D.676 33.21 D.D14 0.603 4.211 fl.879 33.32 0.032 0.587 4.3b5 • 0.883 33.5� b.D60 0.571 4.530 p.89p 33.77 Q.099 0.555 4.707 0_899 39.12 4.150 0.539 4.898 0.912 39.58 p.23.6 0.523 5.103 0.928 35.13 • 0.299 0.507 5.324 0.948 35.79 p.402 0.491 5.5fi3 0.972 35.58 Q.528 0.475 5.823 1.002 37.50 4.683 0.959 6.1d5 1.038 38.56 4.872 0.443 5.4i3 1.082 39.78 1.103 0.427 b.75D 1.135 41.i9 1.384 0.411 7.139 1.199 42.79 �.734 Q.395 7.527 1.275 A4.52 � 2.156 0.379 7.977 1.368 46.70 2.687 0.353 8.478 1.480 49.08 3.355 4.347 9.036 1.616 51.79 4.212 4.331 9.662 1.782 54.89 4.270 4.33D 9.697� 1.791 55.Ob , ------------------------------------------------------------------------------ NO�E 105.50 : KGL =< 2fi8.705>,�EGL= < 266.945>;FLOwLI2IE= < 268.074> ♦t f f Y!Y *f 4 f yr*!4 *rt * YY! YrY YY f Yr Y Y�lki*Yr f f yrfiYryr*Y�}yrYr*Y� �lr Yi * f Mt tYr* f Y**� f Yr **1r f yr*Yr f YrYr Yr#iy�+ FLOW PR�CE55 FROM NODE 105.50 'PO I+70bE Z05.60 I$ CODE = 8 UPSTR£AM IJODE - 105.6D EI,EVA'iIOAI = 26$.07 �FLOW IS AT CRITICA.L AEPTH) ----------------------------.._____________------------------__..____..___------- CALCULA7'E CATCH BASi23 ENTRAI3CE L05SE5(LACFCDI: PIPE �'7,OW = 2. 8p CFS � �IPE DiASdETEA = 18. D0 INCHES FI,OW VELOCTTY = 3.93 FEET/SEC. VELOCI'i`Y HEP.�I = �.240 FEET CATCH SASIN ENERGX LOSS =.2*SVELOCITY HEAD) _.2"( 0.240} = 0.046 __--____--____--__-_---_--_----------- ---------------------------------------- NODE 105.b0 : HGL =< 268.99��EGL= < 26E.993>;FLOWLINE= < 268.070> ♦*w****tix*er***�wt****w*r+�+�**+�,r*�*►�x,www��r+k*a*+**r+�+x*a*>*a**�**�x*r+s+�r UPSTREP.M PIPE FT�,OW COidTROL DATA: NODE N[.TMBER = 105.6D FLOWLINE ELEVATION = 268.07 ASSLfiIED UPSTREAM CONTROL HGL = 268.71 FOR DOWI3STREAM RCiN ADIA,LXSIS ------------------------------------------------------------------------------ ------------------------------------------------------------------------------- END dF GRADUALLY VARIED FLOW ANALYSIS • V- ^� y�J �1� f r� r.IT'� C� •�*wsw*y.i.x+*rtr*tsx+r+.+***wr+r��r�rr*f*wy*+*�*+xrx�*+xtrt>txy-**xwx*+a�s.rfxxr�xxsxx� PIPE-FLQW HYDRAULICS COMPUTER PROGRAM PACKAGE (Aefezence: i,ACFCD,LACRi), P13Ii OCEMA HXDRAiJLICS CRITERTpNf ic} �ppyright 1982-20�1 Advanced Engineeri.ng Software (aes) VEr. 8.4 Release Date: 01/O1/2003 License ID 1509 Analysis prepared by: PROJECTDESTGN CdNSLFLTANTS 701 'B' S'i`REET, SUITE 800 SAN DIEGO, C.A 92101 b19-234-0349 • i »***»**»+*..�*�*++�++�...,** DESCRIPTIDN OF STUDY "'***"*•"•"*"`•"***°+*•`•••Y BRE55I RANCH - ULTIMATE CONDITiONS ��s�,': * SYST�Si laa - LATERAL 9 fALICANTE ROAD $'FA �-i�RTj * 100-YEAR STDRM E1T�Ti' * •+*xww*�w***++**w++*rri**xr*+trrr+r+*w***sx*xr*�*w,w**ww,r�+w*+�a�tt**ti**+*+ FILE NAME: 1�4-4.DAT TIME/DATE OF 5Ti}DY: 11:39 09l30/2002 *�+*+f+*.v.w.�t4�1!li�W4**Yf*Ytk*YrYrMYk*Yr**kfY�#*Yr1�*t�t�f�a*aw*+++trw+s+r***t*+++*�w�** GRADUALLY VART�D FLOW ANRLYSIS FOR PIPE SYSTEM NODAL POINT STATUS 'FABLE (Note:, '*" indicates nadal point data used.} UPSTREAM AUN DOWNSTR�A27 RUN ' NODE MODEL PRESSURE PRESSURE+ FI,pW PRESSURE+ NUi+FBER PROCES 5 HEAI} ( F'T' ) MOMENTlFM { Ppt7�IDS ) DEPTH { FT } MOMEI3'I`UM { POUNDS ) i12.iQ- 3.95* 357.07 0.34 72.74 } FRICTION �J.2.2Q- 1.59* ) CATCH BASIN 112.20- 1.66* 1R6.29 ioa.�i D.72 DC O.7Z DC 45.68 16.16 -------------------------------------------------___-----------------------____ MP.XIMiJM rTiJr3BER OF F,f�iERGY BALAD}CES U5E3� IN EACH PROFILE = 25 NOTE: 57'EAAY FI.�OW HYDRAi7LTC H�-L05S COMPUTATIONS BASEA ON Ti3E MOST CONSERVATIVE FOi2MUL.�E FROM THE CURRENT LACAD,LACFCD, ANT] pCEMA DESIGN MANUALS. � *++xt+w��rrr*rti+**rtr***xxww**w*x*r+i.:*+�+++�r+*+r�+++Wai.�+rr��r*�*t*:+tt�,r+�*xvc� DOWNSTREAM PIPE FLpW CpNTROL DA�'A: 3dODE 3dUMBER = 112.10 FLOWLINE ELEVATION = 293.35 PIPE FLOW = 3.6p CFS PIPE DIAMETER =�8.00 INCHES ASSUMED DOWNSTREAM CONTROL HGL = 297.300 FEET -----------------------------�----- -------------------------------- - NODE i32.1D : HGL =� 297.300�EGL= < 297.364>;F�OWi�INE= < 293.35D ♦y**s*x++f*w****w*xk**rw+w�*sy*f**+�r*�t+**xy****r*wr*:***+r**>*rrxx+aiat+y+tx FLOW PRpCESS FROM NODE 112.10 TO NODE 112.20 IS COI3E = 1 iJPSTREAM NODE 112.2D EL�7ATTpN = 295.76�(FLOW IS UNDEA PRESSUREI --------------------------------------------------------------------�_-_------ CAi�CLTL.�'�'E FFtTCTION LOSSES 1 i,ACFC� ): P�P£ FLOW = 3_60 CFS PIPE DIAMETER = 18.00 TI3CHE5 PIPE LENGTH = 38. 37 FEE'i t+�P.NNING' S N = 4. 01300 SF={Q/K)**2 = {( 3.601/i 105.07a1}'"'2 = O.00Z17 • HF=L*SF = ( 38.37j"(4.00117} = 0.045 ------------------------------------------------------------------------------ r f NODE 112.20 : HGL =< 297.345�1;EGL= < 297.409>;FLOWLINE= < 295.76�>.J * * } k * * Y k f * * f w f M � * + t 4 i 1 W * * * k * * � w ? * * k * f * * * * * fi * R � * * * 1 f * � * * * � * k * * 1 f * 1 * * � * k * R k * * rt � * FLOW PROCE55 FROM �ODE i12.20 TO NObE 112.20 IS CODE _& UPSTREAM NODE �12.20 ELEVATION = 295.76 {FLOW i5 UNDER PRESSUREI ------------------------------------------------------------------------------ CF.L��LATE CATCH BASIN ENTRA�CE LOSSES(LACFCD}; PIPE FLOW = 3.6D CFSV PIPE bTANSETER = 18.00 NCHES FT.,OW VEZ,OCITY = 2.04 FEET/SE� V£LUCITY HEAi� = 5 FEET CA�'CH BASZPi ENERGY L055 =.2*IVELOCITY HEAD1 =.2*� 0.065) = 0.013 NODE 112.2D : HGL = a 297.422>;EGL= � 297.422>;FLOWLTNE= < 295.760> ++��***,rr*�k**�*r***fi*r*+*w*rxa*r{r.�ryr*w***rr**af..+*fw+�*a+wtr*rtrrt:*sy*r+t i3PS�'RF.AM PIPE FLOW CONfiFtOL i?ATA: 230DE I3[JMSER = 112.2D FLOWLINE EL�VATTON = 295.75 ASSUMED L}PST'REAM CONTROL HGL = 296.48 �OR DOWNSTREAM RUN ANAFJYSIS -------------------------------..___�___..___---___------------------------------ --______--_--___-__---------------------------------------------------------------_ END 0�' GRADUALLY �7ARIED PLOW ANALYSIS � • C� ***.�..w,�..*.x..*,.**..�,,.�*.x�*....,.�...**�..,..,..**,.,.**,�,.,��.*,,.., Analysis prepared by: PR0,7EC'PDESIGN CONSi.T�TAi,]TS 7D1 ' B' STREET, S[]�TE 800 SAN DIEGO. CA 92101 ' 519-234-0349 • • ys+rt*:*+arf�:tr*.*w*�rw*++ DESCRIP'TION 0�' $'�'�1i *,•rt�,.rrr*rtr*+ix**r**x*�++ * HRE55I RANCH - ULTIMATE C033�1ITIONS * * SYST�i lOQ - LATE�2AL 5 fA�ICANTE ROAD STA i14+00.90 �T} * * �00-YEAR STORM EVENT ` ****w*�+wi.+��*r*ti*:*****+**x+x++fww�*�+twrtr�f.++W�+v��rw++�rw*kt+a��*�**xsw�. FILE 23P.ME: lOD-S.DAT T�2+1E/DA'I`E OF S`iUDY: 09:51 a4/30/20D2 *�s�rr�**�r�**t*:+w+*+�*w*w+x*,rx*rr**rtrr*�*w+**+rr***rw*+*r+*r+wr*xx*t++r**ti*+ ldODE 23{JMEER 112.54- } 112.6D- } ].12.60- PIPE-FLOW HYDRAI3L��C5 CdMPUTER PROGRAM PACKAGE (Reference: LACFCA,LACRD, AI3U OCEt�4A HYDRAUL�CS CRITERION} (c? Copyright 1982-2001 AdvancEd Engineering Software (aes) Ver. B.0 Aelease Date: O1/bl/2D01 License ID 1509 GRADUALLY VART£D FLOW ANAiYSIS FOR P�PE SYSTEM NOAAi� POIN'T STATUS TABLE (Note: "•" indicates nodal paint data used.} UPSTREAM RLJAi DQW�ISTREAM RTJD3 MODEi� PRESSiJRE PRESSURE+ FI,OW PRESSURE+ PROC�S$ HEA}7 { FT) MOMEN'i'T3M S POUNDS ) DEPTH ( FT) MODfEP7TUM { POt3i�iDS ) 3.95* � 3fi1.45 0.31 59.48 FRICTION 2.54* CATCH SASIDI 2.59* 206.39 r.�Fr.�s:�.� 0.64 Dc 0.64 Dc 33.17 1i.83 ------------------------------------------------------------------------------ MP.XIMCFM NSJMBER OF ENERGY BALANCES USED I23 EACH PRQFILE = 25 ------------------------------------------------------------------------------ NOTE: S�'E.�I3Y FLOW HYDR.AULIC HEAD-LOSS COhSPUTAT10NS BASED ON 'T'HE i�fOST COP?SERVATIVE FOR2+IULAE FROM THE CiJRRFNT LACRD, LACFCD, AND OCEMA DESIGN MP.NUALS. r+tir*rt******ti�*t+*w*+tr**wxr>*+.f*�*+ti*+*t***�**rtt***rw*xs+w+****��++xf+rywra* DOWNSTREP.M PIPE FLQW CONTROL DATA: NODE NUMBER = 112.50 FLOWLINE ELEVATIQN=� 293.35� PIPE �'LOW = 2.80 CFS PIPE DIAME'FER =��_JQ' INCHES ASSUMED DOWNSTREAM CONTROL HGL = 297.3a0 FEET ---------------------___--------------------------------------------------- NODE �12.5D : HGL =< 297.340>;EGL- < 297.339>rFLOWL�13E= < 243.350 Yi �rt i� yrlr** �lr*}k f YrM Yr#Yrf * iFY•i�Y' *f'F Wf t'k t*1� **�kYr* �rYi YrYrYr*Yr*# Yr *� * iF rtYrYr�RlYr*# ii**'�Y #Yr**Y�1rY� kri k FLOW PROCESS FROM NOD£ 112.50 TQ NODE 112.60 IS CODE _� UPSTR�M NODE 112.50 ELEVATION = 294.76 (FLOW IS i32�iDE�t PRESSURE} ------------------------------------------------------------------------------ CA�,C[ILA'iE FRICTION LOSSES(LACFCDf : PIPE FLOW - 2.60 CFS PIPE DIAMETER = 16.00 INCHES PIPE LENGTH = 5.26 FEET MP.NNING'S N= 0.01300 sF=[Q�x�**2 = c� z.ao>i[ 1a4.815)}**a - o.000�i � HF=L*5F = ( 5.26}*(D.40D71) = �.004 NpDE �12.60 : HGL =< 297.344>;EGL= < 297.343>;FLOwLi13E= < 244.760> a�*r+xwytiwyt*t**t*x*+++*xt�*rrwti***rt*t+trxrr�w*rt***�*rtrriw*+ttw++x*x+++a�***+ FLOW PROCESS FRQM NODE 112.6Q TO NODE 112.60 IS CODE = 8 UPSTREAM NQDE }.12.60 ELEVATION' = 294.76J (FLOW IS L7i1DER PRESSURE} CAL,CULATE CATCH SASIN ENTRANCE LOSSES{L,ACFCD}; PIPE Fi�OW = 2. SD CF5 P�PE DIAi�4ETER = 18 . Od INCHES FLOW VELOCI'T'Y = 1.58 FEE`I'/SEC. VELOCITY HFAD = 0.039 FEET CA�'CH SASIN £NERGY LOSS =.2*(VELOCITY HEAD) _.2*[ 0.039) = 0.008 ----------------------------------------------------------------------______-__ NODE 1�2.60 : HGL =< 297.350>;EG�= < 297.350>;FLOWI,INE= < 294.760> rt*.,*.**+*.,+�****+v.w.�,.�***,.***�***.....*«..***x.*.*..�..*«.*.x*+.+�+�...****.** UPSTREAM PIPE Fi,OW CONTROL DATA: NODE slUMBER = 132.6U FLOWLIIdE E.LEVATION = 294.76 ASSU2+9ED UPS'i'REAPS CONTROL HGL = 295.40 FOR DOWNSTREAM RUN ANALYSIS EI3A OP GRAI)UALLY VAiITED FLOW ANALYSIS � � • i # * * * * ? * f f * # * * f Y * � � � i k * t * * * M * � * + f � * * # � * * k k * * } i Y Y Y � ! # * * * # * f * � f * * * * * # # Y * Y k # # t � * * PIPE-FLOW fiYQRAUIaxCS COMPUTER PROGRAM PACKAGE (Aeference: LRCFCD,LACRD, PND OCEMA HYDRAULICS CRITERION) {c) Copyright 1982-2002 Advanced Engineering Software faes} Ver. 8.0 Release Date: O1/O1/2042 License �D 1509 Analysis prepazed by: PROJECT D�SIGN COI�iSUL'PANfi5 7Q1 'B' S'FREET, Si3ITE 800 SAN DIEGO, CA 92101 619-235-6471 **.+..*++****+...+**+*+++*+ DESCRIPTIOI3 OF STUDY "*••**"+*�*`•**++«.**....�+ * BRESSI RANCH - ULTIMATE CONDITIOI�IS '` * SYSTEM 100 - LATERAL 6(GATEWAY CENTER DRIVE STA 25+50 RT) * * 100-YF.AA STORM EVENT "' **.�.�..,�.*+++t.W�**+*++****,..+.+.**+****.*+++��.,.�.+*t*+�.**+��*�+�w�.t*+ FIE.E NAME: ].00-S.DA�` TIME/DATE OF STUbY: 16:29 Q1/16/2UO3 *�***>�w�.**t*****�**,,+.*++,��*t..*.*+,�*�*��++t��+..*,.*�****++�..+r��****x+***. GRADUALLY VARIED FLOW ANALYSIS FdR PIPE SYSTEM NODAL POINT STATUS `I'ABLE (Note: "*" indicates nodal point data used.) iJPSTRE7�l�f RUN DdWNSTREAM RUN NODE MODEL PRESSi7RE PRESSURE+ FL4W PRESSURE+ � NUMBER PROCESS HEAD ( FT ) MOMENTUM ( PO[JNDS ) DEP'PH (�'T} M41+3Ei�FT[Ji�S ( POi7NDS } 124.14- 0.96 Dc 93.55 0.45' 171.4i . ) FRIC'I'I4N 124.11- 0.96*Dc 93.55 0.96*Dc 93.55 } CATCH BASIN 124.11- 1.46* 53.56 0.96 Dc 31.34 ------------------------------------------------------------------------------ MP.XIT7lTAf NUMBER OF ENERGY BAi.ANCES USED IN F.ACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEAI�Y FLOW HYDRAULIC HF.AD-LOSS COMPIiTATIONS �ASED ON THE MOST CQNSERVATIVE FORMULAE FROM �'HE CURREI�}T LACRD, LACFCD, P.3�ID OCEMA DESIGI3 MANUAE,S. ++***t*+++..*��**+�**++++.�ti�*��«**��*++�.�*t**�+�*...*+*�****��+�+t+..,.«***�**� T?QWNSTREAM PIPE FLOW C�NTROL DATA: NODE NLTMSEA = 124.1� F�,OWLINE ELEVATION = 322.67 PIPE FLOW = 6.20 CFS PIPE DTAMETER = 18.00 INCHES ASSUMED DOWNSTREAt4 CONTROL f�iGL = 322 . BflQ FEET *NOTE : ASSUMED DOWIdSTREAt�4 CO?�i'I'ROL DEPTH I Q. 13 FT _} IS LESS THAN CRITICAL DEPTHS 0.96 FT.) _==> CRxTTCAL DEPTH IS A55CR�ED AS DOWNSTREAM CONTROL DEPTH FOR LTPSTREAM RUN ANALYSIS • --------------------------------------- NODE 124.10 : HGL =< 323.122>;£GL= < 325.093>;FLOWi�Ii3E= < 322.670> *+**.+�*��+��+*��+.+.��**,..*t+*�.*.�*>+«t��**f+t�i+�.��.**+++*.�*«.+��**��,.t+ FLOW PRQCESS FROY+1 NODE 124.10 Tp NODE �24.11 IS COI}E = 1 UPSTREAM NODE 124.11 EL,El7ATI0N = 325.20 (FLOW IS SUPERCFiI'�'iCAL) CALCULA`I'E FRICTION LOSSES{LACFCDj: P�PE FLOW = 6.20 CP5 PIPE DIAMETER = 18.00 INCHES " PIPE LENGTH 9.25 F�E'1' MANN7NG'S N� 0.01300 � ----- � -NORMAL-DEPTHIFT�========0-34NY====-====CRITICAL_DEPTHIFTI_^�=====p-96===»=__ UPSTREAM COi+7TROL ASS[iMED FL�4tiTD£PTHIFTI = 0.46 ------------------------ GRADUALLY VARIED FLOW PROFILE COMPUTED INFdAMATION: DISTANCE FROM Yi4Fi0W DEPTH VELOCXTY SPECIFIC PRESSiJFtE+ COI3TROL { F7` ) { FT ) l FT / SEC ) ENERGY ( FT ) MOMET3TlTM ( POUi�iDS f O.OflO 0.962 5.176 1.378 93.55 0.005 0.937 5.336 �.380 93.64 0.020 0.4�2 5.508 1.384 93.93 D.048 0.688 5.693 1.391 99.4A Q.089 O.B63 5.892 1.902 95.17 0.146 D.838 6.1D7 1.417 96.�4 0.222 0.813 6.336 1.437 97.38 0.319 4.788 6.564 1.463 9B•91 4.442 Q.763 6.861 1.445 100.75 0.594 0.738 7.157 1.534 102.93 0.782 0.713 7.479 1.583 105.48 1.012 0.689 7.831 i.641 108.45 1.293 0.664 8.21b 1.713 11�.89 1.636 0.639 B.b40 1.799 �15.84 2.D57 0.614 9.10� 1.9Q3 120.37 2.574 0.589 9.624 2.028 125.56 3.214 a.564 1D.199 2•7.8� 131.A9 A.013 4.539 1a.641 2.366 13B.30 5.029 4.51A 21.562 2.591 146.D9 6.324 0.49D �2.375 2.669 155.D6 6.035 0.965 13.298 3.212 165.40 � ----------9_250----------fl_452-----13_829----------3_423----------_171_41----- N41]E 124.11 : HGL �< 326.162>;EGL= � 326.578>;Fi,OWLINE= < 325.2a4> tirk iF f****�y'Y�'k****ir# **YrYrYrM *i�*t't Y#t***�M * i� *#'t'tYtt****# kY� Y� *i#*ttk 1**i *� * k Y�k *#'t Y tt*ik FLOW PRpCESS FRON3 NODE 129.iZ TO NODE 124.�1 I5 CODE = 8 UPSTREAM NODE 124.11 ELEVATION = 325.20 (FLOW IS SUBCRITICAL} CALCULA'i`E CA'�CH BASIN ENTRANCE LOS5E5(LACFCD}: PIPE FLOW = 6.20 CFS PIPE DIAMETER = 18.40 INCHES FLpW VELOCYTY = 5.18 FEET/SEC. VELOCITY HF'.AD = 0.416 FEET CATCH BASIN ENERGY LpSS =. 2*( VELOCI'I'Y 1IF�AD 1=• z' ( 0. 416 j= Q. 0 8 3 ------------------------------------�__------- NODE 129.�1 : HGL =< 326.662>;EGL= < 326.662�;FLOWLIN£= < 325.2ab> **+,r,.*,r+*v�v.***�*+.++*+*«****��r*++t*.****�*��.,i+*+�+.,r+***,r+sf«*�t*+..x****+*+* UPSTRF.AM PiPE FLOW CO?�iI'ROL DATA: NODE NiJMBER = 124.11 FLOWI.INE EF,EVATION = 325.20 ASSUNSED [3PSTREAM CONTROL HGL = 325.�b FpR DOWNSTREAM RUN ANALYSIS --------------- END OF GRAD[3ALLY VARIED FLOW ANAI�YSIS • � f*�sfe��a**xx+*+++++*k*a*�r*�*++f+W*r�xwk*��r***wir�tw+f*+�w�w*r+��:t�*+t�x++i PIPE-FLpW HYDAAULTCS COMPi7'FER PROGRAM PACKAGE (Re�erence: LAC�CD,LACRD, A13D OCEMA HYDRAULICS CRITERION) fci Copyri.ght 1982-2002 Advanced Engineerang Software iaes) Ver. 8.0 R�lease Date: 41/01/2002 License zD 15D9 Ana�ysis prepared by: PROJECT DESIGN CONSULTANTS 701 ' B' STREE`I', SUITE S00 SAN DIEGO, CA 92101 619-235-6471 .�+.�*****+�++r+*+.*****t++ �ESCRIPTION OF S'PUDY "•*+f*�+***++.+.�*�«.*r+�� * BftESSI RANC!-1 - UL'i'�MATE COIdDIYTONS ` * SYS'FEM 100 - LATBRAL 7 IGATEWAY CENTER DRYVE STA 25+7D LT) ` * * lOD--YEAR STORM EVENT � � �F Y� *i� **'kY#t**tkYr*yr*}+fi t# **M'Yr*## t f *Yr**�lr*+�k�k �k �k * **Yrf *****'k'k*'k'k *'k�k *1r#*�'�'t� * �'* FILE NAME: �Ob-7.DAT TIME/DA�'E OF STUDY: �6:30 02/16/2003 *�kY *'k'k * 11r **'k'k i� i� i�'t'f 1 i * * * k Yr *#*'ki! ****yri�}*YY i i * **!r*#i't� t'k t'k * * ** f'!r**tt**4*# *rt*ir�i * * GFtAD[3ALLY VARTED FLOW ANALYSIS FOR PIPE SYSTEM NOAAL �OINT STATUS TABLE (Note_ '*' i.ndicates nodal point data used.� UPSTREAM Ri.FN AOWN$TRE.AI�4 RUN NODE MdDEL PAESSURE PRESSURE� F7�OW PRESSURE+ NUMBEFt PROCE55 HF.AD { FTi M02+iENTUM I POUNDS } DEPTH { FT ) MDI�EP1`I'E}M ( POUI3D5 ) •' 125.50- ' 8.19 3108.77 0.$8* 3i56.68 } FRICTI0�3 325.60- 2_30*Dc 1343.83 2.30*Dc 1343.83� } CATCH BASII3 125.60- 4.36* 958.36 2.30 Dc 322.43 ------------------------------ MAXTMUM NUMSER dF ENERGY SALANCES USED �N EACH PRQFII.�E = 25 -------------------------------- NOTE STEADY FLOW HYDAAUI,IC HEAD--LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CURREIQT LACRI}.LACFCD, ANn QCEMA DESIGN MANIJALS. +stf�****+*+��ry++i+**wxxx+a,��rt*�**ra.**w*y++�*x+t***ty+i*,rvri�*****r�*a*x**��y++�r DOWNS'f'RF.A�+3 PIPE FLOW COAI'I'FtOL DA`i'A: NODE N�Jt�ER = 125.50 FLOWE.INE EL�lATION = 325.61 PIPE FLOW = 49.90 CFS PIPE DIAMETER � 30.OQ INCHES ASSUMED DOWNSTAEAM CdNTROL I-IGL = 333.8Q0 FEET ------------------------------------------------ NODE 125.54 : HGL =� 325.491>;EGL= < 342.672>;FT.�OWLINE= < 325.614> s*v.��x+t+�*rt*+xx**k+++��re+�++*x*f+*ir�++�*s�+�rrax+***x**++�*+*s*wx++,�ti+*+�+ FLOW PROCESS FROM NODE 125.54 TO I30DE 125.60 IS CODE = 1 UPSTREAM NODE 125.60 ELEVATION = 353.79 (FLOW IS SUPERCRITICALI `CALCULATE FRICTTON L055E5L�CFCD1= PIPE FLOW = 49.40 CFS PIPE DIAME'I'ER = 30.00 7I�iCHES PIPE LENGTH = 104.00 F£ET MANNING'S N= Q_01300 --------------------------------------------- A NORMAL DEPTH(FT1 = 0.82 CRITICAL DEPTI-3(FT) 2.30 UPSTREA�S CONTROL ASSUMED FLOWDEPTH ( F'i'} � 2. 3 0 . ________________________________________��«________==____-_-_____=___-___==__ � GRADUALLY VARIED FLOW PROFILE COMPU�ED �NFORMATION: `DISTRNCE FROM 'FL4W DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT} (FT) (FT/SEC} ENERGY(FT) MOMENTUMfPOUNDS} D.000 2.298 10.563 4.032 1343.B3 0.021 2.239 10.756 4.037 1345.42 0 085 2.180 10.982 4.054 1350.17 6.196 2.121 11.235 4.D62 1358.10 4.355 2.062 11.518 4.123 1369.31 0.570 2.003 11.832 ' 4.�78 1383.98 0.847 1.944 12.]$0 4.299 1402.29 1.195 1.885 12.563 4.337 1429.52 1.625 1.826 12.9$6 4.445 1450.97 2.150 1.767 13.45� A.578 14$2.02 2.787 1.708 13_962 4.737 1518.09 3.557 1.fi49 14.526 4.927 1559.71 4.487 1.59Q 15.148 5.155 1607.47 5.612 1.531 15.835 5.427 1662.09 6.976 1.472 16.597 5.751 1724.43 8.637 1.413 17.493 fi.�4Q 1795.4$ 10.678 1.354 �8.385 fi.6Q6 1876.48 13.207 1.295 19.442 7.1b8 �968.87 16.3$S 1.236 20.628 7.647 2474.45 20.449 L 177 2L 966 8.675 2195.42 25.772 �.117 23.490 9.691 2334.5U 32.989 1.058 25.228 10.948 2495.11 43.299 0.999 27.228 12.519 26B1.57 59.416 0.940 29.548 14.5�6 2899.48 90.a77 O.B$i 32.263 17.054 3156.09 . --------104-000-----y--__0_B81-----32_27�---------i7.062-- -3156.88----- �OpE 1Z5.64 : HGL =< 356.fl88>;EGL= � 357.822>;FLOwLINE= < 353.790> * * * * * * * * i t � � � Y f f * * * * * * * * * * * * * w � Y t # * * * * * # * f � � * Y f i * # * * * * * * * ! * # * � * Y # i i * * * * * } * * rt * t FLOW PROCESS FROM NODE �25.60 TO NODE 125.60 IS CODE = 8 UPSTREAM NODE 125.60 ELEVATION = 353.79 (FLOW UNSEP_LS IN REACH) `TCALCULATE CATCH BASIN ENTRANCE L055E5(LACFCD): P�PE FLOW = 99.90 CFS PIPE DEAMETER = 30.00 ENCHES FLOW VELOCITY =�Q.57 FEET/SEC. VEE,DCI'iY HEAD = 1.734 FEET CATCH BASII3 Ff�iERGY LOSS =.2*{VELOCITY HEAD} __2*( 1.734} = 0.347 -------------------------------- NODE 125.60 : HGL =< 358.169>;EGL= < 358.169>;FLOwLINE= < 353.790> Y� � * yr Yc'k iF**#'t'j"M'!#**�c � � * ir irYr'!r**** t Y' Y 1***ik'k'!r *#*f'F �'f't k * * * * * **MYrYr****'k # *'1t* **Yr**i� #�#�! UPSTR.EAM PIPE FLOW CONTROL DA'PA: NODE NIJMBER = 125.60 FLOWLZNE ELEVATION = 353.79 ASS[3MED UPSTREAi� CONTROL }�GL = 356.09 FOR DOWNSTRFJIM RUN ANALYSIS �END pF GRADUAE�LY VARIED FLOW ANALXS�S . � .**._._.,.*..,..,..*,*�x�.�.,...,��*�,.��.,�.*...,�*.*��...rt*�.«,�...*.�*,_.., Analysis prepared by: PROJECTDESIGN CO23SLFLTAN'P5 701 ' B' STREET, $iJITE &OQ SAN DIEGO, CA 42101 619-234-Q349 . • *wr*r**w*+x+r*rrrxrtxf++r*r DE$CRIPTION OF STUDY *"`**:*w:wrrt+r+kw*w+r*x*�+ * s�ssz RANCH - ULT�MA'I`E co�z��a�s * * LATERAL 8- GATEWAY CENTER DRIVE (STA 25+70 RT) * * }. 0 D -YEAR STQFtM EVENT * *t*w+�+y**�+r*xrr*�+***rr+,�rr*tyrr***+*y+**ytr**yy***rtr+tr**�*w�r*+,r**++.+ FILE NAM£: 140-B.DAT 'I`II+IE/DAfiE OF STUDY: 10:27 �9/3D/2D02 riYrf� Y�lrYr�k* R*M�# M'Yr **iFY�*�k#�i�� *�k Y* *Yr f* Yr1rkltk�k*Yrk*iFf W iFYr#*�k* YrYrk*YrYrlrYrl�'YrYrY� *Yr k Yr *iM+tt�k! #Yr�! t NODE NUMBEA 125.14- } 125.2fl- } 125.2b- PIPE-Fi,OW HYbRAULICS COMPUTER PROGRP.t�S PACKAGE {fteference: LACFCD,LACRD, AND OCEMA HYDRAULICS C}tITERI0I3} fc} Copyright 1982-2001 Ac3vanced Engineering Software (aes) Ver. B.D Re�ease Date: O1/O1/2D41 iicense ID 1509 GRA.DUALi�Y VARIED FLQS+1 ANALY$TS FOR PTPE SYSTEM NODAL POINT STATUS 'i`ABiE (23ote: '*' indicates nodal point data used.] UPS3'REP.M RiRI DOWbFSTREAM RUN MdDF�, PRE55URE PRESSURE+ F'LpW PR.ESSURE+ PROCESS HEAD ( FT ) MpMEN'PUM ( POUNDS ) bEP'I'H ( F7' ) MOMENTUM { POt3NDS ) 7.19* " 725.15 0.59 50.93 FR�CTI�N 6.73* CA7CH BAS�13 b.Bl* 674.76 668.76 �.73 Dc 0.73 Dc 47.54 16.72 --------------------------------------------------------------------------------- MAXIMiFM 23IJt+3BER OF FNERGY BALANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ N0�'E: STEADY FLaW HYDRAULIC HEAT)-LOSS COMPUTA'I`TONS $ASED OAi 'FHE MOST C4N$£RVATiVE FORMULA� FROM THE CURRE3�iT LACRD,LACFCQ, AND OCEMA DESIGN M.ANUALS. „*x***..f+:,r+.x**,r»+++*..**.*.*t*t+****..****�*•*+�**,rr*�*«�+.***+*++***+�rt*t*+ DOWNSTREAM PIPE Fi,OW CONTROL DATA: NODE NUMBER = 125.1Q FLOWi,INE ELEVATION = 326.61 PIPE FLOW = 3.70 CFS PIPE DYAMETER = 18.D0 INCHES ASS[]?+�ED DOWNSTREAM CON'iROL HGL = 333 . B00 FEET ----------------------------------- ---------------------------------j" - NOBE 12� .14 : IiGL =� 333.840�EGL=«� 333 . 868>; FLOWLIi�IE= < 326. 510�/ T r+��***W**rr�r**r*ry**+*:*+w+er*+*****t+i.**t*+*s*x*f+�++**w+*wr*rex+a+�w*a+�+x FLOW PROCE55 FROM NpDE 125.14 TO 2dODE 125.20 I5 CODE = 1 UPSTREAM NOD� 125.2ff ELEVATION = 327.1? (FLOW IS UNDER PRESSURE} -------------------------------------___-_---......____----__---------------------- CAi�CULATE FRICTION LOSSESfLACFCD): PIP� FLOW = 3.7� CFS PIPE DIAMETER = 18.00 INCHES PIPE LEI3GTH = 42 . 76 FEET �SANNISdG' $ 23 = 0. 03300 SF=[Q/K)";2 = !I 3.70)/f 105.056?]**2 = G.OD�24 � HF=L'SF = { 42.76]'f0.00124) = 0.053 - ---------------------------------- - NODE 125 2Q T'HGL =< 333 853 • GL= < 333.921>;�LOWLINE= < 327.126� **.....**.�.*+***.****.*.*.*++*�*+�++�ti*.*�.+****.*+*�*.*�**.**..*..�*..*.�.*� FLOw PROCESS FROM NODE 125.20 TO NOD£ i25.20 IS CODE = 8 UPSTREAM NQbE 125.20 ELEVATION = 327.12 IFLOW IS UNDER PRESSURE) ------------------------------------------------------------------------------ CALCULATE CATCH BASIN EI3�'RANCE LOSSES(LACFCD): PIPE FLOW = 3.70 CFS PIPE DIAMETER = 18.00 INCHES FLOW VELOCTTY = 2.09 FEET/SEC. VELOCITY HEAD = 0.068 FEET CATCH BASIN ENERGY LOSS =.2'{VELOCTTY HEADj =.2*( 0.068f = 0.�14 -------------- - --------______-_____----_�_.. _ NOD£ 125 2D HGLY= < 333.935�GL- <'333.935>;F�OWi�INE- < 327.120ir� f ikfY f*ti **�**xyr! i�Y�}} #t W* W Yti Y f f i f*Y*Yr***Y�***t RYry f*YYYrt ft�Fyrff W#*Y Y*tt*�R t**YrYi arfMY� UPSTREAM PIPE �'LOW CON'F'itOL DA'i'A: NODE NC7MBER = 125.20 FLOWLINE ELEVATTON = 327.22 ASS[Jl�IED UPSTREAM CONTRdL HGL = 327.85 FQR DOWNSTR.EAM R[n3 ANALYSIS E�1D OF GRADUALi,X VAAIED FLOW ADIALYSIS . r� � � t*a*****+*«*r*****wwwrw*r**wx***+************w*****«+*w**++tf+**********a***** PIPE-FLOW HYDRAULICS COMPUTER PROGR�M PACKAGE � (Reference: LACFCD,LACRD, ANU OCEMA I�YDRAULICS CRITER�ON} � (c1 Copyright 1982-2001 Advanced Engineering Software faes} Ver. S.0 Release Date: D1/41/204� License ID 1509 Analysis prepared by: PROJECTDESIGN CONSiJI,TANTS 701 'B' STREET, SUITE 800 SAN DTEGO, CA 92101 619-234--0349 +++******r++yrw**��.�r****w+w DESCRIPTION OF STUDY ***+**+**++++*++t********• * BRESSI RANCH - UI.�'IMATE CONDITxONS * * SYSTEM 1Q0 - LATERAL 9(GATE4VAY CENTER DRIVE STA 32+A0, PA-5 LATERAI�) * * lOQ-YEAR STORM EVENT * 1't ttk*Yr�ki�ii* ###tf f �k # yr j�t**#yrf �t#tt**tk*tk** ***Yr'IrY� �r*�**tktklrtkYrtkY� f�*tk* tktktk tklr*yr f k*�k *** FILE NAME: 10�-9.DA'£ TI�fE/DA�E OF s�u�y: i6:aa 11/06/2Q02 *+*,ra********+*******+****w*****�******,r,rwwww,rv.ww�rW*******v,********w*vr*v�**t+*+ GRADUAL�Y VA}2IED FLOW ANALYSIS FOR PiPE SYSTEM NODAL POIN'i' STATUS TABL,E iNote: "*" indicates nadal point datia used.) TJPS�`REAM RUN DOWDISTREAM RUN NODE MODEL PRESSURE PRESS[TF2E+ FLOW PRESSURE+ NUMBER PROCESS iiFAD ( F�' } MOMEN'i'TJM ( P4UND5 ) DEPTH ( FT j MOMENP[TM ( POi3ND5 ) 139.10- 7.36' 4304.41 1.61 2940.19 ) FRICTION 139.20- 4.8�* 3178.76 2.76 Dc 2343.49 ) CATCH BASIN . 139.20- 7.i5* 2490.89 2.76 Dc 556.46 MAXzMUM NUMBER OF ENERGY BALANCES USED IN EACH PRpFILE = 25 NOTE: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE N30ST CONSERVA�'EVE FORMULAE FROM THE CUR.RENi` L�ACRD, LACFCD, AND OCRh4A DESIGN MANi7ALS. w,r*�+*********+r**wtr*,�,t*x*ww,t+**+***t*3********************+++t+*+****+**,r+*** DpWNSTFtEAM PIPE FLOW CON'!'ROL DATA: 3570DE NTJMBER = 139.10 FLOWI,FNE EL�7ATION = 362.83 PIP$ FLpW = 79.20 CFS PIPE D�AMETER = 36.a0 INCHES ASSUMED DOWNSTREAM CON'i'ROL HGL = 37d.19D FEET NODE i39.10 : HGL =< 370.190>;EGL= < 372.139�,FLOWLINE= < 362.83Q> - *�t**********.**.*******t**+***************�*�***��***************�*****�*,�*f FLOW PROCESS FROM NODE 139.10 TO NODE 139.20 IS CODE = 1 UPSTREAM NODE 139.20 ELEVAT�ON = 366.51 {FLOW IS UI�DER PRESSUR�j -�----------------------------------------------------------------------------- CALCI3LATE FRICTION LQSSES (7�ACFC�1 : PIPE FLOW = 79.20 CFS PIPE DIRMB'PER = 36.00 xNCHES PIPE LENGTH = 84.D4 FEET MpNNING'S N= 0.0130D SF=IQ/K)**2 = ({ 79.201/{ 665.978j)**2 = 0.4�410 HF=L*SF = ( $0.44j*{4.d14i0} - � 1.12B NODE 139.20 : HGL =< 371.318>;EGL= < 373.2b7�;Fi,OWLTNE= < 366.510> st*++***t+*+**t++t*tf*f*t*t*******t*r:**ww++.**t**+r******+r++***,r,r****�***+awir FLOW PROCESS FROM NpDE 139.20 TO NdDE 139.24 IS CODE = B � --CTPSTREANi i+70DE 139.20 ELEVATIQN = 366.51 {FFAW IS UNDER PRESSUREf CALCUL.�TE CA'i'CH BASIN ENTFtANCE LpSSES {I,ACFCD) : PIPE FLOW = 79.20 CFS PTPE DIAMETER = 36.00 INCHES FLOW VELOC�TY = 11.20 FEET/SEC. VELOCITY HEAi? = 1.949 FEET CATCH BASIN E2dERGY LOSS =•2*(VELOCI'F'Y HEAD) _.2*; 1.949) = 0.39� --____�----------------------------------------------------------------------- NODE 139.20 : HGL =< 373.657�;EGL= � 373.657>;FLOWLINE= < 366.510> � ***�**��*�***�******�**+****«************�*+*�++**.*************+*.**+****�*+* UPSTREAM PIPE FLOW CpNTRpL DATA: NODE Ni_TMBER = 139.20 �LOWLINE ELEVATION � 366.51 ASS[i�fED UPSTRE.n.M CON'I`ROL HGL = 369.27 FOR DOWNSTREAM RUN ANALYSIS ------------------------------------------------------------------------------ END OF GRADUALLY VARIED FLOW ANALYSIS � � �7 C��EL�4..1 r�?� �='�E �J s*x*�+*wx*xr**s*++�r�+*�xt+x**rx�>**�x*sx*�*s*yw+axt�x*+xawx+*xws*wax+txxxxxw+ PIPE-FLOW HY�RAULICS COMPU'i'ER PROGRAM PACKAGE {Reference: i,ACFCF,LACRA, AND OCEMA HYDRAUiICS CRITERION} (c1 Copyright �982-2001 Advanced Engineering Software (aesl Ver. 8.0 Releasg Date: 41/O1/200J. License ID 1509 Analysis prepared by: PRp,7EC'i`DESIGN CODiSULTANTS 701 ' B' STREE3', Si1ITE SDD SAN DIEGO, CA 42101 619-234-U349 . *.�»*�..+**.**+**+s+x*..... DESCRIP'iION OF STUDY **tx**ti*.*++*t+*++*t+*x*+* * BRE55� RP.NCH - ULTIidATE CONDITIONS 1� '" *$YSTEM lOD LATERAL 10 {GP.TEWAY CENTER D}2IVE SiA 33+36.78 RT)� S�y,�� '7�*- � * 10 D -YEAR 5'T'ORM EVENT ' + Y� f*YrYrYr,rYrfYr*ti*# tyrk }Yr# *�k Yrt}Yr Yr*ri iF k*Y� Y*k �1rYrYr*k*Y� *Yi * f t**Yrf#Yri Y YYr* YYr* tt* t+� f*Yrt fr FILE NAME: i00-1D.DA'F TIi�1E/bATE OF S�'L7DY: 10:32 fl9/30/2002 +wr*+xwrtf*xx*xx*x+*xr+*rtx+sw**:++�*+�**t+wsxsxR�*w*+*w*w,i.w**rw*,o-rrwx**xx��*+�+ GRADUALLY VARIED FLOW ANALYSIS FOR PI�E SYSTEM NODAi POINi' S'FATUS TABLE {I3ote: "*" indicates nodal point data used.) UPSTREAM RUN DOWNSTAEAM RUN I30DE MODEL PFtESSURE PRESSUftE+ FLpW PRESSURE+ NL�i�'iBER PROCESS HEAD ( FT} MQMENTLfM { PQL7ND5) DEPTH ( FT} MOMFNTUM ( POUNIJSI 140.�0- 0.67 Dc 37.82 a.44* 47.74 } FRICTIOi3 140.20- 0.67*Dc } CP.'I'CH BP,SIId 140.20- 0.98* 37.82 �0.67*Dc 20.33 D.67 Dc 37.82 13.93 MP.XIMUI+� NUMBER OF EbiEFiGY BALANCES USF.D �I3 EACH PROFILE = 25 NDTE: STEADY FLOW HYDRACTLIC HEAD-L05S COMPUTATIONS SASED ON THE M05T . CONSERVA7IVE FQRMUi�.�E FROM 'iHE CURRENT LACRD,LACFCA, AND OCEMA AESIGN MP.2+TUALS. � ' rti� tt 1!f Yik iFk Wtf tk**#* i�# k t�} * M 1r'X *# *� *�'tt iFlY1M�k#ik4'h *** Yr* Y� f ik * k ri Yr* YrYrYrY� YrYr'kkYrYrf kR rt Yr * Yr*ili� U*1� DOWNSTFtEAM PIPE FLOW CONTROL DATA_ NODE NUMBER = 340.10 J / �LOWLINE ELEVATION.= 369.83 PIPE FLOW = 3.10 CFSV PFPE DIAMETER = 18.00 INCHES ASSUMED DOWAISTREAM CONTROL HGL = 370.150 FEET *NOTE: ASSUMED DOWNSTREAM COlSi'ROL DEPTH( 0.32 FT.} IS LESS TIiAfQ CRITICAL DEP`I'H ( 0. 67 FT. }' ___> CRITICP.L DEPTH IS ASSLFMED AS DOWNSTREAM CON'iROL DEPTH FOR �7P5TREAM RUN ANALYS�S ------__�_-J ------------------------------------ NODE `140 1D HGL =� 370.272k,(EGL= � 371.D60>;FLOWL�NE= < 369.830 �L+i f�Ft* *�YiYi� Yr*k 1r kf iFri Y f�*f f k f,Fri # i� f*1 *Y�# Yr�F%� Yr *R 1riF*� M�F# 1r*Y� * iF*�t *1r t�ki* **MYr***f� M* W kYr k*♦ FLOW PROCE55 F'ROM NODE 140.1Q TO I30DE 140.20 IS CODE = 1 UPSTREAM NODE 190.20 ELEVATION = 370.96 (FLOW IS SUPERCRITICAL) • � CALCULATE FR�CTION LOSSES(LACFCD): PIPE FLQW = 3.10 CFS PIPE DIAMBT$R = 1&.Dp INCHES PiPE LENGTH = 42.75 FEET MAi1NTNG'S N= 0.01300 ------------------------------------------------------------------------------ NORMAL DEPTH(FT) = D.43 CRITICAL DEP'I'H{FT) = 0.67 iJPSTREAM CQNTROL AS5q3�SED FLOWDEPTH(FT) = D.67 �_�T «___-_===-�T�====--------------------�_��_�_��___�_��_�___________= GRADUALLY VARIEi] FLOW PROP�LE COS�SPUTEb INFORM.�TTOid: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEP'I'H �7ELOCITY SPECIFIC PRESSURE+ COI3'€'ROL{FT) {FT} (F'i/SEC) ENERGY(FT} MOMENTUM(POUNDS? 4.040 D.670 4.059 0.926 37.82 .� O.fl12 0.660 4.J.35 D.926 • 37.83 4.052 D.651 4.215 0.927 37.87 0.12a 0.64}. 4.297 0.928 37.93 D.22� D.532 4.383 0.930 38.03 0.358 0.622 4.471 6.933 38.14 0.535 0.513 4.563 � d.936 38.29 0.?57 O.b03 4.659 4.941 38.47 1.030 D.594 4.759 4.946 38.68 1.361 D.584 4.853 0.9�2 38.92 1.757 4.575 4.971 0.959 • 39.2D 2.229 0.556 5.083 0.967 39.51 2.789 0.556 5.201 0.975 39.86 3.451 4.547 5.323 0.967 40.25 A.235 4.537 5.451 0.999 40.66 5.165 0.52B 5.585 1.012 41.15 • 6.273 0.538 5.�25 1.027 41.66 7.603 Q.549 5.871 1.044 42.23 9.216 Q.A99 6.025 1.063 42.84 11.201 0.490 6.165 J..084 43.51 13.599 D.480 6.354 1.107 44.23 16.942 D.471 6.531 1.133 45.01 21.367 0.461 6.718 1.I62 45.85 - 27.956 0.452 6.914 1.194 A6.75 39.8fi9 0.442 7.k2i 1.230 47.74 42.750 p.442 7.121✓ 1.230 47.74 -----------------------------------------------------_____---------------------- NODE i4D.20 : HGL =< 371.63Q>;EGL= � 371.886>;FLOWLINE= < 370.950� twi+++*+tf:xx**+*****.*+�++w*�*xr***rrr*r**ts*+rr*:*+rt*r*++r*x:w+*+.***+++++r�* FLOW PRpCES$ FROM NODE 144.20 TO NQDE 140.20 �S CODE = 9 LTPSTRF�M PIODE 340.24 ELEVATION = 370.96 {FLOW I5 AT CRIT�CAL DEP'I'H} CALCUL.�'I'E CATCH BASIN EN'Fi�.�NCE LOSSES(LACFCD} ; PIPE FLOW = 3.10 CFS PIPE DIP.l�IETER = 18.00 INCHES FLOW VELOCiTY = 4.05 FEET/SEC. VELOCITY HEAp = a.25fi FEET CATCH BASIN ENERGY I.�OSS =.2*(VELOCITY HEAD� _.2*( 4.255) = 0.051 _____________________________ ------------------------------------ `NODE 140.20 : HGL =< 371.937 EGL= � 37�.937>;FLOWLINE= < 370.96a>� x*yi�+*x+�yrt+>r*x*+++w�r++tr**+*x*�+++�**+xr++wr+�*�+*+***�**r*+**+w+*wi+r�x>*+* UPSiREAM P�PE FLOW CONTROL AATA: NODE NUMSER = 340.20 FLOWI�INE ELEVATiON = 370�.96 ASS[Tt+IED L}PSTREAM CONTROL HGL = 371.63 FOR I�OWP15�'REP.M RiJAF F�7ALYSIS • � x**w**�x�xx�w+x*x*xxxrrx*xf*t>r.rrrrr��rt>xx*+***�r*w***rx++x�r�***�*x�w+�x**xy PIPE-FLOW HYDRAI3LIC5 COMPLT'T'ER PROGRn.M PACKAGE (Re£erence: LACFCD,i�ACRD, AND OCEMA HYDRAULICS CRITERIpN) Ic) Copyright 1982-2041 Advanced Fngineering Software iaes} Ver. B.0 Release Date: O1/�l/2DD1 License TD 1504 Analysis prepared by: PROJECTDESIGN CONSCTi,TANPS 741 'B' STREET, SUITE 8�0 SAi�I DIEGO, CA 92101 619-234-0349 �v.+�,++aiv.�+f*wx+**+++y,w�+* DESCRiPiIQN OF S'i'UDY '�r*+*�'*ww+w*�x***+t+v,+a,.aa * BRESSI RANCH - ULT�MATE CONDITTON$ * * SYSTEM 100 - LATERAL Z1 {GATEWAY CENTER DRIVE STA 33+36.76 L3`j�� (''� • * 100-YEAR SfiORM EVFNT � " `f c�'",� *Y�fir* * *Yr# *Y� f Yr iF k *lrYri� iF *R�k�Y *�'# iY W f M*MY W *Y*4 # * W *4il�k W+M*!�'!r **i#Yr Yr # *i� #i*i*f *i4 � ♦ Y FILE i3AME: 100-11.I}AT TIME/DATE OF STUDY: 11:5fl 09/30/2Q02 rrt**rw+*****. y�� }�k y�f ��1 f Yrf Y f Y*ti**tktk*Yr*1r�k*Y!Y**Yrlt*!* f! f Yti Y M*i� f YY! *YYr**�tY�lr*1rf YrYi ♦ GAADUALLY VAfiIED FLOW ANALYSIS FOR PIPE SYSTEM N�DAL POINT STATL3S TABLE [Note: '*' indicates nadal paint data used.j UPSTREAM R[Ji�i DOWi�ISTREAIyF RLTN • NODE MdDEL PRESSURE PRESSURE+ FLOW PRESSURE+ NLTMB£R PROCES S HEAD ( FT ) NSOMEN'T'IJ�S; POUidDS J DEPTH ( FT } MbMEid'i'iJM { pOUI3DS } 140.50- 0.67 Dc 37.$2 0.34` 65.39 } FR�CTION - 140.60- 0.67�Dc 37.82 6.67*I3c 37.62 ) CAi'CH BASIN 140.60- 0.98� 20.33 0.67 Dc 13.43 ------------------------------------------------------------------------------ MAXINfL7Ni NL7MBER OF ENERGY SALANCES USED IN �ACH PAOFiLE � 25 ------------------------------------------------------------------------------ NOTE: $TE.�L]X FLOW HXDRAULTC H�D-LOSS COMPT3'I'ATIONS SASED pN '£HE M057' CONSERVATIVE FOAMULA£ FROM THE CiTRRENT LACRD,LACFCD, PND OCEMA DES�GN MPNUA.I,S. :**wtse**r:tit*w*.***�**yxt+axt+r*�***r*�+t+x*x***+*++*�**y*xr**wrt*+++arrw►�x+xi� DOWNSTREP.M PIPE FLOW C�NTROL DATA: NODE NUMBER = 140.50 � F%OWIsINE ELEVATION = 369.83 PIPE FLOW = 3.1D CFS PIPE DIAMETER = 18.OD INCHES ASSUMEfl DOWNSTREAM COiQ'�`ROL HGL = 370.200 FEET *idOTE: ASSUMED DOWNSTREAM CONTROL DEPTH( 0.37 FT.) TS LES$ THAN CRITICAL DEPTH{ 0.67 FT.} ___> CRITICAL I}EPTH IS ASSUMET� A5 DOWNSTREAM CONTROL DEPTH FOR UPSTREAPS RLTId ABiALYSIS ---------------------_____---------------------------------____---------------_ NODE 140.50 : HGL =< 37p.166>;EGL= < 371.Bb6�;Fi0WL2NE= < 369.834,� frtr**�r�.rfr,�r+x+x.+++tr�*atiyxw.w�wrt*:*�x►*r,�r�.+:r*+rrr+ttr��+r*:rt+r*��+x*x FiOW PROCESS F}ZOM NODE 140.50 TO NODE 14�.60 IS CODE = 1 UPSTREAM NODE 1k0.64 ELEVATiON = 371.�4 (FLpW �IS SiTPERCRITICAi�� ------------------------------------------------------------------------------ C � � CAI,CLTiA�E FRICTION L05SESILACFCD): PIPE FLOW = 3.30 CFS PIPE DIAidETER = 18.OD INCHES PIPE LENGTH = 4.75 FEET MANNING'S N= 0.013D0 NORMAL DEPTH ( F� )= 0. 24 CRITICAI, DEPTH [ F`i') = 0. 67 ---------------------------------------------------------------------_---___-_-_ --------------------_------------------------____-___-------------------------- UPST�tEAM CONTRO� A55UidED FLQWDEPTH ( FTj = D. 67 GRADUALLY VARIED FLOW PROFILE COP4PUTED INFOAMATION: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCIT'Y SPECiFTC PRESS[J�-t CONTROL ( FT ) ( FT J { g'i' / SEC ) EIdERGY ( FT } MOMEATTIJi+3 { p0[TNDS } a.flOD 0.670 4.059 0.926 37.82 - 4.043 0.653 4.199 4.427 ' 37.$6 U.Ok4 0.636 4.349 U.929 37.99 4.032 0.6i$ 4.510 U.434 38.20 O.ObD 0.601 4.682 U.942 38.52 4.048 0.584 4.Bfi6 0.952 38.43 Q.149 0.567 5.Ob5 0.966 39.45 0.2�4 0.550 5.280 4.983 .44.11 0.296 0.533 5.5k2 3.OU5 40.E9 0.398 0.516 5.7b3 1.032 41.Bi 0.524 0.498 5.036 3.064 42.88 0.678 0.481 fi.333 �.1p5 44.14 0.857 0.464 6.658 3.153 45.58 1.097 0.447 7.014 �..212 47.23 1.38D 0.930 7.446 i.282 49.13 1.726 0.4J,3 7.E39 3.358 51.34 � 2.i55 0.396 8.319 i.471 53.77 2.590 0.376 8.854 �.596 56.60 3.366 0.361 9.452 1.75D 59.83 4.233 0.344 10.126 / �1.437 63.54 4.750 0.336 10.459� 2.D36 65.39 ----------------------------------------------------------______----______----- NODE 140.60 : HGL =< 371.810>;£GL= < 372.D66>;FLOWLINE= � 371.140> *****+xw*�a+****r*r+xrt►+**w***,r,r*exx*xxxw*wa****xwt***r**�r*r�r+*r*ryxf**:*w*t F�,OW PROCESS FROM NODE 140.60 TO NODE 140.60 IS CODE = 8 UPSTREP.M NODE 140.60 EL�7ATZON = 37�.14 iFLOW I5 A7' CRI�'ICAL DEPTH) CALCULATE CA'i'CH BASIN Ei�l'I'�i.F�II� +�E I,OSSES (J.ACFCDj : PIPE FiAW = 3.10 CFSv PIPE bTArFETER � J.8.4D INCHES FLOW VELOCITY = 4.06 FEET/SEC. VELOC�TY HEAD = 0.256 FEE'T' CATCH BASIN ENERGY LOSS =.2*(VELOCIT'Y HEAD) _.2*( 0.2561 = 0.05}. ------------------------------------------------------------_____----------- - �}ODE 140.fi0 : HGL =< 372.117>;EGL= < 372.117>;FLOWLINE= < 371.140�,� +*tk Wf#}# �t *f *i� 1rYrk iFYrk *YrYc YrYrYr 1rYr* iYYi � f*�r ** Yr *f * kYr�k *Yr *ii i*t kt * ti Yr Y f*i Y YYr#i �k **Yr ***Yr**** * UPSTREAM PIP£ FLOW CONTROL DATA: NOAE NUMBER = 140.50 Fi�0Y7E,INE ELEVA'T'ION = 37i.14 ASSii�fED T3PSTREAM CONTROL HGL = 371.81 FOR DOWNSTREAM RUN ANALYSIS END OF GRP.I7UALLY VARIED FLOW ANALYSIS a � � k * * * * Y W � Y * * * * * # f + i f + � Y � * * * * * * } f * ti i # * * ? k * 1 � * * f t # * * * # * * * * } * * # * * * # Y � f # i * k f * * W * � * * PIPE-FLOW HYDRAULiCS COMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRD, AND OCEi�3A HXAFtAULICS CRITERION) (c) Copyright 1982-2002 Advanced Engineering Saftware faes) Ver. 8.0 Release Date: 41/O1/2a02 License ID 1509 Analysis prepared by: PROJECT DESIG�I CdN5[3LTANTS 701 'S' STREET, SUITE 800 SAN DIEGO, CA 92101 619-235-6471 ' :.t***.**+�.*��***..***+ww DESCRIPTION OF 5�'UDY **+*+*`.�**''.'`*"'�'`.".***`� * BRESSI RANCH - ULTIMATE COI3DITFON5 "` * SYSTEM lOD - LA'iERAL 12 (GATEWAY CENTER DRIVE STA 39+36.90 Ri`) * t * 100-YEAR STORM EVEN�' *Yr*Yr1r*� �'t*#i�'M Y� Y� 1'k *# * f'tf �*** k� iif � y' Y f**� rt iF*i�#*Y**Y#Yi**YrYr*Yr*f # i't�*** #*w'ti�*♦ FILE NAME: 100-12.DAT TIME/DATE QF STUDY: 16:46 Ol/1612003 �***v.**�*��**+�***�**++,.,.+***.t.*�*.,��,,*�,*t+*+�..*�**++�.�t�**�*.**++�**t**�** GRADUAI,LY VARIED Fi,OW ANALYSIS FOR PIPE SYSTEM NODAL POINT STATUS TABLE ' {Note: "*' indicates noda� point data used.) UPSTREAM RUN DOWNSTREAM RUN NODE �70DEL PRESSURE PRESSURE+ Fi�OW PRESSURE+ NLTMBER PROCE55 HEAL7 ( FT j MOMEAiTfTM { POiJNDS ) DEP�i ( FT) ASOMENTUM ( POUNDS ) � }�p.ZQ- 0.80 Dc 59.56 a.63* 64.67 ) FRICTION 160.20- 0.80*Dc 59.56 O.SO�Dc 59.5b } CA'I'CH $ASIN 160.20- 1.19* 32.54 0.80 Dc 20•70 ----------------------------- N3AXIMlFM N13f4BER OF ENERGY BAE�AI3CES USED IN �ACH PROFILE = 25 -------------------------__ NOT�:'$TSADY FLDW H7CDAAULIC HEAD-LQ55 COMPI3TATIONS BASED QN THE MOST CONS�RVATIVE FORNfiiLAE PROM 'i'F-3E C[3RRENT LACRD, LACFCD, AND OC�73A DESIGN MP.NUALS. *�!****1r'!r* ***1t1tY!*t*t**Yc ik �k i� i i� i � 1 t**iF** **f *1�'k't***�F�Ir'k * * * **'1' * Y"A"k * ***'k'kk 1�f Y�1 * **yr'k*# Dt?WNSTfiEAM PIPE FLOW CONTROL DATA: NODE NUMBER = 160.10 FLOWLINE ELEVATION = 383.61 PIPE FLOW = 4.40 CFS PIPE DIAME�`ER = 18.00 INCHES ASSUMED DOWNSTREAM COtF'I'ROL HGL = 383.500 FEET iNOTE: ASSUMEa DOWNSTREAM COId'TR4E� DEPTH{ -Q.11 FT.} IS LESS THAN CRITICAL DEPTH( O.SQ FT.� __-> CRITICAL DEPTH I5 ASSUMEA AS DOW3�IS'FREAM CONTROL DEPTH FOR UPSTREAM AUN ANALYSIS ----------------------------------------------- NODE 160.10 : HGL =� 384.243>;EGL= < 384.641>,FLOWLINE= < 383.6�0� **��«+*****�«,,**++t,,�*t**�*****w.�**+«..****.tww*+****.*****��+.�*+«*.*+��++** FLOW PROCESS FROM NODE 16�.10 TO NODE 160.20 I5 CQDE = 1 UPSTREAM AiODE 160.2Q ELEVATSpN = 384.19 (FIAW IS SUPERCRITICAL) CALCULATE FRICTION L�55ESII.ACFCD}: PTPE FLOW = 4.40 CFS PIPE DIAMETER = i8.00 INCHES PIPE LENGTH = 43_25 FEET i�ANNING'S N- 0.01300 • ------------------------------------------------------------------------------- NOF2MAL DEPTH(FT} - 0.62 CRZTICAL DEPTH(FT) 0.64 � UPSTREAHI CONTROL ASSUMED FLOWDEPTH{FTj=-=--==0=80=====---------=====LL=====-_ GRADUALLY VARIED FLDW PROFILE COMPUTED INFORMATION: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL ( FT } ( FT} ( FT/SEC ) ENERGY f FT} i+10MEN'i'LTM ( I'OUNDS 1 0.000 0.805 4.557 1.127 59.56 0.016 D_797 4.6D8 1.127 59.57 D.067 0.790 4.661 1.12$ 59.59 0.155 0.783 9.715 1.128 59•53 4.2$5 0.776 4.771 1.129 59.68 0.4fi1 0.768 4.828 1.134 59.76 0.586 a.761 4.886 1.132 59.84 0.969 0.754 4.945 1.134 59.95 1.314 0.747 5.04f 1.136 60.07 1.730 0.739 5.069 1.139 60.21 2_225 0.732 5.133 1.142 50.37 2.814 0.725 5.199 1.145 54.54 3.5d7 0.718 5.26b 1.I49 b0.74 A.324 0.713. 5.335 1.353 60.96 �.285 0.703 5.40b 1.157 61.19 5.419 4.696 5.479 l.lb3 61.45 7.763 0.689 5.554 1.158 61.73 9.367 - O.fi82 5.53� 1.174 62.03 11.302 O.b74 5.714 L 181 62.35 13.670 0.667 5_791 1.188 62.70 16.631 0.660 5.874 1.196 63.07 20.453 0.653 5.960 1.205 63.46 � 25.638 0.695 5.048 1.214 fi3.88 33.313 0.638 b.138 1.224 b4.33 43.250 0.633 b.205 1.231 64.67 � NaDE �50 20 : HGL =< 384.995>;EGL= < 365.317>;PLOWi�Ii�7E= < 3$4.190> *+***��.+********,.�**�***+��*�**�*********�t��**.*****+�«+�..rt�***.****��*t** FLOW PROCESS FR02+3 NOiJE 160.20 TO i30�E 160.20 IS CODE = 8 UPSTRE.�M NODE 160.20 EL�7ATIOI3 = 384.19 �FLOW IS SUBCRITICAL) CALCLiLATE CA'TCH BASIN ENTRANCE LOSSESILACFCD): PIPE FI,OW = 4.40 CFS PIPE DZAMETER = 18.Oa INCHES FLOW VFL�OCITY = 4.56 FEET/SEC. VELOC�TY HEAD = 0.323 FEET CATCH SASIN ENERGY LOSS =.2*(VELOCITY HFAD) _.2*( D.323} = O.OfiS ------------------�------------------ NODE 160.20 : HGL =< 385.382�,EGL= � 385.382>;FLOWLINE= < 384.190> *,.*+��***«****.**+*�***�+��*�**.***.*�wxttx*�****�****��+w�t,�*t**.****��**** UPSTREAM PIPE FLOW C�N'I`RpL DATA: IJOrJE NiJMBER = 160.20 FLOWLT2�iE ELEVATION = 384.19 A55CTMEB UPS'I`REAM C�NTROL HGL � 384.99 FOR DOWNSTREAM RUN ANALYSIS END OF GF2�ilUALLY VARIED FLOW ANALYSIS �l � u � �*�k++,try,*y�y,:ax***w*��+,r*r*rtxrr��r,rfr***trt*�y.�+xx+s*x****rr*+**+*�r�x*�+**rx*�e PIPE-FLDW HYDRAULICS CONiPUTSR PROGRAAI PACKAGE (Referance: LACFCD,LACRD, AND OCEMA HYDRAULTCS CAiTERIQ23} (c} Copyright 1982-2601 Advanced Engineering Software (aes) Ver. 8.0 Release Date: D1/D1/2001 License ID 1509 Analysis prepared by: PROJECTDESIGN COI3SULTANTS 701 'B' STREET, SiJITE B00 SAN DIEGO, CA 42101 619-234-D349 +xw*w***�*wtir+w��*iys:++++ DESCRIPTIO�T dF STI��' r�+.�*+��+tr+.�ar,�W+,��.�r� * BRESSI RANCH - ULTII�SATE CONDTTTONS * * SYSTEM 140 - LATERAL 13 {GATEWAY CENTER DRIVE 5TA 3 9+3 fi. 90 )�, �� [iyr� y��* cd � * 100-XEAR STOR25 EVENT * **wr*�*r**�r*frrt*+rt***t*t+rt+wy+wy*+*ytira*rt++rr+rt*a*x*+*f+i+*rrt**+tr*r• FILE NAME: 300-13.DAT TIME/FATE OF STUDY: 14:47 09/30/2042 .*,..«++x++..*+*t*�*�+.*++.�.*.�......*....**�.*�.....*....++...*x:.+++.�>+*..� GR.A�UALLY VARIEi} FLOW A2dALYSI$ FOR PIPE SYSTEM NODAL> POINT STATUS TABLE (Npte: '*' indicates nodal paint data used.l UPSTREAM RUN ' DpWN$TREAM RLTN . NODE MODEL PRESSURE PRESSURE+ FLOW PRESSURE+ NL73+IBER PROCES$ HEAD; FT ) MOMENT[Jr4 { pOUI�IS } DEP�'H ( FT j MOMEN'i'LiM ( POLTNDS 1 360.50- O.BD Dc 59.56 0.34� 127.29 } FRICTION 160.50- . D.80*Dc 59.56 0.80*Dc 59.55 } CATCH BASIi�i 160.6D- 1_19* 32.54 0.$0 D� 20.74 ---------------------------------------------------------------------------___ MP.XIMLI2+S �IUhffiER O�' EfdERGY BRLANCES USED IN EACH PROFIi.E = 25 ------------------------------------------------------------------------------ NOTE: S'T'EADY FLOW HYDRAULIC HEAD-LOSS COI�fPU'PATIONS HASEp OId 'd'HE MOST CONSEi3VATIVE FORMUI,AE FROM THE CURRENi' LACRD,iACFCD, AND OCEMA DESIGN MP.NUAiS. •*wx***+*wrw*>*ta+sr+*+xrr+***+***w�*�r**x*r**+*rys**r**iyrrr*+*.*y*wyr+++,r�x� DOWNSTREP.2+I PIPE FLOW CON'i'ROL 17A'�'A: NODE I3iTMBER = 160.50 / FiJOWLINE ELEVATION = 383.61 PTPE FLQW = 4.40 CFSv PIPE i]IANFETER = 18. DD INCHES ASSUMED DOWNSTREP.?d CONTROL HGL = 363.504 FEET "NOTE: ASSUMED DOWNSTREP.M CQNTRQi, DEPTH( -0.11 FT.) IS LE55 THAN CRITICAL DEPTH{ 0.80 FT.i _�_> CRITICAL DEPTH IS ASSUMED AS DOWI35TREAM COI3TR0�, DEPTH FOR UPSTRF.P.M RUN ANAI,YSIS ------------------------------------------------------ NODE 160.50 : HGi =< 383.950>;EGL- < 387.270>;FLOWLINE= < 383.610 *rw�*++*t+**w*r*r*r**:ry*ryw+w*rrxxri*r�:**�rsr�sr*+rf*+*t*+++s++i.+f*tt*rt:*t+ FLOW PROCESS FROM NODE 150.50 TO NODE 160.50 I5 CODE = 1 UPSTREAM NODE 160.60 ELEVATION = 38b.55 ;FLOW IS SUPERCRITICAL} ------------------------------------------------------------------------------ • ! CALCULATE FAICTION LOSSES(LACFCA]: PIPE FLOW = 4.40 CFS PIPE DIAMETER = 18_DO INCHES PIPE LEIJG�H = 5.25 FEET 41P.NNING' S N = 0. D130D -----------�------------------------------------------------------------------ iJORMAL DEPTH{FT} � 0.24 CRITTCA.L DEP'I'H(FT) = D.80 i3PSi`REAM CO�PI'ROL ASSUMEA FLOWDEPTH ( FT )= 0. BO ______��_�---_-�__,��-�_�_�� « TR===��___=�_______________________________ GRA�3UALLY VARIEb FLOW PROFILE COMPUTED TN�ORMATIOI3: bTS�'Ai�IC� FRdM FLQW DEPTH VELOCITY SPECIF�C PRESS4JRE+ CONTROL ( F'!' 1 ( FT i { FT / 5EC ) F�IERGY ( FT } M42+9EN'i'UM ( POUNi?S J 0.000 0.805 4.557 1.127 59.56 D.OU2 0.782 4.722 1.i26 59.54 0.�20 0.759 4.900 1.332 59.87 0.023 0.737 5.091 1.�40 60.26 O.D42 0.714 5.299 1.251 60.84 Q.D70 D.692 5.523 1.156 61.61 Q.1U7 D.669 5.767 1.186 62.59 D.154 0.647 6.033 1.212 63.81 U.215 0.624 6.322 1.245 . 65.2$ 0.291 0.602 6.640 1.287 67.03 4.385 0.579 6.988 1.336 69.09 4.502 D.557 7.3�2 1.401 71.51 4.646 0.534 7.797 1.479 74.32 4.825 0.512 6.270 1.574 77.57 ]..446 0.489 8.797 1.591 B1.35 1.322 �.466 4.389 1.836 85.71 • 1.569 0.444 10.056 2.Q15 40.76 2. }.J.O 0. 421 10. 613 2.238 46. 63 2.677 0.399 i�.679 2.5J.8 103.46 3.419 0.376 12.675 2.872 " 111.45 4.417 D.354 13.631 3.326 120.84 5.25Q 0.340 14.618✓ 3.660 127.29 ------------------__-------_---__-__--_--__-------------------------------------- NOJ]E 260.60 : HGL =� 3$7.355>;EGL= � 387.677>;FLOWLII3E= � 385.S5D> ww+�t+**rx*x*rr***+*r*�*.�**r*yxr***rwr*i�*�ri+*s*x�****ww*x*�*wx**+**+w*x****+ FLOW PROCESS FRO!'4 NQDE 160.60 Tp NODE J.60.60 I5 CODE = 8 UPST�.EANi NODE 160.6D ELEVATION�= 386.55 (FLOW I5 AT CAITICAL FEPTHj CALCiJLATE CATCH SAS�N EN�`RA23CE LQSSES {L,p,CFCT]} : PTPE FLOW = 4.4p CFS PIPE D�AMETER = 1$.00 INCHES FLOW VELOCITY = 4.56 FEET/SEC. VELOCITY HEAD = D.323 FEET CA'i`CH BASI?�1 ENERGY LOSS =.2* (VELOCITY HEAD} _,2* ( 0.323) = 0.065 ------------------------------------- ---_-_____--------------------------- NODE 1fiD.60 : HGL =< 387.742�L= < 367.742>;FLOWi�INE= < 385.55U� � *w*er�r*w+x**a*�**+�r*xr**t*rrr++***txixr*�+k+��*�txw*x+xwwv.**+**�,rx,rwxx**,t+w�* UPSTREAM PIPE FLOW CONTROL DATA� NODE NUMBER = 160.fi0 Fi,OWLINE Ei,EVATION = 386.55 ASSUMED LiPSTAEP.t�F CON'I'ROL HGL = 38'7.35 FOR DOWNSTREA2+� RUI3 ANALXSIS END OF GRP.DUALLY VARIED FLOW ANALYSIS • � � AFPENDTX 4.1.2 SYSTEM 122 (`D' STREET) � *�***t*++*+*�********tt*wwww**+�xw�w*w+�rtt+*Yt*�txt*+t*ft#**�**�*w*w*�t�+ww+* PIPE-FLOW HYDRALTiICS COMPLTTER PROG� PACKAGE . (Reference: LACFCD,LACRD, AND OCEMA HYD�tAULICS CRITERION) {c] Copyright 1982-2002 Advanced Engineering Software (aesj Ver. 8.0 Release Da�e: 0�/O1/2002 iicense zA 1509 Analysis prepared by: ProjectDesign Consultants 701 B Street, Suit� $00 San Diego, CA 92101 ***y.*t**t***++**y.*w*wwv.w,r,+ DESCRIPTION OF STUDY *+**++*tf**w*w******,+x,r*ww * B�ZESSI RAI3CH - [JL'I`IMATE CONDITIONS � * SYS'FEM 122 (GATEWAY CTR DR STA 19+50 TO P.LxCP.NTE AdAD} * ; 1QQ-YEAR STORM EVENT * f.t**+�*�*****************+**+ti�*.ttt***++..**.,,*.**«.+«+*****�+t*++++++** FILE NAME: P122B.DAT TIME/DATE OF S�`UDY: 07:18 O1/02/20Q3 *�************+*******+****«***,.,,.«.*.,,*****��**�.****�*****+**�****+****+**** GRADUALLY VARIED FLOW AI3ALYSIS FOR PIPE SYSTEM NODAL POISI'I' STATUS TABLE iNote: "*" indicates nodal point data used.} UPS�`REAM RUN DOWDISTREAM RUN NQDE MODEL PRESSURE FRESSURE+ FL4W �RES5LTF2E+ NUMBER PROCESS HEAD ( F�'} MOMFNTUM { POL]NDS ) DEP'PH {�} MOMF3JTL7M ( POUNDS ). �22.00- 4_52* 2660.11 2.65 Dc 1932.04 } FFtIC'TTON 122.10- 4.67* 2728.26 2.65 Dc 1932.04 • } APIGLE-P�INT 122.10- 4.72* 2748.18 2.65 Dc 1932.04 } FRICTION �zz.ao- s.sa* 3129.68 z.z3 aos�.�9 } r�o�� 122.30- 5.33* 3017.32 2.65 Dc 1932.04 } FRzcmzax 122.40- 6.47* 3519.26 2.08 2095.31 } JUi�7CTION 122.50- 6.b�� 3391.52 ' 1.80 2D32.63 } FRICTIQN+BEND 122.b0- 5.49* 2896.50 2.44 �733.16 } FRTC`PION 122.7Q- 5.47* 288$.53 2.58 Dc 1725.52 ) JUNCTTON 122.84- 7.76* 3896.Q1 2.33 175J..OA ) FRICTION 122.90- 7.66* 3853.22 2.58 Dc 1725.52 ----------------------------------------------=------------------------------- MP.XIMLTM NUMBER OF £N£RGY BA�,ANCES USED IN EACH PROFILE = 25 NOTE: S'I'�ADY FLOW HYDRAiJi�IC HEAD--LOSS COMPUTA`i'IODiS BASED ON THE MOST COI3SERVATIVE FORi�7IJLAE FROM THE Ci3RRENT i.ACRD, LACFCD, AND OCEMA DESIGN MANUALS. *ttt+*+++*******+*+*+++*+****++++++�.++�*********++***+*++,«**+*++�**��**,.**+*� DOWI3STREAM P3PE FLOW CONTRpL DATA: NODE NU�7BER = 122.00 FI.OWLTNE ELEVATiON = 298.96 PIPE FLOW = 69.60 CFS PIPE DZAMETER = 35.00 INCHES ASS[TNIED DOWNSTREP.M CONTROL HGL = 303.0D0 FEET � ------------------------------------------------------------------------------ � t�ODE 122.aQ : HGL =< 303.000>;EGL= � 304.505>;FLOWLINE= � 298.480> +i.++*+i.+,tf++�*Wv�***+�*r*r+�*+v.v.*+�**��+r��rr*ry.++�rt�y.*t�w+++�*+r�w+**+w�r** FLOW PROC�SS FROM NODE 122.OD TO NODE 122.10 TS CODE = 1 UPSTREAM NODE 122.10 ELEVATIOiV = 298.78 (FLOW IS iINDER PRESSUREj ------------------------------------------------------------------------------ CALCULATE FRICTIaN LOSSESILACFCD]: PIPE FLOW = 69.60 CFS PIPE DIAMETER = 36.00 INCHES P�PE �ENGTH = 41.74 FEET MANNING'S N= 0.01300 SF=IQ/K)%}2 = (S 69.60)/( 666.990))**2 = 4.01089 • HF-L SF---(-----41_74}*{0_O10$91-'--'---0^454----------- _ * _ NODE �22.�0 : HGL =< 303.454>;EGL= < 3Q4.950>;FLOWLINE= < 298.784� ***x*ww*w*+f**:r**ww+*w**ar+*+*r*w*+ww*wt******+tt***+++��**w**+Ww***+++*r*x* FLOW PROCE55 FROM NODE 122.10 TO NODE 122.10 IS CODE = 6 UPSTREAM NODE 122.10 ELEVATION = 296.78 S�LbW IS UNDER PRESSURE] CALCiJZ,A'2'E ANGLE-POINT LOSSES(LACRD) : PIPE FF,OW = 69.60 CFS PIPE DIAMETER = 36.OQ INCHES PIPE ANGLE-PpINT = 10.a0 DEGREES ANGLE-POINT COEFFICIEN�` KA = 0.03000 FLOW VELOCiTY = 9.85 FEET/SEC. VELOCITY HEAD = 1.505 FEET HAP'I'=KA* {y�,pC��`y HEAD) =(0.43004) *{ i.505) = 0. a45 ------------------------------------------------------------------------------ I30DE 122.I0 : HGL =< 303.50Q>;EGL= < 305.005>;FLOWLINE= � 298.780> �kw* lrir Yr Yr1rw' Y� Y� k' 1' 1'Y� M kir ir�IrYr W Yr�lr�lr�k* �lr* ***�F***�lr�lr�k M k k Yr Yr �FYrt't �ltt i iy�!* Yri Yr YriF' k�k *4 k k%�k�k�k MYr�lr'kyr** FLOW PROCESS FROM NODE 122.14 'I`O NODE �22.20 IS CODE = 1 tJPSTREAM NOD� 122.26 ELEVA�`ION = 344.31 {FL4W xS UNDER PRESSUREj ------------------------------------------------------------------------------- CAI�CLJI�ATE FRIC'1'ION LOSSES (F�ACFCD) : PIPE FLOW = 69.6Q CFS PIPE DIAME'I`ER = 36.00 INCHES PIPE LENGTH = 219.94 FEE�' MANNING'S N- O.Q�300 s�=��2ix}�*2 = cc �s.ba�i{ 6ss.48s�};*2 = 0.03089 xF-LWsF = c zi�.�4�'*(a.a1089? = 2.395 ------_--_----------_�--__----------------------------------------__--------------- NODE 122.20 : HGL =< 305.895>;EGL= < 307.400>;FLOWLIN�= < 300.310> ##i t***�k�1rY�' YrY� k k YrYr Y��I' fr****!�Il�f!**1r t t**tk*tk iktk'M *Y�Yi M� 1r ****** Y� **! Yr* f Y� }}}Yr 1r}Yr YrYr*1rtkYrYr ** * FLOW PROCESS FROM NODE �22.20 TO NODE 122.30 IS CQDE = 2 •• �-iJP$TREAM NODE �22.30 ELEVATION = 300.64 (FL�OW IS iJ2FDER PRESSURE) C�cur,r��r� riarn�Oz�� z�OSS�SiI..�CFcn} : PIPE FLOW = 69.6Q CFS PTPE AIAMETER = 36.00 INCHES FLOW VELOC�TY = 9.85 FEET/SEC. VELOCITY HEAD = 1.�05 FEET H?�FN = .05*iVfiLOC�TY HEAD) _ .D5*( 1.5051 = 0.475 � ..----------------------------------------------------------------------------- NODE 122.30 : HGL =< 3q$_970>,EGL= � 307.475>;FLOWLINE= < 300.640� *********�*��+�*�**************��*****ww.*�*�+.,+,�**.,..+�w*,�ww*wwwww�,�.�w.�***+ FLOW PRDC�SS FROM NODE 122.3D TO NODE 122.40 IS CODE = 1 LFPSTREAM NODE 122.40 ELEVATION = 302.42 (FLOW IS UI3AER PRESSUAE) ------------------------------------------------------------------------------- CAL�CiJLRTE FRIC`i'IQN �,QSSESSLACFCD} : PIPE F�OW = 69.60 CFS PIPE DIAMETER = 36.00 INCHES PIPE LENGTH = 231.24 FEET MAidNING'6 N= 0.01300 SF=fQ/Kj**2 = Si 69.60)/{ 666.9B7f}**2 = O.Olfl89 HF=L*SF = ( 231.241*40.01089} = 2.518 NODE 122.40 : HGL =� 308.488>,EGL- < 309.993>,FLpWLINE= � 302.02Q> +**a*********x*�x�*,r*r�***w+***+*++*«x«*�****��**+****+*t**,t**�**�****+++****w FLOW PROCESS FROt+] �TODE 122.4Q '�'O NODE 122.50 I5 CODE = 5 UPS'i'REA�3 NODE 122.50 EiEVA'F�ON = 302.35 (FLdW IS i]�iDER PF�ESSUREj CAi,CULATE JiFNCTION LOSSES : PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VEI�OCITX (CFSi (INCHES) {DEGREES} ELEVATION DEPTH(FT.) (FT/SEC) UPSTREAM 64.40 36.Q0 0.00 302.35 2.58 9.111 • DC}WNSTREAM 69.60 36.Q0 - 302.�2 2.65 9.$46 • L.A'iERA.L #7. 2. 60 �.s . aa 90 . DQ 3D3 . 52 Q. 61 1. 971 LA'i'ERAL #2 2.60 18.00 9D.00 303.52 0.61 i.471 Q5 0.00===Q5 EQUALS BASIN INPU'�'==- LAC�'CD AND OCEMA FLOW JiTNCTION FOF2MULAE USED: DY=(Q2"V2-QI*V1*COS(DELTAI}-Q3*V3*CQS(DELTA3)- Q4*V4"COS(DELTA4}}/(�A1+A2)*16.1j+FRICT�ON LdSSES UPSTREAM: MANNING'S N= 0.013Qb; �RICT30N SLOPE = O.OD932 DOWAISTREAM: MANNING'S N= 4.Q1300; FRICT�4N SLOPE = 0.01089 AVERAGED FRIC�'ION SLOPE IN JUNC'I'�ON ASSEFMED AS D. D1011 • JiJNCTION I.ENGi'H = 4.00 FEET FRTCTION 3JOS5E5 = O.d4d FEE7' ENTFL�NCE LOS5E5 = O.OpO FEET Ji3NCTI0N i�(?SSES = (T?X+HVl-HV2)+{ENTRANCE LQSSES) JiFNCTION �OSSES = ( D.257)+{ 0.40Q) = 0.257 ----�--------------------------------------------------------------___----------- NODE 122.54 : HGI, _< 348.9b1>;EGL= � 3�0.250>;FLOWLINE= < 302.350� wv.*w**r*******t*f*af**x****xWav�v�+r*�**ww*trwwr+*+t****tt**w,t�**�***********+*** FLOW PROCESS FROM NOIIE 122.54 'FO NODE 122.50 IS CODE = 3 BPSTREAM NODE 122.6Q ELEVATION = 304.45 (FLOW IS i.Ti�IDER PRESSURE} ------------------------------------------------------------------------------ CALCULATE PIPE-BEND LOSSES{pC�M,�J: PIPE ��aw = ��.4a CFS PIPE DIAMET�R = 36.00 INCHES CENTRA�, ANGLE = 90.004 DEGREES i+]AN�IING'S N= 0.013D0 PIPE LENGTH = 70.3� FEET BEND COEFFECIENT(KB1 = 0.250D0 FLOW VELOCITY = 9.i1 FEET/SEC. VELOC3'i'Y HEAD = 1.289 FEET HB=KB*(VELOCFi'Y HEAD) _{ 0.250}*( 1.289i = 0.322 5F=lQ/K)**2 = {( 64.�0}/( b65.991jj**2 = 0.00932 HF=I�*SF R { 70_3�.}*(O.OD932} = 4.655 TOTAL HEP.B i�(?SS�S = HB � HF =( 0.3221+I 0.655} � fl.97g ------------------------------------------------------------------------------ NODE 122.60 : HGL =< 309.939>;EGL= < 311.228>;FLOWLINE= < 304.450� *+++t+*************�**:ft*fttty.y.y.y.++**ff**++++**3**:�***+++,r***,r*wx*«*wwr**+++ FLOW PROCESS FROM NODE 122.60 TO NOdE 122.70 3S CpDE = 1 UPSTREP.M NdDE 122.70 ELEVATION = 304.58 {FLOW IS UNDER PRESSUR�j CAI,CULATE FRICTXON LOSSESfLACFCD}: PIPE FLOW = 64.40 CF5 PIPE DIAi�7ETER = 36.00 INCHES PIPE LENGTH = �2.00 FEET MI�NNING'S N= 0.01300 SF=fQ/K)**2 = {( b4.4d}/( 56b.968)1**2 = 0.00932 HF=L*SF = { 12.00J*{0.00932j = 0.112 iJODE 122.76 : HGL =< 3iD.051>;EGL= < 3J.1.340>;FLOWLINE= a 304.580> .**�*,.*,...*�***,.***�************�**�*.�******,.***.>***«..**t**+**+*t*�t**�*++�* FLOW PROCESS FROM NdDE �22.70 TO NOBE 122.$0 IS CODE = 5 I3PSTREAM NODE 122.$0 ELEVATION = 304.91 fFLOW IS UNDER FRESSU�} ------------------------------------------_----------------------------______-- CALCULATE ,3�LTNCTION LQSSES: PIPE �LOW T}zAMETER ANGLE PLQWLTNE CRZTICAL VELOCITY (CFS) (�NCHES} (DEGAEES) ELEVATION AEPTH(FT.a (FT/SEC) UPSTRE�7 54.Aa 3b.OD 94.QQ 304.91 2.58 9.111 DOWPiSTRFAM 64.40 36.00 - 3D4.58 2.58 9.111 LATERAL #1 Q.dQ 0.00 0.40 0.00 0.00 4.000 LATERAL #2 Q.Qa 0.00 4.40 0.00 D.00 0.6D0 Q5 a.44===Q5 EQUALS BASIN II3PUT=== LACFCD AND OCEl�iA FLOW JUNCTEpN FORMULAE USED: DY={Q2YV2-Q1*V1"�COS(DELTAI)-Q3*V3*COS(DELTA3}- Q4*V4*COS(DELTA4))/((A1+A2j*}.b.1)+pRICTION LC?SSES UPSTREAM: M.�NNzi�TG'S N= O.Ot306; �RICTION SLAPE = 0.00932 DOWNSTREAM: MANNING'S N= 4.013QQ; FRICTION SIAPE = 0.00932 AVERAGED FR�CTION SLOPE IN JUNCi'IpN ASSUMED AS Q.OQ932 JUNCTION LENG`FH = 4.00 FEET FRIC'T'T4N LQSSES = 0.037 FEET ENTFLa,NCE F�OSSES = 0.000 FEE'i JUNCTION LOSSES = (DY�+HV1-HV2)+(ENTRP.I3CE LOSSES) �3UNCTION LOSSES = i 2.615)+( 0.000) = 2.615 ------------------------------------------------------------------------------ AIDDE 122.$0 : HGL =< 312.666>;EGL= < 3�3.955>;FLpWLINE= � 304.910> • w�*+�**��#,r++*****�*�**v.*�**++++*****++�*****+**********+*+***�*«*�+***+**+*** FLpW PROC�SS FROM NODE 122.80 TO NODE �22.90 IS CODE = 1 UPSTREAM NODE 122.90 ELEVATION = 3Q5.53 (FLOW I5 UidDER PRESSUREj ------------------------------------------------------------------------------ � CALCi]LATE ERICTION LOSSES(LACFCD): PIPE FLOW = 54.40 CFS PIPE DIAMETER = 36.�6 �NCHES PIPE LENGTH = 56.00 FEET M.A.NNZNG'S N= D.01300 SF=fQ/K}**2 = (( 64.40)/( fi66.988}}**2 = 0.04932 HF=L*SF = L 56.Q0)*(0.009321 = 0.522 • ----------------------------------------------------------------------- NODE 122.90 : HGL =< 313.188>;EGL= < 314.477>;FLOWLINE= � 3D5.530> *��**�*********�t*�+*+ww�w�**�w****��.+�**w*�ww>*�*>*+�w*w�*******+*******+** UPSmREAM PIPE FLOW CONTROL DATA: NODE I3ZTMBER = 122.9a FLOWLINE ELEVATION = 305.53 ASSi.FN�ED UPSTREAM CONTROL HGL = 30$.11 FOR i>QWNS3'REA?�S RUN A�IALYSIS END OF GRADUALLY VARIED FLOW ANALYSTS • • L� wwwrr+******++*w+++w*w+*+t*t*+**w*****+*«+***+*>*************�«*****�*****wW�w PIPE-FLOW HYi]Rx1ULICS COMPUiER PROG}ZAM PACKAGE {Reference: LACFCD,LACRD, AND OC�MA HYDRAULICS CRIT�R�ON? (cj Copyright 19B2-20a2 Advanced Engineering 5oftware iaes) Ver. 8.D Re].ease Date: O1/O1/2402 License ID 1509 Analysis prepared by: PROJEC'i' DESIGId �0�1S�TL�TANTS 701 'B' STREET, SUITE 804 SAN DIEGO, CA 92101 619-235-6471 .� � J **'*********************** DESCRIPTION OF STUDY ****************+w*www**** * BRESSI }2ANCH - UI,7'IMA'i'E CONDITIONS '" * SYS�'�hS 122 - LA'FERAI� 3{GATEWAY CTFt DRIVE 5TA 19+10.00} * * 10D-YEAR STOFtM EVEN'T * w* * *1�** * * *** *�k** * * * **** * * ** ****%'�lry"h k*+M t *t# # #+#+i�ir�Y**Y+*Y'Y.1� # 1 *'k'�'***irt ***Yr*Yr iF FILE NAME: �22-1.DAT TIME/DATE OF S'i'UDY: 15:�3 42/13/24d3 wv�*wr***f**t*ft***+**rt*++*t*frtt+t***+*******«*******+**+.*t***************�,wWw GRADUALLY VARIED FLOW ANA.LYSIS FOR PIPE 5Y5TEM NODAi� PpINT STA'i`US TABi�E {Note: '*" indicates noda� point data used.} i3PSTREAM RUN DOWPISTFtEAM RUN NODE MODEL PRESS(TRE PRESSU�t�+ P�,OW PRESSURE+ NCTMBER PROCESS HEAD(FT} MO[�NTUMLPOUNDSj DEPTH(FT] MOMENTUM{PpUNDS] 123.10- 5.94* 587.31 0.59 51.00 } FR�CTTON 123.20- 5.47* } CATCH BASIN 123.20- 5.56* 535.89 529.88 0.73 Dc 0.73 Dc 47.54 16.72 -------------------------------------------------------------------------_----- MAX�MUM NUMBER DF ENERGY BALP.NCES i75ED IN EACH PROFILE = 25 -----____....___--------_----__-_-------------------------------------------------- NOTE : S'T'FAL1Y FLOW HYDRAULIC HEAi]-LOSS COMPU'iA'FIONS BASED ON THE N30ST CONSERVATIVE FORMiJLAE FROt�f THE CTJi2REN'I' LACRD, I�ACFCD, AND pCEi+SA DES3GN MP.NCJALS. ****+**********************,«+.**«*+**+*********+*+****�*******,r,r�*wv.w**+******* DOWNSTREAM PIPE FLOW CONTROL DATA: NOBE NUMBER = 123.10 FLOWLINE ELEVATION = 303.02 PIPE FLOW = 3.7D CFS PIPE DIRMETER =�8.00 INCHES ASSUMED DOWNSTREANI CONTROL HGL = 308.950 FEET _----------------------------_-------------------------------------------------- NODE 123.10 : HGL =< 308.960>;EGL= � 309.028�;FLOWLINE= � 303.020> ****�*****.***+**�*.*.*.+.,.**.***+**+**+*�**�++****#�W***+***ww�*.*�********,.* FLOW PROCESS FROM I30DE 123.10 TO NODE 123.20 IS CODE = 1 UPSTREAM NODE 123.20 ELEVATIO�i = 343.54 (FLOW IS L7NDER PRESSURE) ------------------------------------------------------------------------------ CA�,CULA'TE Fx�C'I'TON LOSSES (LACFCD) : PIPE FLOW = 3.70 CFS PIPE qIAME'I'ER = 18.0� TNCHES PIPE LENGTH = 43.25 FEET MPIVNING'S N= O.D1300 SF=(Q/K)**2 = [{ 3.70}/{ 105.053))**2 = 0.40124 HF=L*SF = ( 43.25)*(0.00124) = fl.654 230DE 123.2a : HGL =< 309.014>;EGL= < 309.082�;FLOWLINE= < 303.544> � ****�**r**ww*wwwww�*******��w**x�wWw�x��*wwww*www**********+*+*+**�+*+****** FUOW PROCESS FROM NODE 123.20 TO NODE 123.20 IS CODE = 8 UPSTR�M NODE 123.20 ELEVATION = 303.54 (FLOW IS UNDER PRESSURE) CALCiTLATE CATCH BASIDI ENTRADiCE LOSSES (L�ACFCD) : PIPE FLOW = 3.70 CF5 PIPE DIAMETER = 18.00 INCHES FLOW VELpCITY = 2.09 P��T/SEC. VELOCITY HF,AD = D.d68 FEET CATCH BASIN ENERGY LOSS =.2*(VELOCI'I'Y HEAD) _.2*( 0.06$) = 0.014 -------------------------------------------------------___--______----------- NODE 123.20 : HGL =< 309.09$�;EGL= < 309.095>;FLOWLINE= < 303.54fl> **�********************.****+***************************��*��***+*�+++****+*** UPSTREA.M PIPE FLOW CONTROL DATA: NODE NLTMBER = 123.20 FLOWLINE ELEVATI4N = 303.54 ASSUMED UPSTRF.AM CONTROL HGL = 304.27 FOFt bOWNSTREA.M RUN ANAi�YSIS END OF GRP.DUAL�Y VARIED FLOW �iVALY5I5 r� �J � � * # + � Y k � * * f ! # t f f i i * i Y * * * � i f f * i * i i Y * # * * * k * } # # � 1 M t 1 t * * M f # f # * 1 � * W i � � * w } * w w k f i + 1 * # * PIPE-FLOW HYDRAULICS COMPUTEI2 PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDR.AULICS CRITERI4N) (c} Copyright 1982-20fl2 Advanced Engineering Software (aes) Ver. 8.0 Re�ease 1Jate: al/O1/2pQ2 License IA 1509 Analysis pxepared by: PROJECT DESIGN CONSiiLTAN'PS 701 'B' STREET, SUITE 800 SAN I?IEGd, CA 92101 bi9-235-6471 ***�w+�:f*+**��****++*�*** DESCRIPTION OF SiUDY w+***+t**�*+**��+w+****w*+ * SRESST RANCH - ULTIMATE CQNDITIONS ' � 5YS'iEi�S 122 - LATERAL 2(GATEWAY CENTER DRIVE Si`A 19+10} * * 100-YEAR STORM £VENT * t.*�**.*��+***..**�**+.*****+w*****«�w**+�.*+++�..**++*++��+**t�.*.+**+,.*+ FIF,E NAME: 122-2 . DAT TIME/DATE OF STUDY: 16:00 Ol/16/24D3 � f�# }*k ff##'k1 fi *Yii #1r1�'/r*�ki�li�ti'rty1*tYr*�h�kY�*irtY ittilf�**i�**++�*YY1i�**YrYr?iYi� *'t�*Yi*yr#*i# GRADiiALLY VARIED FLOW ANALYSIS FOR PIPE 5Y5`FEM NpDAL POINT STATUS TABLE (Note: "*" indicates nodal point data used.} UPSTR.EAM RUN DOWAiSTREAM AUN NODE MODEL PRESSURE PRESSURE+ FLOW PRESSi3RE+ � NUMBER PROCESS HEAI?(FT) MOMENTUM(POiTNDS} DEPTH{FT) NfOMENTUM(POUNDS) 123_50- 5.44* 535.6a Q.32 120.06 ] �RICTIOPf ]23.60- 2.37* 196.$5 0.78 Dc 54.33 ) CATCH RASI33 123.60- 2.47* 189.48 0.78 Dc 18.48 ------------------------- MAX�Miift NCIMBER pF ENERGY BALANCES USED IN EACH PROFII.E = 25 --------------------------------- I30TE: STEADY FLOW HYDRAi7E�IC HEAT}-LOSS COMPU'T'ATIOPFS BASED ON 7'HE M05T CO�FSERVATIVE FORMULAE FRQM THE CUIiRENT LACKA,LACFCD, AND OCEN3A pESIGN MANCJALS . *�*.,ratiw**+*+**..***+*+*W*f:**.*,r*+w+.st**+*****f...*+*+**+****�.«r**+****+rt+ DOWNSTREA2�4 PIPE FLOW CQN'I`ROL DATA: NODE NUMBER = 123.50 FLQWLINE ELEVATIOId = 303_52 PIP� FLOW = 4.1D CFS PTPE DIAMETER = 18.00 INCHES ASSL7MED DOWNSTREAM CONTROL HGL = 3Q8.960 FEET --------------------------------- NQDE ]23.50 : HGL =< 308.960>;EGL= < 309.049>;FT,OWLI�FE= < 3a3.520> ***rr>+++**x**+�,�fr�r**�tt**�*x+W��w***��**i�r�r�*x++**rrt�**fi�+r+*++*�*i�+ite*w FLdW PROCESS FROM NODE 123.50 Tp NODE 123.60 �S CODE = 1 UPSTREAM NOBE 123.60 ELEVATION = 306.60 {FLOW I5 UI�3DER PRESSURE) CALCULATE FRTCTION L055SS(LACFCDI: PIPE FLOW = 4.10 CFS P�PE DIAMETER = 18.00 INCHES PiPE LENGTH = 5.25 FEET MANNING'S N- 4.a73DQ Sp-{4/K)**2 = ({ 4.1Q11f 105.0601}**2 = 0.00152 HF=L*SF = { 5.25)*{Q.00152} - 0.408 -----------------------------____----------- � NODE 123.bfl : f-IGL =< 308.966>;EGL= < 309.052>;FLOwLI3QE= < 346.600> � * * k # # 4 f � t * i # * * i * * * * * * * } # w W 4 N # * * * * * � f * * * t � * * } # * Y t Y * t # * � * 1 * } 4 * * k � � t t * * � � � 4 * * i W � * FLOW PROCESS FROM N�DE 123.b0 TO NODE 123.50 IS CODE = 8 UPSTREAM NQD� 123_64 ELEVATION = 306.60 (FLpW I5 iJNDER PRESSURE) CALCL]LATE CATCH SASIN ENTR.�NCE LOSSES{�ACFCD): PIPE FLOW � 4.10 CFS PZPE DIAMETER = 16.q0 INCHES FLOW VELOCITY = 2.32 FEET/SEC. VELOCITY H�D = D.084 FEET CA'PCH BASIN ENERGY LOSS =.2*(IiELOCITY HEAD) _•��I 0.084} � d.017 ---------------------------------------__ NODE 123.60 : HGL =�,309.068>;EGL= < 309.068>;FLOWLINE= < 306.600> *w***�*�**�***�+****.�*�*��**+*****�*,�****�***�**�*tt*****��*+*w,.*+*****�**��,� UPSTAEAM PTPE FLOW CON'I'ROL DATA: � NODE NUMBER - 123.60 FLOWLINE EL�IATI�N = 346.6D ASSUMED UPSTREA3�S CONTROL HGL = 307.38 FpR DOWPiSTAEAM RUN 71NALYSIS ----------- END OF GFtADUALLY VARIED FLOW ANALYS�S . • � APPENDIX 4.1.3 SYSTEM 130 (`E' STREET) �J � � * * * * k * 1 * � i * * k f * * � * # * i W i + # # # * * k f * + * f * * * * 1 + i W i f # } } * * � f * * � f t M M f 1 * k * * * * * t * * k f * k * k � PIPE-�LOW HYDRAULICS COMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACFtA, AND OCEMA HYDRA{JLICS CRITERZON) • (cj Capyright 1982-2002 Advanced Engineering Software (aesj Ver. B.p Release Date: 41/O1/20�2 License ID }.509 Analysis prepared by: PROJECT DESIGN CONSIJi,TAN'I'S 701 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 619-235-b471 i++,r�*,r**r++:Y�*r�+*�****+ DESCRIPTTON OF' STUDY **'�'�*****"***+**+******aa* * BEE55I RANCH - ULTIAIATE CON!}ITTONS * * 36'/30" MAiNL,INE WITH NO FLOW FROM PA-4 * * SYSTEr4 13D : 100-YEAR STORM k,iIEN'i' * t**rt*t*�rf++xw*�*a+y*+*�ryt+**+****+**tiyt�r*�r�f****r*t*+ittr3t��*xx�x*****� F�LE NAME: P130.DA�' TiME/DATE OF STUDY: 17:41 D1/i6/2003 ***iFYrYrYrYrYr **ti 1�f yryr***ii iF*Y� #****f YYyryriy#** * *YrYrY� k Yr***�k �k y� y� ** * *�Ir*f�k� # * iYYY*�1fw�Jr**** GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POIN'I', STATIJS TABLE INote: "*" indica�es nodal point data used.) UPSTAEA2+5 RUN DOWNSTREAM RL7N NODE MQDEL PRESSURE PRESSURE+ FLOW PRE55URE+ NUMBEK PROCESS HEAD(FT) MOMENTUM{POUNbS) DEPTHfFT} MOMEN'i'UM(POUAiDS} 131.40- 2.28 526.36 0.93'' 535.5� ) FRICTIpN+BEI3D 131.10- 1.50 Dc 398.59 Q.96* 514.24 } FRICTZON . �32.00- 3.50 Dc 398.59 1.28* 413.67 } ,7UNCTION 132.90- 1.73 329.60 0.82* 379.74 ) FRICTYON 133_00- 1.31 Dc 285.85 0.80* 391_19 } JUf3CTI0N 133.90- 1.39 Dc 298.83 Q.98* 352.68 } FAICTIOPI 135.Oa- }..3$ Dc 298.83 0.92* 37�.31 ] MPNHOL� 135.90- 1.38 Dc 298.83 1_O1* 393.32 } FRiCTION 336.00- 1.38 Dc 298.83 0.89* 408.19 } J[TNCTION 136_90- 1.96 Dc 304.70 1.15* 333.95 � FRICT�ON+BENA 137.00- 1.46 Dc 349.70 1.31* 314.43 } FRICTION I38.00- 1.46�17c 309.74 1.96*Dc 3D9.70 -------------------------------------------------------------------------------- MAXIMi7M NLTMBER OF ENE�tGY BALAT3CES USED IN EACH PROFILE = 25 ------------------------------ NOTE: STEADY FI,pW HXpRAl7I.,IC HEAD-LOSS COMPUTATIONS SASED ON THE M05T CONSERVATI�iE FpRMULAE FROM Ti-IE CURRENT LACRD,LACFCD, AND OCEMA DESIGN MANUALS. 1r*1r***t*i�k*#f ** k * i *k��f Ytiyey� *Yr**iFY�k***Y! 1 #*kY+#y' } yryrl *Y�Yr**�r **%Yr� *iF}*YriF **# *YrYriktY • DOWNSTRE.AM PIPE FLdW CONTRdL DATA: � NODE NUMBER = 131.44 FLOWLINE ELEVATION = 356.52 PIPE FLOW = 21.70 CFS PIPE DIAMETE�2 = 36.00 TNCHES A55UMED DOWNSTRE.�M CON'T'ROL HGL = 358. BOQ FEET ------------------------------------------------------------------------------ NODE 131.D0 : HGL =< 357.447�;EGL= < 359.565>;F3�OWLzNE= c 356.52D> �4# i i �'Yr** ir #*�t *# i�L y�k � Y#�kyr}*i�i�i��F # iF **Yri iF Y' * i#* i i�*}�}#**�k*Yr *'k�k***# * t*YYr*i� i�A'**� *i *Yri k'!r FLOW P�2QCESS FROM NdDE 131.00 �'O NODE 131.10 IS CODE = 3 f3PSTR.EAM 230DE 331.10 EI,EVATION = 357.31 (FLOW IS SUPERCRITICAL) CALCULATE PIPE-HEND LOSSES(OCEMA): PXPE Fi,QW = 21.7D CFS PfPE DIAI�ETER = 36.OQ INCHES CF.I3TRAL ANGLE = 33.800 DEGREES MANI3ING'S N= 0.0134p PIPE L�IGi'H = 26.51 FEE`I` -----------------------------------.._____-_----------------------------------- NORMI�L DEPTH{F'Y') = 0.88 CRI�'ICAL DEPTH(FT} = 1.50 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------ UPSTREtLM CQNTROL A55UMED FLQWDEPTHIFT) = 0.96 GRADL3ALLY VARIED FLOW PROFILE C0�7PUTED INFORMATIQN: ------------------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELpCITY SPECTFTC PRESSURE+ CONTROL(FT) {FTJ (FT/SEC) ENERGY{�') MOMENTUM(POUNDS) O.00D Q.964 17..066 2.866 514J.24 1.722 4.96D ll.1.18 2.861 51b.02 3.532 Q.957 11.170 2.696 517.82 5.437 Q.954 11.222 2.911 529.63 7.446 4.951 11.275 2.926 521.97 9.570 4.947 11.329 2.942 523.33 � 1J..$20 0.944 11.383 2.957 525.21 19.210 0.941 11.437 2.973 527.�1 Z5.755 0.938 11.992 2.994 529.44 19.478 0.934 J.1.�47 3.046 530.98 22.397 0.931 11.5D3 3.023 532.95 � • 25.542 0.92$ Z1.659 3.040 534.94 26.5�p 0.927 �1.675 3.045 535.51 --.._..�_�--------------------------------------------------__-_w__________--___ NOi�E 131.10 : HGL =� 358.274>;EGL= � 360.176�;FLOWLINE= � 357_310> yr #*f f Yr Yr Yr ik# YrYr******tti i 4ik 1� rt t�ii �iF+Y �k**i�Y*ikY�ly�k�i i �Y �kik# * i fii}*f * k*?!* **iFYr}YriF}Y� YrfYrlr* FLOW PROCESS FROM �30DE I31.10 TO NODE 132.fl0 TS CODE = 3. UPSTREAM NODE 132.D0 ELEVATION = 358.79 (F�OW IS SUPERCRITICALI • CALCULRTE FRICTION LOSSES(I�ACFCD): PIPE Fi,OW = 21.70 CFS PIPE DIAME'f'ER = 36.00 �NCHES PIPE LENGTH = 49.9D FEET MAI+INING'S N- D.01300 NOR2�AT� 13EPTH {F'I'j = 0. 86 CRITICAL DEPTH {F`i`) _ ?. 50 ------------------------------------------------------------------------------ UPSTRF.AP7 CONTROL ASSUMED FLOWDEPTH { F'7' )- 1_ 2 8 ------------------------------------------------------------------_.._____.._.._-- GRADUALLY VARIED FLOW PROFILE COMPUi'ED �IdFORt�E.�TION: ----------------.._..----------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL ( F"i' j { FT } ( FT / SEC ) ENF.�2GY { g'I' ) MOMENTLF[�3 ( POiJNDS } O.ODO 1.280 7.543 2.164 413.67 Q.523 1.264 7.669 2.176 416_12 1.323 1.248 7.796 2.193 418.76 2.1Q8 1.232 7.932 2.214 421.67 � 2.985 1.216 8.070 2.22$ 424_79 3.968 1.200 8.212 2.298 928.15 5.�65 1.385 8.359 2.270 93�.75 6.291 1.169 8.512 2.294 935.62 7.661 1.153 8.669 2.321 939.75 9.�95 1.137 8.832 2.349 444.15 10.935 1.121 9.001 2.38p 448.85 12.898 1.105 9.176 2.414 453.85 15.428 1.089 9.357 . 2.450 959.16 17.495 1.074 9.545 2.469 964.79 2D.303 1.056 9.740 2.532 470.77 23.519 1.042 9.943• 2.578 477.11 27.230 1.026 1D.153 2.628 483.82 31.559 1.D10 10.372 2.682 49a_93 35.672 0.994 10.599 2.740 498.44 92.818 0.979 10.835 2.803 506.39 49.900 0.969 11.06fi 2.$65 514.24 NODE �32.00 : HGL = � 3b0.Q70>;EGL= < 3b0.954>;FLQWLINE= < 356.790> *w+++tt+��++��*�*..�*.***+��++****��+�+++++***�t*.*+�+*****�+�****.**.*�*.+�*� FLOW PROCESS FROM NODE 132.00 TO NdDE 132.90 TS CODE = 5 UPSTREAM NODE 132.90 ELEVATION = 359.12 {�1,(}W FS SUPERCRITICALf ------------------------------------------------------------------------------ CALCULATE JUNCTION LQ55ES: PIPE FLOW DTAM�TER ANGLE FLOWi�iNE CRITICAI; VELOCITY { CFS } � INCHES }{ pEGREES ) ELE11ATiON DEPTH { F7'. j [ F7'/ SEC } UPSTREAM �5.$0 36.00 D.OD 359.12 1.31 14.637 DOWAISTREAM 2�.70 36.00 - 359.79 1.50 7.546 LATERAL #� 2.95 16.00 90.00 36D.12 fl.65 3.997 I�TERA.L #2 1.95 18.0� 90.00 360.12 0.53 3.527 � Q5 4. QD===QS EQUAi�S HASIAI IAIPUT=== LACFCD AND OCEMA FLOW ,7UNCTION FORMULAE USED: DY=(Q2*V2-Q1'V1*COS(DELTAI.1-43*V3"COSII�ELTA31- (�4*V4'COS(DELTA4j)/((A1+A2?*16.1j+FRICTION L05SE5 UPSTREAM: MAIdidING'S AF = fl.4I300; FRICTION SLOPE = 0.02324 DOWNS`1'REAM: MANNING'S N= 0.01300; FRICTIOTi SLOPE = O.p0738 AVERAGED FRZCTION SLOPE IN JUNCTI�i�7 ASSUMED AS O.Q1531 JiJNCTIOAi LENGTH = 4.00 FEET FRICTIOAi L055ES = 0_ Obl FEET EN�'P,}iNCE LOSSES = 0. 000 FEET JUNCTION LOSSES = {DYtI-nI1-HV2)+(�TRANCE LOSSES) JUNCTION L05SES ={ p_'7qg}+( 0.000) = d.74$ I30DE 132.90 : HGL =< 359.945>;EGL= < 36�.7D2>;FLOWLI23E= � 359.120> ++*t***:+**r**�*�++++****+«*.+��.*+�.*.��.*«*.*��+.***+*�.+�++f*��+�.�++��*..+ FLdW PROCESS FROM NODE 132.90 TO NODE 133.00 I5 CODE = I UPS7'REAM NODE 133.00 ELEVATION = 366.00 (FLOW TS SUPERCRITICAL) --------------------------------------------------------_____-----------------_-- C1�L�Ci3LATE FRiCTION LOSSES (LACFCD} : PIPE FLOW = 16.78 CFS PIPE DIAM�TER = 36.00 INCHES PIPE LENG'FH = 29$.00 PEET MANNiNG'S N- 0.613D0 ------------------------------------------------------------------------------ NORMAL DEPTH(FT} = Q.83 CRITICAL DEPTH(FT) = 1.31 UPSTRF.AM CONTROL ASSlJ�7ED FLOWDEPTH(FT} = Q.80 --------.��..�------------------------------------------------------------------ GRADUALLY VARIED FLOW PROFILE COMPUTED INFOR�7ATION: DISTANCE FHOM FLOW DEPTH VELOCITY SPECIFIC PRESSi3RE+ � CONTROI., { �'T ) { FT? ( FT / SEC } EAFERGY ( FT ) MQMEN'PUM ( POUNDS ) 0_ODD 4.8Q1 11.070 2_705 391.19 • 1.951 I 3.981 I 6.095 I 8.302 I �0.611 I 13.032 I 15.57$ I 18.262 I 21.102 I 24.1I8 I 27.334 I 30.779 I 34.491 I 38.515 I 42.914 I 47.7b2 I 53.169 I 'S9.283 l 66.323 I 74.628 l 84.766 f 97.803 f 115.133 ( 197.436 { 298.000 { -------------------------- NODE �33.OD : HGL = < }.SQ2 11.050 2.699 394.55 }.803 11.031 2.694 390.12 }.SQ4 11.012 2.688 389.59 }.8d5 10.943 2.682 389.47 1.SQ6 30.974 2.677 388.59 }.807 i0.955 2.671 388.Q2 }.SOS 30.936 2.656 387.50 ).SD9 �0.917 2.651 38b.98 I.810 30.$98 2.655 385.97 1.811 1D.860 2.650 385.95 ).812 10.861 2.b95 385.44 1.813 1D.842 2.639 384.93 1.814 10.824 2.634 384.42 1.815 10.805 2.629 383.92 1.816 �0.787 2.624 383.41 1.817 10.768 2.61$ 382.91 1.818 1�.750 2.613 382.41 1.819 10.732 2.6Q8 381.91 1.620 1D.713 2.643 391.42 1.821 14.695 2.598 380.92 I.B22 1Q.677 2.593 360.43 1.823 1D.659 2.588 379.94 1.824 1Q.64� 2.583 379.45 1.825 10.623 2.578 378.97 - I.825 10.621 2.578 378.92 �---------------------------------------------------- 3G6.801>;EGL= � 358.705>;FLOWLIAIE= < 366.000> x,ra.,t***��**i.**,r+irw****�+*�+a*«++**a�**++*+*t++*�i***t.yi**��r�r+*�r�rw*+*�*w+i�** FLOW PROCESS FROM NODE 133.OD TO NODE 133.9fl IS CODE = 5 •' LTPSTREAM NODE 133.9� ELEIIATION = 3b6.50 (FLOW 7S SUPERCRITZCALi CALCi7LATE JUNCTION LOSSES: PIPE FLOW pIAMETER ANGLE FLOWLIidE CRFT�CAL VELOCITY (CFS} (INCHES) {DEGREES} ELEVATION DEPTHiF�'.} (FT/SEC) UPSTREAM Z6.78 30.40 O.flO 366.50 1.38 9.460 DOwNSTREAM 16.78 36.04 - 36b.00 ]..3i 11.0�3 I.ATERAI, #1 O.D4 0.06 0.00 a.00 0.00 0.000 LATERAL #2 0.00 D.00 0.00 0.00 a.aa 0.000 Q5 0.00===Q5 EQUALS BASIN INPUT=-= LACFCD AND OCEMA FLOW �7LT�IC'I'ION FOR3�SULAE USED: DY=(Q2*V2-Q1*V1*COS(DELTAI}--Q3*V3wCaSSDELTA3}- Q4*V4*COS{��,TA9)f/{(A�+A2}�16.1)+FKICTIQN LOSSES UPSTREAM: MAI333ING'S N= 0.413Q0; FRICTION SLOPE = 0.01614 DOWNSTREAM: MA?�FNING'S N= 4.4i300; FRICTIQN SLOPE = O.D2604 AVERAGED FRICTION SIAPE IN JUNC'I'�OId ASSUMED A5 0.02109 �7UNCTION LENGTH = 4.Q0 FEET FRZCTT04�I IASSES = 0. 084 FEET E3�ITRANCE LOSSES = 0. D00 PEET JUNCTION LC}SSES = (DY+HV1-HV2 ) + ( EN'i'RANCE LOSSES) JTJNCTION LOSSES =( D.160j+( O.00D1 = 0.160 NODE 133.90 : ttGL = � 367.476>;EG�.= < 368.865>;FLOWLINE= � 366.5D0> • �v��*++�f,r*f.+.+**+*f*+*:�***.+*.*�.+*+****+tt+f*ti**.**�rrf+t+****+*++++++t+�+* FI,OW PROCE55 FF�OM NQDE 133.90 TO NODE 135.00 IS CQDE = 1 UPSTREAM NODE 135.OD ELEVATIpN = 37�.29 {FLOW IS SUPEACRITICAL) ------------------------------------------------------------------------------ CALC[]LATE FRICTION i,05SES{i�ACFCD) : PIPE FLOW = 16.78 CFS PIPE DIAMETER = 30_00 TNCHES PIPE L�JGTH = 296.OD FEET MP,NNING' S N = 0. 013DD • --_�-------------------------------------------------------_----------------- NOi�t7AL DEPTH(FTj = 4_98 CRITICAL DEPTHfF�) 1.36 ------�----------------------------------------------------------------------- UPSTREAM CONTRpL ASSUMED FLOWDEPTH(FT) = 0_92 -----------------------�_--------------------------------------------------------- ------------------------------------------------------------------------------ GRIIDUALLY VARIED FLOW PROFILE CpMPLJ'I'ED �NFORM.�TIQN: ----------------------___-----------------__�___-------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL ( FT ) ( FT j ( FT / SEC } ENERGY ( FT ) MQMFI�ITUA1( POiJ23DS ) O.OD4 0.922 z0.205 2.540 371.31 2.187 0.924 i0.172 2.532 370.45 4.455 D.926 10.139 2.524 369.61 6.8�0 0.929 i0.14b 2.516 368.77 9.2b4 0.931 10.473 2.507 367.94 11.815 0.933 30.441 2.50D 3b7.11 14.486 0.935 i0.OQ9 2.492 366.30 17.285 0.938 9.977 2.464 365.49 24.228 0.940 9.945 2.476 364.68 23.330 0.942 9.9].3 2.469 363.89 25.513 0.944 4.88I 2.461 363.10 30.�Q2 0.946 9.85Q 2.454 362.31 33.828 0.949 9.8T9 2.447 361.54 37.829 0.951 9.788 2.939 360.77 92.152 0.953 9.757 2.432 360.01 46.859 0.955 9.727 2.425 359.25 52.Q31 0.958 9.696 2.418 35B.50 57_778 0.960 9.666 2.41� 357.76 64.255 0.962 9.636 2.405 357.02 71.6$5 0_964 9.606 2.338 356.29 • $6.421 0.966 9.576 2.393 355.57 91.046 0.969 9.547 2.385 354.85 1D4.661 0.971 9.517 2.378 354.14 123.733 D.973 9.488 2.372 353.43 156.1$4 �.975 9.459 2.3b6 352.73 296.000 0.976 9.457 2.355 352.68 ------------------------------------------------------------------------------ NODE 135.00 : HGL =� 372.162>;EGL= < 373.780>;FLOWiIlJE= � 371.240> *t*****++*+tt*�*�**r�Ww+*+*a*t***w,r,rw�*+rtit***w+Yw�r�***v.*�w**�*v.w*�**�*�,�*ttf* FE�OW PROCESS FROM NpDE 13S.OD TO NODE 135.90 iS COD� = 2 UPSTREAI� NODE 135.90 EL�VATION = 371.57 (�'LOW TS SUPERCRITICAL} CALCUL��TE MANHOLE LOSSESfLACFCDj: PIPE FLOW = �6_7E CFS PIPE lazAMETER = 30.00 I�iCHES AVERAGED VELOCITY HEAD = 1.446 FEET HNiN -.05*{AVERAGED VELOCITY HEAD) _.05*( 1.446} = 0.072 ------------------------------------------------------------------------------ NODE 135.90 : HGL = a 372.57$>;EGL= < 373.852>;FLOWLINE= < 37I.57Q> i*yr * fit****i�YrtYi t*�k 1��k i iFYr'h#tt'k**'F'k1tY'k#*4 *Y�'t�k�Y�Y*YY� i�Y� 1 f Y Y�k'k#�Y�k'4# **}i#t #*�F#�*�iik �k Yi�** FLOW PROCE55 FROM NODE 13S.9fl Tp NQD� 13fi.DQ IS CODE = 1 UPSTREAS�] NpDE 136.40 ELEVATION = 375.24 (FI,CIW IS SUPERCRITICA�[,) ------------------------------------------------------------------------------ CALCiTLATE FRICTION LOSSES(LACFCD): PIPE FLOW = 16.78 CF5 PIPE DIAMETER = 30.OQ TNCH�S PIPE LENGTH = 2$9.24 FEET MANNING'S N= 0_013�fl -----------------_------------------------------------------------------------- NORMAL DEP`FH{F'i'j = 1.01 CRITICAL DEPTH(FT) = 1.38 ------------------------------------------_--___---________----------------------- ------------------------------------------------------------------------------ . UPSTREAM CONTRQL ASSUMED Fi,OWDEPTH(FT} - 0.84 � --GF{ADiJALLY VA�2�ED FI,,pW FRQFILE COMPUTED INFORMATION: --------------------------------------------------�------------------------ bISTANCE FRQM FLOW I}EPTH VELOCI'I'Y SPECIFIC PRESSURE+ CONTROL ( FT ) ( FT ) ( FT/ SEC ) ENERGY ( FT ) MON3ENTiJM ( POi3�IDS j O.ODO 0.$40 11.562 2.924 40B.19 2.871 0.847 11.452 2.885 404.59 5.819 0.854 11.324 2.847 401.D9 8.851 0.861 11.199 2.81D 397.67 17..975 0.868 11.077 2.774 394.35 15.200 0.875 10.957 2.740 391.11 18.536 0.882 10.839 2.'707 387.95 21.997 0.889 10.724 2.676 384.87 25.597 0.$95 l0.bi1 2.645 3$1.88 29.352 0.903 30.500 2.615 378.96 33.283 0.914 10.39i 2.587 37fi.12 37.415 fl.917 10.285 2.56d 373.35 41.777 0.924 I0.184 2.534 370.b6 45.448 4.931 I0.477 2.508 368.43 51.359 4.938 9.976 2.484 365.98 55.676 0.945 9.877 2.460 362.99 62.453 0.951 9.78a 2.438 350.57 68.794 Q.958 9.685 2.416 358.21 75.851 0.965 9.591 2.395 355.92 83.844 0.972 9.499 2.374 353.69 93.119 D.979 9.408 2.355 35 L S2 104.252 0.986 9.319 2.336 ' 349.41 116.323 0.993 9.232 2.316 347.35 137.761 1.000 9.146 2.3D0 345.36 17p.36D 1_007 9.062 2.283 343.42 • _259_240-------^_A1«007"_�^_9�058 2.282-----------343_32----- NODE 136.00 : HGL =� ��.a9a>;EGL= < 378.124>;FLOWLINE= < 375.200> *t# *1� �k * # # # f YY�i�k4�l*}*# *Y� * �k * Yr#**iktkikiklrlr k f�k *'k �k ****� * t*# #t*Y 1��kiFyr�k*******i� **** ***# *'k FLOW PF20CESS FRpM NODE 136.OQ Td NODE 136.90 IS CQDE = 5 UPS'i'REAM NODE 136.90 ELEVATION = 376.03 ;FL,OW IS SUPERCRITICAL�} _______......-------------------------------------------------------------------- CALCi7I.�ATE JiJ2�3CTI0N IASSES: PIPE FLOW DTAME'PER AiVGL� FLOWI,INE CRIi'ICAi, VELOCZ'I'Y ;CFS) iINCHES} iDEGREES) ELEVATIOiV DEPTH;F�`.) fFT/SEC) UPSTREAM 16.32 24.Ofl 0.00 375.D3 1.46 8.73$ DOWNSTREAM 16.78 30.Q0 - 375.2D 1.38 11.585 LATERAL �Z 0.46 18_�0 90.00 375.7D Q.25 0.410 LATERAL #2 0.00 a.00 0.00 4.OD Q.00 0.000 Q5 0.00===¢5 EQUALS BASIN INPUT=== LACFCD AND OCEN3A FLOW JUNCTION FORMULAE USED: DY=(Q2iV2--Q1*VJ*COS(DELTAI}-Q3*V3*C05(DELTA3}- Q4�V4*COSIDEL�'A9))/((A1+A2i*16.1}+FRICTIQN LpSSES UPSTREAM: MANNING'S 23 = 0.01300; FRICTI�N SLOPE = 0.01320 DOWNSTREAM: MI�NNING'S �T = fl.01300; FRICTION SLOPE = 0.02829 AVERAGED FFi�C'I'�ON SLOPE IN JUNCTION ASSiJDfED AS 4.02072 ,NNCTION LENGTH = 4.04 FEET FRICTIQN LOSSES = 0.0$3 FEET ENTRANCE iOSSES = 0.40D FEET JUNCTION LOSSES = (DY}HV}.-HV2j+(EN'FRANCE LOSSES) NNCTION LOSSES =( 4.240)+( 0.000) = 4.240 NODE 136.90 : HGL =< 377.179>;EGL= < 37$.365>;FLOWF�INE= < 376.030> ��++i+f.***+++xr�x***x*+*yxt+aa�*��w+++w++w��*+�rat+s++r*tkr***+t�r.wt�+xxx+xx*� • FLOW PROCESS FROM NODE 135_90 TO NODE 137.OD IS COAE = 3 � UPSTREAM NODE 137.00 ELEVATION = 377.42 (FLOW IS SUPERCRITICAL) CALCUI�AT� PIPE-BEND LOSSESi0C�1- PIPE FLOW = 16.32 CFS PIPE DIAMETER = 24.00 INCHES CENTRAL ANGLE = 90.000 DEGREES MANN�NG'S N= 0.013aD PiPE LENGT3-I = 7D.69 FEET ------------------------------------------------------------------------------ NORMAL DEPTH(FT) = 1.13 CRIT�CAi� DEPTH(F'T} - 1.46 ------------------------------------------------------------------------------ UPSTRF�M CONTROL ASSUMED FLOWDEPTH(FT) _- 1.31 GRADUALLY VARIEB FLOW PROFIL£ COMPU'I`ED INFORMATIQN: DISTANCE PROM FLOW T}�PTH VELOCTTY SPECTFIC PRESSURE+ CONTRQL ( FT } ( F�' j ( FT / SEC ) ENERGY ( F"I' } MOI+IEI�I'I'UM I POUNDS ) 0.000 1.313 7.454 2.176 314.43 0.758 1.3Q5 7.512 2.182 314.95 1.590 1.298 7.561 2.186 315.53 2.500 1.291 �.611 2.191 316.09 3.498 1.283 7.662 2.195 316_73 4.59� 1.276 7.713 2.200 317.36 5.79D 1.268 7.7b6 2.205 318.09 7.1Qfi 1.261 7.819 2.211 318.75 8.553 1.254 7.873 2.217 - 319.54 10.�95 1.246 7.927 2.223 320.28 11.945 1.239 7.983 2.229 321.10 13.859 1.231 8.440 2.236 321.95 16.019 1.224 8.497 2.243 322.93 18.437 1.217 8.156 2.250 323.75 • 21.25� 1.209 8.215 2.258 324.71 24.219 1.2D2 8.276 2.266 325.71 27.716 1.194 8.337 2.274 326.74 31.742 1.167 8.399 2.283 327.82 36.441 1.160 8.463 2.292 328.93 42.420 1.172 8.527 2.302 330.08 • 46_804 1.165 8.593 2.312 331.27 57.334 1.157 8.659 2.322 332.51 68.625 1.150 8.727 2.333 333.79 70.690 1.149 8.736 2.335 333.95 iJODE 137_00 : HGL =< 376.333>;EGL= < 379.J.98>;FLOVJ�INE= < 377.020> **tk*'k'k*Yr k * �k f*'k'ktM'kk tk * * k tk * * � � **�A' Y�'Yi * **lrYrw*i� Y� i� *iF*iF#*k �h YrY� Y� * * Yi k k Yrtktkf �M k**'k'kk**f ***i� ii� FLOW PROCESS FROM NODE 137.OQ TO I30DE 138.00 ZS CODE = 1 UPSTREAM NODE 138.00 ELE�/ATION = 378.17 (FLOW IS Sl3PEACRITICALa ------------------------------------------------------------------------------ CALCULATE FRICTIQN iASSES(LACFCD): PIPE FLOW = 16.32 CFS PIPE DIAMETER = 29.OQ INCHES PiPE LENGTH = 128.43 FEET MP.?�INING'•S N = Q.013UQ NORM?�L DEP`I'k3 (FT) = 1. 31 CRITZCAL DEPT'H ( FT) = 1.46 llPSTREAM CONTROL ASS[3MED FLOWDEPTH{FT) = 1.46 -----------------------------------------------______------------------------- --------------------___-------------------------------------------------------- GRADF3ALLY VARIED FI,OW PROFILE COMPUTED IidFORMATION: DISTANCE FROM FLOW DEPTH VELOCITY SPECx�'IC PRESSiJRE+ CONTROL{FT} (FT} {FT/SEC} EN�RGY(FT} MOMENTLTM(POUNDS) O.00D 1.456 6.657 2.145 309.70 • 0.023 1.450 6.686 2.145 304.71 O.D93 ].499 6.715 2.145 309.73 � 0.214 1.438 5.745 2.145 309.77 0.393 1.932 b_�75 2.146 349.82 0.633 1.427 5.806 2.146 349.89 0.992 1.421 5.837 2.147 309.98 1.326 1.415 6.8b8 2.147 310.68 1.799 1.409 6.899 2.146 310.19 2.357 1.403 6.931 2.149 310.33 3.027 1.397 6.969 2.150 310.98 3.818 1.391 6.997 2.151 310.64 4.74$ 1.3$5 7•030 2.153 310.83 5.839 1.379 7.D53 2.�54 311.03 7.124 1.373 7.097 2.155 311.29 8.628 1.367 7.132 2.�57 311.48 10.408 1.361 7.156 2.159 311.73 12.527 1.355 7•2Q2 2.161 312.00 15.079 1.349 7.237 2.�63 312.29 18.182 1.343 7.274 2.165 312.59 22.056 1.337 7.310 2.157 312.92 27.D42 1.331 7.347 2.170 313.26 33.784 1.325 7.385 2.172 313.62 93.733 1.319 7.423 2.175 314.00 51.543 1.313 7.461 2.178 314.40 128.430 1.313 7.464 2.178 314.43 NODE �38.00 : HGL =< 379.626>;EGL= < 360.315>;F'LOWLINE= < 378.170> ***s*x*+++*�+*f*++t*w++r+�**rtr�+swt+*+++*w��x*x*****w****ww**+�w+r*++f+a��ry• UPSTREAM PIP� FLOW CONTAOL DATA: NODE NUMBER = 138.OD FE,OWLINE'ELEVATION = 378.17 ASSUMED UPSTREAM CONTROi, HGL = 379.63 FOR DOWi�iSTRF.AM RUN ANALYSIS � __________________________________��__________________________________---_-_ END QF GRP.Di7ALLY VARIED FLOW ANAi,YSIS • • tyx�****x++s*�*x�a�rr�+s�xit++�++++++ft**x+�a�+++*++�+x*xiitti**�+***�+�+*�t*+x PIPE-FLOW HYDRAULICS CO3�iPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYARAUi�ICS CRITERION) Ic) Copyright 1982-2002 Advanced Engineering Software (aes} Ver. B.� Release Date: D1/O1/2002 License 7D 1509 Ana3.ysis pre�ared by: PROJECT DESIGN CONSLFLTANTS 7Q1 'B' STREET, S[IITE B04 SAN ASEGO, CA 42101 619-235-6471 ws++++�+*�w**++s+t**++r�** DESCRIPTION OF STUDY +**+ti+*r++****s++**,r�r*�* * BRESSI RA13CH - Ui.TiMATE COEVDITIONS � "` SYSTEi�S 130 LATERAL 1( INNOVA�'ION WAY 1+98 RT} * * * 100-YF'.P.R STORi�S EVENT w::****,r+�.wf**ti**...++.Wft**.��.w*++*..*tf.*+ti*....++++r*****..**+r*+**. PILE NAME: �3Q-1.DAT TIME/DATE OF ST'UDY: 08:07 O1/17/2d03 �k 1� k k iF ***'t'� *## ii'i ** k f if ffi t**Yr�/r*##1'Y***1�*#*Y! Y**'k�Fk k*# i� *4ili****Yr*i� ##f #i*1rYr*#'k't'r GRADUALLY VARIED FLOW ANAi�YSIS FOR PIPE SYSTEM NODRi POINT STA'TUS TABLE �Note: "*" indicates nadaJ. point daCa used.} UPSTREAM RUN Df]WIdSTREAM RUN NODE MODEL PRESSIiRE PRESSIFRE+ FLOW PRESSiFRE+ . NUMBER PROC�SS HEAD ( F'I' ) MOMEN�'UM f pOUNDS } DEPTH ( FT ) l90MENTiJkS { POfJNDS j �32.1D- Q.79 Dc 56.06 Q.59* 62.83 } FRICTION 132.2D- 0.79*Dc 56.06 0.79*Dc 56.Ob } CATCH BASIN " 132.2a- 1.16i 30.54 0.79 Dc 19.55 -------------------------------- MA.XII�FUM NIiMBER OF ENERGY EAL7INCES USED IN EACH P3tQFILE = 25 • -------------------------------------- NOTE: STEADY FLQW HYDRAULIC HEAD-LOSS COMPUTATIQNS BASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CLFRRENT LACRD,LACFCD, AND OCEMA �ESIG13 MANIJALS. yry� ## t�1�YY ir1� �*ir4*iF*# 1 i y� * 4 Y t# ir #*�#*'�'r**** f'l�'t*� **Yr**i�i+Y#t**I� �k*i�' *# i i*i i*1� ir�F # 1�rt *'k DOWNSTREAM PIPE FLOW CON'I'ROT� L7ATA: NODB NU[�BER = 132.10 FLOWLINE ELEITATION = 359.95 PIPE FLOW = 4.20 CFS PIPE UTAME'I'ER = 18.00 INCHES ASSUMED DOWNS'f`AEAM CONri'ROL HGL = 36�.590 FEET *NOTE: ASSUMED DOWNSTREAi+] CONTROL QEPTH( 0.59 FT.} IS LESS TI�AN CRITICAL DEPTH( 0.79 F`P.} ___> CRITICAL DEPTH YS ASSIJASED AS DOWNSTREAM CONTROL DEPTH FdR iiPSTREAM RUN ANALYSIS -------------------------------------------------___ NOD� 132.1D : HGL =< 360.541>;EGL= < 361.196>;FLOWLI�IE= < 359.950> .�.�**»*��t�w.�.�.*..«�*��.*.*.��..�***�*�*t.*�***�*�.�r��*..**t�.*�..+�� FLOW PROCESS FROM NODE 132.�0 TO I30DE 132.2a IS CODE = 1 UPSTREAM NODE 132.20 ELEVATIOI3 = 360.54 {FIAW IS SUPERCRITICAL} CAI,CUi,ATE FFtICTIOi�I LOSSES [LACFCD} : PIPE FLOW = 4.20 CFS PIPE DZAMETER = 18.00 INCHES � PIPE E,ENGTH = 43.25 FEET -_MANNING'S iV = 0_01304 i------------ --------------rv---------------__ � '-NORMAL-DEPTHIFT)========0-58=====---===CRITICAL-DEPTH(F"i')==--=-==0=79=---=__ UPSTREAM CONTROL ASSUMED FLOWDEPTH(FT) = 0.79 ==----------------_--_---------_------ GRAI3UALLY VARIED FLOW PROFILE COMPU'iEI] Ii3F'ORMA'I'ION: yDISTANCE FROM FLOW^DEPTH VELOCITY SPECYFIC PRESSURE+ COiV'I'RpL S F'P 1 ( FT ) ( FT/ SEC a ENERGY ( FT j t+30MENTL3M ( POLTNDS 1 Q.006 D.7$5 4.484 1.D98 56.06 fl,p16 p.77'l 4.544 1.098 56.07 D.db6 0.769 4.605 1.09$ 56.10 D.�54 0.76� 4.658 1.099 56.15 0.2B4 0.752 4.733 1.100 5f•22 p.456 0.744 4.BOD 1.102 5b.31 0.664 4_736 4.868 1.�04 56.A2 4.965 0.728 4.939 1.107 56.55 1.3f0 fl.7i9 S.Q�� 1.110 56.71 1.725 0.711 5.086 1.113 56.89 2.223 0.703 5.163 �.7.17 57.10 2.813 0.695 5.242 1.122 57.33 3.509 a.687 5.324 1.127 57.59 q,329 0.678 5.408 1.133 57.87 5.296 D.670 5.495 1.139 58.19 b.438 O.b62 5.5$4 1.147 58.53 7.794 0.654 5.576 1.159 58.89 9.413 0.64b 5.772 1.163 59.29 11.369 0.637 5_870 1.173 59.72 13.765 0.624 5.972 1.183 60.19 16.766 d.621 6.077 1.I95 60.59 � 20.644 0.613 6.185 1.2Q7 61.22 25.911 O.b05 6.297 1.221 61.79 33.7�8 fl.596 6.4�3 1.235 62.39 43.250 0.59� 6.494 1.246 62_83 ------------------------------------------------ NODE 132.20 : HGL =� 361.425>;EGL= < 361.738>;FLOWLINE= � 360.64a> t*+**rx�***+**t++.**wx*+��rstt�i+�+*+**,r*w*f++*+ti��*�*�r�+*stt++*x�sfy++x+*+�f FLOW PROCESS FRONS NODE 132.20 TO NODE 132.20 IS CODE = B UPSTRE.AM NpDE 132.20 ELEVATION = 3bd.64 (FLOW IS SUBCRI'PICALi ----------_----------------- CALCULAT� CATCH BASIN EN'T'RANCE LOSSES(LACFCD}: PIPE FLOW = 9.20 CFS PIPE DIAMETEft = 18.OD TNCHES F'LOW VELAC�TY = 9.46 FEE'i/SEC. VELOCITY HEAD = 0.312 FEET CATCH SASIN RIERGY LOSS =-2*{VELOCITY HEAD} -.2*{ D.312j = 0.062 ----------------------------�--------------------___ NODE 132.20 : HGL =< 361.800>;EGL= < 361.80D>,FLOWLIN�= � 360.640> *# yr ** *i#`��"1#t+*w'iF***iri y� * Y fir**# ** 1�' 1 kt*** ** i� #'1Y�Y***ri YrY�'k ##'ty'y'y i****'M'k # Y� Y*#*'kYrii *X' * UPS'FREAM PIPE FLOW CONTRdL DATA: NODE NUMBER = 132.24 FLOWLINE ELEVATIO�I = 350.64 ASSUMED UPSTREAM CONTROL HGi = 361.43 F�R DOWNSTREAM RUN ANALYSIS ----------------�_-------- END OP GRADLTALLY VARIED FLOW ANALYSIS . � • C J � Yr **#'t * k** **!rt??#1k *f'tk ik f*yr*i #+�k1# i �r�'k* *+i YYri� t ik Y1�t't'1Y* 1**'kYr**ri #Y ##'tMt*tkYr h#'tY PIPE-FLOW HYDRALTLTCS COMPU`PER PROGRAM PACKAGE (Reference: LACFCD,LACRD, A4�FD OCF.MA HYDRAULICS CRT'i'ERIONj (c) Copyright 1982-2D02 Advanced Etsgineering Software iaes? Ver. B.Q Release Date: O1/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTANTS 701 'B' STREET, SUITE 600 SAN DIEGO, CA 92101 619-235-6471 . r� �J +++ww+,taa*t:*++t+,r�*a+**+* DESCRIPTION QF STUDY +**+.****+,ts�++i*t*+r,�+*r+** * BAE55I RANCH - ULTIMATE CONDITIONS * * SYSTEM 130 - LAiERAL 2(INNOVATION WAY 5TA 1*98 L'P] * + * �00-YEAft STORrS EVENT x,t*�+�*t+a**wwi�i�*++**+r,r�,r��+*****w*++++:**r�*w,r+++r*�yt*+t*+r+*++r*s++wx* FILE NAME: 13Q-2.DAT TIME/DATE OF STUDX: Q8:59 O1/17/2003 **w*rt*+,r�*�*a��ytt+ww*y*++�xi*r*wx*++rt�x�x*�+++�r*t+*+*x*t**+**+**y+**,t+�s*t*w GRADUALLY VARIED FLOW AI3ALYSIS FQR PIPE SYSTEM NODAL POINT STATUS TABLE fNote: '*' indicates nodal poin� data used.) UPSTRF.P.M �2UN 1�UWNSTREAM RUN IJODE MODEi, PRESSUR� PRESSURE+ FLpW PRESSURE+ NUT7B�R PROCESS f-IEAD ( FT J MOMEN�'UM ( POL7I�FD5 } DEFPH ( FT j i+]OMENTi3I� ( POUNDS f 132.50- 4.89 Dc 76.02 �.50* 112.82 } FRICTION 132.60- 0.84�Dc } CATC}i BASIN 132.64- 1.33* 76_Q2 42.27 0.89}nc O.B9 Dc 76.Q2 25.97 -----------------�-----------�----- MAXTMUM NUMBER OF EidERGY BAJ�ANCES USED IN EACH PROFTLE = 25 NOTE' STEADY Fi,OW HYDRAULFC HEAD-LOSS COMPi3TATIONS SASED ON THE i�S05T CONSERVATIVE FOR�Si]T�AE FROM THE CURRENT LACRD,LACFCD, AND OCEMA DESIG[d MANiJALS. t*�*...�+*�,��.�*+***��*�..�**�*..�*�.*.*�..�.**++�rt�**.,«.�*+�*..+f*****�.*+.*** DOWNSTREAM PIPE F'LOW CONTROL DATA: 1VODE 1dlJMBER = 132.50 FLOWLINE 8LE1/ATIdN = 36D.12 PIPE ELOW = 5.30 CFS PIPE DIAMETER = 16.00 II3CHES ASSUMED DOVTNSTREAM CONTROL HGL = 359.95D FEET "NQTE: ASSi3MED DOWNSTREAM CQN'FROL DEPTH{ -�.17 �'T.) IS L,ESS TH.AN CRITICAL DEP'E`H( Q.89 FT. } ___> CFtITICAL 17EP'I`H IS ASSUMED AS DOWNSTREAM CONTROL DEPTH FOR UPSTREAM RUN ANALYSIS -------_-_------------------------------------- AIODE 232.54 : HGL =< 350.618>;EGL= � 362.279>;FLOWLIPFE= < 360.120� **i.xx+�++*t+t**x*i.�*t�x*+**+++i�+tt��*+*++r�**t�+w*++*a+r�*r***x,t++�*tf�*++*�** FLOW PROCE55 FROi�S NODE 132.50 TO NODE 132.60 IS CODE = 1 UPSTREAM NODE 132.60 EL�IATION = 361.17 (FLOW IS Si3PERCRITICAL} CALCI}LATE FRICTION LOSSESfLACFCDJ: PTPE FLOW = 5.30 C�'S PIPE bIAMETER = 18.00 INCHES PIP� LENGTH = 5.25 FEET MANN�NG'S I3 = 0.0130a � NpRMAL DEPTH(FT) = 0.34 CRITICAL DEPTH(FT} = 0.89 -=--------------------------------- UPSTRFAM CONTROL A55UMED FLOWDEPTH(FT} - 0.$9 ---------___--_----------- GRADUALLY VARiED FLOW PROFILE COMPUTED INF4I�3�4ATIOi�T: DISTANCE FF�OM FLOW DEPTH VELOC�'T'Y SPECIFIC PRESSURE+ CONTROL { F"I' j ( F�' ) ( FT / SEC ) ENERGY S F`I' ) MOMENTUM ( POUNDS ) 0.000 0.$87 4.8"]1 1.256 76.02 0.006 D.$b5 5.021� �.257 76.49 4.023 O.B43 5.1B0 1.260 76.31 �.Q54 0.821 5.351 1.266 76.69 0.�43 0.799 5.533 1.275 '77.23 O.lb6 0.777 5.729 1.267 77.96 0.252 0.756 5.94Q 1.309 78.89 Q.362 0.734 6.1b7 1.325 8Q-Q2 0.499 0.712 6.417. 1.351 81.38 4.670 0.690 6.675 1.382 83.4D � 4.879 0.668 6.962 1.421 B4.88 1.134 0.646 7.273 1_4b8 87.06 1.445 0.624 7.611 1.525 89.56 1.822 0.603 7.981 1.592 92.43 2.282 0.581 8.386 1.673 95.71 2.845 0.559 8.83� 1.771 99.44 3.536 0.537 9.322 1.887 103.69 4.394 0.515 9.865 2.027 106.5� 5.25D 4.498 10.340 2.�59 112_82 ---------------------------------------- NdDE 132.6Q : HGL =< 362.057�;EGL= < 362.426>;FLOWLIi3E= < 361.170> � 4tt****w**�r�s*+++***x**x***W*tw*,�a<x++f�y*+a***�**++i.�r*st*++,rx�+**s��**�*�w+*� FLOW PROCESS FROM NODE 132.60 TO NODS 332.6Q IS C�DE = B UPS3'REA3+3 �IODE 132.60 ELEVATION = 351.17 (FLOW IS SUBCR�TICAE�) -----------------_ CALCUi�ATE CATCH BASIN ENTRANCE LOSSES(LACFCD}: PIPE FLOW = 5.30 CFS PIPE DIAMETER = 18.D0 INCHES FLOW VELOCITY = A.87 FEET/SEC. VELOCITY HE.�D = 0.369 FEET CATCH BASIN ENERGY LOSS =.2*IVELOCI'PY }IEAD1 =-Z�f 0.369) � 0.074 --------------------------- NODE�Y'132 60 : HGL =< 362.499>;EGL= < 362.499>;FLOWLINE= < 361.170> ♦rt*****xx+++�*r*w**a**+*w*�tr*�*t�+x+xa�a+�tf*+*�*+**+t�►*f***�wx++s�r++**,r**+ UPSTREAM PTPE FIAW CONTROi� DATA: NdDE NCFMBER = 132.50 FLOWi�TNE ELErIATION = 361.17 ASSiJi+]ED UPS�'A�,.�M CQNTROL HGL = 362.46 FOR DOWNS'I'FtEAM RUN AI�IALYSIS ENC3 pF GRADUALLY VARIED FLOW ANALYSIS • � � } * � + i x * * i # * i * * * * * * k % M # t � 1 � * * w * � * * * i Y Y ! Y * 1 * # � ! f # # * i Y � 4 + * Y Y * * � i * # � k } * f f � + Y Y i * i * 1 PIPE-FLOW EiYDRAULICS COMPUTER PROGRP.M PACKAGE (Reference: LACFCI?,LACR9, AND OCEMA HYDRAULICS CRxTERIOfV} (c} Copyright 1982-2002 Advanced Engineering Software iaes? Ver. B.D Release Date: 011D1/2002 L�cense ID 1509 Analysis prepared by: PRO.TECT DESIGN C033SL7i�TANT5 7Q1 'B' STREET, SUITE 800 5AN AIEGO, CA 92101 519-235-6471 ***.**��v.+�.tti��*+**�w�+t DESCRIPTION OF STUDY •***•�**��:*.*+�*.k**++. " BRE55I 4�ANCH - [Tf�TIMATE COI�TDITIONS ` * SYSTEM 130 - LATERAL 3(IPii�FOVATION WAY 1fl+64.97} * * 100-YEAR STORM EVENT � * *i�t'� Y�c �� Yr**tkYr}iFY� *i *'/�4}Y 1 f Yrir'k'k'lrlr#**'ti Y�k * ir f 1� k*Yr*#i i 4 rt*Y Y#***� iM i 1� #***#*Yy Y!*# FILE AFAME: 130-3.DA'i' TIMElDATE OF STUDY: 17:42 O1/15/2063 rxtt****+t�i.f+tr***+*t****wx*trrtyt�+r+:*��rfytit+*x**w*�+�s***ff*��rt++t*w+*�h��* GRADUALLY VARIED FLOW ANAI.YSIS FOR PIPE SYSTEM NODAL POINT 5i`ATIiS `I'ABLE ;Note: "*' indicates nodal point data used.} UPSTREAl�7 RU13 DOWNSTREAM RUN i�iODE MODEL PAESSURE PRE55URE+ FLOW PRESS[TRE+ � �Fi34�SBER PROCE55 HF.AD {�7`1 MOMENTUM ( POUhFDS ) DEPTH ( FT} F]OMENTi]T1( POUNDS ) 136_10- 1.99� 76.85 4.29 7.11 } FRICTION 142.OD- 1.01* 36.01 0.33 Dc 6-83 } CAT'CH SASIN � 142.OD- 1.02* 35_31 0.33 Dc 2.51 --------------------_------------------------------------------------------------ MAXIMUM NLFMSER OF II3�12GY B,I�LA3VCES USED IN EACH PROFIE�E = 25 ----------------------- NOTE STEADY FLOW HYARAULIC HEAD-LOSS CQMPUTATIONS SASED ON THE MOST CONSERVATIVE FORMULAE FRQM THE CLFRRENT LACAD,LACFC�, AND OCEMA DESIGN MANi3ALS . JUNCTIpN ANALYSIS USING FULL INTEGR.ATION FORMUF�ATIbN *t*****tt�-ki.�+t��********wx*+��*f*�+*rx�*+art*r**r***+*��+*++�*y+x+*w*i.t+�st*+ DOWNSTF2EAM PIPE FLOW CONTftOL DATA: NODE NLlMBER = 136.10 �'LOWLINE ELEVATI073 = 375.70 PIPE FI,OW = Q.81 CFS PIPE IJIA�IETER = 18.00 INCHES ASSUMED DOWI�STREAM CON�'320L IiGL = 377.190 FEE'I' YNODE 236 10 � HGL^= � 377 14Q>;EGL= < 377.143>;FLOWLINE= < 375.�00> **�***+t�.**�:+�+��.....*«t+,�*��+,+..+�+�++.*:�*.*******t++*+.,*+**��*+��.:t*.� FLOW PROCES$ FROM NODE �36.10 TO NODE 142.00 IS CdDE = 1 UPSTREAM NO]]� 142.00 ELEVATION = 376.13 (FLdW IS SUBCRITICAL) CALCiTLATE FRICTION LOSSESILACFCD): PIPE PLOW = 0.81 CFS PIPE DIAMETER =�S.�D TNCHES PIPE LENG�H = 45.00 FEET MANNII�G'S N- 0.01300 ------------------------------------- NORMAL DEP`i'Fi ( FT) 0. ZS CRITICAL DEPTH ( FT} = 0. 33 • DUWNSTREAM CONTROL�ASSL7MED FLOWDEPTHfFT] _ `1 44 + ` � GRADUALLY VARIED FLOWTPROFILE COMPUTED INFORMATION ` Y ------------------------------------------------------------------------------ DISTANC� FRQM FLDW DEPTH V�LOCITY SPECIFIC PRESSURE+ COTPI'ROL ( FT ) ( FT ) 1 FT / SEC } ENERGY ( FT j MQMENTUM I PCIUNDS 1 O.OQQ 1.940 0.464 1.493 76.85 4.639 1.396 0.473 �.399 72_Q9 9.275 1.352 D.483 � 1.355 67.43 13.908 1.307 0.995 �.311 62_88 18.538 1.2b3 d.510 1.267 58.45 23.1b5 1.219 0.525 1.223 59.17 27.789 1.175 0.545 1.�79 50.03 32.410 1.131 0.567 1.136 45�05 37.028 i.086 0.591 1.092 42.22 41.641 �.042 0.618 1.Q48 3$.57 95.000 1.010 0.640 1.016 36.01 ----------------..____--------------------------------------------___---------- NODE 142.D0 : HGL =< 377.144>;EGL= � 377.146�;FLUWLINE= < 376.130> *****��.t��*****.�.**,.�**.:w.+t***�**.***w....****�..*�*.*.***,.**.«**+*Ww�� FLOW PROCESS FRQM NODE 142.OD TQ NODE 142.QD IS CODE = 8 LFPSTREAM NODE 192.00 ELEVATION = 376.13 {FLpW I5 SUBCRITICALj CALCULATE CATCH BASIN ENTRANCE LOSSES{LACFCD): PIPE FLOW = 0.81'CF5 PIPE DIAMETER = 18.00 INCI-iES FLOW VELOCITY � 0.64 FEET/SEC. VELOCITY HEAD = 0.006 FEE`i' CATCH SASIN EPIERGY LQSS =. 2* LVELOCITY 4�EAI?1 =• Z'` { 0. 046 j= 4. 001 ---------------------------------------------------------------------____------ NpDE 142.00 : HGL =< 377.148>;EGL= < 377.148>;FLOWLINE= < 376.130> � �*.*t��.�.i*�tt+***�,.**.**r*+++,.+,.+**�,,�,r*++***�,�*.+W�w..*+*�**+*******+�+w� UPSTREAM PIPE FLOW CON'FRQL DATA: NODE NUMBER = 142.00 FLOWLINE ELEVATION = 376.13 ASSUMED UPST'ftEAM CpNTROL HGL = 376.46 FOR DOWNSTREA�3 RUN ANALYSIS END OF GRADUALLY VARI�D FLQW A�IALYSIS `J � APPENDIX 4.1.4 SYSTEM 2�0 (`A' STREET) i ,-- i • tw*t�*ryw�+******�tx+�*****�+�**x*+��*rr�**sx++++w++ay+x**s+�rx**+frt*+t��ia** PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,I�ACRD, AND OCEi3A HYDRAUL3C5 CRITERION) Ic} Copyright 1982-2002 Advanced Engineering So�tware Saes1 Ver. 8.0 R�lease Date: O1/4�/2002 License ID 1509 Analysis prepared by: PRO�TECT DESIGN CONSIJLTAN'I'S 7D1 'B' STREET, SUITE B00 SAN DIEGO, CA 92101 619-235-b97J. ++w+*+*�***+*�***,�+�+++**+ D�SCRIPTEO�I OF ST43DY **+*�*r***+t+*****««*«**k� * BRESSE RANCH - INTERIM MASS GRADED COAiDITI033 " * SYSTEM 240 - PA-6 3+5A55 GRADED TO DESILT BASIN " 100-YEAIt STORM EVENT * �r*r�rtti*t**+y*yxt++w*++*a*+***+.*+.wxx*+**i*�+i.+++v.t+++w+i.++��*�*��rt*tx+st FILE NAME: L200I.DAT TIME/3]A'FE pF S`I'UDY: 09:58 Ql/17/2003 * ****1'kY� w Yr *Yr*iFiFYrk'k * i�Y�***##i�f#f #*�Y�*y t �t'1YY� t t***t******t�rtt*'kk *�F**'k1� Yr* *Yr*Y�# **** GRADUALLX VARIED FLOW AI3ALYSIS FOR PIPE SYSTEM NODAL PDXEQ'I' STATUS TABLE (Note: "*" indicaCes nodal point data usecl.f UPSTREP.M RiJid DOWI3STREAM RUN NODE MODEL PRESSURE PRESSLTRE� FLOW PRESSURE+ NUMBER PR�CESS HEAD(FT) MOMENTUNI(POUNAS) DEPTH(FT) MOMFN'T'UM(POUNDS} • 200.00- 9.22* 4036.79 1.00 2208.30 ) FRICTTpI3 ] IiYDRAULIC 3UMP 205.14- 2.2b*Dc 1142.47 2.25*Dc 1142.A7 ) JUNCTIOAI 205.50- 3.91 1696.36 1.1Q* 1974.51 ) FRICTION 205.64- 2.26 Dc 1J.42.47 1.23* 1718.87 ) MANHOLE 205.70- 2.26 Dc 1142.47 1.24* 1702.76 } FRICTION 205.8Q- 2.26''Dc 1142.47 2.26*Dc 1142.47 ] CATCH BASTN 205.Sa- 3.58* 915.84 2.26 Dc 359.45 ----------------------------_______-_---------------------------------------_-_ MAX�MUM NL7MBER OF ENERGX BAI.ANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEADY FLOW HYDRAULIC HEAA--LOSS COMPUTATIONS BASED ON THE MOS'i` CONSERVATIVE FORMULAE FROM THE CURRENT LACFtT7,LACFCD, AND OCEMA DESIGN �SAiVUALS. ♦Y1# fttiti�*i*iiiti�Yr* *�k t*! *Y i� **i�Y**Yrkk *Yr *Y� f ## * i*t#'k+t}i**i�k#1i*+�k4*Y4tt �k*i** DOWNSTREAM PIPE FLOW COfFTROL DATA: NOI?E 13LThfBER = 200.OQ FLdWLINE ELEVATION = 2$6.1$ PIPE FLOW = 98.00 CFS PIPE DIAMETER = 36.00 INCHES ASSUNfED DOWNSTREAM CONTROL HGL = 295.400 FEET ------------------------------------------------------------------------------ NODE 2DO.OD : HGL =< 295.400>;EGL= < 29fi.116�;FLOWLINE- < 28b.180> .*,..*�*+++t*�+�++�+�*��..*+�.**��.�ti,.**�*.�****..».�*��+�..*��...,,*.****.+**�** FLOW PROCESS FROM NQDE 200_DO TO PiODE 245.14 IS CODE = 1 : --UPSTREAM NODE 205.1� ELEVATION = 30b_09 [1-IYDRAiFLIC JUi� OCCURS) � -------------------------------------------------------------------- • CALCULATE FRICTION LOSSES(LACFCD}: PIPE FLOW 48.00 CF5 PIPE DIAMETER = 36.Dfl INCHES PIPE LENGTH = 183.68 FEET MANNING'S N- 0.01300 ------------------------------------�___-------------------------------------- HYDRAULIC JUMP : DOWNSTRF.�1M RUN ANALYSIS RESiJL'i'S N�RMAI, DEPTH(FT) = 0.95 CRITICAL DEPTi-1(FT} - 2.26 --------__--__..---------------------------------------------------------------- ' UPSTREAM CONTROi� ASSUMED FLOWDEPTHIFT) = 2.25 GFiADC3ALLY VARIED FL04�I PROFILE COMPUTED INFORMATION: --------------------------------------------------_-_-----...._------------------ DTSTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL {�' � { FT } ( FT/ SEC ) ENE32GY ( F"I' ) MOMENTUM { p{}��S ) Q.000 2.254 8.424 3.356 1192.47 Q.027 2.202 e.b31 3.359 1143.44 0.108 2.150 8.853 3.367 1145.26 4.250 2.096 9.091 3.362 1151.05 0.460 2.046 9_347 3.403 1157.92 0_748 1.993 9.621 3.432 11fi7.U2 ?.125 1.941 9.916 3.469 1178.50 1.603 1.889 10.233 3.516 1192.54 2.198 1.837 1D.574 3.575 1209.34 2.930 �.785 10_993 3.646 1229.12 3.821 i.733 11.390 3.731 1252.Z2 4.901 1.681 11.770 3.$34 1278.54 5.204 1.629 12.236 3.956 1309.42 7.777 1.577 12.742 4.1aQ 1343.52 9.677 �.525 13.293 A.271 1382.88 II.981 �.473 13.894 4.472 1427.32 • �9.784 1.421 14.551 4.71.1 1477.51 �8.241 1.369 15.272 4.993 1534.15 22.536 1.317 16.066 5.327 1598.06 27.9b4 Z.265 16.992 5.725 1670.19 34.963 �.213 17.9�5 6.200 1751.71 44.362 l.lbl 18.997 6.769 1844.0� 57.550 �.109 20.209 7.954 194B.7b 77.B15 1.057 21.571 8.287 206B.03 I15.650 I.005 23.ii1 9.3a4 2204.37 183.680 1.003 23.155 9.334 2208.3a --------------------------------------------------------------------__--------- HYDRA[,Ti�IC JUMP: UPSTREAM RUN AI�IALYSIS R�Si]i�T5 DOWNSTREAM CON'I`ROL ASSUMED PRE55URE HEADiFT) = 9.22 PRESSURE FLOW PROFILE CdMPUTED INFORMATION: ------------------------------------------------------------------------------ DISTANCE FROM PRESSUftE VELOCITY SPECIFIC PRESSi7RE+ CONTROL ( F�' ) HEAD ( FT J { FT / SEC ) ENERGY ( FT j d+30MENTLiI� ( POiTNDS ) O.Q00 9.220 5.791 9.936 4036.79 60.262 �.oaa b.791 3.716 1293.27 --------------------------------------....___----------------------------------- ASSiTt�4ED DOWAISTRF.AM PRESSURE HEAD 1 FT j= 3. 00 GRADUALLY VARIED FLOW PRO�'ILE COMPUTED TNFOftMATI0i�7: DISTANCE FROM FLOW DEPTH VELOCITY SpECIFIC PRESSURE+ CONTRQL i F"I'} ( FT i ( FT/ SEC } ENERGX ( FT f MOMENTUM ( POUI3D5 ) b0.262 3.000 6.769 3.716 1293.27 • &0.527 2_970 6.BOQ 3.669 12B1.21 50.772 2.940 6.823 3.663 1270.06 • 61.0�3 2.911 6.848 3.639 1259.53 61.229 2.881 6.88Q 3.616 1249.53 61.435 2.851 6.916 3.544 1240.01 61.637 2.821 6.957 3.573 123p.95 61.83� 2.792 7.001 3.553 1222.32 62.016 2.762 7.054 3.534 1214.12 62.193 2.732 7.�OI 3.516 1206.34 62.352 2.762 7.157 3.498 1198.9B 62.522 2.673 7.215 3.4B2 1192.04 62.674 2.b43 7.277 3.466 1185.52 62.$17 2.613 7.343 3.451 1179.43 62.952 2.583 7.412 3.437. 1173.77 63.�78 2.554 7.489 3.424 1168.54 63.194 2.524 7.560 3.412 1163.76 63.30Q 2.494 7.b4d 3.401 1159.43 63.396 2.464 7.723 3.391 1155.57 63.481 2.q35 7.810 3.382 1152.1B 63.555 2.905 7.90� 3.375 �149.27 53.b17 2.375 7.995 3.368 1146.B6 63.b57 2.345 8.094 3.363 1144.96 63.743 2.315 8.197 3.359 1143.59 b3.726 2.286 8.304 3.357 1142.75 53.733 2.256 8.4i5 3.356 1142.47 �83.6$0 2.256 8.415 3.356 1142.47 ------------------------END OF HYDRAULIC JUMP AI3ALYSIS----------_______------- PRESSURE+MOMENTUM BALANCE OCCl3RS AT 40.21 FEET UPSTREAM OF N4DE 200.OD j DOWNSTR�IM ]7EPTH = 5.069 PEEfi, UPSTREAM CONJUGATE DEPTH = 1.D04 FEET � ---______---------------------------------------------------------------------- NOpE 2Q5.10 : HGL =< 30B.344>;EG�= < 309.946>;F'LOWLINE= < 306.090> • 'k'M*fYrk flrYr f1r**YrYi YrYr'k#*tY*#f ***#iitY�ttt*�lr***YrYrYr*iMkki��k*i��*1�i#*Yt*i i*itt! i*iiA**fif FLOW PRDCE55 FROM I�iODE 205.10 �`O NODE 2fl5.50 IS CODE = 5 UPSTI2EAM NODE 205.50 ELEVATION = 305.42 {FLOW IS SUPERCRITICAL) CALCULATE JiJNCTTON %,OSSES: PIPE FLOW DIAMETER ANGLE �'LOWLTNE CRITICAI, VELOCTTY (CFS} (IidCHES) {DEGREESj EL�7ATYDN DEPTH{FT.) (FT/SEC} UPSTREAri 48.00 35.Q0 90.OQ 346.92 2.26 24.5�� DUWNSTREAM 98.00 36.00 - 306.09 2.2b 8.427 LAT�RAL #1 0.00 0.40 0.00 Q.00 0.40 0.040 LATERAL #2 0.40 O.QQ 0.00 �.44 0.40 0.000 Q5 O.QO===QS EQUALS BASI3�I INPUT=== LACFCD AND .00EMA FLOW JLTNCTIQN FORASULAE USED: DY={a2*V2-Q}.*V1*C05(DELTA�}-�3*V3*COS{DELTA3)- Q4*V4*COS(DEi,TA4))/((A1+A2)*16.1}+FRICTION LOSSES UPSTREAM: MANNING'S N= O.D13D0; PRICTIObI SLOPE = O.fl6354 DC3WN5TREAM: MAI3NTNG'S N= 0.01340; FR�CTION SLOPE = 0.�0621 AVERAGED Fi2IC�'�ON SLOPE YN JUNCTION ASSUMED AS 0.03487 JUNCTTON LENGTH = 4.44 FEET FRICTION LOSSES = 0.139 FEET �NTRAI3CE LOSSES = 0.000 FEET Ji3PiCTI023 LOSSES =( DY+I-IVI-HV2 }+( ENTRANCE LOSSES } JiJNCTION LOSSES =( 4.603)+( 0.4Qd1 = 4.6D3 NObE 205.50 : HGL =< 3fl7.5I7>;EGL= < 3�4.649>;FLOWLINE= < 306.42fl> wr+*r*r**a+**r***rr***.*i*i*+a+t+**+*+*,��*+�*+****�***+**t*r��rt�*�*f*�*iYrtrtxr:** FLOW PROCESS FROM NODE 2Q5.50 TO NODE 2Q5.60 IS CODE = 1 UPSTRF.AM NODE 205.60 EL�IATIObI = 308.48 (FLpW xS SUPERCRZTICAL) -----------------------------------------_____-____---------------------------- � CALCULATE FRICTION LOSSES{LACFCD}: • P�PE FLOW = 48.D0 CFS PIPE D�AMETER = 36.D0 INCHES PEPE LENGTH = 8.25 FEET MANNING'S N O.Q1300 ------------------------------------------------------------------------------ NORMAL DEPTH(FT) = 0.77 CRITICAL �EP�`H(FT) = 2.26 UPSTREAM CONTROL ASSUMED FLOWDEPTH(FT) _ �.23 GRAdUALLY VARIED FLOW PROFILE COMPUTED INF03�MATION: ----------------------------------------___-------------------------------_____-- PISTAt3CE FROM FLOW DEP'FH VELOCITX SPECIFIC PRESSURE+ CONTROL(FTf IFT} (F'T/SEC} F.NERGX(FT} MOMENTUM{pp�TNDS) O.D00 1.233 �7.525 6.005 1718.87 0.859 1.215 17.B83 6.183 1746.99 1.767 1.196 18.254 6.373 1780.47 2.740 1.17$ �8.640 6.576 1813.38 3.876 1.159 i9.042 6.793 �$47.80 5.056 1.14D 19.460 7.D29 �883.81 6.339 1.122 19.895 7.272 3921.50 7.74Q 1.103 20.349 7.537 1950.96 8.250 1.097 20.504 7.629 1974.51 ------------------------------------------------------------------------------- NODE 205.60 : HGL =< 309.713>;EGL= < 314.485>;FLOWLINE= < 3Q$.980> ..+��**��.��.+.**..*�****��*+***.*,�*.�.*.**++++*��.�..**�..+��*******�**+ FLOW PRpCESS FROM NQDE 205.b0 TO NODE 205.70 �S CODE = 2 UPSTRF.AM N017E 205.7D ELEVATION = 306.81 (FF,pW TS SUPERCRITICAL) --------------------------------------------------------------------_____------- CALCIJ�,ATE MANFi03.�E I�C}SSES (i,ACFCB} : PIPE FLOW = 48.04 CFS PIPE DIA�+IETER = 36.00 INCHES AVERAGED VELOCITY HEAD = 4.720 FEET • HMN =.05*(AVERRGED VELOCFTY HEP.Di =.a5*( 4.-rza� = a.236 NODE 205.7D : HGL =< 310.053>;EGL= < 314.72��;FLOWLINE= < 3D8.810> ' **�****t*+*+�+t***i.*i.ii+�+�*+r��,r*tit+t****w*+,r*x**i.**�*�+tx�*�i.Ww*tyrtttaw*,r** FLOW PROCESS FKOM NODE 205.70 TO NODE 205.80 IS CODE = 1 UPSTRSP.M NOD£ 205.84 ELEVATIDN = 317.13 {FLAW IS SUPERCRiTICAL} ------------------------------------------------------------------------------- CALCULATE FRICTION LOSSES(LACFCD}: PIPE FLAW - 9$.44 CFS PTP� DTAMETER = 36.QQ INCHES PIPE LENGTH = 69.QQ FEET MANNING'S N= 6.02200 230RMAL DEPTH (FT) = 1. 20 CRITICAL DEP`�'fi ( FT] = 2. 26 ___..-----------------------------------------_---__------------------------ iJPSTREAM CONTRQF, ASSLTMED �'E,OWDEPTH ( FT) = 2. 26 GRADUALLY VAFtTED FLOW PRpFILE COMPUTED INFOR�+3ATION: DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTR�L { F"I' } ( FT j ( FT / SEC j ENERGY ( FT ) MOMENTUM ( PO[F�TDS } 4.000 2.256 8.415 3.356 1142.47 0.015 2.214 8.561 3_358 1143.05 4.061 2.172 $.757 3.363 1144.B3 O.lA3 2.129 8.943 3.372 1147.86 0.264 2.087 9_140 3.385 ].�52.24 0.929 2.045 9.349 3.403 1157.99 0.692 2.003 9.570 3_426 1165.20 0.9�2 1.961 9.804 3.454 1173.96 1.245 1.914 1Q.052 3.489 1184.36 � l.fi5d 1.676 Z�.316 3.530 1196.49 2.138 1.634 I0.596 3.579 1210.46 . 2.723 1.792 10.894 3.636 1225.40 3.421 �.750 11.21i 3_703 1249.45 4.253 1.708 11.546 3.78a 126A.79 5.295 1.665 11.908 3.869 12B7.99 6.431 1.623 12.292 3.471 1312.75 7.857 1.561 12.703 4.088 13A0.86 9.582 1.539 13.142 4.223 1372.01 1L 695 1.497 13.614 4.377 �40b.46 14.320 1.455 14.i21 4.553 1499.51 17.656 �.912 14.667 9.755 1486.50 22.Q34 2.370 15.255 4.986 1532.81 28.073 1.328 15.691 5.252 1583.87 37.170 1.286 16.58D 5.557 164�.19 53.848 1.244 17.328 5.409 1702.36 64.00Q 1.243 17.333 5.911 1702.76 ----------------------------------------- NODE 20$.80 : HGL =< 319.386>;EGL= < 320.486>;FLOWLTNE= < 317.130> t**r*ssr*r*+ef++�*y+*i+�xx***w*t++***+***w*�+�.atir*a+*++*ww+xttt�+titi*xrt*�*xxx FLQW PROCESS FROM NODE 2D5.80 TO NODE 2Q5.80 YS CQDE = B UPSTREAM NODE 205.80 ELEVAT�ON = 317.13 {FLdW UNSEALS IN REACH) CALCfTLATE CATCH BASIN EN'I'RANCE LOSSESILACFCD}: PIPE FLpW = 48.00 CFS PIPE DIAMETER = 35.00 INCI-fES FLOW VEL4CITY = 8.42 FEET/SEC. VELOCITY HEAD = 1.1�0 FEET CATCH BASIN ENERGY LOSS =.2''fVELOCIT�' HEAD) _.2*( 1.1Dfl} = 0.22Q -------------------------------------- NODE 205.80 : HGL =< 32D.7Q6>;EGL= � 320.7D6�;FLOWLIidE= < 317.130> yr�.+i#****� k*iFi �k i*}***�' **i!*t**ik'k#1r *#'F Y Y i***Yr Yr�**i�i *�'tYi**�t***Yr*1� # Yc*Yri�k 4 fY***}Yr* . UPSTRF.AM PIPE FLOW C�NTROL DA�'A: NQDE NUMBER = 205.$0 FLOWLFNE ELEVA'i'30N = 317.13 ASStTMED UPSTREAM CON'I'ROL HGL = 319.39 FOR DDWNSTREAM RUN ANALYSIS END bF`GRAUUALLY VARIED FLC1W ANALYSIS � � * * * * * * * * * � * * # * * * * * � � w * 4 � � k Y � Y t * Y t # # i � 4 f w * * t # � * * * * * * � t � 4 � i * + * * # # i * * * * * * * * # f k i W i PTPE--FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Aeference: LACFCD,i�ACRD, At3D OCF.MA H7CDRAULICS CRITEFtION) (c1 Copyright 1982-2002 Advanced Engzneering Software {a�sj Ver. 6.4 xeJ.ease Date: Ol/Ol/2QQ2 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTANTS 701 'B' STREET, SUI3'E 800 SAN DIEGO, CA 92�01 619-235-6471 +*�+*+**+w************,r��* DESCRIPTION OF STUDY ***+*********+****"****wx* * BRESS� RP,NCH - ULTIMATE CONDITIONS * * SYSTEM 200 (PA-6) TOWN GARDEN DRIVE * * 100-YEAR * **�**ir**+**+++irt*tt++*w*��+++++*t*++t****+****+i+t**t�ri�**r�y�y,��w,rw*t��+�w FILE NAME: L200R.DAT TIME/DATE OF ST[JDY: 16:24 01/20/2003 ***+*++t�***,r***�*�*****�****��.,.**,.**�,.**�*�**�+****.******,.*�.************** GRADUALLY VARIED FLOW AI3P,I,YSIS FOR PIPE SYSTEM NODAL POINT STATUS TABLE {Note: '*" indicates nodal point data used.) UPSTREAM RUN DOWIVSTREAM R[]1�3 NODE MODEL PRESSURE PRE55URE+ FLOW PRESSUR�+ � NUMBER PROCE55 HEAD {�m ) MOMFNI'l7M f POUNDS ) DEPTH ( PT J MOMEId'I'S]M ( PpUNDS ) 20d_00- 9.22* 5203.87 1.34 4425.A1 ) FfiTC�'TON } HYDRALTI,�C .7CJMP 205.10- 2.78 Dc 2425.91 1.88* 2958.34 } JUNC'i`ION 205.90- 3.54 2308.10 1.51* 2933.41 } FR�CTION 210.D0- 2.68 Dc 2D18.66 2_03� 2241.93 } JUNCTIOIV 210.90- 3_46 1625.58 1.23* 2D08.02 } FRIC'T'IOI3 215.40- 2.29 Dc 1307.25 1.41* 17A4_24 } riANxOLE 215.90-- 2.29 Dc 1307.25 1.42* 1726.a5 } FRzc�rzorr • 22p.00- 2.29 Dc 1307.25 �.45* �b87.06 ) �3�UNCTION 220.90- 2.56 1213.62 1.29* 1659.76 } FRICTION 225.00- � 2.23 Dc 1156.18 1.60� 1351.27 } JUNCTION 225.90- 2.49 1489.21 1.42�' 1320.39 } FRiCTION 23D.40- 2.18 Dc 1454.64 1.52* 1245.53 ) JUNCTI�N 234.9Q- 2.73 971.28 1_15* 1223.89 ] FRICTiON 235.00- 2.Q4*Dc 841.37 2.44�"Dc 641.37 } JUNCTION 235.90- 2.38* 762.38 1.57 735.31 � } FRICTION } HYDRAULIC ,7UMP 235.91- i.93 Dc 714.67 1.70' 732.23 � ) FRICTION+SEND 236.40- 1_93rDc 714.67 1.93*Dc 714.67 ) ,TUNCTION 236.90- 2.64* 588.44 1.63 Dc 933.07 ) FRICTION+SEND 240.00- 2.84' 626.94 1.63 Dc 933.07 ) FRICTTON 240.I0- 3.03* 6b4.92 1.63 bc 433.07 ] JUNCTION 240.20- 3.51* b90.57 1.52 Dc 351.42 } FRICTFQN 240.41- 3.58* 7p2.66 �.16 387.59 } MAN�E�OLE 240.92- 3.27* 642.41 1.52 Dc 351.42 } FRICTION 240.45- 3.72* 730.65 1.52 Dc 351.42 ) CATCH BASIN 240.45- 4.32* 651.59 1.52 nc 109.70 ----------------------------------------------__--------------------_--___--__--_ MAKIMUM NUMBER QF �7ERGY SALANCES [35ED IN EACH PROFILE = 25 NOTE: STEADY FI�OW HYI7RAULIC HEAD-LOSS COMPUTATIONS BASED ON �`HE M05T CONSERVATIVE �D�MUi�AE FROM THE Ci7RRF..f+FT LACRD, LACFCD, AND OCEMA DESIGN MANUALS. i*Yr*�ktYrY� Y� * Y� k Yr * f h f!!r *�lrYril �k k*lYrYc�k ******'M't1� 1'k �"� ***Yi #Y� Y YYi*y��Jryr�Y# ti yr Yy�+iFY#i Y�k **t**�r* DOWI�STREAM PIPE FLOW CONFROL DATA: NODE NUrFSER = 2QQ.00 FLC�^TLI?�iE EL�IATTON = 2$b.18 PIPE FLOW = 81.00 CFS PIPE DIAMETER = 36.00 ZNCHES ASSUMED DOWNSTREAM CONTRQL HGL = 295.400 FEET ------------------------------------------------------------------------------ . NODE 200.OQ : HGL =< 295.400>;EGL= � 297.439>;FLOwE�INE= < 286.16D> k�F YrYrf * ** #** i� *1r* * *******i� * *!rM*i� * * ***'k*1y Y�k �k �k t1r**it * Y�* Y*Y tittY Y yr Y y�Y��l****#ir*ik1r'!r*yr FLOW PROCESS FROM NODE 2Dfl.40 Tp �10DE 205.10 IS CODE = 1 UPSTREAM NODE 245.1fl ELEVATION = 306.09 {I-[yDRAt7F,7C JUMP OCCi]R5] -------------------------------------------------------------------___--------- CALCULATE F�tICTIQN LOSSES(LACFCD}: PIPE FLOW = 81.00 CFS PIPE DIAMETER = 36.04 INCHES PIPE i�ENG'i'H = 183.68 FEE'�' MP.DiNING'S N = 4.Oi300 HYDI�AULIC �UMP: 1]OWI3STREAM RUN ANALYSIS RESULTS _____________________________�_..---------------------------------------------- NORMAL I?EPTH ( F'T ) � 1. 2 fi CRE'FICAL DEPTH { FT }= 2. 7 B ------------------------------------------------------------------------------ -----_____--____---------------.._�___------------------------------------------- UPS�`RE.AM CONTROL ASSUMED FLOWDEPTH(F'i'} - 1.88 __---------------------------_-------------------------------------------------_--_ GRADUALLY VARIED FLOW PROFILE COMPUTED TNFpRMATIQN: DISTANCE FROM FLOW DEPTH VELOCI'i'Y SPECI�zC PRESSi3RE+ CONTROL(FT} (FT) IFT/SEC} ENERGY(FT) M�MENTL73�7(POL7NDS} D.000 1.885 17.319 6.595 295B.34 1.549 L 850 17.59}� 6.668 2993.94 3.223 1.835 17.874 6.799 3031.21 5.432 1.810 18.167 6.938 3070.23 6.94i 1.7$5 18.471 7.086 3117.06 9.117 3.760 18.786 7.243 3153.80 1�.428 1.735 19.113 7.411 3198.53 13.948 �.710 19.453 7.590 3245.34 16.700 1.585 19.806 7.78D 3249.33 : 19.717 1.660 20.173 7.983 3345.51 23.035 1.635 20.554 8.199 3349.28 � 26.699 1.610 20.950 8.430 3455.47 34.763 1.585 21.363 8.577 35�4.31 35.295 1.560 21.793 8.94D 3575.94 90.381 1.536 22.240 9.221 3644.49 96.131 1.511 22.707 9.522 3708.15 52.691 1.486 23.194 9.844 3779.06 6d.258 1.451 23.701 10.189 3853.43 69.110 1.436 24.232 10.559 3931.45 79.651 1.411 24.786 10.456 4d�3.33 92.513 1.386 25.366 11.383 4499.31 1a8.749 1.351 25.972 11.842 4189.64 130.340 1.336 26.607 12.336 4284.59 161.733 1.311 27.273 12.868 4389.46 193.680 1.3fl1 27.546 13.�91 4425.41 HYD3tAULIC J1R3P: UPSTREAM RUAI AT7ALYSIS RESULTS DOWNSTREA.M COPFTROL ASSUMED PRESSURE HE.�II(F'F`) = 9.22 ' ------------------------------------------------------------------------------ ---------------------------------------------------------------------- - ------ PRESSLTRE FLOW PROFILE CO�SPUTED INFORMATION: DISTANCE FROM PRESSiiRE VEI.�OCTTY SPECTFTC PRESSURE+ CONTROL {�'T } HEAD f FT } ( FT / SEC } EI+�ERGY ( FT 1 FfOMEN�'CTM f POUNDS ) 0.000 9.22D 11.459 11.259 5243.87 66.420 3.000 11.459 5.039 2960.35 ASSiJ�fED DOWIQS'i'REAM PRESSURE HEAD(FTy = 3.00 ------------------------------------------------------------------------------- ------------------------------------------------------------------------------ GRADUALLY VARIED FLOW PROFILE COMPi7TED INFORt�SATION: ------------------------------_-------------------------___-___-____..r_...._----- • DISTA23CE FRQM FLOW DEP'FH VELOCI'PY SPECIFTC PRESSUA�+ CONTROLiFT) IFT) (FT/SEC} E[$iERGY{�} MOMENTUM(POUNDS} 66.420 3.OD0 11.456 5.039 24GQ.35 66.542 2.991 11.959 5_D31 2456.94 66.574 2.982 �Z.969 5.029 2453.94 b6.640 2.974 11.472 5.018 2451.20 56.701 2.965 Z1.480 5.013 2448.68 b6.756 2.956 �1.990 5_007 2496.34 66.8Q8 2.947 11.5Q1 5.OD2 2444.17 66.857 2.938 11.5i3 4.998 2442.16 66.901 2.929 11.526 4.943 2440.29 6fi.943 2.92�. 11.539 4.989 2438.55 66.981 2.912 11.554 4.986 2436.95 67.017 2.903 11.569 4.982 2435.A6 67.050 2.899 1]..585 4.979 2434.10 67.060 2.BB5 11.601 4.976 2432.85 67.107 2.B76 11.619 4.974 2431.71 67.132 2.Bb8 11.636 4.971 2430.b8 67.154 2.859 11.655 4.9b9 2429.76 57.179 2.850 11.674 4.967 2428.94 b7.39� 2.$4� 11.fi94 4.966 2428.22 67.2p6 2.832 11.71A 4.964 2427.60 67.219 2.823 I1.735 4.963 2427.d8 67.229 2.815 �1.7�7 4.962 2425.66 67.237 2.806 1�.779 4.961 2426.33 67.243 2.797 11.801 9_961 292b.10 67.246 2.788 11.824 9.960 2925.95 67.247 2.779 11.848 9.96D 2925.91 183.6B0 2.779 11.848 4.964 2925.91 . ------------END OF HYDRAiJE�IC JUMP ANALYSIS------------------------ � � PRESSL3RE+MOMEN'Pi7M BALANCE OCCURS AT 19.74 FEET UPSTREAM OF NODE 200.00 � � I-_-----DOWNSTREP.M RBPTH = 7.372 FEET, UPSTREA�1 CONJllGATE DEPTH = 1.310 FEET � NODE 205.10 : HGL =< 307.975>;EGL= < 312.635>;FLOWLINE= � 306.490� i*++***�**+*+rt+*tr++**x*x**ftt*t*+*��t*��ay**+r��+***�++***+*�++*�*��*t****+ww FLQW PROCESS FROM NODE 2�5.10 TO NODE 205.94 IS CODE = 5 UPS7''REAI� NODE 2D5.9Q ELEVATION = 346.42 (FLOW i5 SIiPE}tCRITZCAI�) CALCULATE JUNCTION LQSSES: PI�E FLOW DIAMETER ANGLE FLOWI�INE CRITICAL VELpCITY ( CFS ) ( II3CHES ) ( DEGREES } ELEI7AT�ON DEP'F'H ( FT . ) ( FT/ SEC ) UPSTRF�RM 7L 7Q 36.00 O.DO 306.42 2.68 20.082 DOWNSTREAM B1.00 36.00 - 306.09 2.78 17.324 I�AT£RAL �kl 5.40 36.OD 90.aa 306.92 0.79 1.761 LATERAL �2 2.90 1B.00 94.�0 307.92 0.65 3.976 Q5 0.00===Q5 EQUALS BASIN IIdPUT=== LACFCA P.ND OCEMA FLOW JLFNCTION FOR�7iTLAE USED: DY={QZ*V2-Q1*V1"COS(DELTA1i-Q3*V3"COSf�ELTA3)- Q4*V4'COS{DELTA4J}/((A1�+A2)*16.1j+FRICTION L055ES UPS3'REAM: MAN�IING'S N= O.a1300; FRICTION SLOPE = 0.04499 DOWNSTREAM: MAt3�IING'S N= 0.41300; FRICTION SLpPE = 0.02896 AVERAGED FRIC'i'ION SLOPE Ii�I JUNCTION ASSUMED AS 0. D3672 �iTNCTION LEPiG'i'H = 4.04 FEET FRTC'i'ION LOSSES = fl.147 FEET ENTRANCE LOSSES = 0.040 FEEi' JUNCTION LOSSES = (1�Y+HV1-HV2)+SENTRANCE LOSSES} J[7NCTION LOSSES =( 1.559?+! a.Q00) = 1.559 NODE 205.90 : HGL = � 307.932>;EGL= � 3�4.194>;FLOWLIAiE= < 306.420> • ****.+.*.*+..,....**��,.�.*«*.*....*...��+*��..+.*.+�*+*�.***.*.....��+******.*„ FI.OW PROCESS FftOt�4 fVODE 2 0 5. 9 0 TO NODE 210 . 0 0 I S CflDE = 1 UPSTREAA7 NODE 210.00 ELEVATION = 312.03 (FLOW IS SUPERCRx`I'ICAI,) ------------------------------------------------------------------------------- CALCTJF�A�'E FRICTIOEV LOSSES (LACFCD) : - PIPE FLOY7 = 71.70 CFS PIPE DIAMETER = 36.40 INCHES PIPE F..F.I+7GTH = $8 . 13 FEET MP.NNiNG' S N = 4. 013D0 ------------------------------------------------------------------------------ NORMAL DEPTH{FTf = 1.37 CRITICAL DEPTH{FT) = 2.68 UPSTRF�t4 CONTgOL ASSUMED FLOWDEPTH(FT) = 2.03 GRADUALLY VARIED FLOW PROFILE COMPUTE)J INFORl7ATTON: I7ISTANCE FROM FLOW DEPTH VELOCI'i'Y SPEC�FIC PRESSURE+ CONTROL(FT) ;FT} (FT/SEC) ENERGYIFT) MOMENTUM(POi1NDS} a.00a 2.028 14.D97 5.115 2247..93 1.950 2.002 14.306 5.18� 2262_72 3.d52 1.975 14.523 5.252 2289.71 4.788 1.949 14.749 5.328 2347.96 6.585 1.922 19.982 5.4i0 2332.51 8.759 1.895 15.225 5.498 2358.41 11.031 1.869 15.477 5.591 2385.73 13.523 1.893 �5.739 5.692 29i4.52 16.264 1.817 ib.010 5.799 2494.66 19.265 1.790 15.293 5.915 297b.80 22.525 1.764 16.5$7 6.438 25�0.43 26.332 1.737 16.892 6.17J. 2545.B3 30.464 1.711 17.210 6.313 2583.07 • 35.091 1.684 17.541 6.465 2b22.26 40.306 1.658 17.685 6.628 2563.49 � � • 96.224 1.632 18.245 52.999 1.6a5 16.619 54.840 1.579 19.010 70.D41 1.552 19.417 81.029 �.526 19.843 88.134 i.512 20.076 6.809 270b.86 6.992 2752.49 7.149 2804.51 7.411 2851.03 7.649 2904.2Q 7.774 2933.91 ------------------------------------------------------------------------------ NpDE 214.00 : HGL =< 314.05B>;EGL= < 317.145>;FLOWi��NE- < 312.430> # Y***# * f i. i�f ##yri *#iY.?i1 i Y� *�M i. i i� i#}}if 1�kf Y#Y Y i i*�r *tYi *ir �* i*t Y t**t # t##1 �k f**#!*! t***�k FLOW PROCESS FROM NODE 214.D0 TO NODE 210.90 IS CODE = 5 U1'STREAM NQBE 210.90 ELEVATION = 312.53 {��,QW xS SUPERCRIT�CAS.�} CAI.CI3LATE JiJNCT10N LOSSES : PIPE �'LOW D�AME'TER ANGLE FiOWLINE CRITICAL VELOCI3'Y SCFS) (INCHES) (D�GI2EBS1 ELEVATION DEPTH{FT.i (FT/SEC) UPSTREAM 49.00 30.OD 0.00 312.53 2.29 20.318 DOWNSTREAM 71.70 36.00 - 312.03 2.b8 19.10Z LATERAL #1 22.70 30.00 6D.�0 312.53 1.52 6_740 LATERAL #2 D.04 0.4a O.OD O.OQ 0.40 0.000 Q5 O.flO===QS EQUALS BASIN IPIPUT=== LACFCA AND OCEMA �'LOW JUNCTIpN FORMUi�AE iiSED: DY=I4�*v2-41*V1*COS(DEI,TA1}-Q3*V3*C05(DEi,TA3}- Q4*V4*COSIDELTA4})/{{A1+A2)*16.1)+FRICTION LOSSES UPSTREAM: MANNING'S N= Q.013D0; FRICTION SLOPE = 0.059$3 DOWNSTREAM: MANNING'S N= Q.Q1300; FRICTTON SLOPE = O.Q1810 AVERAGED FRICTION SLOPE YN JUNCTI�N ASSIJrSED AS O.D3897 JUNCTION LFNGTH = 4.00 FEET FRTCTION LQSSES = 0.156 FEET ENTRANCE L055ES = 0.000 FEET JUIdC'T'�QN LQSSES = (DY+HVI-HV2]+(ENTRA.NCE LOSSES) �L7NCTIQN LQSSES =( 3.02$}+( 0.000) = 3.028 NODE 214.9Q : HGL =< 313.763>;EGL� < 32D.173>;Fi,OWLINE= � 312.530> *�.**t�.*********+**.�+�******..**,...�*.+�..�.+..f�.*�++�.++�+*++�++f�**��.,..t** FLOW PROCESS FROM NODE 210.90 TO NQDE 215.00 TS CODE = 1 UPSTREAM NODE 215.OQ ELEVATION = 32$.51 (FIAW �S SUPERCRITTCAL} ------------------------------------------------------------------------------ CALCULA'T'E FRICTION LOSSES{LACFCD}: PIPE FLOW = 99.44 CFS PIPE DIAMETER = 30.00 INCHES PIPE LLNGT}i = 261.88 FEE'I' MANNING'S N= 0.01304 ?dORMAI, DEPTH(FT} - 1..23 CItIT�CAL DEPTHIFT) = 2.29 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------ UPSTREAi�3 COid'I'ROL A55UMED FLOWDEPTH ( FT) = 1. 41 GAAL)UALLY VARIED FLOW PROFILE COMPUT�D If�TF'ORMATIQN: ------------------------------------------------------------------------------ DISTA�FCE FROM FL,OW DEPTH VELOCI'i'Y SPECYFIC PRESSURE+ CONTRpL ( FT ) ( FT } { FT / SEC } E13ERGY ( ET } MOMENTUM { ppTJNi}S ) 0.004 1.405 17.23'7 6.022 I749.24 2_339 1.398 17.34b 6.D73 1753.31 4.809 1.391 17.957 6.12b 27b2.52 7.407 1.384 17.558 6.179 1771.88 �Q.160 1.377 17.682 6.239 178�.39 13.d78 3.3b9 17.'19b 6.294 �792.66 16_178 1.352 17.913 6.348 1800.88 19.481 �.355 78.031 6.4Db 1810.66 23.010 1.348 18_15a 6.466 1821.01 26.792 1.341 18.271 6.528 1831.31 � 30.86Q 35.256 90.D26 95.232 50.95D 57.279 64.347 72.330 81.474 92.13B 104.880 12D.634 141.153 170.374 220.929 261.880 1.334 1.326 1.3I9 1.3�2 1.3D5 1.298 1.29Q Z.283 1.276 1.269 �.262 3.255 3.247 1.240 1.233 �.233 18.394 18.519 1B.59� 1B.773 18_943 19.D35 19.1b9 19.304 19.442 19.582 19.723 19.&67 20.Q12 20.16Q 20.31D 20.312 6.591 6.655 6.721 6.786 6.857 6.927 7.000 7 .074 7.149 �.227 7.30b 7.367 7.474 7.555 7.692 7.693 1841.74 1852.44 1863.26 1874.26 1885.43 1B96.8fl 1908.34 1920.08 1932.41 1944.19 1956.97 1969.00 1981.75 1994.70 20fl7.87 2008.Q2 -----------------------------_�-__----__--_______-------------------------------- NODE 215.00 : HGL = t 329.915�;EGL= < 334.532>;FLOWLINE= � 32$.510> *+*�*+..*.*.*.�w�t�****...****«��..**.**,..w..*.***��+�..*.*..****�+*.*+***�* FLOW PROCESS FAOM NODE 215.00 TO NODE 215.90 I5 CpDE = 2 UPSTREAM NODE 215.90 ELEVATIQN = 326.84 (FL4W TS SUPERCRI3'ICAL) ------------------------------------------------------------------------------- CALCUI.ATE MANHOLE LOSSES(LACFCD}; PIPE FLOW = 49.Ob CF5 PIPE DIAME'£ER = 34.00 INCHES AVERAGED VELOCITY HEAD = 4.558 FEET I-II�I = .45* (AVERAGED VELOCTTY HEAL7j = .05' ( 4.558) = 0.228 NOiiE 215.90 : HGL =< 33Q.260�;EGL= < 339.760>;FLOWLIbIE= < 328.84D> . *+.***�+��,++*++++++.**.*�..******...*+****.�.�.****+*...��+�*f+....**....<.,..x�+ FI,pW PROCESS FROM NODE 215.90 TO NOBE 22Q.00 IS COiiE _� UPSTREA1�fI30DE 224.00 ELEVATION = 338.10 (FLOW IS SUPERCRITIC}�L) ------------------------------------------------------------------------------ CALCULATE FRICTION L05SES{LACFCD): PIPE FLOW = 49.DQ CFS PIPE DZAkiETER = 30.04 INCHES PIPE LENGTH = 246.p0 FEET MANNING'S N= 0.01300 C � --------------------------------------------------------------------------__--__ NORM.�I, DEPTH(F'T') = 1.42 CRITICAL DEPTH(FT} - z.29 UPS�'REAM CQNTROL ASS4JMED FLOWDEPTH(FT) = 1.95 GRADUALE�X VARIED FLOW PROFILE COMP47TED INFORMA`i'IpN: ------�----------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SP�CxFIC PRESSURE+ CONTROL ( FT J ( Fi' ) i F'i' / SEC 1 ENERGY ( FT } MOMFNTUM { pOiJFIDS } 0.604 1.454 16.544 5.705 1687.05 3.123 1.452 1fi.563 5.715 1688.63 6.386 1.451 16.582 5.723 1690.22 9.801 1.449 16.602 5.732 169�.82 13.382 1.448 16.621 5.740 1693.40 17.145 1.447 16.641 5.749 1695.00 21.110 1.945 16.6b0 5.758 1b96.60 25.297 Z.A44 16.580 5.767 1598.21 29.732 1.942 16.700 5.'175 �b99.82 39.445 1.441 35.719 5.784 1701.44 39.473 1.440 16.739 5.793 1703.46 99.859 1.438 16_759 5.802 1704.b9 54.655 1.437 16.779 5.813 1706.33 56.926 1.435 16.799 5.B2Q 17D7.97 63.761 L 439 16.619 5.829 1709.fi� � 71.260 1.433 i6_839 5.838 1711.26 79.566 1.431 1fi.859 5.847 1712.91 88.B71 1.430 I6.879 5.856 1714.57 99.440 1.426 16.899 5.866 1�16.24 111.656 1.427 16.920 5.875 1717.91 126.155 1.926 16.940 5.884 1719.5B 143.923 1.424 16.960 5.894 1721.26 166.876 1.423 16.981 5.903 1722.95 199.238 1.421 17.001 5.912 1724.64 246.000 �.42D 17.018• 5.920 1726.06 ------------------------------------------------------------------------------ NODE 220.00 : HGL =� 339.554>;EGL= < 343.SQb>;F�OWLxt,i�= < 338.100> *****�w*�x�*��*****#�**��*ww.***w��**+***.****************��.*��**��**�*. FLOW PROCESS FROM NODE 220.00 TO NODE 220.90 Y5 CODE = 5 UPS�REAM NODE 220.90 ELEVATION = 338.43 {FLi?W IS SUPERCRITICAL) ------------------------------------------------------------------------------ CALCULATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FI�OWLINE CRITICAL VELpCITY (CFS) {INCHES) (DEGREES) ELEVATION DEPTH(FT.} (FT/SEC1 UPS'FREAt� 45.40 3D.D0 D.40 338.93 2.23 ].7.816 DOWNSTR� A9.00 30.OQ - 338.10 2.29 16.549 LATER,AL #1 3.6D 18.00 45.00 339.10 0.72 4.260 LATERAL #2 0.00 0.00 D.00 0.00 0.00 Q.4Q0 Q5 O.aO===QS EQUALS SASIN INPUT=== LACFCD ANB OCEMA FLOW JUNCTION FORMUl.AE USED: ' DY=(Q2*V2-Q1*V1'COS{DELTAl}-Q3*V3*COS(DELTA3)- Q4*V9*COSSDELTA4}}/((Al+A2j*16.1)+FRICTION LOSSES [TPSTREAM: MAid�]ING'S N= O.D�300; FRICTION SLOPE = 4.04436 . DOWNSTREAM: MAi3i+7ING'S N= 0.0�3aD; F3tICTYON SLOPE = 0.03465 AVERAGED FRICTTON SLOP� �N JUNCTION ASSUMED AS 0.0396Z JUNCTZON I�FNGTH = 4.DD F�ET FRICTIQN i,05SE5 = 0.158 FEET ENTRPNCE L05SE5 = O.ODO FEET ,NNC'i'ION �,05SES = (DY+1-EV1-HV2 ) + ( ENTRAIVCE LOSSES) , JLTNC3'ION F�OSSES =( 0. 841) +( a. 000 )= 0. 841 ------------------------------------------------------------------------------ NODE 220.90 : HGL =< 339.717>;EGL= < 344.647>;FI,OWLINE= < 338.430> ****+�Ww.+*.�.�w.�+*++�+.w++�+�+*++++�++**++*+.t*+***..k+**,..*****�.*+*****.�.. FLOW PFtpCESS PROi4 NODE 2 2 D. 9 0 TO 230D£ 2 2 5. 00 I S CODE = 1 UPSTHEAM R30DE 225.00 E�,EVATION = 35D.49 {FL(3W I5 SUP£RCRITICAL) CAT,CUI.ATE FRICTZON LOSSES SL�AC�'CD} : PIPE FLOW = 45.40 CFS FIPE DIAMETER = 30.Q0 INCHES PIPE LEidGTH = 263.00 FEET t+IANNING'S N = 0.01300 NORl�1AL DEPTH ( FT) = 1. 27 CRZT�CAL DEP'I'f3 ( FT) = 2. 23 UPSTREAM CONTROi, A55UMED FLOWDEPTHfFT) = 1.6a ---------------------------------------------_--__--_------------------------------- GRADUAZ.LY VAR�ED �'LOW PROFTLE COMPUTED INFORMATION: DI5'FANCE F'ROM FLOW DEPTH VELOCZTY SPECTFIC PRESSURE+ CONTRpL ( FT } S F'I' } { F`F / SEC } ENERGY ( FT i MOMENTUM I pOli13D5 ) O.OQ4 1.595 13.725 4.522 1351.27 1.B50 1.583 13.$59 4.565 1360.02 3.824 1.570 13.98fi 4.609 1369.04 5.933 1.557 14.121 4.655 1378.34 . $.190 1_544 14.259 9.703 1387.93 10_510 1.531 14.4D0 9.753 1397.82 � s • 13.214 16.411 19.Q36 22.313 25.875 29.763 34.026 38.724 43.936 49.760 5b.328 63.815 72.471 $2.659 94.943 134.268 13q.406 �59.337 249.834 263 . fl00 1.519 1.506 1.493 1.4B0 1 .467 1.454 1.442 1.429 1.416 1.403 1.390 1.3�7 1.365 1.352 1.339 1.326 1.313 1.300 1.288 1.287 14.595 14 . 692 14.843 14.99$ 15.�56 15_3�7 15.483 15.b52 15.826 16.003 i6.185 16.371 16.562 �b.757 Zb.957 17.162 �7.373 �7.568 17.809 17.B13 4 4 4 4 5 5 5 5 5 5 5 5 5 5 5 5 6 5 b 6 805 860 916 975 036 1D0 166 235 307 382 46Q 542 626 715 807 9D3 003 107 216 2i7 }.908.02 1418.53 1429.36 144D.51 1452.01 1463.85 �.476.05 1488.62 1501.57 1514.93 1528.54 1542.79 155'1.37 1572.3$ 1587.84 1603.77 1620.17 1637.47 1654.99 1654.76 NODE 225.00 : HGL =< 352.D85>;�GL= < 355_012>;FLOw�FNE= < 350.99D> .*.*......�*y�.*t****+xx*x*�*.,,.*.**.....**,.**..,..****+�**�*..w.�**w*.�*�ww*.�w FLpW PRpCESS F1�OM NODE 225.Q4 TO NODE 225.90 IS CODE = 5 UPSTREAM NODE 225.90 ELEVATION = 350.82 (FLOW TS SUPERCRITICAI,j --------------------------------------------------------_--_-------------------- CALCLTLATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE PLpWLTN� CRITICAL VELOCITY (CFS] {INCHES? i1»GR�ES) ELEVATION DEPT}3(FT.} {FT/5EC) i7PSTREAM 42.40 30.OD p.DU 350.82 2.18 14.737 DOWNSTREAM 45.4D 30.00 - 350.49 2.23 13.729 LATERAL �kl 2.25 18.04 90.04 351.82 b.57 3.679 LATEAAL #2 0.75 18.00 90.Oa 351.82 D.32 2.458 ¢5 O.OD===QS EQUALS BASIN INPUT=== �ACFCD P.ND OCEMA FLOW JUNCTION FORMULAE USED: DY=SQz"V2-Q1*Vi*COSfDEL�'A1)-Q3*V3*CpS(DELTA3)- Q4*V4*COS{DELTA4})/{{p,�+A2}*36.1f+FitICT10N LOSSES UPSTREAM: MANNICdG'S rr = o.o�3aa; FRICTION SI,OPE = 0.02$12 DOWNSTREAM: MANNING'S N= 0.0�340; k'RICTIOAi 5J�(7PE = 0.0225$ AVERAGED FRICTION SLOP� IN JUNCTION ASSUMED AS Q.02535 JUNCTIO�I LENGTH = 4.00 �'EET FRICTION LOSSES = Q.lal FEET ENTRAI3CE LOSSES = 0.000 F'EET ,TUNCTION LQSSES = (AY+HV1-HV2)+(ENTRANCE LOSSES} JUNCTION LOSSES =( 0.6001+( 0.000} = 4.600 NODE 225.9fl : HGL =< 352.24fl>;EGL= < 355.612>;FLOWLTNE= < 350.$20> **iFlrYriFiF*f**Y�ki***t**Y1itYf Yik�Y*+Y�kYY t �iiii�r iyr+f �*}*#*##Y�Yr�k�kk�kkkl�kir*yr#* *# #*lrkyr*iFf FLOW PROCESS FRQM NODE 225.90 Tp NODE 23Q.D4 IS CODE = 3 UPSTREAM NODE 230.pD ELEVATION = 357.29 {FLOW �S SUPERCRITICAL) ---------------------------------------------------------------------___________ CALCULAT� FRICTION LOSSES(LACFCD): PZPE FLOW - 42.40 CFS PIPE DIAMET'ER = 30.00 INCHES PIPE LENGTH = 227.76 FEET MANNING'S N= D.01300 -------------------------------------------------------------------------------- N4RMP.L DEPTH{Ffi} � 1.4] CRITICAL DEPTH(FT} = 2.18 UPSTREAA'S CONTRQL ASSUMED FLOWDEPTH{FT} = 1.52 . GRADUALLY VARIED FLOW PROFILE COMPUTEI7 INFOI2NFATIQN: DISTANCE PROM FL4W DEP'I'H VELOCITY SPEC�F�C PRE5Sl3RE+ CdNTROL(FT) (FT) (FT/SEC} EI3ERGY;F`I`) MOMENTUM(POUND51 D.Q40 1.517 13.6D1 4.391 1245.53 2.547 1.513 23.644 9.405 1248.32 5.425 1.509 13.688 4.420 1251.14 8.397 1.505 13.732 9.435 1253.99 11.927 1.501 13.777 4.450 1256.87 14.679 1.497 �3.822 4.455 1259.77 18.�21 1.492 13.867 4.480 1262.71 21.775 1.486 13.913 4.496 12b5.67 25.bb4 1.484 13.958 4.512 1268.67 29.81b 1.480 14.445 4.52B 1271.69 34.267 1.476 14.051 4.544 1274.75 39.057 1.472 14.098 4.560 1277.83 44.236 1.466 ].4.145 4.577 1286.95 49.868 1.464 14.�93 4.594 1284.10 56.031 1.460 14.241 4.611 1287.27 62.827 1.456 14.289 4.628 1290.48 70.389 1.452 14.337 4.646 1293.72 78.849 1.448 14.3$5 4.663 1297.p0 88.609 1.444 14.936 4.661 13QQ.30 99.893 1.939 14.485 4.704 1303.64 1�3.325 1.935 14.535 4.718 1307.01 129.873 1.431 ].4.586 4.737 1310.41 351.346 1.927 ].4.637 4.756 1313.85 181.613 1.923 14.688 4.775 1317�.32 227.760 1.42a 14.733 4.792 132Q.39 --_--_--_-_------------------------------------------------------___...._--__-------- • NODE 230.00 : HGL =< 358.807�;EGL= < 361.581>;FLdWl,INE= < 357.290> .�**�,..,*******,.*�x*x***.***+***t��..��***::�***�*.*.***.***....*.�*,.****f+++.�.� FLOW PROCESS FROM NODE 230.00 TO NODE 230.9Q IS CODE = 5 UPSTRF�IM NODE 230.90 EI,EVATIOI3 = 357.62 (Fi�OW IS SUPERCRITICAi) ------------------------------------------------------------------------------ CALCULATE JUNCTION LOSSES: PiPE FLOW DYAMETE32 ANGLE FLOWLINE •CRI'PICAL VELOCITY {CFS} (INCHES) (DEGREES} EI,EI7ATION DEPTI-i{FT. ) (FT/SEC} UPSTREAM 36.20 3a.Q0 4.00 357.52 2.44 16.504 DOWNSTREAM 42_40 30.Q0 - 357.29 2.18 13.605 LATERAL �}1 5.20 I8.00 90.00 358.62 Q.96 5.177 LATEFtAL #2 0.00 � 4.QQ 0.00 4.00 o.aa 0.000 Q5 fl.00==�¢5 EQUALS BASIN INPUT=== i,ACFCD P.ND OCENL� FI.,OW JUNCTION FpFtP4[.iLAE iiSED: DY=(Q2*V2-Q1*V1*COS(DELTAI)-Q3*V3*C05{DELTA3}- Q4*V4*COS{DELTA4)�/((A1+A2)*16.1)tF'RIC'I'TON L055ES UPSTREAt7: MANNING'S N= 0.41300; FRICTION SLOPE = 0.04213 DOWNSTREAM: MANNING'S N= 0.41300; FRICTION SLOPE = a.02288 AVERAGED FAICT�pN SLOPE IN 3UNCTION ASSUMED AS 0.03251 JUNC'FION LENGTH = 4.00 FEET FRICTION LOSSES = 0.130 FEET ENTRANCE �055ES = 0.000 FEE'� JUNCTION LQSSES = (DY+HV1-HV2J+(FNTRANCE LOSSES) JUNCTION LC355E5 = i�.3141+( 0.000} = 1.319 t�70DE 230.90 : HGL =< 356.765>;EGL= < 362.995>;FLOWLINE= < 357.620> *..w�*+.�*�**...*..�.��...�.+ti�**.�.+*..�*��.*.�>.�«.......*>...*.�*t.**.*x�* • �'LOW PROCESS FROi�] NODE 230.90 TO NODE 235.00 I5 CODE = 1 UPSTREAM NODE 235.04 ELEVAT�ON = 36fi.35 IFLOW IS SUPERCRI'�ICAL} . ------------------------------------------------------------------------------ CAI�CUI�ATE FRZCTION LOSSES(LACFCD) : PIPE FLOW - 35.20 CF5 PIPE DIAMETER = 3Q.D0 I13CHE5 PIPE LE�7GTH = 184.76 F�ET MANNING'S N= 0.0134d NORMA.L DEPTH(FT) = 1.11 CRITICAL DEPTH(FT) = 2.04 -------------------------------------------------- -----__-__--_-___---__------- UPSTREAM CONTROL ASSUMED FLOWDEPTH(k'�') = 2.04 GRADl3ALLY VARIED FLQW PFtOFILE COMPUTED �NFOfLMATIpN: ____________________...._________.._____________--_-..---------------------------- DISTANCE FROM FLAW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL { F'I` ) { FT � ( FT / 5EC j ENEFtGY { FT } MOMIIdTUM ( POi7NDS ) 0.400 2.040 8.439 3.146 841.37 4.090 2.D03 8.586 3.1.�8 841.79 4.�69 1.965 $.742 3.153 843.05 0.38� 1,928 8.908 3.}.6i 845.19 0.700 1.891 9.085 3.173 848.25 ]..133 1.854 9.273 3.190 852.28 1.692 1.B16 9.473 3.211 857.32 2.395 1.779 9.685 3.237 863.42 3.259 1.742 9.910 3.268 87D.65 4.30$ 1.705 1Q.150 3.305 879.07 5.569 1.6b7 10.404 3.349 8B8.75 7.074 1.630 14.675 3.40Z 899.77 8.666 1.593 10.963 3.464 912.22 10.996 1_55b }.1.270 3.529 426.20 13.528 1.518 11.597 3.608 441.81 16.549 1.981 11.947 3.699 459.37 • 20.17D 1.944 12.320 3.802 978.91 29.544 1.4Q7 12.719 3.920 999.70 29.SB6 1.37a 13.146 4.D55 1�23_20 36.511 1.332 13.605 4.208 1049.09 44.911 1.295 14.098 4.383 ��77.59 55.910 1.258 14.628 4.583 1108.95 73.055 1.221 15_200 4.810 i193.45 93.824 t.183 15.818 5.071 �181.4Q 135.384 1.146 16.487 5.370 3223.16 184.750 �.145 16.499 5.375 Z223.89 -----------------------------------------------------------------_______------- NODE 235.00 : HGL =� 366.390>;EGL= < 369.496>;FLOWLINE= < 366.350> :t+*rs*+++t*+**tt*tt++**y.�**rt**rtr*tyYtss*r*r***,rs***�rf+*��*+�+x+*****s++*fi.t�+ FLOW PROCESS FRQM 330DE 235.00 Tp NODE 235.9D IS CODE = 5 UPSTREAM 3�]ODE 235_90 ELEIIATIQN = 366.68 (FT,OW i5 SUBCRITICAL) CALCUL.�TE JUNCTIpN LpSSES: PIPE FLOW DIA.METER ANGLE FLOWLINE CRITICAL VELOCITY (CFS} {�NCHES) (DEGREESy ELEVATION QEPTH{FT.) (FT/SECi UPSTREAM 32.24 30.00 0.00 366.66 3.93 b_6B2 IJOWNSTREAM 36.20 30.00 - 366.35 2.D4 8.442 LATERAL #� 4.00 18.00 90.00 357.35 d.77 2.359 LATERAL #2 0.00 0.00 0.00 O.OD 0.00 0.000 Q5 O.Qp===QS E4UALS BASxN INPUT=== 31ACFCD A�iD OCEMA FLOW Ji.iNCTION FORMULAE USED: DY=(Q2*V2-Q1*V1*COS(DELTAI)-Q3*V3*COS(DELTA3}- Q4*V4*COS(DELTA4}f/((A1+A2)•15.�)+FRECTION Lp$SES UPSTREAM: N3ANNING'S N= 0.01300; FRiCTION SLOPE = Q.00539 � DOwNSTREAM: MA23NING'S N= 4.01300; F'RICTION SI�OPE = 0.00785 AVERAGED FRICTION SLOPE IN JUNCTTON ASSUMED AS 0.0066D • JUNCTION LENGiH = 4.00 FEE� FRICTION LOSSES = d.026 FEET ENTRAI3CE LOSSES = 0.000 �EET JUNCTION LOSSES = (DY+HV1-HV2j+(ENTRANCE L05SE5} JUNCTION I,OSSES = 1 0.254)+( a.OD01 = 0.254 NODE 235.90 : HGL =< 369.057>;EGL= < 369.754>,FLOWLINE= < 366.680> ��*.*.«*�.**..*+f+*��*.......*.,+**�.,..w++*�.*�+�*��....�*,.�.��t�t.,�*+w.�.+,*� FLOW PROCESS FROM NpDE 235.90 i'O NODE 235.9� E$ CODE � 1 UPSTREAM NODE 235.91 ELEVATION = 357.32 {HYDRALTLIC JUMP OCCURS) -------------------------------------------------_----------------------------- CALCULATE FRICTIOPi LOSSES(LACFCD): PIPE FLOW = 32.20 CFS PIPE DIAMETER = 30.00 iNCHES PIPE LENGTH = 63.64 FEET MANNING'S N= O.Q13Qp ------------------------------------------------------------------------------ HYDRAiII,,IC JUMP: DOWNSTRE.�h4 RUN ANALYS�S RESULTS -----------------------------------------___-_____----------------------------- NORMAL DEPTH{FT} - 1.57 CRITICA.L DEPTH(FT) = 1.93 iIPSTRF,IIM CONTRQi, ASSIJME�7 FLOWAEPTHfFTI = 1.7D `A'^ ' T -------------------- GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: D�Si'ANC� FROM Fi,OW DEP'FH VELOCITY SPECIFIC PRESSURE+ CON'I'ROI. ( FT j ( FT ) ( FT / SEC � ENERGY ( FT ) MOMEN'i'UM { POiJAiDS } �.000 1.699 9.063 2.975 731.23 1.731 1.697 9.071 2.976 731.44 3.547 1.696 9.079 2.977 731.64 5.454 1.695 9.087 2.9?$ 731.85 7.953 1.b93 9.D95 2.979 732.06 ' • 9.578 1.692 9.103 2.98a 732.27 �1.816 1.691 9.112 2.981 732.48 �9.188 1.689 9.Z20 2.962 732.69 �.b.77.Q 1.688 4.�28 2.983 732.94 19.4D0 Z_b87 9.136 2.9B4 733.1i 22.279 �.585 9.144 2.9B5 733.33 25.373 1.689 9.153 2.986 733.55 28.715 1.583 9.161 2.987 733.77 32.344 1.68i 9.169 2.988 733.99 36.311 1.680 9.177 2.989 739.21 40.678 1.679 9.1B6 2.994 734.43 45.533 1.677 9.194 2.991 734.66 50.988 1.676 9.202 2.992 734.86 57.2a5 1.674 9.21i 2.993 735.11 63.6A0 1.673 9.218 2.99A 735.31 -------_---------------------------------------------------------------------- HYDRAUL�C JIJMP: UPS�`REAM RUN ANALYSIS f�ESULTS -------------------------------------------------------------------------------- ---------------------- - --------_________--__---------------------------------- DbWI35TREAM CONTROL A55UMED FLOWDEP'i'H(FTi = 2.38 GRADUALLY VARIED FLOW PROFI�,E COMPUTED INFORMAT�ON: �R� �� -------------------------------------------------------�-_--------------------- DIS�'ANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ C4NTROL S FT J ( FT } S FT / SEC ) �:NERGY { gT ) MOMEN�'UM ( POC7N�DS ) 0.000 2.377 6.68D 3.07a 762.38 2.547 2.359 6.748 3.058 758.77 � 4.999 2.39Z 6.737 3.047 755.33 7.362 2.323 6.769 3.035 751.98 9.b92 2.3Q6 5.802 3_D25 748.$Q • 3i.842 2.288 b.837 3.014 745.75 13.965 2.270 6.874 3.004 742.84 � �6.a12 2.252 b.913 2.995 790.06 i7.984 2.235 6.953 2.986 737.93 19.881 2.217 6.995 2.977 739.92 21.704 2.199 7.439 2.959 732.56 23.45Q 2.181 7.084 2.9b� 730.33 25.118 2.163 7.131 2_953 728.25 26.706 2.19b 7.180 2.947 726.30 28.211 2.128 7.230 2.990 724.50 29.629 2.110 7.283 2.934 722.84 30.956 2.092 ,7.337 2.929 72�.32 32.186 2.074 7.393 2.929 719.96 33.314 2.057 �.950 2.919 718.74 34.332 2.039 7.5�Q 2_915 717.68 35.231 2.02� 7.571 2.912 71b.77 36.aD4 2.003 7.635 2.9D9 716.02 36.629 1.985 7.704 2.907 715.43 37.10� 1.968 7.7b7 2.905 715.01 37.4a0 1.95d 7.836 2.9D4 714.75 37.505 1.932 7.908 2.904 714.67 63.64Q 1.932 7.908 2.9D4 714.67 ------------------------END OF HXDRAULEC �UMP ANAT.YSIS______------------------ I PRESSURE+MdMEN�`UM BALANCE OCCURS AT 20.16 PEET UPS�REAM OF NODE 235.90 � DOWNSTREP.M DEPTH = 2.214 FEET, UPSTREPM CONJUGATE DEPTH = 1.678 FEET � ------------------------------------------------------------------------------ NODE 235.91 : HGL =< 369.019>;EGL= � 37D.295>;FLOWLINE= < 367.320> ***��*w.�...�..��,w.,�*��.�.��.�..+�*****+�t******�*��+++*f�*+�+��****..*.,.*«� F�OW PROCESS FROM NODE 235.91 7'Q NQDE 236.OD IS CODE = 3 UPS'FRF.AM NODE 236.40 EL�VATTON = 368.06 {FLOW I5 SUPERCRITICALj ------------------------------------------------------____-___----------------- • CAi,CiTE,ATE PIPE-BEND i3OSSES {OCEi�SA) : PIPE FLOW = 32.20 CFS PIPE DIAl�SETER = 30.DD INCHES CENTRAL ANGLE = 35.940 DEGREES MANI�ING'S N= 0.0�3a0 PIPE LENGTH = 75.22 FEET ------------------------------------------------------------------------------ NpRMP.L DEPTH(�'T) = 1.fi8 CAITICAL DEPTH(FT) = 1.93 ---------------------------------------------------------------------------_---- DPSTREAM CONTROL ASSL7MED FJ�C}fnIDEPTH{F�ri) = 1.93 ------------------------------------------------------------------------------- GRADUAI.Z,Y VARIFD FLOW PROF��,E COMPUTED INFOR34ATTOPI: DISTAi�FCE FROM FLOW DEPTH VEiACI'I'Y SPECIFIC PRESSURE+ CONTROL ( FT } { FT ] ( F�`/ SEC ) F.AiERGY ( FT ) MONSENfiCTM ( POIJNIIS } fl.OD� 3.932 7.908 2.944 714.67 fl.039 3.922 7.949 2.944 714.70 0.152 1.912 7.992 2.9Q9 714.78 0.374 1.9D2 8.035 2.905 7i4.93 0.685 1.892 8.078 2.906 ��5.13 3.1Q9 1.881 8.123 2.907 7Z5.39 �.64i 1.871 8.168 2.908 7i5.71 2.309 1.861 8.214 2.909 7}.6.10 3.122 1.851 8.261 2.911 716.54 4.099 1.841 B.309 2.913 717.05 5.261 1.B31 8.357 2.916 717.62 6.632 1.B20 8.906 2_918 71$.2b 8.243 1.61D 6.456 2.921 718.96 10.133 1.BDQ 8.507 2.925 719.73 12.350 1.790 8.559 2.926 720.56 14.956 1.78a 8.6�1 2.932 721.46 • 18.D34 1_770 8.6b5 2.936 722.44 21.694 1.7b0 8.713 2.941 723.48 • 26.093 1.749 8.774 2_946 724.59 31.454 1.739 8.830 2.95� 725_78 38.146 1.729 8.687 2_956 727.44 46.747 1.719 8.945 2.962 728.37 58.375 1.709 9.D04 2.966 729.78 75.224 1.699 9.063 2.975 731.23 NODE 236.Q0 : HGL =< 359.992�;EGL= < 370.964>;FLOWL�N�- < 368.060� ****+*+tt*�.+*******�w��*t..*��*��..�.��.��+.+�**�**.*..*****+*+...*��,�� FLOW PROCESS FROM NODE 236.00 TO NODE 236.90 IS CODE = 5 UPSTRF'.AM NODE 236.90 ELEVATION = 36$.39 IFLOW UNSF,ALS IN REACH) CALCULATE JUNCTION L05SES: PIPE FLOW DiAMET�R ANGLE FLOWLId3E CAITICAL VELOCITY ICFS} {TNCHESj (AEGREES} ELEVATIOid DEPTH(F3'.) (FT/SECI UPSTREAM 24.80 24.QD 0.00 368.39 1.63 6.621 DOWNSTREAAf 32.20 30.D0 - 366.06 1.93 7.910 LATERAL #1 31.9D 24.00 90.00 368.56 1.21 3.652 LATERAL #2 0.0� O.DO 0.00 0.00 O.DO 0.040 Q5 U.QO===QS EQLiALS BASIN YNPUT=== LACFCD P.ND OCEMA FLdW 3iJNCTION FpRMLTLAE USED: DY=I42'V2-Q1*V1*C05(DELTA1f-Q3*V3*COS(DELTA3j- Q4*V4*Cd5{DELTA4))/((A1+A2}�kb.1j�+FRICTION LOSSES UPSTAEAM: MANNING'S N= 0.013Q0; FRICTIO�I SLOPE = 0.00845 DOWNSTREAM_ MANNTNG'S N= D.D13QD; FRICTION Si3OPE = 0.00693 � AVERAGED FRFCTION SIAPE IN JUNC'�'I0�7 ASSUMED AS 0.00769 JUNCTION LENGTH = 4.00 FEET FRICTION LOSSES = 0.033 FEET ENTR�NCE LOSSES = 0.00� FEET . ,7UT7CTION LUSSES = (DY+HV3-HV2)+(ENTRANCE LOSSES) JUNCTION LOSSES =( 0.747)+( O.00D} � 0.747 NODE 236.90 : HGL =< 37 L D30>;EGF�= < 371.711>;FLOwLINE= < 366.390> �.****.****�**�tr�W*�r****�.**��+,..******+*****++�+.**�,�.s��+*�******�******,�.+ FLOW PF20CE55 FRpM NODE 236.90 TO NODE 240.OD I5 CODE = 3 UPSTRElAi+4 NODE 240.OD ELEVATIQN = 368.56 (FI�OW I5 UNDER PRESSURE) CALCULATE PIPE-BEND L05SE5iOCEMAI: PIPE FLOW = 20.80 CFS PTPE DIAMETER = 24.00 INCHES CEN'I'F2AL ANGLE = 16.500 DEGREES MANNING'S N= 0.01300 PZPE LENGTH = 39.72 FEET BE�TD COEFFICIEI3T(KB} = O.1Q704 FLOW VELOCITY = 6.62 �'EET/SEC. VEI.00ITY HEAD = 0.581 FEET Ha=KBfcv�LocF�r HEan� = c o.zo�r*c 0.681} = O.fl73 SF={4/Ki**2 = ii 20.80)/( 226.228ij**2 = O.D0845 HF=L*SF = ; 34.72)*(0.008451 = 0.294 TOTAI, HEAD i3OSSES = HB + HF =( 4.473i+( 0.2941 = 0.366 ------------------------------------------------------------------------------- NODE 240.00 : HGL =< 371.397>;EGL= < 372.077>;FisOwi,INE= < 368.550> i*+#'ttttf#}y.�y*�k�k*Yr�tk�**Y��t1i�Y�F#�i} y i*iF+*xf ** *****YriY*Yrri ri Yr*YrYriFyryr*1� **Ytif f Y�i*�Y�Yk'�kU * FLOW PROCESS FRQM NQD� 24p,00 TO NODE 240.10 I5 CODE = 1 UPSTREAM i�IODE 24a.1D ELEVATION = 368.96 (FLOW IS UNDER PKESSUREj -----------------------------------------------------�-------------------------- CALCULATE FRZCTI0I3 L05SES(LACFCD}: PTPE FLOW = 20.80 CFS PIPE bIAMETER = 24.00 INCHES PIPE LENGTH = 58.4fl FBET MANI3ING'S N= 4.01300 SF=f4/K1''*2 = ({ 2D.8D}1i 226.228})**2 = Q.04845 •• HF=L*5F = f 58.9Q)*{4.00845) _ __ __4_494-"_ '- ------------------------------------- --___--_----------------- NODE 240.10 : HGL =< 371.$90>;EGL= < 372.571>;FLOWLINE= < 368.860> -` ��*.�****�**x�+*�*.****.***t***��f��w�,�y*�***�.*��+t��..*��.�.***�** FLOW PROCESS FROM NODE 240.10 TO NODE 240.20 rS CODE = 5 UPSTRF.AM NODE 240.20 ELEVATION = 369.19 (FLOW IS UNDER PRESSURE) --------------------------------�---_____------------------------------------- CALCULAT£ JUNCT�ON L055ES: PIP� FLOW DIAMETER ANGLE FLOWLINE CRITICAi� VEi�OC��'Y (CFSj (TNCHES) (DEGREES} ELEVATION DEPTH(FT.) {FT/SEC1 UPSTREA�+I 17.90 24.00 45.Ofl 369.19 L 52 5.698 DOWNSTFEAM 20.80 24.00 - 368.86 1.63 6.62i LATERI�I� #1 �.25 18.00 90.OD 369.99 0.42 D.707 LATEFAL #2 1.25 �8.00 90.00 359.99 0.42 0.707 Q5 D. 40===45 E4L7A�,S SASI�i INPUT=== L�ACFCD AND OCEMA FLOW J134VC'I`ION FORMLTLAE USED: DY=(Q2*V2-Q1*V1�C05{DELTAI}-Q3*V3*CQS(DELTA3?- 44*V4*COS(D�L'T'A4J)/ffA1tA2)*16.I)+FRICTiON LQS5E5 UPSTRERM: MA�iNING'S 13 = d.D13D0; FRICTION SLQPE = 0.40626 DOWNSTREAM: MANi�7ING'S N= O.D1300; FRICTION SLOPE = O.Q0845 AVERAGE!} FRICTION SLOPE IN JUNCTION ASSUMED AS O.Q0736 JUNCTION LENGTH = 9.00 FEET FRICTION LC?SSES = O.Q29 FEE�' ENTFtA[dCE i�OSSES = Q.136 FEET JUNCTION LC?SSES = IDY+HVI-3-IV2 )+( EN'i'HANCE LOSSES) �7[7NCTION LOS5E5 = f 0.5011+i 0.13b} - 0.637 ---------------------------------------------------------------------------- NODE 290.2D : HGL = � 372.7b4>;EGL= < 373.209>;FZOWLINE= < 369.190> +*********.+****++�+�+.*+�*+++��..�*+***��*++*+*.+**+�**�****++*�..,.+��+** FLOW PRbCES5 FRONi�IODE 24D.20 'TQ NODE 290.4� �S CODE = 1 --UPSTAEAM NODE 240.41 ELEVATION = 369.43 {FLOW IS LTNDER PRESSiTRE} CALCUi�A'FE FRICTIOI3 L05SE5 (LACFCD} : PIPE Fi�OW = 17 . 90 CFS PIPE DIP.METER = 24. DO INCFi�S PTPE LFNG�'H = 48.19 FEET MP.NNING'S N= O.Q�30Q SF=(4/K)* 2=(( 17.90}/{ 226.228?)''"'2 = 4.00626 HF=L*SF = ( 48.19)*(O.DOb261 = 4.3D2 NQD� 240.41 : HGL =< 373.4Q6>,EGL= < 373.5i0>;FLOWLINE= � 369.43Q� *�Y*****t*ik**Yr1r}�F}YrYr*�k Yr Yr**�F'k'F ik ***!r*i� *# i�**##+f�i �! 2! 4 i 1** i!4l�� i i ik Y f f Y�lYrY*t****ikYr'M'h i� FLOW PROCE55 FROI� NODE 240.41 Tb NODE 290.42 I5 CODE = 2 UPSTREJ�M NODE 24D.92 ELEVATIbN = 369.76 {pl,(}W IS LTNDER PRE55UAE) CALCULATE MANHOLE LdSSESfLACFCD�: PIPE FLOW = 17.40 CFS PIPE AIAME�'ER = 24.00 INCHES FLOW VELOCITY = 5.70 FEET/SEC. VELOCI7'Y HF.AD = 0.544 FEET HMN = .05�fVELpCITY H�D} _ .D5*f 0.504) = Q.025 � NODE 240.A2 : HGL =< 373.D31�;EGL= < 373.535>;FLOWLINE= < 369.76D> +******«**.,.*..**.*«*�*�*�..*.*.�*.*.*+++++t�.+�*+�.*.+.��...�*��r.**++*+...** FLOW PROCESS FROM NODE 240.42 '3'Q NODE 240.45 xS CObE = 1 UPSTREAM NpDE 240.45 ELEVATION = 359.94 (FLOW IS UNDER PRESSLTREj CALCiJLA'I'E FAiCTI�N LOSSES {�,ACFCD) : PIPE F'LOW - 17.94 CFS PIPE bZAMETER = 24.OD INCHES PIPB i,ENGTH = 35.40 FEET NIANNING'S N- O.p22aQ SF=(Q/K1**2 = (( 17.90)/f 133.67711**2 = 0.01793 • HF=L*S�' _ ( 35.00)*{0.01793) _ �.628 � NdDE 24D.45 : xGL �� 373.654>;EGL= < 374.153>;FLOW�INE= � 369.940> tx*t*��++*a�:t*t*y+yt*xar*��+�r�*wt***+**+++f�ar�+tr�a*�r��rf*****t�at*t+��x+* FLOW PROCESS FROM NODE 240.45 T� NODE 240.45 IS COD� = 8 UPSTREAM NODE 240.45 ELEVATIpN = 3fi9.94 (FLOW IS UNDER PftESSUREj CALCULATE CA'I'CH BASIN EN'F3�P.NCE LOSSES {LACFCD) : PYPE FLOW = 17.90 CFS PIPE DiAMETER = 24.04 INCHES FLOW VELOCITY = 5.70 FEET/S�C. VELOCI�Y HEAD = 0.509 FEET CATCH BASIN ENERGY LOSS =.2*(VELOCITY H�AD) _.2*( O.SO4} = 0.�41 NODE 290.45 : HGi. _< 374.264>;EGL= < 374.264>;FLOWLINE= < 369.940> �*+�kxti+itrt*+**tiaft*+*r�**+wrs*►*��+,t,ti.*+**�+>r**�*s�Ww�+�+*��*tYt+rtrtt�***r*w*x UPSTREAM PIPE FLOW COt3'I'ROL DATA: NODE �IUMBER = 240.45 FLOWL�NE ELEVATYON = 369.94 ASSLTMED UPSTREAM CONTROL HGL = 371.46 FOR DOWNSTREAM RUN ANALYSIS END OF GRADUALLY VARIED FZ,OW ANALYSIS . • W+xx*rrw+*+rx�rrix�irri�+�w��» *.r.*krx+*x��wrr.r*+x*:*��**y*�ws*.**st+:ws**>r PIPE-FLdW HYDRAUL3CS CO2+IPU'I'ER PROGRAM PACKAGE � ;Reference: LACFCD,LACIt�I, ANiJ OCEMA HYDRAi3i�IC5 CRITERI023) ' [c1 Copyright 1982-2001 Advanced Engzneering Software (aesj Ver. 8.0 Ael.ease Date: O1/O1/2001 License ID 1509 Analysis prepared by: PRdJECi`DES2Gid CONSiILTANTS 7DJ. 'B' STREET, SUITE 800 SAN DiEGO, CA 92101 619-234-0349 *rt**+***�Yfy.�+y.w*r�rr*:+r+ DESCRIP'I`IOAI �F' $'iL1DY '**:�rsrrtw+iwr*t**xr**x+** * BRESSI RANCH - ULTIMATE CONDITIOi�15 * * SYS'I`EM 200 - LATERAI. 1{TOWN CP.RDEN ROAD ST 20+91.99 RT) " * 100-YEAR * ♦��rr�*x*+t+�*+r�++y.rr*rtw**rt+twtrt++*i*t*+i+**+trrrry.*y,**y,Yrt�ryr�r+***x++ FILE NAME: 2D0-1.DAT TIME/DATE OF $TLTDY: 15:41 10/24/2002 �lr*YriFk * M1rYrYr **t *f tYr*ttkik*�M*YrY� iF *YrY�1r *�k1r f KY� Yr* *Yr T***# k*YriF Yrf Y� YrYriFk k YrY�1r * f*! �# f Y�Y�i�* ** f tk*M GRADUALLY VAfiiED FLOW ANALYSIS FOR PIPE�SYSTEM NODAL POIi3T STATUS TABLE �Note: '"' indicates nodal. point data used.) � uPsmxEars xtrN nowrrsTR�ar� Rvx NODE MpDEL PRE55URE PRESSURE+ FLOW PRESSURE+ 31[.7MBER PROCE55 HEAD ( FT) N50MENTUM ( POUi1DS ) DEPTH ( F'i') P70MENTU3�S ( POUNi}S 1 205.�0- 4.66 Ac 3b.26 0.33* 63.50 j FRICTION 205.20- 4.65*Dc 36.26 0.65*Dc 36.26 } CATCH BASiN . 205.20- -4_96*-------------19_47--------4'66^De-----------12_89_ iL�}CTMiJM NU'MBER QF FI+IERGY BALANCES iJSED IN EACH PROFIL£ = 25 ---------------------------------------------------------------------__--___---- 3�TOTE: STEAL}Y F�OW HYAFtAiJLEC H�AI}-T,OS$ COMPUTATTONS BASED ON THB MOST CONSE�tVATNE FOA2+�ULAE FROM THE CURRENT LACRD, LACFCD, AND OCEMA DESIGN MAN�[JALS . www*+*t.*wr***..«�*.*..*x*..*x*:.+..f*t**+***i�+**x�.*..x.*..x.+e.+t++�rrrt�r.rtt+ bOWNS'TF�.�M PTPE FLOW CONTROL DA�'A: i�IODE NUMBER = 205.10 FLOWLINE ELEVATION = 307.92 PIPE Fi,OW = 3.04 CFS PIPE DIAMETER = 7.8.OD II3CHE$ ASSUMED DOWNSTREAM CON'1'ROL HG� = 307.960 FEET *NOi'E: ASSUMED DOWNSTR£AM CONTROL DEPTHf O.D4 FT.) � IS LE55 THAN CRITICAL DEPTH( 0.65 FT.) � ___> CRTTICAL DEPTH IS ASSi1MED A5 DOWI35TREP.M COid'iROL DE�TH FOR UPSTREP.M Ri3iV ANA,LYSIS NpDE 205.10 : HG� _< 308.247>;EGL= < 309.969>;FLpwL�NE= < 307.920> x*,r.r++*+*txt+ytx++,r+*+++*a*r**x�rx,r�**w***�w*w*�*******+rw+********+�++*+*++fr P�,OW PROCE55 FROM NODE 205.1D TO NpDE 205.20 IS CpAE = i UPSTREAM NODE 245.20 ELEVATION = 31D.15 (FLpW T5 SUPERCRITICALj CALCULA'I`E FR�CTION LOSSESILACFCD�: PIPE FL04V = 3. RO CFS P�PE DIAMETER = 16. 00 �NCi-i�S PIPE LENGTH = 22.25 FEET MANNING'S N= 0.0130D idORMAL DEPTH{FT} - 0.30 CRITICAL DEPTH(FT� = 0.56 ===--=---=-----===========-==---=----===--=-===-=====-=---=---==-�=_=��_T==== tJPSTREAM CON'd`ROL ASSUMED F'�OWDEPTH{FT} � 0.66 . GRADUALLY^VARIED FLQW PROFILE COMPUTED INFORMATIObi ^� �' ------------------------------------------------------------------------------ DIS'FANCE FRQM F�,OW bEPTH VELOCTTY SPECIFIC PRE5Si1RE+ CONTROLfFTf (FT� {p�/SEC1 ENERGY(FT} MOMENTUM(PQLTNDSI 0.000 0.658 4.017 0.9p9 36.2fi 0.006 D.644 4.134 0.91� 36.28 � 0.027 0.63Q 4.257 0.912 35.37 ' D.062 0.63.6 4.38'i 0.915 36.51 0.115 0.602 9.525 0.92p 3fi.72 0.188 D.588 4.672 D.927 37.Q0 0.264 D.573 4.827 0.936 37.34 0.4p5 0.559 9.993 0.947 37.77 0.557 D.545 5.169 0.960 38.27 0.742 0.531 5.357 0.977 38.86 D.968 0.517 5.559 0.947 39.54 1.241 0.503 5.774 1.021 40.33 1.570 0.989 fi.005 1.049 41.22 Z.965 0.474 5.253 Z.062 42.23 2.441 0.460 5.521 1.12Z 43.37 3.DI5 D.446 5.B09 �.166 44.65 3.713 O.Q32 7.122 i.220 46.09 4.5b5 � 0.418 7.4b1 3.263 47.70 5.639 0.4D4 7.830 i.35b 49.5D 5.943 0.389 8.233 i.442 51.51 8.643 D.375 � 8.fi73 1.544 53.76 10.897 0.361 9.�57 i.664 56.28 14.041 0.347 9.fi91 1.B05 59.10 18.83D 0.333 10.282 �.975 52.27 22.250 fl.327 ,10.527 2.049 b3.60 ---------------------------------------------------______---------------------- NODE 245.20 : HGL =� 310.8D8>;EGI.= < 3I1.059>;F"LOWLINE= < 310.,150> +#r*yrrtft.w**y.x+frtt+**�r***�r*+*rtx:w:*y*�ity**rrrswtw�rwwr�f*i�f**,r*firxx**tr*f*#irwr+t FLOW PROCESS FFtOM NODE 2D5.20 TO NODE 205.20 IS CODE = 8 � UPSTRE.�M NODE 2D5.2D EF��i/ATION = 310.15 SFLOW IS AT CRITICAL DEP'T'H} � CALCULATE CATCH HASIid ENTRANCE LOSSESILACFCDj: PIPE FLC)W = 3. DO CF5 PIPE DIAhfE'�'ER = 18 . 00 INCHES FLOW VE�OCITY = 4.02 FEET/SEC. VELOCITY HEAD = 0.251 FEEr1` . CATCH HASIN ENERGY L055 =.2*fVELOC�T`Y HEPD) _.2*( 0.251) = 0.450 _------------------------------------------------------------------------------ NODE 205.2D : HGL =< 3�1.109>;EGL= < 311.109>;FLOWLINE= < 310.150> *xx**wv.*r**f+**xir*wrt�****ti*�***r*r►�**trr++*��*�**w*,rr***t++x*t*+**+rrs*w+r**w UPSTFtEAM PIPE FLOW CONTROL DATA: NODE NUN�3ER = 2 0 5. 2 0 FLOWI,INE ELEVATI ON = 310 . 15 A5SL3MED UPS'I`REAM CONTROL HGL = 31D.81 FOR DOWfiS'I'REAM AUN ANALYSIS ______�_______,��_��R__________________�=__________________� « �_____________ �ND OF GRADUALLY VARIED FLOW ANALYSTS i w.*.,*,*.*..*�t****,�..��*��..�r�.�{��**.��*��,**t,...�..�*.�.,.}�*� PIPE-FLOW HYDRAULTCS COMPU'I'ER PROGRAM PACKAGE {Reference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERIpNj tc) Copyright 1982-2002 Advanced EngineEring Software (aesi Ver. 8.0 Release Date: 01/01/2402 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSUL'I'AN'i'S 701 'B' STREET, SUITE $00 SAN DIEGO, CA 9210I 619-235-5471 v.�*�*.�+�t��x�**+x*«*..*** DESCRIPTION OF Si'LTDY **•****+t.�+**+��*+�..t�tt * BRESSI RP,[dCH - ULTIMATE CONDITIONS * * SYSTEM 200 - LATERAL 2{Tpy+TN GARDEN ROAD STA 2Q+91.99 LT} * * 100-YEAR * tt��**,rwr***t**af**�**�r�ray.�w*r�r**�s*ryt*f***s�r*++v.+*++**+*x��wwi�t*x*w�* FILE NAME: 200-2.DAT TIME/DATE QP STUI7Y: 10:7.0 01/17/2603 ***�**�t*�+*+xx�*i.***x***,ir*r*�****+****w*xx**w*rw+*tir++*rytst�ri,�rtrt�iry�***r** GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POENT STA'I`US TABLE (Note: "*" indicates nodal point data used.) UPSTREAM RUN 1]OWNSTREAI+� R[JN NQDE MODEL PRE$SURE PR�SSURE+ FLOW PRESSURE+ � NLTMBER PROCESS HEAD (�'T' � MOM�.NTUi-f ( PpUi�FUS ) AEPTH S FT) I�fOMENTUM ( POUNDS} 500.50- 1.56* 18D.33 0.38 161.37 } FRICTIpN } HYDRAULIC JiJi]P 5D0.60- 0.80*Dc 85.i4 0.80*Dc 85.14 } CATCH BASI23 500_b0- 1.14* 45.09 O.BO bc 31.13 ------------------------------------------------------___--------------_____-__ 1�AXINfUM NUF4SER OF ENERGY SALANCES USED IN EACH P12pFTLE = 25 NOTE: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTAi`IONS BASED ON THE MOST CONSERVATIVE FO}�MULAE FROM THE CURRENT IIACRD,I,ACFCD, AND OCEMA DESIGN MA?�TUALS. 'k'k� 1' 1'k't�Y�*1# k'k�r # i�* ** fYr ***YrYrYriFiFfiF�k Yr * k*�***!r ****rtiFYrM*tkYr*Yr* * t*** i f ti*YY�k*i i Yr*t�c *** DOWNSTREAM P�PE FLOW CONTROL DATA: NpD� �E� � saa.so FLOWE�INE ELEVATION = 3Q6.42 PTP� FLOW = 6.50 CFS PIPE DIAMETER = 36.00 INCHES ASSUMED DOWNSTREAM CONTROL HGL = 308.000 FEET ------------------------------------------------------....___----------____--_-- NODE 5a0.50 : HGL =< 308.Od0�;EGL= < 3D8.046>,FLOWLINE= < 306.920> +*��*******+�*..*.��.+*+�****++++*��+.*++*+*+»+.***...��.«*��.***.**�*�.�* FLOW PROCESS FRQM NODE 500.50 TO NODE 500.54 IS CODE = 1 UPSTREAM [dODE 500.6Q ELEVATION = 3Q8.48 (HYDRAULIC JUMP OCCUFS) CAi�CULATE FAICTION LOSSES(LACFCD): PIPE FLOW = 6.50 CFS PTPE DIAMETER = 36.40 INCHES PIPE LENG7'H = 8. 25 FEET MAIdNZI3G' S N = 0.013Q0 --------_---------------------------------------------------------------------- HYDRP.ULIC �Ut�fP: DOWNSTRF�M RUN ANALYSIS RESEJLTS --------------------------------------------------------__--------------------- �10RMAL D�PTHfFT} = 0.29 CRI'I'ICAL DEPTH(FTj = ❑.80 � �_UPSTREAM-CONTROL_ASSLTMED-FLOWDSPTH(FT}-=-----0`80--------------------------� GRADUALLY VARIEI7 FLOW PROFILE COMPUTED INFORIiATION: DISTANCE FROM FI,OW DEPTH VELOCITY SPECIFIC PRE55URE+ COT3TROL f FT ) ( FT j ( FT/ SEC ) �i�iERGY ( F'T} MOM£NTUM { pOUN�S ) 0.000 0.801 4.287 1.087 85.14 O.Q04 0.7B1 4.995 1.D86 85.24 0.418 0.760 4.614 1.091 85.54 D.p82 D.740 4.795 1.09� 86.45 O.Q79 0.719 4.988 1.106 86.SD 0.130 0.699 5.I96 1.116 87.79 0.198 0.678 5.439 1.135 89.44 0.285 0.656 5.6b0 1.156 90.5$ 0.394 0.638 5.920 1.182 92.92 0.531 0.617 6.20� 1.215 94.6d 0.699 0.597 6.507 1.255 97.]5 0.904 0.576 6.89� 1.303 lOD.10 1.156 0.556 7.243 1.362 103.50 1.4b4 0.535 7.6�1 1.433 107.40 1.840 0.515 8.039 1.519 131.$b 2.303 0.495 8.523 1.623 116.95 2.876 0.474 9.058 1.744 i22.76 3.590 0.454 9_655 1.902 �29.38 4.493 0.433 14.322 2.069 135.96 5.652 0.413 1�.072 2.318 �45.53 7.�75 0.393 1I.920 2.600 i55.60 8.250 0.382 12.446 2.773 161.37 ------------------------------------------------------------------------------ � --HYDRAULIC-JUMP�-UPSTREAM»Rl7N-ANAE,YSZS-RESULTS_______________________________ DOWNSTREAM CONTROL ASSi3MED F�OWbEPTH{F�') = 1.58 ------------------------------------------------------------------------------ GRP,DUALLY VARIED FLOW PROFILE COMPU'I'ELi INPO�tMA`i'TON: ---------------------------------------------------------------------.._..__----- DISTAPICE FA0�7 FLOW DEPTH VELOCY�`Y SPECIFIC PfZESSUREt CONTROL[FT) (FTi (FT/SEC) ENERGY(FT} MQMENTUM{pQ[JNDS� D.D00 1.580 1.722 1.626 18Q.33 0.115 1.549 1.765 1.597 �73.64 0.230 1.518 1.911 1.569 167.15 0.344 1.487 1.860 1.540 160.88 , 4.457 1.455 1.911 1.512 154.82 4.569 1.424 1.965 1.484 198.98 0.660 �.393 2.022 1.457 193.36 Q.789 2.352 2.082 1.429 137.96 0.898 1.331 2.146 1.402 132.79 1.004 1.300 2.214 1.375 127.85 1.109 1.268 2.286 1.350 123.14 1.2�2 1.237 2.363 1.324 118.67 1.3�3 1.2d6 2.445 1.299 114.44 1.411 1.175 " 2.532 1.274 110.46 1.506 1.144 2.525 1.251 106.73 1.598 1.113 2.724 1.228 1D3.26 1.697 1.081 2.83f Z.206 1D0.05 1.770 1.050 2.996 1.185 97.13 1.849 1.019 3.07D 1.166 94.48 3.923 0.988 3.203 1.147 92.13 3.989 0.957 3.348 1.131 90.09 2.047 0.926 3.54A L 116 B8.38 � 2_097 0.894 3.675 ]..109 87.00 2.135 0.863 3.861 1.095 65.99 M k K Y rt* t w 1 M* f* w w rt��* w k f* f i f + f}+ x t x t t� t t � f i t+ t t v W f t 4� t�*** w* w w f f f?! W*+ t� i f f� i �+♦ PIPE-FLOY+1 HYDRAiJi�ICS COMPUTER PROGRAM PACKAGE • {Re�erence: LACFCD,LACRD, AND OCEMA H]'DRAULiCS CfiITERIDN} � {c1 Copyright 1982-2�01 Advanced Engineering 5oftware (aes) Ver. 8.0 Release Date: 41/41l2041 License ID 1509 Analysis prepared by: PROJECTDESIGN CONSULTANFS 70� 'S' STREET, SUITE 80Q SAI3 3?IEGO, CA 92103 619-234-0349 +**rt.*....«.*«�***...�+�*+ DESCRIPTION OF STUbY ***•x*....*.*�+*.*f�.�+..+ * BRESSI RANCH - ITLTIMA'i'E CQNDITIOD}S RESIDENTIAL � * PA-6: LATEFtP.L 4(PIPE N0. 7 0Id 5H'i' 7 OF DWG 400-8C} * * 1fl0-Y£AR STORM EVENT * *.«»**..++**+*...+*.,.+..w...+**,..*+.+{,.t.**+�.�.+..*.,...x,,.�*.**.,.�+*..+��*.+ FILE NAME: 200-9.DAT TIME/DATE OF STiTDY: 15:21 14/24/2002 *ay.►v.wv�w*+***�ta�+*�rrtw*****+xrt*++w*aria**t++*+xe*rtf*rrtfr*ex+xx�*i.+w*x*****�w GR�UALLY VARIE�} FLOW ANALYSIS FOR PIPE SYSTEM � NODAL PO�NT STATi35 TABLE (3�Iote: """ indicates nodal point data used.) UPSTREAM RUN DOWNSTREAM RUN i�]ODE MODEL PRESSURE P1�SSURE+ FI,OW PRESSiFRE+ Ni iMBEA PRpC E5S FiEAD { FT ) MOMENTtTM ( POi3I3D5 ) DEPTH ( F'i' ) MOMENTL7M ( POL7NAS ) 220.10- 4.78 Dc 54.33 0.42* 83.99 } FFtICT�dN 220.20- U.78*Dc 54.33 0.78*Dc 54.33 } CATCH BASIN • ' ---220_20--------------1_14* __29_55________0_7$_Dc�+--------_38_98_ MA.XIMLTM I317MBER OF ENERGX HAL.�NCES LiSED IN EACH PROFiL� = 25 ______-__-----------____--------------------------------------------------------- NOTE: ST£ADY FLAW HYDRAULIC HEAD-J10S5 COMPUTATIONS BASED ON THE M�ST CONSERVATIVE FORMULAE FROM THE C[iRREN'I' LACRIJ,LACFCD, AND OCFT+SA D�SIGN MP.NUALS. �.*rr.wt:*+*t+*+�r.�r.w�+*t+srx*+++***r.*.ra*.«*+a*+.i*t+�+w**+**«.«**x*+*+*Wt DOWi3STREA�i PIPE FLOW CdNTROL DATA: NOAE NLTMBER = 220.10 FLOWLINE ELEVATION = 339.10 PIPE FLOW = 4.10 CF5 PIPE DIAhlETER =. 18.00 INCHES A55iFMED DOWNSTREAM CO�I'i'ROI.� HGL =� 339.70D FEET *i5i0TE: ASSUNSED DOWNSTREAM CONTROL DEPTH{ 0. 64 �"�. } I5 LESS TH.�N CRITICAL DEPTH{ p.78 FT.J -__> CRITICP.L isEPTH IS ASSU�'iED AS DOWPISTREAM CONTROL AEPTH FQR UPSTREP.M AUI3 ANALYSIS ------------------------------------------------------------------------------ NODE 220.10 : HGL =� 339.523>;EGL= < 341.079>;FLOWLIIVE= < 339.ZQ0> r�r*�r*y.t*fkKwftir++*v.*w�+*rti►y*�ttt+x>�*+rx*ts*i****t*yr**yyrt*xt+x+**r*w+t�+*+ FLOW PROCESS FROi�1 NODE 220.J.4 TO NOpE 220.20 IS CODE = 1 iiPSTREA�S NODE 224.20 HLEVATIOi�I = 340.40 iFLOW IS SUPERCRTTICAi�i CAI�CULATE FRTC'I'TON L085ES {�CFCD) : PFPE FI,OW = 4.1D CFS PIPE DIAMETER = 18.00 INCHES PIPE �F.�FGTH = 12. 96 F'EE� MP.NI3ING' S N - 0. D130D NORMP.i, AEPTNI�'T} = 4.36 CRITICAL DEPTH{�T? = 0.78 UPSTREAM CONTROL ASSiJMED FLOWDEPTH ( k'T j= 0. 7 8 ====--==---=======-��==__��« t,�_��______�_��___��_-��_�w��_=�________==_ . __GRADUALLY VARIED FLOW PROFILE COMPUfiED I13FORMATIdN: ---------------------------------------------------------------------__-___ DISTF�NCE FROM FLOW AEPTH VELOCITY SPECIFIC PRESSU�+ CONTROL[FT? (PT) [F�/SEC1 FNERGY(FT) MOMENTi.JM(PQUI3DS} D_OD4 D.775 4.448 1 063 54.33 O.D08 0.759 4.573 1.OB3 54.37 • 0.032 0.742 4.705 1.086 54.49 ' 0.074 D.725 4.845 1.09a 54.7Q D.138 D.7fl8 4.993 1.096 55.D1 D.225 D.69� 5.151 1.109 55.42 0.339 0.675 5.319 1.119 55.93 0.4$4 D.658 5.497 1.�27 55.55 0.664 0.641 5.687 1.349 57.30 0.886 O.fi24 5.891 1.163 58.17 1.156 0.507 5.108 1.187 59.19 1.482 0.591 fi_341 1.215 60.35 1.875 0.574 6.592 1.249 61.67 2.348 0.557 6.861 1.288 63.18 2.917 0.540 7.152 1.335 64.87 3.505 0.523 7.465 1.389 66.78 4.k39 D.5D7 7.806 1.453 68.92 5.46D 0.490 8.175 �.528 7i.32 5.724 0.473 8.577 1.616 74.00 8.311 0.956 9.017 3.719 77.00 10.351 a.44D 9.498 i.841 BD.37 12.950 0.423 10.048 1.979 83.99 NODE 220.20 : HGL =< 391.175>;EGL>= � 341.483�;FL04JLINE= < 340.40D> **f***k*f***�***#****fk****#*f#};*}+�Y*f+kkkiM##}*#****�w***#N**��M%w�fR4lwtYf FL,OW PROCESS FROM �ODE 220.20 �`0 NODE 220.20 IS CODE = 8 UPSTREAM NO�E 220.2D E�EVATION = 340.4D (FI,OW IS AT CRITICAL AEPTH} ------------------------------------------------------------------------------ CAI..Ci7LATE CATCH aASIN ENTRANCE L055E5 (LACFCD} ; PIPE FLOW = 4.i0 CFS P�PE DIAMETER = 18.00 213CHES FLOW V£LOCITY = 4.45 FEET/SEC. VFLOCI'F'Y I-�EA,D = 0.307 FEET CATCH BA52N ENERGY L05S =.2*lVELOCT'T'Y H�AD} -.2*{ 0.307) = 0.061 • �-----------___..__....------------------------------------------------------------ NODE 220.20 : HGL =< 341.549>;EGL= < 341.594>;FLOWLINE= < 340.40D> *w**x*s,o-****x*t*+ra**w**�xtwx*�k+w+*tr**,t�k++++v.t�r�s++*++k++*+w+#�+*+�rrt**r**t+ U�STREAM PIPE FLOW CONTAOL I}ATA: NODE NUMBER = 220.20 FLOWLINE ELEVATION = 340.40 ASS[JMED UP53'REAi4 CON'i`ROL HGL � 341.18 FOR DpWNSTREP.M RUN A�iAI,YSTS F�TD OF' GAADUALLY VARI£D FLOW AI�iP.I,XSIS • * * rt a * k * k Y rt * k f k 1 � A x * # # � * * / � � * * # � t � * * * � * f * * * * * i i R * * * f # * # i * + * * Y � � w * * * * f f k i } * i � # Y k PTPE-FLOW HYDRAUiICS COMPUTER PRbGRAM PACKAGE IReference: LhCFCD,iACRD, AND OCEMP. HYDRAULICS CRIT�RTpN} • •- fcj Capyright �982-2001 Advanced Engineering Software {aes) Ver. 8.0 Release Date: O1/D1/20a� License ID 15D9 Analysis prepared by: PROJECTDESTGN CONSLTI,TAN'PS 701 'B' STREET, SU�TE S00 SAN DIEGO, CA 921�1 619-239-0349 wx****�**r+*�*+***x*�+.++* DESCRIPTiON OF S`i`L7DY +***r++**�***++**+*x*,r*x+f * BRESSi RADiCH UL'?'IMA'T'E CONDIT�QNS * * SY5'TEM 200 - LATERAL 5(TOWN GARF}EN ROAD STA 29+67 RT} * * 104-YEAR ' *+�***+**+****+*r*+w*kw**w*frt��ry*tt*+xt+ry*t*+rrr*ti***rtt*rtt**s*�rr�k****+ FILE NAi�fE: 2Q0-S.DAT TIME/DATE OF STUDY: }.5:22 10/24/2002 ..+.++>+��.**�++.+*:�t,...�*..+.*.,.,,.*...*.,.*«*.x«*.x.*.+*.*,.+��t+.*..***«*+...k GR�UALLY VAR�ED FLOW ANALYSIS F�R PIPE SYSTEM . NODAL POII3'P STATUS TI�iBLE (�ote: "*' indicates noda]. point data used.) iJPSTRE.�M RUN DOWN$TREAM RUN NODE MODEL PRESSURE PRESSURE� FLOW PRESSURE+ NUi�iBER PROC ESS HEAI7 ( FT } MOMENTLTN4 { pOUNDS ) DEPTH ( FT ) MQNSENTUM { pOUNf?S 1 225.10- 0.52 Dc 31.fi5 D.33� 51.39 } FRICTIOI3 225.64- 0.62*Dc 31.65 0.62*Dc 3�.65 • } CATCH BASIN ---225_60--------------Q-91*____--__------16_9fi------ D.62 Dc ___--__11^31- -------------- MA}iIMiJ2+4 NUMBER OF ENERGY SALANCES T3SED IN EACH PROFILE = 25 � NOTE: STEADY FLQW HYDi�AULIC HEAD-LOSS COMPU'I'ATTONS SASED Obi THE MOST CONSERVA'FIVE FORMLTLAE �'ROM THE CiJR�tENT �ACRD, LACFCD, AND OCEMA DESIGN MANiJAY,5. ��f*+w+arw*,t*,.�+wfw.*�r**++t***.«.+***.«*+*.*�**i�x*w**+*+*t+�s.�**+****.+i�.*+ DOWI35TREAM PIPE Fi�OW CONTROL bA'I'A: NODE Nt3MBER = 225.14 r^LOWI�INE ELEVATIOAF = 351.82 PiPE Fi,OW = 2.70 CFS PIPE DIAt�SETER = 1B.00 INCHES A55LiMED DOWNSTREAM CONTROL HGL = 352.200 FEET *NOTE: ASSUMED AOWI�i$TitEAi+f CO23TROL DEPTH( D.38 FT. j IS LESS 'I'HA.A} CFtITICAI, AEPTH( 0.62 FT. } __=> CRITICAI, DEPTH IS ASSUMED A5 DOWNSTREA�S CONTRdL DEPTH FOR UPSTREAM RUN ANALYSIS '^NODE " 225.�0^: HGL = � 352.150>;EGL= < 353.510>;FLOWLINE= < 351.820> a*+x+*+*i�xk+w*�+wrt+a*t�rfr*y**ta++***w+*w*�+*+r*rrr,r**w��w*w*++*+r+rtr****+*+xw* FF�OW PROCESS FROM DiODE 225.1D TO NODE 225.60 TS CODE = 1 UPSTAEAM 130DE 225.6a EL�VATION = 353.51 (FLOW I5 SUPERCRITICALI -------------------------�----------------------------------------------------- CALCCTL,ATE FRICTION LOSSES(LACFCD}: PTP� FLOW = 2.70 CF5 PIPE DIA.METER = 18.00 INCHES PIPE LENG'T'II = 22.00 FEET MPNNTNG'S N = D.01300 NORMP.L DEP'i'HIFT] = 0.31 CRITICAL DEPTH(FT) = 0.62 �UPS'FREAM CONTROL ASSUMED FLOWABPTH(F'i) = 0.62 • " GRADUALLY_VARIEi1-FLOW_PROF3LE_COMPUTED-INFORMAT�ODi __---_--J-__^-_________�_ DISTANCE FROM FLC?W 1JEPTH VBLOCITY SPECIFIC PRESSURE+ C ONTROL { F'i` j (�'T ) f FT / 5EC ] ENERGY ( FT } MOMF_.N'i'UM ( POUI�iDS 1 O.Q00 0.623 3.688 a.858 31.65 0.007 D.611 3.994 D.859 31.68 � D.029 Q.598 9.107 D.860 3�.74 ' D.069 4_585 4.226 D.863 33.Bfi 0.127 0.573 4.351 0.867 32.02 0.24'7 �.5fi0 4.463 0.873 32.23 0.3�3 �.548 4.623 0.880 32.50 0.444 �.535 4.771 0.889 32.82 D.608 0.523 4.926 0.9d0 33.21 0.809 0.51d 5.D95 0.913 33.66 1.053 D.497 5.272 0.929 34.16 1.347 0.485 5.461 0.948 34.77 • 1.699 0.472 5.563 0.973 35.44 2.121 0.46D 5.879 0.997 36.20 2.627 0.447 6.109 1.027 37.46 3.235 D.434 5.357 i.062 38.41 • 3.970 0.922 b.523 1.103 39.08 4.864 0.409 fi.909 2.151 40.26 5.964 0.397 7.218 L 206 4�.58 7.339 Q.384 7.553 1.270 43.D4 . 9.495 4.372 7.916 1.345 44.67 11.411 0.359 8.3].a L 432 46.48 i4.623 0.346 6.741 1.534 48.48 �9.486 • 0.334 4.213 1.553 5Q.71 22.�00 0.334 9.354 1.690 51.39 ----------------------------------------------------__---___------------------- NODE 225.64 : HGi, _� 354.133>;EGL= < 354.358>;FLOWLINE= < 353.510> +s*i.*a*i.+r�***f.v.*rr*��r**x+***+r*w***rtx,r***+**�wxx**w*x**xxx**+*twrr**t*:+**** FLOW PROCESS FROM 230DE 225.6D TO NODE 225.bD IS CQDE = 8 UPSTREA�i NODE 225.60 ELEVATEON = 353.51 iFLOW I5 Ai` CRIT�CAL bEPTH) --------------------___-_------------------------------------------------------- • CALCULATE CATCH BASI�I EI3'I'P.ANCE LOSSESlLACFCD) : PIP£ FLOW = 2.74 CFS PIPE DiP.ME�ER =�8.OQ INCHES FLOW VELbCITY = 3.69 FEET/SEC. VELOCIi'Y HEAD = 0.235 FEET CATCH BASTN ENERGY L055 =.2*(VELOCITX HEAD) _•2*{ Q-235j = 4.D47 --------------------------------------------------__--__--_____----------------� I30DE 225.6D : HGL =< 354.415>;EGL= < 354.415�;f'LOWLINE= < 353.5i0> .++++�+.*�*�r+**v�*v.t*w.�.t.,**+*+**..x**..»,.��***..*****.*�***+*+*w+�.**+.*..�«* iiPSTREP.2h PIPE FLOW CONTROL DATA: I30DE NUMSER = 225.60 FLOWi�INE ELEVATION = 353.51 AS$UMED UPSTREAM CONTROL �IGL = 354.13 FOR DOWIIISTREAM RUN ANALYSTS -----------------�___��_______________==_________=_=____==_====�___________ END OF GRADUALLY VARIED FLOW AI+�A�YSIS � * � i + # � t + * * * y T � * * * i * t i x k * * * � k * * # * f * * * * + � � � w ! Y f W i � s * Y Y * i f * Y * Y * * # * t * t * � f k f * * * * � i fi PIPE-FLOW HYDFtAULICS COMPUTER PROGR.AM PACFCAGE � (Reference: LAC�'CD,LACRD, AND OCEMA HYDFtAULICS CRITERIONj ' fc] Copyright 1982-2001 Advanced Engineering Software (aes} Ver. B.0 Re].ease Date: O1/�1/2001 License ID 1509 Analysis prepared by: PR0,7ECTDESIGN CONSULTANTS 701 ' B' STREET, SiF�TE 800 5AN DIEGO, CA 92101 619-234-0349 *��..+�..++*+++�r=s..**.**+ DESCR�PTTON OF S'I'UbY >+'�**�s••+++�..*+�.*.*.+*+ * BRESSI RANCH - i7LTIMATE CdNDITION$ ' * SYSTEM Z00 - LATERAL 6{TpWN GARDEN ROAD 5TA 29+67 LT} * * 100-YEAR ."` *rtwr+xx*+�xrt**t+++t+��r**wr*r+***wrt*+w:ty.�r++,r�+**a�tr�+r*v.**ryx*r**iw*rw* F�LE idAME: 2D0-6.BAT T�ME/DATE OF STC7DY: 15:23 10/24/2042 fw+t*r*+�rtr+�**rtrwf+a*rwwxx***v.**w**tx*****+*+**wtr*�a**rw***+*rtw+****re*r*x*i GRAAiJALLY VARIED FLOW ANALYS�.S FOR PiPE SYS7'EM NOBAL PO�NT Si'ATiJS TAB�,E (Note: "*" indicates nodal goint data used.} UPSTREAM R�TN DOWNSTREAM RUN 3�FODE 3�40D�L PRESSURE PRESSURE+ FLOW PRESSiJRE+ . I3LfiLBER PROCESS HEADLFT] MOMENTUM(POUNDS} DEP'£HfFT) MOMENTUMIPOiFND5) 225.50- . 0.38 7.88 0.15' 17.57 } FRICTIOAi 225.54- 0.35*Dc 7.81 0.35*Dc 7.81 • } CATCH BASIN ---225_60--------------0-50*---------------4-13- -0-35�Dc------------?-87- MP.XI�IiTM 23iJMBEA d�' EI3ERGY BALANCES USED IN EACH PROFILE = 25 `+NOTE' ST�A�IY FLOW HYDRALTLTC HEAD-LOSS COMPUTATIOAiS BASED ON THE MOST CdNSERVATlVE FORMUI�AE FRdM THE CURR�NF LACRD,LACFCD, AND OCEthA i�ESTG�1 MA2d[JALS. �}yrk f f M*i! i* *YY *R! Yi ##* YryrYr Yi 1r *Yri�M %1tYrY yritf **ir***Yr�#tyrYrYrk* *k f? Yrk �k*}}� yr*�Yt*#*�Yrk* * DOWNSTREAI�3 PIPE FI�OW CONTR4� DAi`A: NOi3E NUMBER = 225.50 FLOWLINE ELEVATION = 351.82 PFPE FLOW = 0.9� CF'S PIPE DIAMETER = 18.00 INCHES ASSUMED AOWNSTREP.M C�NTROL HGL = 352.200 FEET ------------------___----------------------------------------------_--_____----- NODE 225.50 : HGL =< 351.969>;EGL= � 353.465>;FLOWLINE= < 351.820� •+�xx�+*++**�*+*�k+++�*t+rttttar*,r*�xx+*+�*+**srtr�*ry+*******+***+**+.**+++�++*ra* FLOW PROCESS FROM NODE 225.50 'I`O NODE 225.50 IS CODE = 1 UPSTREAM NOi7E 225.60 ELEVATION = 353.68 (FIAW TS SUPERCRITICAII} CAI,CULATE FRIC'FION LOSSESILACFCb}: PIPE FLOW = 0.90 CF5 PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 8.25 FEE�` MANNING'S N= O.Q1300 NORMP.L DEPTH(Fi') _^ 0.1� CR�TICAL DEPTY;FT} = D.35 ��UPS'£FLEAM CON'iROL ASSU�'IED FLOWDEPTH { FT} = D. 35 GRALIUALLX VARIED FLOW PROFILE COi1PUTEA INFORMATTON: DISTRI3CE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSUREf • CONTROL { � } { gT } � FT / SEC ) ENERGY { pT } MOMEPI'FUM ( PO[JNDS 1 O.D�a 0.353 2.833 0.476 7.81 a.D02 0.345 2.935 0.476 7.82 a.OD7 0.336 3.043 0.48D 7.64 0_41� - 0.327 3.158 0.4B2 7.69 0_032 0.319 3.281 D.486 7.95 0.053 0.31fl 3.413 0.491 8.03 � 0.081 D.303 3.554 0.498 8.14 ' 0.116 D.293 3.70fi 0.506 8.27 0.160 0.284 3.869 0.517 8.43 0.215 • 0.275 4.045 0.�30 8.61 0.282 0.267 9.236 0.545 8.83 0.365 0.258 4.442 0.565 9.08 0.465 D.249 4.667 0.588 9.36 0.587 0.241 4.912 0.615 9.69 0.736 �.232 5.180 D.649 10.06 0.917 0.223 5.474 0.689 10.48 �.�41 D.215 5.797 0.737 10.96 1.419 0.206 6.156 4.795 11.50 1.767 �.197 6.553 O.BbS 12.12 2.212 0.189 6.997 D.949 12.82 2.792 0.180 7.494 1.D53 13.52 3.575 0.171 8.D55 1.179 14.54 4.6Bfi O.lb3 8.691 i.33fi 15.59 6.413 6.154 9.418 1.532 16.B4 6.25a o.149 9.e77 1.b65 17.57 ------------------------�_-_-------------------------------------------------- NpDE 22S_6D : HGL =< 354.233>;EGL= < 354.35B>;FLOWLINE= < 353.860> t+aft++a*+i*+t**w+*w**k+f+*�a�++r**rr**i*��*yr+rrry*x*rrr+tis+�aw+t**+**w*x*+** FLOW PROCESS FROM NODE 225.60 TO NODE 225.60 IS CODE = 8 UPSTREAM NODE 225.50 ELEVATION = 353.88 (FLOW TS AT CRITICAL DEPTH) CA.LCiiLATE CATCH SASTN �N'i�RANCE LOSSES ( L�iCFCD) : PTPE FLpW = 0.90 CF5 PIPE pIAMETER = 18.DD INCHES FLOW VEi�OCITY = 2.$3 FEET/SEC. VELOCTTY HF,Ab = 0.125 FEET , CATCH BASIN ENERGY LOSS =.2�(VELOCITY HEAD} -,2*� 0.125) = �.025 - ------------------------------------------------------------------------------ � NODE 225.6D : HG� _� 354.383>;EGL= < 354.383>;FI.�OY�INE= < 353.880> .r...*�...�.+*+�+.*«*.,..*+*.t.��..�s....t.�*.....**..*.t*..*.ti*�+.*+.�..**.x.,.** I}PSTREAM PIPE FLOW CpNT120L DATA: NdDE ?�iUMBEFt = 225.60 FLOWLII3E ELEVATION = 353.68 ASSUN4ED LFPSTREAM COI3'T�tOL HGL+ = 354.23 FOR DOYFNSTREAM RUN ANALYSIS F�TD OF GRADUALLY VARIED FLOW ANALYSIS � C � *w+*w�x*aw�x**.�a�w*w+*.�++r�**wr*+�r+x+f+xyw*fx+*r*x+*xx�*Y�yy�**+k�*�*++++r* PIPE-FLOW HYDRAULICS CpMPUTER PROGRAI� PACKAGE � (Reference: LACFCD,LACRP, A?�I� OC�MA HYDAAULYCS CR�TERION) ' {c} Copyright 1982-2001 Advanced Engineering Software iaes} Ver. 8.0 Re�ease Date: Oi/Oi/20D1 Li�ense ID 15D9 Analysis prepared by: PROJECTDESIGN CONSUiTA13TS 701 'B' STREET, SU�TE 8D0 SAN DIEGO, CA 9210}. 61.4-234-0349 .t.�..�*��.�..***+f..{��,.�* DESCRIP'£ION OF STUDY .+.*...*+.*.***.**+��t.+. * BRE55I RANCH - iJi�TTt+�ATE CONDITIONS RESI�ENbT�AL * * SYSTEth 200 - LATER.AL 7(N0. 12 SHT. 8 dF DWG 4D0-8C} � * lOd-YEAR STO�2M EVENT * r**ra�w*t*+*+*wxy+*w*++++f++�#.+*#+f++wx�x*►�***vrr*tx*r**:*r**�*t+*:t**t+� FILE NAME: 200-7.DAT TTME/DATE OF STUAX: D9:a2 1a/25/2Q02 wr�r***w**t**�***rt*arw*t*++t***+**+t+f*tw�f**:yr*rr*ir.:+y**.*x++rt.*r+a***�r�+i GRAL?UALLX VARIED Fi,OW ANALXSIS FOR PIPE SYSTEM NpDAL POIDT'i' STATUS TABLE - (Note: '*' indicates noda� poin[ data used.} UPSTFtEAM R[7I3 DOWNSTREP.M RUN NObE MpDEL PRESSURE PRESSLTRE+ FLOW PRESSURE+ NiJMBER PROC E5S HE.n.D; FT ) MOM£N'f'Ui�f { POL7NDS } bEPTH ( FT ) MpMENP[JM { pdLFidDS i 23D.10- �.01 Dc 105.82 0.86* 1U9.73 } FRICTION 23�.20- 1.01*Dc 105.82 ]..D1*Dc 1D5.82 ------------------------------------------------------------------------------ . MAXiMU�I NL7MBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 NOTE: STEADY FLOW HYDRAULiC HEAD-L055 COMPUTA'I'TQNS SAS�D ON �HE NSOST CONSERVATIVE �'aRMU�,AE FROM THE CLTRFtENT L�ACAD, LACFCD, ANB OCEMA DESIGI3 MAI�F[TAi,S. 1*� �f Yiki# f Yr *1�* * Yr ** ir* iY iFY� **Y� *?! i�#��* i �FiFw�kyr �k f*�yr *�k *Yr ** 1�**Y� Yrlr*Yr�FiM 1rlYrk * YrYr1 *Yr ****Y}* DOWNSTREAM PIPE FLOW CONTROL DATA: NOAE 3dUMBER = 230.�0 FLOWLIAIE ELEVATION = 358.62 PIPE FLOSnT = 6.80 CFS PIPE DIAMETER = 16.00 INCHES AS5[JihED DOWNSTR�AM CONTROL f-iGL = 358.800 FEET' *NOTE: ASSUMED D04VNS'�'REAM CONTROL D£PTH { 0. 18 FT. ) IS LESS THAN Ci3ITiCAL DEPTH( 1.Q1 FT.j -==> CRITTCAL DEPTH IS ASSLTMED AS DOWNSTREA3Q CONTROi. DEPTH ' FOR tTPSTREAM RUN ANALYSIS . NODE 230.10 : HGL =� 359.479>;EG�,= � 36D.134�;FLpw�Ti,IE= < 358.52fl> +�,++�+*.»..+,.***�**..****+��**+�+****+*+*****..,***...�.**.*�.**+***..�*w.*.*+* FLOW PROCESS FitOM NOb� 230.10 TO NODE 230.2a IS COpE = 1 UPSTREAM NODE 234.20 ELEVATION = 35$.BS (FLOW IS SUPERCRITICAL} ____--------------------------------------------------------------------------- CALCULATE FR�CTION LOSSES(LACFCDI: PIPE FLOW = 6.80 CFS PIP� DIAt�4E'�ER = 18.OD INCHES PIPE LENGTH = 21.36 FEET MP.NNING'S I3 = 0.0130D ------------------------------------------------------------------------------ NpRM.AI, DEP'FH {pT} = 0.63 CRITICAi DEPTH (FT} = 1. dl ----------------------------------------------------------�__....____----------- UPSTREAM CONTROL A55[TMED FLOWDEPTH(Fi) = i.01 GRADL7AI,LX VARIEE} P�LOW PROFIL� COMPUTED II3FORMATIOiV: ___________________�_------....___-_------..________-------------------------___.. � DISTANCE FROM FLOW DEPTI-1 VELOCITY SPECIFIC PRESSUKEf CON'I'ROL (�'T } ( FT ) ( FT / SEC } EN£RGY l FT } MOMENT[R�3 ( POUND51 0.000 ].DD9 5.376 1.458 105.82 � 2.160 a.832 4.064 1.069 85.36 2.169 Q.801 4.287 1.087 85.�� 8.250 0.801 4_287 1.OB7 85.34 ------------------------ENfl OF F[YDRACTLIC JUMP ANALYSIS------------------------ I PAESSURE+MQMENTUM SALANCE OCCURS AT 0.37 FEET UPSTRFsAM OP NODE 5Q0.50 � I DOWNSTREAM DEPTH = 1.479 FEET, UPSTR��M CONJUGATE DEPTH = 0.386 FEET I �onE 500.b0 : HGL =� 349.2si>;EGL= < 309.5b7>;��owr.rxE= < 3o8.4sa> *+*x�*+��r�rrr**��*******rtx+*++x*r*****t�*iyytrt***+*+rx*tt+++**+*t+*>��r****+ FLOW PROCESS FRQM NODE 500.60 TO NODE 500.60 IS CpDE = B UPSTREAM NODE 500.60 ELEVATION = 3D8.4B (FLC}W IS SUBCRITICALi ----------------------------------------------------------------------------�- CP,LCULATE CATCH BASIN ENTRANCE LOSSES(LACFCD): PIPE FLOW = 5.50 CFS PIPE DIAMETER = 3b.0a INCHES FLOW VELOCITY = 4.29 F�E'I'/SEC. VELOCTTY HEA]] = 0.285 FEET CATCI-f BASII3 ENERGY LOSS =.2�fVELOCITY HEAD) _.2*( Q.285) = 0.057 M1^NdDE 500.60 : HGL =� 309.624>;EGL= � 3Q9.624>;FLOWI,�N�= < 308.480> *w�*�W+tirt+ti*****+i+*+*t***t*www�x***ft3r*t*trs*��++t+r+r++a++**kw**�*x+x�+**++*+ UPSTFtEAAf PIPE FLOW CONTROL DATA: NODE NUI+�BER = 500.60 FLOWLINE ELEVATIObI = 348.46 ASSiJMED [iPSTR�AM CON'I'RQL HGL = 309.28 FOR DOWNSTREAM RUN ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS s � +**w*xr�fx�xx�++xrx�x*xwr>ra�+r�ri�ff+r�+xrrfr++x.**rr�t�r.xrx�+x�a*�*�*rt*�xr PIPE-FLpW HYDRAULICS COMPUTEFt PROGRAM PACKAGE � (ge�erence: LACFCD,LACRD, AND DCEt�fA HYDRAUF,ICS CRIT�RIqN) ' (cj Copyright 1982-2DOi Advanced Engineering Software (aes) Ver. 8.0 Release Date: O1/Ol/2001 �icense Ip 15�9 Analysis prepared by: PROJEC'i'DESIGN CONSULTAi�Y€`S 70� 'B' STREET. SUITE 840 5AN DIEG�, CA 92101 619-234-4399 a*tx+�*xw*r+*r*w*****x+x*� DESCRIPTION OF STUDY **�*x++*+++*r+t++****+*w�* * BRESSI RANCH - ULTiMATE CQNDITIQNS * * SYSTEM 200 - LATERAL 3{'rpWN CARgEN ROAD AT 'GA5' STREET} * * 100-YEAR * **rw++**«.te+++*r*a*+w..r.*+,r*«�.w.r*��a*«�.w++r+*+****+�**+****rw*+.+*kr* FILE NArfE: 2D0-3.DAT TIt+iE/DATE OF STUDY: 15:00 �0/24/2042 ♦+t+*►t*++r+***�+**i-+fw*t+*+tt*xir�rt**sry�*rri.tf+*�xi�+f+r++++*�+ttrr*rtyr*+wrt GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POINT STATUS TAAL$ {Note: "*" indica�es nodal point data used.) i3PSTREAM RUI3 DOWNSTREAM RUN NODE MODEL PftE55iTRE PRESSURE+ FLOW PRESSURE+ NU�ffiER PROCESS HEAD ( FT ] MOM�NTUM { pp�g j DEPTH {�'T ) MOMENTiJ1�S ( POUNDS } 210.50- 1.69 Dc 495.68 1.10" 522.61 ) FRICTION 210.60- 1.69*Dc 495.68 1.69*Dc 495.b8 � __MAXIMUM_NETMBER-OF_ENERGY_B.�LANCES_USED_IN-EACH_PROFILE_=__25__---__-_-�`--_` NOTE: ST�ADY FLOW HYDRP,i7LIC FiEAD-LOSS COMP[TPAT�ONS BASED ON THE MOST CONSERVATIVE FO�tMULAE FRONS THE CURREPT� LACRD,LACFCD, AND OCEMA • DES IGb} MAi�TIJAi,S . ' ♦+*+***rw*+xrx*rt**w+rt**+++w+*a*,r*k,r*k**rt*rrrt,r*r�++t**wt*xr*�Rx*a�r**++**:t�*�+ DOWNSTREAM PIPE FLOW CONTROL DAmA: NODE NUMBER = 210.50 FLOWi�INE Ei,EVAT'IdN = 312.53 PIPE FLOW = 24.6� CFS PIPE DIAMETER = 30.Q0 �NCHES ASSUMED AOWI3STREAM CONTROL HGL = 3i4.070 FEET *NOTE: ASSUMED bOWNSTREP.M CdNTROL D£PTH( 1.54 FT.) IS LE55 TH.�IV CRITICI�LL DEPTH{ 1.69 FT. } ___> CRITICAL D£PTH IS ASSUMED AS DOWNSTRE.�M CONTROi DEPTH FpR UPSTAE7�3 RUN ANALYSIS - ------------------------------------------------------------------------------ NbDE 210.50 : HGL =� 3.13.632>;EGL= < 3J.5.793>;FLOWi,INE= < 312.530> *k*tt**+rt*ryrttt*r�r***r**+t*�t*+w�**�*x**+*+*yx*+:xr**4**rrs**+w+xx*t+**,r*�*+ FLOW PROCESS FROM NODE 2�D.S0 TO NpAE 210.5D IS CODE = 1 UPSTREAM NODE 2�0.60 ELEVATTON = 313.75 fFi,OW IS SIiPERCRITICALj CALCi.TL�A'F'E FR�CTION LOSSES [LACFCD) : PIPE FLOW - 24.60 CFS PIPE DIAMETER = 30.DD INCHES PIP�. LENGTH = 25.47 FEET MF.FVNING'S N- 0.�1300 --------------------------�___-------------------------------...._...._----------- NORMP.L IIEPTH {FT) = 0.89 CRITICAL DEPTH ( FT'y = 1. 69 i7r S�`REAM CONTROL ASS[JriED FLOWDEPTH ( FT j= 3. 69 __��_______________�_________-_________�_��_____=______�__��__�_________ GRADUALLY VARIED FLDW PRQFILE COMPUT£D �NFORMATIpN: � ------------------------------------------------------------------------------ i}�STANCE FROi+3 FI.�OW DEPTH VELqCITY SPEC�FIC PRESSUR£+ C4NTRpL(FTJ (FT) �FT/5EC) FNERGY{FT) MOMENTUM(POUNDS} 0.000 1.589 6.967 2.444 495.68 a.o29 1.658 7.118 2.445 495.95 0.1i9 1.626 7.277 2.449 495.75 0.277 1.544 7.4C4 2.455 498.11 �0.511 1.562 7.621 2.465 SDO.D7 ' � a.631 1.530 7.808 2.476 5D2.65 1.248 1.499 8.D66 2.q94 505.9R �.774 1.467 8.215 2.515 509.84 2.A24 1.435 8.436 2.54� 514.53 3.2k7 1_403 8.670 2.571 519.99 4.175 1.371 8.918 2.607 526.29 5.323 1.340 9.182 2.650 533.47 6.696 1.308 9.462 2.699 541.61 6.334 1.276 9.761 2.756 550.76 10.289 1.244 ,10.079 2.B23 561.00 12.629 1.212 14.418 2.699 572.43 15.493 1.181 10.78i 2.987 585.12 16.B55 1.149 11.169 3.087 599.19 23.033 1.117 11.585 3.203 614.76 25.470 1.102 11.792 3.263 622.61 NObE 210.60 : HGL =� 315.439>;EGL= < 316.194>;FLOWLTNE= < 313_750> ***www+�+wtx+tr*xw***rx�rx�*��+x*wx+wyw+**x++�*xx*+*+*r**r**kwr**++wxx�***�rxs UPSTREAM PIPE FLOW CONTROL DATA: NODE NUNffiER = 210.6D FLOWLINE £LEVATION = 313.75 ASSUMED T3PSTREAM CONTROL HGL = 315.44 FOR DQWI3STREAM RLFid ANAI.YSIS -------------------------------------------------------------------------------- ------------------------------------------------------------------------------ END OF GRADUALLY VARIED F�,OW ANALYSIS � • 0 019 : 0.�80 I D.184 I � 0.338 I 0.546 I 0.812 I 1.145 I 1.552 I 2.041 I 2.b24 I 3.313 I 4.i25 I 5.480 I 6.2D3 I 7.52b I 9.091 I 10.957 I 13.2a5 I 15.952 I 19.383 I 21.360 I -------------------------� NpD� 230.20 : HGL = < .D02 5.42k 1.458 105.83 1.994 5.46fi 1.459 1D5.B5 ).987 5.512 1.459 1D5.$9 ).980 5.559 1.460 105.95 ' )_972 5.607 �.461 lOfi.03 ).965 5.65fi 1.462 105.12 1.958 5.7Db 1.464 lOfi.24 1.950 5.758 1.4fi5 105_37 ).943 5.810 �.468 105.52 1.936 5.853 1.470 106.69 1.929 5.917 1.�73 106.88 1.921 5.973 1.475 107.a9 ).914 6_030 1.479 107.32 1.907 6.088 1.482 1�7.57 1.899 6.147 1.466 107.84 1.892 6.208 � 1.49� 1D8.14 1.885 6.27D 1.445 108.45 1.877 6.333 1.5D0 108.84 ).870 6.397 1.506 109.1b ).863 6.463 1.512 109.55 I.$59 6.493 i.519 iO4.73 ----------------------------------------------------- 359.889>;EGL= < 3b0.338>;FLOWLINE= � 358.860> ***r*+++**tt*r+wi*w+*ax***►��***k*+ww****+tx+*++*rtx*�wrtYri*+tr**►y+*xrsrtt***• UPSTREAM PIPE FLOW CON'I'ROL DATA: . � NODE NUMBER = 230.20 FLOWLINE ET.,ELrATIpN = 358.88 ASSUMED UPSTREAM CONTROL HGL = 359: B9 FOR DOWNST�tL.�M RUN AI3ALY5I5 ------------------------------------------------------------------------------ END OF GRA�3UALLY VARIED FLOW ANP.LYS�S � . } * 1 * * * * * x � Y * � � Y * ! k r � t * r rt * # # * * * k k * t * M # fi f * ? * � * f # * * f * * k * # # * * # rt * * * � * * * * * k } � * # 1 i + � i PIPE-FL4W HYDRAi.TF�iCS COMPUTER PROGRAM PACKAGE • {Reference: LACFCD,LP.CRD, P.23D OCEMA HYpRAULIC5 C�ZITERION? ' (c} Copyright i982-2001 Advanced Engineering Software (aes) Ver. 8.0 Release Date: 01/0�/2001 License zD ].5D9 Analysis prepared by: PROJECTDESIGN CONSULTANTS 701 'B' STRE£T, SUITE SOD 5AN DIEGO, CA 923D1 619-234-0349 *****+*+**rw*rr***a�*+:r*• DESCRIPTION OF ST[3DY r+**fwt*+**+*+*a*w�xr�***� * SRES52 RANCH - tTLTIMATE CONi]ZTTpNS ' * SYSTEM 204 - LATERAL 8{TOWN GARDE�1 ROAD 5TA 33+41.44 LTj * � 1D0-YEP_R * +**ftrtt**r+y.rrwr**�tr+*x*+ta**+.**ww**w+**r**a*tw*+twrta***itia*+i***w*x**t+ FTL$ 23AM£: 20U-B.DAT TIME/DATE OF S'I`[JDY: 15:30 10/24/2602 Y� iFYr f Yrk***Yr**Yr1�**** ri Y� f YriFiF iriri�Y��k* fY� *+�kf ik*�Y �*�f ii �►�Y}y� yr* f*f * Y� Ki*} }�k W+ikY�y YY�YrY***�r* k GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POIN�' STATUS TABLE (Note: '*' indicates nodal point data used.) UpSTREAN3 RUN DOWAiSTREAi+3 RUI3 siOF7E SriObEI, PRESSURE PRESSURE+ FLOW PRESSiJRE+ I3i3hffiER PROCESS i3EAD ( FT ) MOMENFUM ( POCTNDS } D�PTH ( FT ) MOMEIV'riJM ( POLiNDS ) 235.10- 1.69* 1Z3.93 0.66 61.00 } FRICTIOI3 235.2D- 1.46* 99.�7 0.79 Dc 57.80 • T'MAXIMUM-NUMBER_�F'ENERGY_BAF�ANCES_USED_IN_EACH_PROFILE_=__25-________-__^___ NOTE: STEADY FLOW �-iYDRAULIC HEP.D-L�C155 COMPUTATIONS SASED ON THE MpST CO3�FSERVATYVE FOitMULAE FROM THE CLTRREt1'i' LACAb,LACFCD, AND OCEMA bE$IGN MANIJALS. �.++.*W+r.y,*a,t*+**+r.,r�rv..*.*fr*�**+****+*+*+«*+�*+t****+t++*****�wa*.�*�v�***** DOWfISTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = 235.10 Fi,OWi�INE ELELIATTQN = 367.35 PIPE FLOW = 4.30 CFS PIPE D�AMETER = 16.OQ I�ICHES ASSUMED DOWNSTREAM CONTROL HGL = 369.D4D FEET DI017E 235.Z4 : HGL =< 3b9.040>;EGL= � 369.332>;sLOWLINE= < 367.350> *«,..*.�*.+*****.**..**«*»...*.,**.++.�,.�,.t.��*f+*+�+**+,.++**,,,.++�.�*.*.+t+++*.* FLOW PROCESS FRpM NODE 235.1ti TO I30DE 235.20 IS COBE = 1 iJPS�'RE.n.M NODE 235.2D ELEVATIOI3 = 367.63 {F�,OW SEALS IN REACHj ------------------------------------------------------------------------------- CALCULATE FRICTION LOSSES(LACFCD}; PIPE'FLOW = 4.30 CFS PIPE DIAMETER = 18.D0 INCHES P�PE LENGTH = 21.37 FEET MP.NNZNG'S N= 0.013fl4 bpWNSTREAi� CONTROL ASSUMEi7 PRESSiTRE HEAD{F'F)" = 1.69 PiZESSURE FLOW PRdFILE COMPUTED INFORMATION: DISTANCE FR02+! P�SStTRE VELOCITY SPECIFTC PRE55URE+ CONTROi(FT) HEAUfFT} (F'P/SEC) ENERGY{�'� M�MENTUM(POUNDS) 0.000 1.590 2.433 �.7B2 123.93 18.113 i.500 2.433 �.592 102.98 ---------------------------------------------------_----_-___-__---------------- • ==NORSSPT�-T]EPTH[FT�========0=63====-==---=CRITICAL_DEP'I'HfFT1=----===�=79=====__ ASSLTMED DOWNSTREAM PFtESSURE HEAD(FT} � �.5p ------------------------------------------------------------------------------ GRADUALLY VAFtIEf] FLOW PRflF'I�E COMPUTED INFORMA'i'IdN: ------------------------------------------------------------------------------ DISTANCE FRQM FLOW DEPTH VELOCITY SPEC�FIC PRE55URE+ � CONTROL, { FT ) ( FT � ( FT / SEC j ENERGY ( F'I` ) t+fOMENTUM ( POUNDS 1' �8.1�3 1.504 2.433 i.592 102.98 20.7�4 1.472 2.443 3.565 99.96 21.37� 1.464 2.4A8 �.557 99.17 ------------------------------------------------------------------------------ NODE 235.2D : HGL =< 369.074>;EGL= < 359.167�;FLOWLINE= < 357.610> k i itt*iYYri� Y� Yr *#*Yr fYrlrYr k*Yr►Y� *i�Y� t?f+f iF�i*x W�*f *}'kt� R*Yr# Yr*k *YriFk 1r frYi f1r k�Y �k �FYrri Y� Yr *-Y iF iF* fr i�t*i� UPSTREAM PxPE FLOW CONTROL DATA: NODE NUMBER = 235.2d FLOWLIi�FE EL�IATIOI3 = 367. fi1 A55L7A3ED UPSTREAM CONTROL HGL = 358.40 FOR DCSWNSTFtEAM RUN ANALYSIS ENA OF GRADUALLY VARIED FJ�OW ANALYSIS . • �x+.ww*rr�+xxra��aryx*.�.i�+++..r�a*��rx+►****r��**�*.�t*ywr�**•.++.�*xx*a+�� PIP£-FLOW HYDftAULICS COMPVF£R PROGRAM PACKAGE • (Reference: LACFCD,LACRD, ANA OCEMA HYDRA[7LIC5 CRiTERION} (cp Copyright 1982-2001 Advanced Engzneering Software (aes} Ver. 8.D Release Date: 01/O1/20U7, License ID 1504 Analysis preparad by: PROJECTDESIGN C�NSULTAN'S'S 7Q1 '$' STREE7', SUITE 800 SAN DTEGO. CA 421D1 619-234-0349 +xw*trt*rr*tr�r++�.v.ri*r+�ti** DESCRIPTION OF STiTDY *++r*rr�ry.ry,*swr**�rt***t*+ * BRE5S2 ]ZA.i�ICH - �7LTIMAiTE CONDITIONS * * SYSTEM 200 - LATERAL 9('V' S'Fi�ET STA 5+85 RT} * '� 1 Q 0 -YEAFt * ♦* i4 Y� ��i! W#*# #*}iiYrt� U?1�#f �t*�kf *1� Y Y** **� 1 W 3**Y#YY t 1* W�I*� tll�tt �FMi Y�*M }M? Y�i* i W f i�* YY FIL� NAME: 200-9.DAT TIME/bATE OF S'i'iTDX: 15:31 10/24/2002 *iFYr ik*�F*Yr� Yc iYrt##Y#fYr1� #*i� i*i **f ri* Yrf YrYrri iFY� iYlr**Yr* *ri iF kx iFYri� YrYrY� �FYrY� k**Y� YrYr M*}iFiFi� * iFYri#f # GRA.AUALLY VARIEb F�OW ANALYSIS FOR PTPE SYSi`� NQDAL POINT STATiJS TABLE {Note: '*' indicates nodal point dara used.) UPSTREP.i+f RUP7 DQWNSTRFJ�i�i RUN NODE MODEL PRESSURE PRE55URE+ FLOW PR£SSURE+ NUMBER PROCE55 HEAD{FT) MOMENTUM{pOUNDS) DEPi'H(FT� 2+10lIENTUM(POUNDSj 29D.40- 2_41* 185.24 0.21 25.52 } FRICTION 290.50- 1.04' 40.61 0.44 Dc 13.fi8 . } CATCH HAS�N ---240`50 " ____________1_Q6*_�_.._---_____3�^61________0_44_Dc_ . __4�96_ MP.XI2+5L1M NUS�ER OF II�7ERGY BALA23CES USED IN EACH PROFILE = 25 ----------------------------------------------------------------------------W- NOTE: STEADY FLOW HYDRAULIC HE,�D-LOSS COMPiT�'ATIONS HAS�A ON THE MOST CON$ERVATIVE FOR2hi.TLAE FROM 'T'HE CURREN'i' E.,ACRD, LACFCD, AND OCEMA i]ESIGN MANUALS. +*+*w+****ax+t+++t+tfw+xf*t++.w*ww+**w+rwk*rx*s�*Rr*w**w*r*a***rr***x*x*��k+�y*♦ AOWNSTREAM PIPE FLOW CONTAOL DA'F'A: NODE NUMBER = 240.40 FLOWLIN£ ELEVATION = 359.99 PiPE FLOW = 1.4� CF5 PIPE DIAMETER = 18.D0 INCHES ASSLif�ED DOWNSTREAM C�NTROL HGL = 372.400 FEET NODE 240.44 : HGL =< 372.4a4>;EGL= < 372.410>;FLOWLIi�iE= < 359.990� Ki��tt'�*�1'LiF}+*# Y1�#�t tt�1t y.ikYf kYi 1 Yr YrYr*fti Y* tlYYr i YrlY YYrY *#Y *�1 * fyrikf i4i#Y Yetf* f*#* f1r /r'!r �'LOW PROCESS FROM N�DE 240.40 TO NODE 240.50 IS CODE = 1 UPSTFtEAM NODE 24D.54 ELEVAT10N = 371.35 (FI,OW SEALS IDi REACH) CALCiTi�ATE FRTCTION L055E5(LACFCD): PIPE FLOW = 3.40 CF5 PIPE DIAMETER = 18.DQ INCHES PIPE LEI3GTI-i = 8. 25 FEET MANfiING' S N = 0. 0�300 ------------------------------------------------------------------------------ ______-------_--__----_-____-------------------------------------__-------------___-- DOWNSTREAM CONfiRDi� ASSLTMED PRESSiJRE HEAD ( FT j= 2. 4� -------------------------------..____________________-----------____----------- ------------------------------------------------------------------------------ PRESSURE FLOW PROFILE COI�EPUT�A INk'ORMATIDN: DTSTANCE FROM PRESS�JRE VELOCITY SPECTFIC PFtE55URE+ CONTROL ( FT f HEAD ( FT ) ( F'i / 5EC } EI�iERGY { FT ) M02+9£NTUD3 ( POL7NAS } 0.000 2.4�a 0.792 2.420 185.20 • ___--�____--5TS26T--------_J._540------a_�92-------___1^510J_�____--___ 69.85 NOR2hAL DEPTH(FT} = O.i9 CRITICAL DEPTH(FT} - 0.44 ASSUMED DOWi45TREAM PRESS�RE HEAD(FT) = 1.54 GRADUALLY VARIED FLOW PROFIY,E C6MPUTED INFQRMATION: � --------------------------------__---_--______-__-----------------------------'- DISTRNCE FROM FLAW DEP'FH VELDCITY SPECIFIC PRESSUFtEf CONTRO�, ( FT } ( FT } ( FT / 5EC i ENE�GY ( FT j MOMENTi3M { POLTATAS 1 5.525 1.500 D.792 1.510 8A.85 5.7$2 1.458 D.798 1.468 80.22 6.D37 1.415 0.8�0 1.426 75.6b 6.241 1.373 0_826 1.384 71.19 6.545 , 1.331 O.B44 1.342 65.B2 6.798 1.289 O.B6b 1.300 62_56 7.050 1.246 0.892 1.259 58.43 7.302 1.204 0.920 1.217 59.43 7.553 1.162 D.953 1.175 5�.58 7.8D3 �.124 0.969 1.135 46.87 8.Q52 i.077 1.030 1.p94 43.33 8.25D 1.044 1.066 i.06� 4D.61 ------------------------------------------------------------------------------ NODE 240.50 : HGL =< 372.394>;EGL= < 372.4J.1>;F'LOWi�INE= < 371.350> +w,.f.w...+*�,.�v..t{...,....*....**.+.*..�*...�*..*.t*ti..*.*..w.*+**+�*+��.**.x�* FLOW PROCESS FROM NODE 24D.50 TD NODE 240.5D IS CODE = 8 UPSTREAM I30DE 240.50 ELEVATION = 371.35 (FLOW iS SL7BCRITICAL) ------------------------------------------------------------------------------ CAI,CiJLATE CATCH BAS�N EN�!'FANCE LOSSHS (LACFCD} : PIPE FLOW = 1.40 CF$ PIPE DIAMETER = 18.Op TNCHES FLOW ilEI,OCI�'Y = �.D7 FEETlSEC. VELOCITY i-IEAD = 0.418 FEET CATCH BASIN EiJERGY LO55 =.2*fVELOCI'FY HEAD1 =.2*i 0.018} - p.004 ------------------------------------------------------------------------------ NdDE 240.50 : HGL =< 372.415>;EGL= a 372.415>;Fi,QWLINE= a 371.350� r+rtr**t**y�f��**+>**ti*+*****+t*++rxw�*�,r*�x**�++wx*+**+*wix+wwx*xt„rt„r*�+xxx+>kxw UPSTREAM PIPE FLOW CQNTROL DATA: • NODE NUMBER = 244.50 FLOWLINE ELEVATIpN = 373.35 A5Si7MED UPSTREAbS CONTROL HGL = 37�.79 FOR DOWNSTREAM RUN ADiALYSIS __--_-------____---___------------------------------------------------------------ END OF GRAAUALLX VARIED FLOW ANALYSIS u � r*�w*r+**+i+*+��wtit*+*+:+�*w��*t�*r**>*�*+r�+**r+�*ar�+>+�y��x+*+�*y*+*rt�a*s* PIPE-FLOW HYDRAUL7CS C0�'3PUTEA PROGR�M PACKAGE {Reference: LACFCD,F�71CRI3, AND OCEMA HYDFtA[TL.ICS CRITERION} (c) Copyright 1982-20Q2 Advanced Engineering Software {aes) Ver. 8.0 Release Date: O1/O1/2Q02 License ID 1509 Analysis prepared by: PROJECT DESTGI3 CONSULTAIdTS 741 'B' STREET, SUITE 8Q0 SAN ➢EEGO, CA 921d1 b19-235-647� +r**+w�+,r***w**w*,r*w****ww DESCR�PT�ON OF' STUI)Y {+*�***+*++t,r***w�+**+++*� * BRESSI RANCH - ULTIMATE CONDIT30NS * ' TOWN GARDEN FZOAD - PA-15 * ' 1D0-Y£AR STORM EVENT * �Je �k f�k Yyr#YY# �l*�Y�4f}##yryr+�F�F**`1*1!' y Y i*yr!*****ii k k*ikik'k'k*� i******#tttti i#****t� t* Fzz�E Nr��: zaa-a�.�a�r TIME/DATE QF 8'I'UDY: 13:54 O1/17/2003 tt�++.+**.*.****�..****.*******+,..**++*�++++�+��**.if++**w*+*�*,r*+�,r+�++++..*t GRADUALLY VAAIED FLOW ANALYSTS FOR PIPE SYSTEM NODAL POINT STATUS TABLE {Note: "*" indicates nodal poini da�a used.) UPSTftEAM RUN DUWNSTRF�P� R[TN NQDE MOD�i PRESSUR� PfLESSURE+ FLOW PRESSURE+ . NUMBER PRpC�SS HEAD(FT) MOMENTUM(POUNDSj DEPTH{gT) MOMENTTJN3IPOUNDS} 237.OD- 3.77* 1094.98 I.20 940.73 } FRICTIOPi+BEND ) }iYDRALILYC 3i.JN3P 237.10- 2.66 677.86 1.21* 937.58 } FRICTION+BEND 238.00- 1.86*Dc 737.9� 1.86*Dc 737.91 } JUNCTIOid 238.70- 4.23* 687.95 0.79 17I..75 } FRIC`PIO�I+BEND Z�s.�o- i.s9* a2g.sa a.�� 1�6.�0 } gRICTION ) HXDAAULIC JUMP 239.0�- 1.10 Dc 148.74 D.56* 296.4D ) JLiriCTION 239.14- 1.18 Dc 164.49 - 0.67* 239.16 ) FRICTION 239.24- 1.1B*Dc 1b4.49 1.1B*Dc 164.49 ---------------------------------------------------------------------------__-- 3dAXIMLlM NLFMBER OF ENERGY BALANCES USED �N EACH PROFILE = 25 ------------------------------------------------------------------------------ NO'I'E: STEA�Y FLQW HYDR.AULIC HEAD-LOSS CdMPUTATIONS BASED dN i`HE MOS3' CONSERVATTVE PORMLTI.AB FROM 'PHE CiTRRENT LACRD,LACFCD, AND OCEMA DESZGN MANUALS. *�..**.��.,..�..*..*.+***.�+..***.��.*++.i�***.it+r*�+��f**�++t****+*�s.*rt.�*f*+ DOWNSTREAM PIPE FLOW C4NTROL DATA: NODE NLTMBER = 237 . Q4 FLC}F7�,INE ELEVATION = 368 . 57 PIPE FLOW = 29.90 CFS PIPE DIAME�'ER = 24.00 INCHES ASSiTI+IED DOWAISTREAM CONTROL HGL = 372.340 FEE'I' NODE 237.00 : HGL =< 372.340>;EGL= � 373.747>;FLOWLINE= � 368.570> � iii{ *i t#++i? **i �k1Y iYrilYrYi ti++*? t*#*****�kiY #*ri iF M}*iY iY � Y� i 1 i Y}** ir# *Yr*Yr� ***iFf ri* Y# fiK* t FI.�OW PROCESS FROM I30DE 237.Q0 TO NODE 237.10 IS C4DE = 3 � UPSTREAM NOpE 237.10 ELEVATION � 37�.00 (HYDRAULIC JUMP OCCURS) ------------------------------------------------------------------------------ CALCULATE PIPE-BEND LpSSES{OCE�1A): PIPE FLOW = 29.90 CFS PIPE DIAMETER = 29.QQ INCHES CFNTRAI� ANGLE = 35.100 DEGREES MP.I3NING'S N= 0.01304 PIPE LENGTH = 63.10 FEET HYDRAEFLIC �3lJNiP: DOWI3STREAM RUN Ai3ALYSI5 RESUJ�TS ------------------------------------------------------------------------------ NORAfAI� I�EPTH ( FT }= 1. 2 0 CRI TICAL DEPTH ( FT }- 1. 8 6 UPSTREAM CONTROL ASSUMED FLOWDEPTH(FT) = 1.21 GRADUALLY VARIED FE,OW PROFILE COPfPUTED INFOAMATION: DZSTANCE FROL+S FI,OW DEPTH VELOCITY SPECI�IC PRESSURE+ CON'I'ROL(FT) (FT) (FT/SEC) ENERGY(FT) MOMENTUMiPOUNDS) 0.000 1.249 15.059 4.732 937.58 2.511 1.20$ 15.063 4.734 937.77 5.130 1.208 15.067 4.735 937.97 7.866 1.208 15.071 4.737 938.17 10.731 1.208 15.075 4.738 93$.3b 13.738 1.207 15.079 4_790 938.55 15.900 1.267 15.083 4_742 938.75 20.234 L 207 15.087 4.7Q3 938.95 23.761 1.2a6 15.091 4.795 939.�5 27.504 1.206 15.095 4.746 939.34 3�.490 1.2D6 15.098 4.798 939.54 35.753 1.206 15.1a2 4.75Q 939_74 � 90.334 1.205 15.106 4.751 939.94 95.289 1.205 15.110 4.753 940.13 50.668 1.205 35.114 4.754 940.33 56.5b7 1.205 15.118 4.756 940.$3 63.092 1.204 15.122 4.758 940.73 • - 63.J.Q0 1.204 15.122 9.756 940.73 ------------------------------------------------------------------------------ HYDRAL7E,IC JUMP: UPSTAEAM R[FN ANALYSIS RESLTL'I'S � DOWNSTREAM CONTROL ASSUMED PRE55URE HEAD(FT) = 3.77 ------------------------------------------------------------------------------ PRESSi]RE FLOW PRO�'Yi.E COMPUTED INFORMAT�ON: T�ISTAI+FCE FROM PRESSURE VE�OC�TY SPECTFTC PRESS[iRE+ CONTROL{F'I') HEADIFT) (PT/SEC) ENERGY(FTi MOMEN'iUM(POUNDS) O.00fl 3.770 9.5�7 5.177 1094.4$ b3.100 2.665 9.517 4.D72 877.85 ------------------------END OF HYDRAULIC JUMP ANAi,YSIS------------------------ I PRESSiJRE+�OMENi`UN3 SALANCE OCCURS AT 45.35 FEET �JPS�'REAM QF NODE 237.OD f DOWNSTREAM DEPTH = 2.976 FEET, UPSTREAM COI3JUGA�'E DEPTH = 1.207 FEET � ------------------------------------------------------------------------------ NODE 237.10 : HGL =< 372.209>;EGL= < 375.732>;FLOW�INE= < 371.Oa0> • 4 r # * i ri *# i� i� r1r***-Y * * * i T r�lr * k #� �k �k1r** ** x * ### # # # fill * ***�k k * w Yrkik********Yr*Yr** *�Jrrt-Y **i** FLOW PROCESS FROM NODE 237.10 TO NODE 238.00 IS CODE = 3 UPSTRF.I�M NODE 238.OD ELEVATION = 374.46 {FLOW TS SUPERCRITICAL) CALCULATE PTPE-BENll LOSSES{pCEMAj: • PIPE FLOW = 29.9� CFS PIPE DTAMETER = 24.00 IPICHES CENi'RAL ANGLE = 8. lOfl DEGREES MP.iJNING' S N= 0. 01300 � PIPE LENGTH_=-----_72_58 FEET � NORMAL DEPTHiFT} = 1,22 CRITICAL DEPTHfFT) = Z.86 UPSTREAM CONTROL ASSLTMED PL4WIJEPTH{FT} = 1.86 GRADUALLY VARIED FLOW PROFI�.,E COMPUTED INFOAMA�`IOI3: DISTANCE FROM FLOW DEPTH VELOCTTY SPECIFIC PRESSURE+ CON'I'ROL { FT i ( FT } ( F�I' / SEC ) ENERGY ( FT j MOMF�iTi.Ti�f ( POUNDS a O.QQO 1.861 9.814 3.357 737.91 0.058 1.831 9.916 3.359 738.26 4.230 1.B02 Z0.030 3.365 739.32 0.521 1.772 �0.155 3.374 741.06 0.935 1.742 1fl.290 3.388 743.49 1.481 1.713 30.43b 3.405 746.62 2.158 1.683 10.593 3.927 750.45 3.010 1.654 10.760 3.453 755.01 4.024 1.624 10.940 3.984 760.32 5.229 1.594 11.131 3.52Q 766.4D 6.651 1.565 11.335 3.561 773.29 8.320 1.535 11.551 3.608 781.02 10.273 1.506 11.782 3.&62 789_63 12.559 1.476 12.026 3.723 799.16 15.238 1.946 12.286 3.792 809.67 • 18.389 1.417 12.561 3.8b8 821.20 22.115 1.387 7.2.654 3.955 833.83 26.558 1.358 13.165 4.051 847.62 31.417 1.328 13.496 4.158 Sb2.59 38.484 ' 1.29$ 13.64$ 4.278 878.9$ 46.71A 1.269 14.222 4.411 896.72 57.36$ 1.239 14.620 4.560 9i5.98 • 71.877 �.2�4 15.D45 4.726 935.87 72.580 �.249 15.059 4.732 937.58 --------------------------------------------------------------------------__---- NODE 238.D0 : HGL =� 375.341>;EGL- � 377.837>;FLOWLIAIE= < 379.480> � � � _ _ _ _ ` _= N. _ _ �11'\' �• � � � � � � � _ _ _ _ � _ _ _ _ _ _ _ _ _ _ _ _ _ � � � � � � _ _ _ _ _ _ _ _ _ _ � _ � � � _ _ _ � � � � _ � � _ _ _ _ _ _ _ _ _ _ � � _ _ _ _ _ � � + i 1*ti ** ****yr�Yr tM Yr'k1r'kf tk***'k * Yri� * **iiiF�i*i Y�Y**�!** Yr * * * *******#�ktFYr*tkikikiF*iF*i� # #�'t'� *'k * ** FLOW PROCESS FRO�I NODE 238.40 'T'0 NdDE 23$.70 IS CODE = 5 UPSTREAM NODE 236.70 ELEVATTpN = 379.81 iFLOW [FNSEAI�S Ii�7 REACHI CALCULATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCZ'i'Y (CFS) (INCHES) (DEGREES) ELEVATIpN DEPTH(FT.} (FT/SECi UPS'rx�+M 9.40 29.4Q + 4.00 374.81 1.10 2.992 DOWNSTREAM 29.90 24.00 - 374.48 1.86 9.817 LA`FERAL �I 20.50 �8.00 90.00 375.31 1.47 i1.6D1 LATERAL �2 0.00 a.ao 0.00 0.00 0.00 O.00Q Q5 0.40===Q5 E¢UAT�S BASTN INPU'P=== LACFCD AND OCEMA FLOW JUNCTION FORMULAE USED: DY={QZ*V2-Q1*V1*CQS(DELTAI)-Q3"V3*COS(DELTA3J- Q4*V4*COS{DELTA4))/{(A�+A2}*16.1)+FRICTION LOSSES UPS`d'REAM: MANNIt3G'S N= 0.01300; FRIC`!'IQN SLOPE = 0.00173 DOWNSTREAM: MANNII�iG'S N= 0.01300; FRICTIQN SLOPE = D.d1511 • AVERAGED FRxCTION SLOPE IN JUNCTION ASSUMED A5�0.00842 JUNCTION LENGTH = 4.OQ FEET � FRICTION LOSSES = 0.034 FEET ENTRANCE LOSSES = 0.000 FEET JUNCTiQN LOSSES = fDY+}N1-HV2)+[EfVTRANCE LOSSES} ,3liA7CTI0iJ LOS5E5 = S 1• 34Q) +( 0. 0001 = 1.340 ----------------------------�-------------- NODE 238.70 : HGL =� 379.039>;EGL= < 379.�78>;FLOWLINE= < 374_810> *x+i�*r+****�f*�ay:titfi�r*i�t**r++�*x++t*rs��x+++r�+rt*+++�*w*t*�k+****+*wi�*i�v.*ttvr FLOW PF20CES5 FRO�'3 NODE 238.70 TO NODE 238.90 iS CODE = 3 i7PSTRF..AM NODE 238.90 ELEVATIOI3 = 377.45 (FLOW SEALS IN R�CH) � CAF�CULATE PIPE-BEND LdSSES{pCEMAj_ PIPE FLOW = 9.40 CFS PIPE DIAMETER = 29.00 TNCHES CENTRAi� ANGLE = 19.000 DEGREES MANNING'S N= 0.01300 PIPE LENGTH = 168.36 FEET BENB COEFFICIEN'I'(KB1 = Q.11227 ADJUSTED CENTRAL ANGLE _{19.00Oi*f 16�.83/ 156.36? = 1$.1'S� FI.�OW VELOCZTY = 2.99 FEET/SEC. VELOCI`I'Y HEA� = 0.139 FEET xB=xs*�vELocz�r H�) = f a.1i2)•f a.139) = o.oi6 sF=a.00i-�2 HF=i,}SF = ( 168.36}*(0.001721 = 0.289 TOTAL HEAD L055E5 = HB + HF = f 0.015J+{ p.289} = 0.305 � DOWNSTREAM CONTROL ASSLTMED PRESSl3RE HEAD(FTJ = 4.23 �Pi2E5513RE FLOW PROFILE COMPUTED INFQRMI�TION: � ------------------------------------------- DYS'I`ANCE FRONS PRESS[FRE VELOCITY SPECIFIC PRESSUR�+ CONTitOL { FT ) HEAD ( FT ) ( F`i' / SEC } ENERGY ( f"I' I t40i7EN�UM S POUNDS } 0.000 4.229 2_992 4.368 687.45 160.835 2.000 2.992 2.239 250.54 • -NORhL�1L-DEPTHIFTI--====Y=0-79-===Y====-=CRITICAL-DEPTH(FT}====--==1=10=--==__ ASSUMED DOWNSTREAhi PRESS[JRE HEAD { F'i'? = 2. 00 �GRADUALLY VARTED FE,OW PROFTLE COMPUTED INFQitM.ATION: ---------------------------------------- DISTANCE FROM �'LOW DEPTH VELOCITY SPECiFIC PRESSURE+ CONTROL(FT) {FT) (FT/5EC) ENERGY(FT} MOME�+7TlTI�IP0UND5) 160.835 z.aoa 2.991 2•139 250.54 163.329 1.954 3.Qd4 2.104 243.68 165.736 1.928 3.025 2_070 23'7.06 168.�90 1.891 3.456 2.037 230.62 168.360 1.867 3_050 2.033 229•$8 ----------------------------_--------------------_ NQi]E 238.90 : HGL =< 379.337>;EGL= < 379.483>;FLOWLINE= < 377.950> ***+�+i*:*+*��x+ta*s*t+*+***�aws+++++*ar�+t�at��+*+++t**��xw+*++�*+++�*+*+�**** FLOW PRQCESS FRpM NODE 238.9b Td NODE 239.00 IS CODE = 1 i3PSTFtEAM NQDE 239.OQ ELEVAT�ON = 379.68 {HYDRA�FLIC .7UMP OCCCiRS) CALCiFLATE FRICTION LOSSE5f�1CFCP): PIPE FLOW = 9.40 CFS PIPE DIAMSTER = 24.60 INCI3ES PIPE LEI�iGTH = 141. 98 FEET MANAiING' S N - 0. 01300 HYDRAUI,IC J[3MP �DOWNSTREAM R[FN ANALYSTS RESULTS --------------------------------------------------- - NORMAL DEPTH(FTj 0.77 CRTTICAL DEPTHIFT) 1.10 � UPSTREAM CONTR03, ASSUMED FLQWDEPTH{FT) = 0.56 • -----________________________�� « ___=_______====__________==__�-_____=__�_____= -------- GRI�DUALLY VARIED FLOW PROF�LE COMPU'�'ED INFQAMATION: r 1 � • • DISTP3VCE FROM CONTROL { F`i' ) 0.400 2.5�5 5.089 7.7�9 10.910 13.i79 16.029 18.959 22.O1d 25.169 28.497 31.878 35.977 39.274 43.309 47.610 52.254 57.3ib 62.908 69.397 76.437 $5.060 95.87� 110.b79 135.293 141.98Q FJ,OW DEPTH (FTj 0.563 0.572 0.580 0.5B9 0.597 0.605 0.614 0.622 0.631 0.639 0.648 0.656 0.665 0.673 0.682 0.690 0.699 D.707 0.715 0.724 0.732 0.741 0.749 0.758 0.766 0.766 VELOCITY ( �'T/ S�C ) 12.946 12_680 �2.423 12_175 11.937 11.706 11.483 11.266 11.060 10.859 �0.664 10.476 10.293 10.116 9.945 9.779 9.617 9.461 9.309 9.162 9.Q19 B.BBO B .745 6.613 6.486 6.486 SPECIFIC ENERGY{��) 3.167 3.070 2.976 2.892 2.811 2.735 2.663 2.595 2.531 2.471 2.415 2.361 2.311 2.253 2.21$ 2.176 2.136 2.098 z.os2 2.02$ 1.996 1.9b6 1.937 1.9i0 1.885 1.B85 PRESSURE+ MOMEN'I`UM ( POUNAS 1 246.90 241.93 237.fi5 233.54 229.50 225.82 222.19 218.70 215.35 212.14 209.fl5 206.09 203.24 20fl.�0 197.88 195.35 192.93 19D.60 188.36 186.21 184 . ].5 182.Z7 180.27 178.95 176.70 1�6.70 HYDRAi3Z,IC JUMP : UPSTREAM RiiN A�3ALYSTS RESEJLTS DOWNSTREANi CONTROL ASSiINSED FLOWDEPTH(FT) = 1..89 __--__--___--___------------------------------------------------------------------ ------------------------------------------------------------------------------- GFADUALLY VARIED FLdW PROFILE COMP�I'I'ED I1dF'ORMATION: ------------------------------------------------------------------------------ DISTANCE �'ROM CONTROL(FTj 0.000 �.836 3_646 5.430 7.189 8.923 10.632 12.313 13.96b 15.588 17.179 18.734 20.250 21.724 23.150 24.525 25.840 27.OSB 28.261 29.346 30.331 31.199 31.93� FLpw D�PTH (FTj �.ss� 1.856 1.824 1.792 1.761 1.729 �.697 1.5bb i_b34 1.602 1.574 1.539 1.507 1.475 1.444 1.412 1.380 1.349 1.317 1.285 1.254 1.222 1.19fl V EI,OCI TY c�'r�sEct 3.060 3. fl91 3.126 3.165 3.2�4 3.256 3.306 3.351 3.920 3.4$3 3.55� 3.623 3.760 3.782 3.870 3.963 4 _ 063 4.169 4.283 4.404 4.534 4.672 4.B21 SPECIFIC ENERGY ( F�' } 2_033 2.fl04 1.976 1.948 1.920 1:$94 1.867 1.841 1.816 1.791 1.766 1.743 1.720 1.698 i.676 � 1.656 1.637 1.639 1.6fl2 1.587 1.573 1.563 1_55�. PRESSURE+ 2+30MENTUM { POUNDS } 229.88 224.41 219.Q7 213.88 2Q8.84 203.95 199.22 �94.64 }.9a_24 166.01 181.96 17$.09 174.42 170.96 167.70 164.66 161.84 154.27 156.94 ].54.87 153_DB 151.57 15D.36 • 32.446 1.159 4.980 1.544 149.47 32.871 1.127 5.151 i.539 148.93 33.007 1.695 5.336 1.538 148.74 141_9$0 1.095 5.336 1.538 148.74 ------------------------END OF HYDRAULIC JU1+SP ANALYSIS------------------------ � PRESSURE+MOMENTUM BALANCE OCCURS AT 18.95 FEET UPSTREAM OF NODE 238.90 � DpWNSTREAM DEPTH = 1.534 FEET, UPSTREAM CONJUGA�E DEP'I'N = D_762 FEET ^ NODE 239»00 HGL =< 3B0 443>;EGL= < 383.D47>;FLDWLINE= � 379.880> t*++**�+*tw�*�t+*+***�*�***+w..+***��.��++.�*.**++******��.+*++*��*.***++*��++ FLOW PROCESS FRpM NQDE z39.aa TO N4D� 239.10 IS CODE = 5 UPSTREAM NODE 239.10 ELEVATION = 380.38 {FIAW IS SUPERCRITICAL) CALCULATE JUNCTION LOSSES: PxPE FLOW DIAMETER ANGLE FLOWLINE CRITTCAL VELOCITY iCFSi (INCHESi (DEGREES) ELEVATION DEPT'H(FT.} {F"P/SECj UPSTRF.AM 9.40 J.8.00 O.DD 380.3B 1.18 12.401 D{}WNSTREAM 9.40 24.00 - 379.$B 1.10 12.950 i,ATERAi� #3� 0.00 0.00 0.00 Q.00 0.00 0.040 L�ATERAL #2 O.aD o.aa 0.00 O.aO D.4Q 0.000 (�5 0•pO===QS EQUALS HASIN INPUT==- LACFCb AND OCEMA FLOW JUI�CTIdN FORMULAE USED: nY=(42*�2-41•�1*COSIDEi,TA1}-(Z3*V3"COS{DELTA3)- Q4*V4�COSfDELTA4})/((A1tA2}*16.1}+FRECT�QN LOSSES UPSTREAM: MANNING'S N= 0.01300; FRICTX4N SLOPE = 0.09$38 DOWNSTREAM: P3PNNING'S N= 0.01300; FRICTIQN SLOPE = 0.05759 AVERAGED FAICTxON SLOPE IrF J[FNCTI013 ASSUMED AS 0.05298 � JUNCTION LENGTH = 4.00 FEET FitICTION LOSSES = D.212 FEET ENTRANCE i�OSSES = O.00Q FEET JUNCTION L�SSES = {DY+I-I�11-HV2 j + (ENTRP.NCE LOSSES} JUNCTION LOSSES ={ 0.387)+( 6.QOQ) � 0.387 ------------------ NODE'^ 239 10 : HGL =< 381.Q4b>;EGL,= < 383.434>;FL04TLINE= < 380.38D> �**�+**.x.*�.*�..,..*t..*:******++t*t.+*+**..f�+�..*.�t********+�++�..,:�*****t+ FLOW PROCESS F'ROM �FODE 239.10 `i'Q IVODE 239.20 �S CODE = 1 UPSTREAM NOI�E 239.2d ELEVATIOPI = 387.76 {�L,pW �S SUPERCRITICAL) CAL,CULATE FRICTION LOSSES(LACFCD): PIPE FLOW = 9.40 CFS PIPE DIAMETER = 1$.00 INCHES PZPE LEIVGTH = 136.51 FEET MAAiNING'S N= 0.0130a --------------------------------------- _ NORASAI� DEPTH(FT} = 0.65 CRITICAL DEPTH(F'I') 1.18 UPSTR.F.AM CONTROL ASSUMED FLOwDEP'rx i F'I'1 = 1.18 GRADUALLY^VARIED FLOW PROFILE COMPUTED INFORMATIdN_ +AxSTANCE FROMJ FLOW DEPTFi VELOCITY SPECTFTC PRESSURE+ CONTROL ( FF ) ( FT ) ( FT / S�C j F�IERGY ( F'T ) MOMENTiJ3�7 ( POUNDS j 0.000 1.185 6.277 1.797 169.49 0.019 1.163 6.391 1.796 164.57 0.479 1.142 6.512 1.800 169.81 0.183 1_�2Q b.54Q 1.805 165.22 0.337 1.Q98 6.776 1.812 165.81 0.596 1..077 b.92d 1.821 166.59 0.816 1.D55 7-073 3.833 167.57 • 1.357 1.039 7.235 i.847 i68.75 1.57fi 1.012 7.407 1.8b5 170.15 � 2.085 0.991 7.569 �.885 171.79 2.fi98 0.969 7_762 1.910 173.67 3.433 0.948 7.9B8 1.939 175.81 4.303 0.925 8_206 1.972 178.23 5.341 0.944 8.439 2.�11 180.94 6_576 0_883 8.686 2.055 183.98 $.OSO 0.861 8.954 2.10b 187.35 9.818 0.84D 4.232 2.164 191.a9 11.954 a.818 9_533 2.23D 195.23 14_S64 4.797 9.855 2.306 �99.80 17_802 0.775 10_200 2.392 2D4.83 21.948 0_754 10.571 2.490 2�0.38 27_286 Q.732 10.970 2.602 216.47 34.b92 0.724 11.400 2.730 223.16 45_827 0.689 I1.865 Z.$76 230.55 66.153 0.667 12.367 3.044 238.66 136.610 0.666 12.398 3•054 239•16 -------------------------------------- NOAE 239.20 : HGL =< 388.945>;EGL= < 389.557>;FLOWI.,INE= � 387.76�> ****.******�w..*+*�**t*.****�+...*+*�*�***..�w�*�*�***��.�*.**+*+.�.*****.**� UPSTRER.M P�PE FLOW CONPROL DATA: NODE NUMB�R � 239.20 FLOWLINE �LEVATION = 3$7.75 ASSETMED UPSTAEAs7 CONTROL HGL = 3$8.94 FdR DOWNS3'�tEAM RUN ANALYSZS END OF GRFaDUALLY VARIED FLOW ANALYSIS f ' � xx**��**.aa�tr*r**+r��+wt*�x�x*+**+*�t**s+**wwr�*�r�+i++fr#7*rxx*+*+t�+t��:+�t PIPE-FLOW HYDRAULICS CONfPUTER PROGRAM PACFCAGE � IReference: LACFCD,LACRD, AND OCEMA HYDRAULiCS CRITERTON) ' {c] Copyright 1982-2DD1 Advanced �ngineering Software (aes) Ver. 8.0 Release Date: D1/O1/2001 License ID �509 Analysis prepared by: PROJECTAESIGN CONSULTAN'fS 701 'B' STii£ET, SUI'FE 8D0 SAN DIEGO, CA 92]01 614-234-0349 *.***...,.+�.+..��v.+..*.�. DESCRIP�'ION OF STUDY *+�.+.+*.**...*+�.�s.�++,.. " BRESSI RANCH - UL�IMATE C013DI'i20id5 * * 'AA' STREET: PA-15, LATEAAL 1 * * iO4-YEA,R STORI+4 EVFNT * ♦Y )t t i1 i�1 i Yr* ii *? k1r *i�Y�i1kY� �**� *Yt W s*41l�YY 4*4tM1�f Y�* iF 1Yr * W* YrYr1r*ik iFiFiFYriFY�*YI Yc* # f Y' f i# FILE I3AME: 240-AA3.DAT T'TME/DATE OF STUDY: 16:28 10/24/2Q02 rw*r*ttt+*r****xrrtr***+**+*+*r*w**,r�*x,rw+*,rrt+r+*+xx*w*r*rttir*x*+t**+*r+*rw**x** GRADUALLY VARIED FLOW Al1Ai,YSIS FOR PIPE SYSTEM NODAL POINT STATUS TABLE fNote: "*" indicates nodal point data used.? UPSTR�PM RUN DOWI3STREAM ftUiQ NODE MODEL PRESST3RE PRESSURE+ FLOW PRESSURE+ NUMB£R PROCESS iiEAD ( F"I' } I�OMENTiJDS ( POUNDS } DEPTH { FT ] MOMEN�'UM { POL7ND5 j 238.10- 3.69* 350.52 0.46 1D5.47 } FRICTION 238.20- 2.47* 215.77 0.85 Dc 68.57 } CATCH BASIN 238.20- 2.61* 205.24 b.85 Dc 23.61 MAXIMUP4 NL7MBER OF ENERGY BALA23CE5 USED IN SACFi PROFILE = 25 ------------------------------------------------------------------------------ NOTE : STEADY FI�OW HYDRAi}LIC HEAD-LQSS COMPUTA�`IONS BASED OI+} THE �IOST CpN$EI�VA'iIVE FORMLiL�AE FROM THE CURRENT F�ACRD,LACFCD. ANA OCEMA D £ 5I C�i MP.I3f.iALS _ **.,,**x.,.+�.+�*+*�**.�**.+*...,.,...,,,.�*,.,,**�,..*.�*:*x.**.*+*.....+:,..**x****++* bOWNSTREAM PIPE FLOW COI3TROL DATA: NODE I3[TMi3ER = 238.1Q FLOWLINE ELEVATIQbI = 375.31 PIPE FLOW = 4.90 CFS PIPE DIArfETER = 18.00 INCHES ASSUMED AOWNS'£RERM CONTROI.� HGL = 379.000 PEET ------------------------------------------------------------------------------ 230DE 238.10 : HGL =< 379.D00>;EGL= < 379.119>;FLOWLINE= < 375.3�.0� s*y*�**x*r+�tv.+�f��.x�*�+*+�ry�*r�tir*t+*+*+x*twrrt***��rsaaa+*+f++++*�+�*y+t++*++x FLOW PROCESS FROM NODE 238.�0 Td N�i}E 238.2D I5 CODE _ � UPSTREAM idODE 238.20 ELEVATIpI3 = 376.55 {FIAW IS UNDER PAESS[7R£} CALCULATE FRICTION LOSSES(LACFCD}: PIPE FiOW = 4.9D CFS PZPE DIAkhETER = 1B.00 INCHES PIPE LEt3GTH = 8.25 FEE� MF�iNTNG' S N = 0.01300 SF=[Q/i4j**2 = (( �.90}/{ 105.D65})*�Z - D.4p218 HF=L'SF = f 8.25}�{O.D021$1 = 0.018 ------------------------------------------------------------------------------ NODE 238.20 : HGL =< 379_O18>;EGL= < 379.137>;FLOwL�NE= < 376.550> tY+w+�.+i.+.**w+t*x**+wxx*x.��.++rf+ti�tawr*rr�r**+x**r�*,rr+*+*�+*�+**�ftw******s FLOW PROCESS FROM NODE 238.2D TO NODE 23$.20 IS CODE = 8 UPSTREAM NODE 236.20 Ei,EVATION = 376.55 {gLOW I5 l7NDER PRESSURE} • ----------------------------------------------------_------------------------- CALCULA'i'E CA'I'CH BASII3 ENTRPNCE L05SES(LACFCD) : PIPE FLOW = 4.94 CFS PIPE DIAt�ETER 18.40 INCHES FLOW VELOCI`I'Y = 2.77 FEET/SEC. VELOCITX HEAD = 0.139 FEE'i CATCH BASTN ENERGY L05S =.2"[VELOCITY HEAD} -,z*( 0 1191 = 0.024 ------------------------------------------------------------------------------ NODE 238.2� : HGL =< 379.161>;EGL= < 3�9.161>;FLOWLINE= < 376.550� � >***rrt*<*+++*+s*+ax*+r*x*r*��wxx*##xxwr**w�rr**xrx*++**x+*rw*++xrx*+xr+*+w+*** UPSTRF.PsS PIPE FLOW CONTROL DATA: AiODE NUMBER = 238.20 Fi,OWLIDTE FT,EVATION = 376.55 ASSUMED UPS'i'REAM CONTROL HGL = 377.�0 FOR DOWNSTREAM RUN ANALYSIS ------------------------------------------------------------------------------ END OF GRADUALLY VARiED FLOW ANALYSIS s • � APPENDiX 4.1.5 SYSTEM 400 (`A' STREET) � s i` � * * * * f 1 f 1 * ! # i � � * w k k * * * * * � � ? * * * + * + * * � * � Y * * * � w * � * # * * * � * * * * * i w * k k * k � i * � * * * * � � * f * } f PIPE-FLOW HYDRAULICS CO3�3PUTER PAOGR�1t�S PACKAGE iReference: LACF'CD,LACRD, AND OCEMA HYDRAI]LICS CftITERION} (c) Copyright 1982-2Q02 Advanced Engineering Sottware (aes} Ver. 8.0 Release Date: Q1/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTAN'I'S 7dl 'B' STREET, SUITE $00 SAN DIEGO, CA 921D1 619-235-6471 *�+++iit+++�**ttf***++**t� DE$CRIPTION OF STi7DY +x**+*+**+++*+ftw+**s*++.++ * BRESSI RANCH - ULTIMATE CONDI'3'IO]VS * * SYSTIIH 4d0 - PA2 TOWN GARDEN ROAD S'FATION B+ld * * 100-YEAR NODES 440 TO 945 (DOWNSTREP.M OF CDS UNI'I') * .**++i�*i.*+++**x�*xww*r«***w**:��+++.***�*++,t�w+***t*+�***+�+i+,t**r++**�wt+ FILE AiAME: L400A.DAT TIME/DATE OF STUDY: Q8:44 dl/17/2003 ww*�r*y+rtii*++�rtt*+s*rs**rr*:ssst***+tts*+t�+tt**+*t*st**aa*++t+*tt*w+t**+****w . GRADUALLY VARIED FLOW ANALYSIS FOR PFPE SYSTEM NOBAL PpINT STATUS TABLE {Note: '}' indicates nodal point data used_) UPS'i'RF.AM RUN 170WNSTREP.M RUN NODE MODEL PRESSURE PRESSURE+ FLOW PRESSi7AE+ C3LTMBER PROCESS I-iEAD ( FT? MOMEid'I'UM { POUNAS) DEPTH ( FT ) MOMENTiFM { POiJ�IDS j �" 400.00- 5.47 4349.50 0.96* 9512.53 } FRICTIdN 401.00- 5.47 435i.09 a.94* 9870.88 } FRICT�ON 405.00- 3.10*Dc 3075.78 3.1D*Dc 3a75.78 MAXiMUM NUI�fBER OF ENERGY BAT�ANCES US�A IN EACH PRQFTLE = 25 NOTE: S'I'EAI)Y FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS SASED DN THE MOST CONSERVATIVE FdRMULAE FROM THE CURRENT LACRD,LACFCD, AND OCEMA DES�GN MP.N[JALS. ! �k!**tk �1rtkYrlr*'M k'ki **tk # # t*t �k Yr * # *#tt tir* * * k*'k'kYrkilr'M * f� k *Yr } Yr Yr *Yr'k f iY 1r *i'k*'k** *Yr }M k�kM ri Yc*1r * * DOWNSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = 400.00 Fi,OWL�NE Ei,El7ATION = 197.53 PIPE FiOW = 102.50 CF"S PIPE DIAMETER = 42.00 INCHES ASSUMED DOWNSTREAM CpNTROL HGL = 203_400 FEET ------------------------------------------------------------------------------ I3pDE 400.00 : HGL =< 198.493>;EGL= � 233.704>;FLOWLINE= < 197.53D> ,r.tf++�.+�+��w�,r*x.x.*r�*..****...*s**�**�++�*,rw****,rt+***x*.+r+***++*++tr�r.r+ FLOW PROCESS FROM NODE 4Q0.4Q TO NOdE 401.OD IS CODE = 1 UPSTREAM NODE 401.a0 ELEVATION = 197.6D {FLOW IS SUPERCRITICAL) -------------------------____-------------------------------------------------- CAL�CiTi�A'PE FRIC'?'I4N LOSSES (LACFCD) : PIPE FLOW = 102.50 CFS PIPE DIAN3ETER = 92.OQ INCHES PIPE LENGTH = 7.00 FEET MAI3NING'S N= 0.01340 ------------------------------------------------------------------------------ NOFLMAL DEPTH{FT) = 2.93 & 3.49 CAITICAL DEP'FH{F'F) = 3.10 NOTE: SUGGEST CONSIDERATIpN OF WAVE ACTION, UNCERTAINTY, ETC. ' ------------------------------------------------------------------------------ � ------------------------------------------------------- - ---------------------- UPSTREAAS CQNTitOL ASSiTMED FIsOWDEPTH {FT) = 0_ 94 � GRADUALLY VARTED FLQW PROFILE COMPUTED INFQF2hSATION ` " VT==== --------------------------------------______---------------------------------- DISTANCE FROM FLdW DEP�'H VELOCITY SPECIFiC PRESSURE+ COAI'I'ROL ( FT } ( Ffi ) ( FT / SEC } EI�ERGY ( FT j MOMENTUM i POUNDS ) 4.000 0.938 99.428 38.897 9870.88 7_000 fl.963 97.608 36.179 9512.63 NDDE 401.00 : HGL =< 198.536>,EGL= < 236.497�;FLOWLI�IE= < 197.600� i� � f *#M#'t'� # t *�'*t1 fY #i i i �k�! i� t �t i �k Yt * t i*t*'k *tkYriF*Yc� * *Yr***fir#*# *****# �'k **14*Y�#'k#Y�tt'kY�*y"t FLOW PROCESS FROM I30DE 401.00 TO NODE 405.00 IS CdDE _� UPSTREAM NODE 405.00 ELEVATION = 262.Qa (FL�OW IS SUPERCRITICAi,) ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSES(LACFCDj: PIPE FLOW = 102.50 CFS PIPE DIAMETEA = 92.00 iNCHES PiP� LENGTH = 153.00 FEET P3ANNTNG'S N= p.01300 NOitMP.L DEPTH(F'P} � 0.94 CRITICRi DEPTH[F'i'} - 3.10 UPSTREAM COI3TROL ASSUME]J FLOWDEP'TH(FT) = 3.16 GRADUALLY VARIED FLOW PROFILE COMPIi'I'ED INFORMATION: ------------------------------------------------------------------------------ DYSTANCE FFZOM FLOW DEPTH VELOCITY SPEC�FIC PRES513RE+ CONTROL ( FT ) ( FT i { FT/ SEC ) FNEKGY ( FT ) MpE�ENTUM { p(}[JprDS ) O.Q00 3_096 11.381 5.�09 3D75.78 fl.017 3.O1D 11.542 5.i16 3079.b2 0.069 2.923 11.936 5.137 3091.29 0.161 2.837 12.266 5.175 3�11.13 � 0.296 2.751 12.633 5.230 3139.63 D.481 2.664 13.039 5.306 3177.38 0.724 2.578 13.489 5.9D5 3225.11 1.a33 2.492 13.986 5.531 3283.69 1_42D 2.405 14.536 5.fi88 3354.16 1.900 2.319 15.�44 5.882 3937.76 2.490 2.233 15.817 6.Z2D 3535.92 3.214 2.146 16.565 6.910 3650.39 9.101 2.060 17.397 6.763 3783.23 5.1BB 1.974 18.326 7.192 3936.91 5.527 1.887 19.367 7.715 4114.43 8.185 1.B01 20.539 8.355 4319.45 10.254 1.715 21.863 9.141 4556.46 12.865 1.628 23.367 i0.I12 9831.03 Ib.2D5 1.542 25.a88 }.3.322 5150.15 20.559 1.456 27.070 12.841 5522.72 26.38fl 1.359 29.37D 14.772 5960.19 34.495 1.283 32.064 1.7.258 b477.49 46.232 1.197 35.253 20.506 7094.53 65.1Qfi 1.110 39.070 29.829 7838.23 101.933 �.024 43.706 34.705 8745_98 153.000 4.938 � g9.426 38.897 9870.88 NODE 405.00 : HGL =� 265.096>;EGL= < 257.109>;PLOWLINE= < 252.000> �*.***f�.�t.*f***.****��.*t�*�*t�+>�,.***�k**>.******.,,�******....*�.�...*>+�* UPSTREAM PIPS FLOW CONTROL DATA: NODE AiiJMSER = 405.00 FLOWLTNE EL�VATION = 262.00 ASSUMED UPSTREAM CQNTROL HGL = 265.10 FOR DOWNSTREAM RL7N ANALYSIS • ===--T��-�=�______�________________________________________________ti��r�====_ • * } # f * * * * * # * * * * * * i * * t * # * i � N 1 Y i Y ti Y t � k � t f i i Y i * � i ! i # * i k * * * * * f * * * W k � Y * * * � f f * # � i * i h k PEPE-FLOW HYDfiALTT.,ICS COMPUTER PROGRAM PACKAGE (Refexence: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION) (c) Copyright 1982-2002 Advanced Engineering Software (aes} Ver. 8.0 Rel�ase Date: D1/Oi/2002 License FD 1509 Analysis prepared by: PROJECT DESIGN C�NSIJF,TAN'I'S 70Z 'B' STREET, SUFTE B00 SAN DIEGO, CA 92�01 619-235-b471 *****.+****+t++:�**+*,r++s* IIESCRIPTIQN OF STUDY ******r**�*4°*+*+***�++*�* * BRESSI R�I+1CH - C7LTIMATE CQNDITIONS * � SYSTEM 440 - PA2 TOWN GARD�7 ROAD STATI03d $+10 * * PIPEFLOW NOAES 405.1 TO 410.3 * *********�+,.�,.*****ttttt****..+�+.*��ww..+*��+*�.***„**,.�*.**�*****tt�*** FILE NAME: L400B.DAT TIME/DATE OF STLTDY: 0$:49 01/17/2D03 YY##Yi #�k * i i Y#i rt t�k1i �*#**** Y� }Yri�M #* Y� *Y� Y� kYrYi Yrfk *YrY� f**�kt# t tY 4f! �k iii;*****i� f* i****# * GRADUAI�LY VARIED FLOW AI3ALYSIS FOR PIPE SYSi'EM NODAL POINi' STATUS TABi,E SNate: '*' indicates noda� poin[ data used.) UP59'REAM RUN DOWNSTREA�] RUI3 NODE MODEL PAESSURE PRESSURE+ FIAW PRESSUR£+ NUMBER PROCES S HEAD ( Fi' } MOMENTUM { pQt7NpS } 17�PTH {� J MOb4F�iTUM ( POLiNDS j 905.10- 5.20y 2952.38 1.76 1829.74 } FRICTIOI3 446.10- 5.00* 2392.38 1.78 181$.O1 } ,TUNCTTON 406.90- 6:16* 2310.20 1.18 1801.95 ) Fxzc�rzorr 410.10- 5.66* 2158.36 1.10 1959.80 ] JUNC7'IdN 4J.0.20- 5.79* 2067.90 0.95 1984.99 } FRICTION } HYDRAULTC JUMP 410.30- 2.16*Dc 1fl7.8.93 2.16•Dc 1018.93 } CATCH BASIN 41D.30- 3.73* 760.�6 2.15 Dc 281.65 MA.XIMUM NU2+3BER pF ENERGY BALANCES USEd IN EACH PROFYLE = 25 ------------------------------------------------------------------------------ NpTE: S'FEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIQNS BASED OTI THE MOST CONSERVATTVE FORMLTi,AE FROM THE CURRENT LACRD,LAC�'CD, ANp OCF.MA �ESTGN MP.NUA3,5. # i� ** i f Y� }#* iF �h * 1r Yr ** iF **** t! Yr Y 1 1 Y� i Y* Y 1 Y Y f 1 Y f�F ik �k i## f#}* y� y� * yr y� y yr *�Ir * t*#*# Y i Y# Y i Yr �c Y Y* �c t DOWNSTREAM PIPE FLOW CONTROL DATA: NODE NL7MSER = 405.10 FLOWL�NE ELEVATION = 2b3.00 PIPE FLOW = 56.10 CFS PIPE DIAMETER = 30.OD INCHES ASSUMED D04J[QSTRF.AM CON'PROL HGL = 258.200 FEET NODE 405.10 : HGL =� 26B.200>;EGL= < 270.228>;FLQWLINE= � 263.000> �*.**.�.*****+�.��+�+++***+t++��....,�*....,,..*�.*,.**>**�x..�..++�{�**.��+**.*�***++ FLOW PROCESS FRONi NODE 405.10 TO NODE 406.10 I5 CODE = 1 • UP5TF2EAM NODE 406.10 ELE�7A'3'ZON = 263.57 (FLOW IS UNDER PRESSURE} _----------------------------------------------------------------------------- • CALCULAT� FRICTI4N LOSSES(LACFCD): PIPE FLOW 55.10 CFS PIPE DIAMETER = 30.00 INCHES PIPE LENGTH = 24.d0 FEET MANNING'S N= 0.013DQ SF=fQ/K}**2 = ({ 56.101/� 410.164}a*t2 - p.01871 HF=L*SF = f 24.40)*(4.61871) = 0.374 NODE 906.10 : HGL =� 268.574>;EGL= < 270.602>;�LOWLINE= < 2b3.570> .*�+*.*.*.t*�.�*.**�t*+*f**�***�.�++*�**�.**.**+*�+**�**.3�,.*.+��.+.*�.+.�.*. FLOW PROCESS FRpM NODE 4a6.10 TO NODE� 406.90 IS CODE = 5 UPSTREAM NObE �a�.ga ELEVATION = 253.90 (FLpW IS UNDER PRESSURE} ------------------------------------------------------------------------------ CALCULA'i'E JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CRITiCAL VEi,OCITY {CFS) (TNCHES) (DEGFtEES} ELEVA'd'ION l7Ep`i'H�FT. f (F'I'/SEC} UPSTREAM 45.20 30.00 4.00 263.9Q 2.23 9.208 DOWNSTREAM 56.10 30.00 -- 263.57 2.36 11.429 I,ATERAi. #� 10.90 24.OD 94.00 264.07 3.18 3.470 LATEFtAI, #2 0.40 O.DO Q.00 4.D0 4.40 D.000 Q5 0. bO===Q5 EQUALS BASII3 INPiJT=== LACFCD �1ND OCEMA FLOW JUNCTION FORMULAE IJSED: DY=;Q2*V2-Ql*V�"COS(DELTAI)-Q3*V3'CQ5(DELTA3)- Q4`V4*COS{BELTA4})/((A1+A2)*16.1)+FRICTION L05S�S UPS'TREAM: MANNING'S N= O.D130D; FRICTION SLUPE � 0.0121.4 D4WNSTREAI�4: MAPTNING'S N= 0.01300; �'RTCTTpN SLOPE = 0.01871 AVERAGED FRICT�ON SLOPE IN 3UNCTION ASSiiMED AS 0.07.542 JUNCTION LENGTIi = 4.00 FEET FRICTION LOSSES = 0.062 FEET EI3`I'RANCE LOSSES = a.Q00 FEET • --JUNCTION LOSSES = (DY+HV1-HV2j+(ENPRANCE L055E5) JUNCTION LOSSES =( 0.773i+( 0.000} = fl.773 � NODE 406.90 : HGL =< 270.059>;EGL= < 271.376�;FLOWLINE= < 263.90D> t�f.wv.�r.�*��r++*+**��**,.*.,,.�******++*+++*+*+�+***+�**+*�*<*.*****.**�*�+*+��r FLOW PROCESS FROM NODE 406.90 TO NODE 410.10 IS C�DE = 1 UPSTRF.AM NODE 410.1D ELEVA'I'IQN = 264.76 (FLOW IS UNDER PRESSUREJ ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSESfLACFCD): PIPE FLOW - 45.24 CFS PIPE DIAN3ETEFt = 30.00 iNCHES PIPE LENGTH = 30.Oa FEE'i MAA€idING'S N = Q.01300 SF={Q/K}**2 = ({ 45.20)/{ 410.182})�t2 = O.Oi214 HF=L*S�' _ ( 30.Q0)*(0_di214) = 0.3b4 ----------------------___-------------------------------____-_--___--____-__---- NQDE 410.10 : HGL =< 27D.423>;EGL= < 271.740>;FiOwE.zI3�= < 264.764> **+t�f+.+r+*��i**��***�.,*..�....�++i..+++�++.+,r++,,.**.,f.*.*�.�,..*.,�.,...*****t+ FLOW PROCESS FROM NODE 410.1D TO NOD� 410.2Q IS CdDE = 5 93PSTREAM NppE 410.20 ELEVATION = 265.10 (FLOW IS UNDER PRESSURE) ------------------------------------------------------------------------------ CALCULATE JiFNCTI033 LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CRI`PICAL VELOCITY (CFSf IINCHES? {DEGREESI ELEVATION p�PTH(FT.j {FT/SECJ UPSTRF.� 41.40 30.D0 0.00 2b5.10 2.15 B.434 DOWIVSTREAM 95.20 34.00 - 254.76 2.23 9.208 LATERRL #1 3.$D 18.00 90.D4 266.10 0.75 2.150 LATERAi� �2 a_QO 4.04 O.OQ 0.0� O.OQ O.d40 Q5 a.ao-=-g5 EQUALS BASIN INPUT=== • I.ACFCD AND OCEMA FLOW JUNCTION FORr3ULAE USED: DY=(42*V2-Q1*V1*COS(DELTAIJ-Q3*V3'COS(DELTA3)- � Q4*V4*COS(DELTA4}J/((A1+A2)*16.1)fFRICTION LOSSES UPSTREAM: MANNING'S N= 0.01300; FRICTIO� SLOPE = O.OI019 DOWNSTREAM: MANNING'S N= 0.01300; FRICTTpN SLOPE = O.Q�214 AVERAGED FRICTION SLOPE IN JUNCTION ASSUrSED AS �.01116 �UNCTION LENGTH = 4.OQ FEET FRICTxON L05SES = 0_D45 FEET ENTRANCE L05SES = O.fl00 FEET JUNCTION LOSSES = (DY+4-IV1-HV2)+(ENTRP.NCE T,OSSES) �[FNCTION LOSSES = f 0.257f+( O.OD4) = 0.257 NODE 410.20 : HGL =< 270.892>;�GL= < 271.997>;FLpWLINE= < 265.100> �i i 1 i yrY#Yr**i t*tY##Yy � 11�! �k �ki �i 11! �F Y******� M k**Yr *YrYrY� *Yril Y� YriY Y� Yr*i'M *tM *� ir�k k** �'k* �FYrtk*ri 1� Y� Fr,OW PROCESS FRO[�S F30DE 410.20 TO NODE 41D.34 I5 CODE = 1 UPSTAF.AT7 NODE 410.30 ELE�iA'rlpN = 276 _ 62 (HYDRAULIC ,7E1MP pCCU�t51 ------------------------------------------------------T-----___--_-_-_--------- CALCULATE FRICTION LOSSES(LACFCD): PIPE FLOW = 41.40 CFS PIPE DIAMETER = 30.00 INCHES PIPE LENGTH = 72.00 FEET MANNING'S N- 0.01300 ------------------------------------------------------------------------------- HYDRAULIC ,TUMP: bOWNSTREAM RUN ANAi,YSIS RESULTS ______________..----_______________-------------------------------------------- fVORM�� DEP'£H ( FT }= 0. 6 6 CRITICAL DEPTH ( FT j= 2. 16 ------------------------------------------------------------------------------ UPSTREAt+9 CONTROL ASS[FMED FLOWDEPTH(k"I'} - 2.16 _____�_�____�_________�------------------------------------------------------- GRP.DUALLY VARIED FLOW PROFIi,E COMPLTTED INF4RMATION: ------------------------------------------------------------------------------ DISTAI3CE FR4M FLOW DEPTH 1TELOCITY SPECIFIC PRESSURE{ COi3TROL ( FT j ( FT � ( FT / SEC j EPiERGY ( FT ) I�OMENTEiM f PUUNDS i 0.000 2.158 9.187 3.469 1018.93 D.022 2.706 9.379 3.473 1019_84 0.09p 2.054 9.590 3.463 1022.63 �.210 2.002 9.822 3.501 1D27.38 0.386 1.950 10.075 3.527 1034.20 0.626 1.B98 10.352 3.563 1�43.20 0.938 1.846 10.653 3.609 1054_5A 3.333 1.794 10.984 3.667 1D68.39 1.624 1.742 11.337 3.738 1084.94 2.425 1.689 11.725 3.B25 1104.41 3.156 L 637 12.148 3.930 1127.07 4.OA1 1.585 12.6Q9 9.055 �153.22 5.108 �_533 13.1�3 4.205 �183.20 b.397 �.481 13.554 9.382 �217.41 7.954 t.429 14.2b9 9.593 �256.34 9.84b 1.377 14.935 4.843 �3Q4.52 12.157 1.325 15.669 5.139 �350.61 15.OD5 1.273 1b.480 5.493 i447.38 16.559 1.22i 17.381 5.935 �471_74 23.074 1.169 �8.3B6 6.921 t544.8J. 28.927 1.117 19.510 7.03i 1627.93 36.793 1.064 2a.779 7.�70 1722.73 �7.915 1.D72 22.205 8.673 1831.24 65.105 0.960 23.632 9.785 1955.98 72.000 0.949 24.208 10.Q55 1984.99 ------------------------------------------------------------------------------ HYDRAULSC �Ti[�4P: UPSfiREAM RUN ANALYSIS RESUi,TS ------------------------------------------------------------------------------- --------------------------___-_--_---------------------------__------------------- DOWNSi'REAM C�NTROL ASSUMED PRESSURE HEAI)(FT) = 5.79 ----------------___---------------------------------------------------------------- ------------------------------------------------------------------------------ � PRESSURE FLOW PAOFILE COMPUTED INFORMATION: ------------------------------------------------------------------------------- • DISTANC� FROM PAESSURE VELOCITY SPECIFIC PRESSURE+ CONTROL(FTj HEAD{FT) (FT/SEC} ENERGY{FT) M4MENTUM{POUNDS) Q.000 5.792 8.934 5.897 2p57.90 21.975 2.50D 8.934 3.6Q5 1Q59.52 __===____�_____________________��_�_______________==___________==_==_=__=_=_ ASSUMED DOWNSTREAM PRE55URE HEAD(FTj = 2.50 ------------------------------------------------------------------------------ GitADUALI.�X VARIED FLOW PROFILE COMPiJTED INFORMATION: -----------------------------------------_------------------------------------- T7ISTANCE F�t4M FLdW DEPTH VELOCITY SPECIFIC PF2ESSURE+ CON'T'RpL { � ) { � ) ( FT / 5EC j ENERGY � FT ) MOMENTLJM ( POUNDS ) 21.975 2.500 8.431 3.605 1059.52 22.05fi 2.986 6.437 3.542 Z055.BD 22.12$ 2.973 8.4g6 3.581 1052.47 22.195 2.959 6.461 3.571 1049_39 22.257 2.945 6.478 3.562 i046.52 22.3i6 2.432 8.446 3.553 �043.84 22.371 2.418 8.516 3.545 1041.33 22.922 2.4D4 8.539 3.537 1038.97 22.971 2.39i 8.563 3.53D 1036.76 22.5�6 2.377 9.5B8 3.523 3034.7Q 22.558 2.353 8.615 3.517 1032.77 22.598 2.350 8.6A4 3.511 103a.97 22.b35 2.336 8.674 3.505 1029.3� 22.5fi9 2.322 6.7D5 3.5D0 1027.77 22.7D1 2.349 8.738 3.995 1026.36 22.730 2.295 $.773 3.491 1025.07 22.75fi 2.28i 8.808 3.987 1023.91 22.779 2.2b8 8.845 3.9$3 1022.86 • 22.SD0 2.259 8.883 3.980 1021.94 22.$19 2.290 9.923 3.977 102�.15 22.834 2.227 &.963 3.475 • 1D20.47 22.$4'7 2.2i3 9_005 3.473 1019.92 22.857 2.199 9.D49 3.471 7.019.48 22.864 2_186 9.493 3.47D 1p19.17 22.868 2.172 9.139 3.970 1018.99 22.87Q 2.158 9_187 3.469 1018.93 72.000 2.158 9.187 3.959 1Q18.93 ------------------------END OF HYDRAUi�IC ,7UMP ANALYSIS----------------------- � PAESSUAE�MOMENTUM BALANCE OCCU�tS AT �.99 FEET UPSTREAM 0�'i30DE Qia.za I � DOWNSTREAM DEPTH = 5.494 FEBT, UPS�'REAM CONJUGATE DEPT1-I = 0.952 FEET � -------------------------------------------______-----------___---------------- NO�E 41d.30 : HGL =< 278.778>;EGL= < 284.089�;F�,pWLINE= < 276.520> +�*�r,.**+r��*�*++t�***+�t+i*f*****.,.*...*******+++*t++++*+*�****+*,r*v.*�r***+*** FLOW PROCESS FROM NpDE 910.34 TO NODE 410.3a IS C017E = 8 UPSTREAM NpDE 410.30 ELEVATION = 27b.62 (FIAW UNSEALS IN KEACH) -----��---_�-_____-_-------___--------------------------------------------------- CAi,CULATE CATCH SASIN ENT'RP.NCE L05SES (E,ACFCD) : PIPE FLOW = 4�.4� CPS PIPE DIAMETER = 30.00 INC3iES FLOW VEi,OCITY = 9.19 FEET/SEC. VELOCITY HEAD = 1.3i1 FEET CATCH BASII3 ENERGY LdSS =.2* fVEI.�OCITY IiEA17) _.2" { 1.311) = 0.262 130DE 410.30 : HGL =� 280.352>,EGL= < 280.352�;FLOWI�INE= < 276.620> *rt�++*r*�****+r+�rr�r�,r**�*+�**aii*i�*��r�*y�ts*�rrt�+*x***ft*�i��++***�*r+****� lIPSTREAM PIPE FLOW CONTROL DATA: i30DE NUMBER = 410.30 FLOWi,INE E�,EVATTON = 276.62 ASSUMED [3PSTREAIy3 CONTROL HGL = 27$ _ 76 FOR DOWNSTREAM RL7N ANALYSIS • ___________________�T�====__-_-_____=_====_======____==_______===_==__________ • •*k{f:y*t**ryrtx*trrx�r+*ti*:+*x***«*r+xr*xx**xxsrr*x**xx*rxx*r*w*t,***rt*xrrxr.k+** Analysis prepared by: ProjectDesign Consultants 701 B Street, 5ui[e 600 5an Diego, CA 92301 (6�9) 23�-6471 C� i ***.�.**.....+..**+***...+. DESCRTPTiON OP STUDY ••*+••'*+**+•*+*.=+�w+..+. * BRESSI RANCH - ULT'IMATE CONDITIONS * * SYSTEM 40Q - LATERAL 1{TOWN GARDEI3 ROAA STA 7+95_�6 RT) { * 100-YEA�t STORM EVEN'f . * **+**i.t*t******�+***�**�W�r*tr*+*****ttt+*++tta�*rtrrr�*wra**++++f++r+**r*** FILE NAME: C:\2244\L400-1.AAT TTME/DATE �F STUDY: 15:59 10/23/2002 wYri*� *!*tf iY *i**Y! *i�rtYr!* f 1'yrYr M'f f Yr *Y� Y' ** Yr **f *i�Yr#YrYr fiYr�k i YrY� f*YrYr *Yr#Y�irYr'k1 #i'Y�Y�+1YY i*YrY PIPE-FLOW HYDRALTLICS COPiPUTER PROGRAM PACfCAGE {Reference: LACFCD,LACRD, AND OCEMA HYDRAUL�CS CRITERION) (c1 Copyright 2982-2001 Advanced E�gineering 5oftware (aesi Ver. 8.0 Release Date: 41/DI/2001 License FD 1509 GRADUALLX VA�TET} FLOW A1�ALY5IS FOR PIPE SYSTEM idODAL POIN3` STATUS TABLE fNote: "*' indicates nodal point data used.l . UPSTREP.M AUN DOWNSTREAM R�7N MODEL PRESSi3AE PRESSURE+ FLpW PRESSURE+ PRpC�SS HEAD ( FT? MOMENTUM ( POUNDS ) DEPTi3 ( F'T } MOIiENfiU�I { pOCII3DS } 4.81* 619.Q4 0.74 364.07 FRICTION CA`d'CH BASIbi 2.85* 402.90 1.33 Dc 247.20 405.2�- 3.7B* 33k.35 1.33 Ac 64.79 MP.XTMLTiYi NUMBER OF ENERGY BP.LANCES USED IN EACH PROFILE = 50 NpTE: STEADY F'I,OW HXARAULiC HEAD-LOSS COMPU'i'ATIOI35 BASED ON THE sf05T CONSERVATIVE FORMULAE FROM THE CURAENT LACRD,LACFCD, P.ND OCE3�SIa DESIGN MAid[IALS. ♦t,r*x*+*,tw****�k**x�**x**wfw+.i.t**�+x*s***xtyti***rt*ys*****r*e*w�rtr*+�*+t**x**xi DOWNSTREAM PIPE FLOW CONTROL BATA: I30DE NUMSER = 405.10 FLpWLINE ELEVATION = 253.5a PTPE FLpW = 12.54 CFS PIPE DIAMETER = 18.00 INCHES ASSUMED DOWNSTFtEAM CONTROL HGL = 268.310 FEET -----------------------------------------------___-_______--------------------- PIODE 405.10 : IiGL = � 266.310>;EGL= � 269.D87>;FLQWLT3�iE= < 263.540> NODE NUMBER 405.10- ) 405.20- ) +�.r*•wx*+rxsx+++**+w+ry,f+rrr*t*rr.fxtt+*tx+wt+trt�***+artttw**+fw***+.w*x++twf.+** FLOW PROCE55 FRdM NODE 405.10 'FO NODE 405.20 IS CdDE = 1 UPSTREAM NODE 405.20 ELEVATTON = 255.61 (Fi.,OW IS LJ2�FDER PRE55[JRE) CALCLTLA'T'E FRICTIOI3 LOSSBSlLACFCD) : PIPE FLOW = 12.50 CF5 PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = i0.58 F'EET MA.NNING'S N= O.D13D0 SF={�/K)**2 = {( 12.5D1/( 105.046)f'*2 = D.01416 . � HF=L�SF = ( 10.56y*i0.01416) = 0.150 NODE 905.20 : HGL =< 266.4b0�;EGL= < 269.237>;FLOWLINE= < 265.510> «�***+**�*�r.**w*.w****w*»�w**�++�+***a�**rri*.+++*.ax.+w�***w****.w.+*f****�+ FLOW PROCESS FROM NODE 405.20 Tp NODE 405.20 TS CDAE = B UPSTREAM N4DE 405.20 ELEVATION = 2fi5.61 ;FLpW IS TJI3DER PRE55URE} CALCULATE CATCH BASIN EN�RANCE L055ESSLACFCDI: PIPE FLOW = 12.50 CF5 PTPE DIAMETER = 18.00 INCHES F�,OW l7�LOCITY = 7.07 FEET/SEC. VELOCITY HEAD = 0.777 FEET CATCH BA5IN ENERGY LbSS =.2*(VELOCTTY HEAD) _.2*( D.777) = 0.155 NODE 405.2D : TiGL =� 269.392>;EGL= < 264.392>;FLpWLIAIE= a 2b5.61D> **sw+x*x*+w:r+w*wrw*+st,*w*��,rx**xwx*+*fx+**++�wxsy+*�**,rwxr**x*****ww*�x**x+*+t UPSTREAM PIPE FLOW CDNTFtOL DATA: NODE N[3MBER = 405.20 FLOWi�INE ELEVATIdN = 265.61 AS5[TMED UPSTREAM CONTROL HGL = 266.9A FOft AOWI3S'i'REAM RUI3 ANALXSiS END OF GRADUALE,Y VARIED FLOW Ai�TALYSTS � � � y*wyrxr-**wrri.v�xfaw�xxx***rrrrW**s*xxx***rr*s***wti*�y.x**.i.*r��k**�x�w+++rtri.fiww*w Analysis prepared �y: ProjectDesign Consu�tants 701 B Street, Suate BDO San biega, CA 92101 (6�9} 235-6471 � =. *�*ww*****r*+*+t**+****+++ DESCRIPTION OF STCTDY ***+*+**+r+.+**+**+*rw***x+ * BRESSi RANCH - ULTIMATE CONDITIONS ' * SYSTEM 414 - LATERAL 1(TOWN GARDEN ROAD 5TA 12+49.53 �tT) * * 140 YEAR S'FORM EVEN'i` ' +*.*+*k+*w*�*..w�,r*w***++.,r*v.,.*.+++f+�,��sr*..*wt,rf*+**+*s++rwf�+�f.+..s+r+ F�LE NAME: C:\2244\L414-1.DAT TIME/DATE OF STUDX: 16:12 1D/23/2002 .*+.*.*�*.t.*�*.�...*�****+*«�««...«.***..:.*......+*�*.***�*+.**�*.*......**++ NODE N'UMB�R 420.10- } 420.20- } 420.20- PIPE-FLOW HYDRAULICS COi�SP�T'F'ER PROGRAM PACKAGE (Reference: T�ACFCD,LACRD, AND OCEMA HYD}tAi7L�ICS CRITERIpN} {c} Copyright 1982-2001 Advancec3 Engineering Software (aes) Ver. S.0 Release Date: O1/Ol/2401 License ID 1509 GRADi7ALLY VARIED FLOW ANAL,YSiS FOR PIPE SYSTF�I NODAL POINT STATUS TABLE (Note: "*' indicates noda3 point data used.) UPSTREP.N1 RiFN DOWNS�R�AM RUN I+50AF�, PRESSURE PiLESSUREt FiOW FRE55URE+ PROCESS HEAD{FT} MOMENTUM(POLJNDS} I]EPTH(FT) MOMEN'FUM(POUNDS) a.67 Dc 37.82 0.41* 51.9A FR3CT�ON CA'FCH BASTN 4.67*Dc 4.98* 37.82 20.33 0.67*Dc 0.67 Dc 37.82 13.93 -------------------------..____-----___..-----------______..__-..----_______------ MP.XIMUPS NUMBER QF ENEFtGY BALP.NCES USED IN EACH PROFILE = 50 --------------------------------------------------------------------------_-__-- NOT£: STEADY FLOW i�iYI}RAULIC I�iEAb-L05S COMPUTA�'IONS BASED QN THE MOST CpNSEFtVA'iIVE Fpi�iJLAE FROM TH£ CURREI3T LACRD,LACFCD, Ai�FD OCEP4A DESIGN MP.NUALS. x*x*,r*++*x.'*w****.***x«***.++*+v.r.++**.�r�rr�.r+�wv.,r*+***w.+**awa+*++�+�+w>*.+* DOWNSTREAi�i PiPE FLOW CON'I'ROL DATA: NODE NUMBER = 424.10 FLOWLINE ELEVAT�ON = 274.88 PIPE FLOW = 3.10 CFS PIPE DTAME'i`ER = 18.0� INCHES ASSUMED DOWNSTREAM CON'TROL HGL = 275.480 FEET *I30TE: ASSUMED DOWNSTREAM CONPROL DEPTHf O.fiO FT.J IS LESS THAN CRITICAL DEPTH{ 4.67 FT.j , ___> CRITICAIJ DEP'i'H IS ASS[7MED AS DOWNS'£REAiY! CON'T'ROL DEPi'H FOR UPSTRE.�M RUN ANALY5I5 ------------------------------------------------------------------------------ NODE 420.1D : HGL =� 275.288>;EGL= < 276.274>;FLOYTLINE= < 274.88D> �**+e*x**x**rxxxt�wsw+x***,t+a+t*�xv.+r�v.�**rtaw�wv.�++**,txx+,rx*w�x**++v�t*rtxr***+ FLpW PROCESS FRpM NODE 42D.i0 TO NdDE 420.20 IS CODE = 1 UPSTREAl�S NODE 420.2D ELEVATION = 276.44 (FLOW IS SUPERCRITICAL) • � CALCLTLATE FRxCTION LOSSES(�CFCDJ: PIPE �LOW - 3.1D CF5 . PIPE bIAt�ETER = 18.aQ INCHES PIPE LENG�H = 43.25 FEET MAI3NING'S N- 0.01300 NORMAL DEPTH(FTi = D.40 CRIT�CAL DEPTH(FTj = D.67 UPSTREAM CONTROL ASSUMED FLOWDEPTHfFT} = O.fi7 ___---------------------------------------------------------_------________--_-___ GRAI)UALLY VARiED FLOW PRO�'ILE COMPUTED INFORMA'T'IpN: D�STAI3CE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSL3RE+ CDNTROL{FTj (FT} (FT/SEC} ENERGY(FT} MOMFNTUM(PO[JNDS} O.00Q 0.670 4.Q59 0.926 37.82 4.D03 D.664 4.102 D.926 37.82 0.011 0.659 4.146 0.926 37.84 D.026 0.654 4.191 0.927 37.86 0.046 �.648 4.237 p.927 37.89 0.073 0.643 4.284 0.928 37.92 0.106 0.637 4.332 0.929 37.97 U.144 0.632 9.381 D.930 38.Q2 4.196 0.627 4.432 0.932 38.09 0.256 0.62}. 4.483 0.933 38.16 4.322 0.61fi 4.535 D.935 36.24 Q.397 D.610 4.�89 0.938 3B.34 0.462 0.605 4.643 D.940 38.44 0.578 0.604 4.699 0.943 38.55 0.689 0.544 4.756 0.946 3B.b7 0.802 0.569 4.815 0.949 38.81 0.932 D.563 4.875 0.953 38.95 1.075 0.578� 4.936 0.957 39.I1 1.234 0.573 4.994 0.96J. 39.27 .1.407 D.567 5.Q63 0.965 39.45 1.597 0.562� 5.129 0.971 39.b4 1.BQ4 0.555 5.196 0.976 39.85 2.D30 fl.551 5.265 0.982 40.Ofi 2.277 4.546 5.336 D.488 40.29 2.545 D.540 5.409 0.995 . 4p.53 2.638 Q.535 5.483 1.d02 40.79 3.�57 4.529 5.559 1.010 41.0� 3.5D5 4.524 5.638 1.018 41.34 � 3.883 0.519 5.718 1.Q27 41.69 4.297 D.513 �.8D4 1.036 41.95 4.748 0.508 5.685 1.D46 42.28 5.241 0.502 5.972 1.056 42.62 � 5.7$2 0.997 6.061 1.068 42.49 b.374 0.492 fi.152 1.OBD 43.37 7.026 0.486 6.297 1.092 43.76 7.�46 0.481 6.343 1.1Dfi 44.18 8.54� 0.475 6.443 1.12U 44.62 9.425 0.470 6.545 3.13fi 45.07 10.414 0.465 6.fi$1 i.152 45.55 11.523 D.459 6.759 1.159 95.04 12.777 D.454 6.8']1 1.187 45.56 14.208 a.448 6.986 1.207 47.10 15. 858 0. 443 7. ].05 1. 22'7 4? . 67 17.785 0.438 7.227 1.249 48.25 � 2D.07$ 0.432 7.353 1.272 48.87 l J . 22.874 0.427 7.483 26.367 0.421 7.b18 31.D53 0.416 7.756 37.817 0.4�1 7.899 43.254 0.408 7.956 1.297 49.51 1.323 50.�8 1.351 50.87 1.380 51.50 1.394 51.94 ------------------------------------------------------------------------------ NODE 42Q.24 : HGL =� 277.110>;EGL= < 277.3fi6>;FLOWLI�IE= < 276.440> *�Y *� W 1t�lr/� i �r�*i� fi�ki� **iF* *Yr***Yck i� *Y�ri * i� *Yr%� Y� i*#� RiF*M1�1r*Yr*t�k **Yc #**�t**#* # f***#! * k�FYrYrYr * FLOW PRpCESS FROM NODE 420.2p TO NQDE 420.2� IS CODE = B UPSTREAM NODE 420.20 Ei,E�7ATIpN = 275.44 (FLOW IS AT CRI�`ICAL DEPTH) ----------------------------------------------------------------------------__ CALCUE�ATE CATCH BASIN ENTRANCE LOSSES{LACFCDi: PIPE FLpW = 3.10 CFS PIPE DIRMETER = 18.00 INCHES FLOW VELOCI7'Y = 4.06 FEET/SEC. �1ELOCTTX H�A�I = �.256 FEET CA'I'CH SASIN E2dERGY L(?5S =.2* (VELOCITY HEAD1 =.2* f 0_256f = 0.451 ------------------------------------------------------------------------------ NODE 92D.24 : HGL =< 277.417>;EGL= < 277.417>;FLOWE�INE= � 276.444> *.*,.**�*...+***+*+*+�**+*+**********+*+*******t�*t�+**+*...**.*..+..**...**.*�. UPSTREAM PiPE FLOW CONTROL DATA: NODE NUMBER = 420.20 FLOWLINE ELEVA�`IOid = 276.44 ASS[JMED UPSTR�AM CONTROL HGL = 277.11 FOR �10WNSTREAM RUN A33ALYSIS _�______________________________________��_�� «____« ��__��-�_��--��______ ENi) OF GRAI)iJAi�LY VARTED FLOW ANALY5I5 L � • ;.,r^3��n.� • � � .�. { � . '4,` � ' " . . �;, - 'T . ' !.`_ " - � . ,, � • ' ' � , , � - - ti : •Mr w+�.. . _�...►r L. . _. , ,....»� .. � . , rr. _ w��. � a . . ,. .> . � « . ` ' ' . . J... ► �_�r , . _ , . , , c _ . . � . a ti .�. . . ,+� ' .� • - �. , , , . r � ., . . . �� , , , s a .� . .w',. , " � . > , a . . � . 7 . - { ,i . � � � _ • '} . . , .� • � � ` . � � ' ' � � 1 � e Y+ . ' • t r!-' . � . • l " . • _ .. . ' _ r � . . � . w � . ' . r � S� , ,.. � - � _ _�� .-si �_yv� � -f[!• . _ �.. ... -e „ i' _ i . . �. .�. �._^ .....s __ _ . 4 ' _ � _ _.� � .f�►, 9 � x M t�?fk f�rk YYi Y rt*Y��F1rk * k***�FiFY� Yr *Y�f �* y Y�>Y� Y�Y��k eri Y�K*YrY� f*Yi Yr�FYr* i Yr*Ytt *YrYk *x� 4*Yr� YYiL 1r ft+ PIPE-FLOW HYpFtAUL�CS COMPi7'I'ER PROGRAi�S PACKAGE (Reference: i,ACFCb,LACRD. AND OC�MA HYDRALFLICS CRFTERIOI3} {c} Copyright 1982-24D1 Advanced Engineering Software {aEs} Ver. 8.Q Release Date: 01/01/200}. License ID 1509 Analysis prepared by: PROJECTDESIGN CONSUE,TAN'PS 703 'B' STRE�T, SUITE 80fl SAi�7 DIEGO, CA 9210� 619-234-0349 :*++**.+�...+**+,...*...*«� DESCRIPT�ON OF STUDY +*�**,�*�*.**....*«.+**..+** * BRE55I RA23CH - ULTIISATE CONDITIONS ' ' SYSTEM 414 - LATERAL 2{TQWN GARpEN ROAD STA 12+49,53 LTj " * 1D0-YEAR STORM EVENT * ****,r***a**a**t**r**s+w+*�s+*+ww*w*w�w**w+*+ttx++**r*w�**w*x*rr*�rw�rr***tir FILE NAME: L414-2.DAT TIME/DATE OF 5'I'i3DY: 16:36 D9109/2�42 Y M* f f*1** *Y�#►!*'kiik'Fi tklr#} tt�1t1�# W*'� *�i i f Yr*iY W �1'k* *i*itk Yr* *YriFY� Y�* YrYr*YrYrYrklrYrY�lrYrYrYr f Y�1rYr1r GRADUALLY VARIED FIAW Ai�IALY5I5 FOR PIPE SYSTEM NdFAL POINT STATUS TABLE (Note: "*' indicates nodal point daCa used.i . LiPS'i'REP.M REJN DOWi1STREP,M RUN • NOAE MODEL PAESSfFRE PRESSURE+ FLOW Pi2ESSiFRE+ NitMBER PROCESS �IEAD ( F'I' } I�40MFNTUM ( POU23D5 } DEPTH � FT ] MOMFNTiJM � POUNDS ) 420.50- 0.67 bc 37.82 0.34* 65.48 } FRICTION 420.60- 0.67*Dc 37.$2 0.67*Dc 37.82 } CATCH BASiN 420.60- 0.98} 2Q.33 0.67 Dc 13.43 ------------------------------------------------------------------------------ MAXiMC7M NUMBER OF ENERGY BALANCES iTSED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NO'I'E : Si`EADY FLOW HYDRAULIC HEAD-L(?S5 COMPUTATIONS $ASEF} Oid THE MQS'T' CONSERVATIVE FORMi7LAE FRdM THE- CURR�f' LACRD,LACFCD, AND OCEMA DESIGN MAAT[JALS. ww**ww*+r*x*r*a+*t*t+*****rx*t*a*****++**wt**sxryr�**tiw�ki.+w**+*v.i�t*+i.*i.wrrrtYw*t DOWNSTREAM PIPE FLOW CONTROL DATA: NOD£ NUMBER = 420.50 FLOWL�I3E ELEVATI033 = 274.88 PIPE FLOW = 3.1D CFS PIPE DIAMETEI2 = 1$.UO INCHES ASSUMED pOWNSTREAN3 CQNi`ROL HGE� � 275.4B4 FEET 'NOTE: ASSL}M�D DOWNSTi3EP.i�4 CRNTROL DEPTH ( 0. 60 FT. } IS LESS THAN CRITICAL DEPTIi{ 0.67 F'T'. } -=_> CRITICAL DEPTH iS ASSUMED AS DOWNSTREAM CONTRpL bEPTH FOR UPSTREAi�i RUN P.riALYSI5 ------------------------------------------------------------------------------ NODE 420.50 : HGL =< 275.218>;EGL= < 276.899>;FLQWLINE= < 274.880> *�.**«***«.****++**�t**++*�..*t*+.*+*****�**.+�****+tx�*++»*..,��*+xw+f�..r..�* FLpW PROCESS FROM NODE 420.50 TO NODE 420.60 IS CODE = 1 UPSTREAM i�TpbE 420.6Q ELEVATION = 276.19 {FiOW IS SLTPERCR�TICAI,j -----------------------------------------------------------------------____--__ • � CALCULATE FRICTIDid LOSSES{LACFCD}: PIPE FLOW 3.1D CF5 PIPE D�AMETER = 18.OD iNCHES PIPE LENGTH = 5.25 FEE7' M.P.NNING'S N= D.01300 NOF2hSAL llEPTH(PT] = 0.25 CRITICAL D£PTH(FT? = 0.67 UPSTREAM CONTROL ASSUMED FLOWDEP'I'H(FT) = p.67 GRADCiALLY VAR�ED FI.,OW PROFILE COMPUTED �DIFORMATION: DISTA�lCE FROi4 FLOW DEPTH VELOCITY SPECIFTC PRESSUAE+ CQNTRO� ( f`P 1 i FT 1 I FT / 5 EC ? Et+IEF2GY ( FT ) i+SpMENTUM ( POiiNDS j O.00D 4.670 4.059 0.926 37.82 0.0�3 4.653 4.197 D.927 37.86 0.015 4.63b 4.345 0.929 37.98 0.034 4.619 4.503 0.934 38.19 �.069 0.602 4.672 0.941 38.5D D.105 4.565 4.853 0.951 38.9Q 0.160 0.568 5.048 � 0_9b4 39.41 ' 0.23D 4.552 5.258 0.9$1 40.04 0.317 0.535 5.4B5 1.OD2 4D.79 0.426 0.538 5.73Q 1.028 41.68 D.56}. 0.541 5.996 1.Ofi0 42.73 0.'725 0.484 6.285 1.D98 43.93 �.925 0.457 5.602 1.144 45.32 3.170 0.450 b.948 1.2U0 4fi.92 1.4fi9 0.433 7.327 1.257 48.74 3.835 0.416 7.745 1.348 50.82 � 2.289 0.399 8.208 1.446 53.19 2.852 0.383 8.722 1.565 55.69 3.562 0.356 9.296 1.706 58.98 4.972 D.349 9.940 1.884 62.51 5.250 0.33B 14.403 2.019 65.08 NODE 420.60 : HGL =< 276.860>,EGL= < 277.116>;Fi,OWLINE= � 276.190> .*.+�....*�.�.****��...*«.,.*.,...*�.,,,**+....«.*.+t***+��*.�....�**�f++***,�,�+�+v..+.+* FLOW PROCE55 FROM NObE 42D.60 T'0 NODE 420.60 IS CODE = 8 iJPSTREAM �IODE 420.60 ELEVA`P�ON.= 276.19 fF�OW-I5 AT CRiTICAL DEPTH) CAi,CULATE CATCH BASIN ENfiP.ANCE LOSSES(LACFCD}: • PTPE Fi,OW = 3.10 CFS . PIPE DIAMETER = 1$.DO INCHES FiOW VELOCITY = 4.06 FEETlSEC. VELOCITY HEPS) = 0.256 �'EET CATCH BASIN ENERGY LOSS =.2*fVELOCI'I'Y H�AD} _.z*( 0.256) = 0.051 --------------------------------------------------_---___----------------------- NODE 420.60 : HGL =< 277.167>;EGL= < 277.1b7�;FLpWI�II+iE= < 276.190> rt*+�*swtr*x++tit+****x**r*txrrr**+*tr+�y,+�.�ki+e*,r+*ww+,o-x*rixtw*yw*+*f**++**x*�x IIPSTREAM PIPE FLOW CONTR�L DATA: NpDE NUMBER = 420.60 �'LOWLIN£ ELEVATION = 276.19 A55UMED UPSTREAM CONTROL HGL = 276.66 �'OR DOWidSTREA2� RUIJ ANALYSIS END OP GRADUAi�LY VARIED FLOW ANALY5I5 ' • r- ��l, .. � a � P, ' , - '.. ±,�, . ._ - i � ' ' . , ' � n ' �_ " 1 , . + S � ' L s ` ' " . � - �s� +�r � ..��► � ._ �.w . s- +w . . . . . . . .. ._ „ , r.. .r . . , - _ '.t..��. , .. + . r , _ � -, � � , � • , rw :', . , , � , e , ., � y � � .. � - -i�' , . ' . . � , . � �� . � -- • - � � 'x` ' � � � - . 9 _ . . . " ' j d ' 1 - ` '�7 �*' - . , . _hr: ' i . ' � . � � • , ' a . V ,i T �# � , � � . . , � ; T � ' � � � t . _.. `'.�L� � . ' � ri� • A�.�_ i .� :i. +t ~• . ,ya. +��.r_. �k� _ . ` • .. _ ... ' t �f" s� _�.'_" . . _ '� L1� YG.+ " � **s*rt*r*t+r:+*xw*r+*,r*rwk*f+**++wxwax***+*x*e****+wt*wr**�r*:***�*r*�v.*+ti��t�:* Analysis prepared by: PROJECTDESTGN CONSULTAN'PS 701 'S' STREET, SUITE 800 SAN AIEGO, CA 92101 619-234-0344 r � �� +t*r**x+*�rw:rw.�t**w**e** DESCRIPTION OF' S'7'�Y *****rtrt*�*r****wr�**xx�*x* * BRESSI RANCH - ULTIMATE CONDITIbNS ' * SYSTEM 404 - I.A3'ERAL 2 * * 100-YEAR STORM EVENT " *i# ** f Y� Yr YrYrYr*i�#*M*tYr iFY�!*tkYrYrYi YrM1rMY� k YrYr* *Y� f*i t�c*#* f� f**4 �#1. #'t i� i*#}1�tkt iiY�i1� tY�kYr FII,E NAi7E: 440-2.DAT TIME/AATE OF 5'I'LTDY: 1D:45 09/1]/20D2 *t**...,****...+«�+f+.��«..*..�....*..*+.*,..�,.*�.**.,.*....****.**.«.*�.*�....*x* NODE NUPfBER 410.44- } 410.50- - } 410.50- PIPE-FLOW HYDRAULTCS COMPiJ�'ER PROGRA.M PACICAGE (Reference: 71ACFCD,LACRII, ADm OCEMA HYDRAULICS CRITERIONf (c) Copyright 1982-2401 Advanced Engineering Software {aes) Ver. 8.D Release nate: O1/01/204i License ID 15D9 GRA➢L7ALLY VARiED FLOW ADIP.LYSIS FOR PIPE $YSTEM I30AAL POIN'i` STATUS TABL£ {Note: '*" indicates nodal point data used.} UPSTREP.M RLTAI DOWNSTREAM RiJN PiODEL PRESSURE PRESS[JRE-r FLOW PRESSURE+ PROCESS i-IEAD ( FT } MOMEN�'iiM f POUNDS } DEPTH { F�') MOMENTU3�1( PdLFNF15 ) 5.24* 522.53 0.39 136.33 FRICTION 2.51* CATCH BASIN 2.65* 222.03 211.07 0.86 Dc 4.85 Dc 70.43 24.19 ------------------------------------------------------------------------------- MAXIML]M NLT�LBER OF ENERGY HAL.�NCES USED �N EACH PROFIiE = 25 I30TE: STE.ADY FIAW HYDRAULIC HEAD-LOSS COMPUTATIONS BASEb ON THE hSQ$7' CONSERVATTVE FORMUI,AE FRdM THE C47RRENT LACRA, LACFCB, PND OCEi+�A DESIGN MP.NUALS. • *++******+.,....*,,..**+**+**.+*+**,.«*�+*.+*.r+**++*.**..ww�r�*++*++«�v.*+.w...*t DOWNSTftEAM PIPE FI,OW COAPI'ROL DATA: NODE NLiI�iBER = 41D.40 FLOWLIAiE ELEVATION = 255.7fi PIPE F'I,OW = 5.00 CFS PIPE DIAMETER = 18.OD INCHES ASSIFMED DOWNSTREAM CONTROL HGL = 271.000 FEET NODE 414.40 : HGL =< 271.D04>;EGL= � 271.12A>;FLOWLINE- < 2fi5.750> *v.+w*. yr* 1� �k*f /rYrYrlYrYrYrYrYrYrYr YrtYrYrlr YrYr Yrk Yr�! Yr / frYrk f YrY� Yr*lrlrRyr kYrYr tYY y Y�*! W kY f W f Y*! i! YY�tf 1*Yrt♦ FLOW PROCESS FR02+5 NODE 410.40 Ta NODE 410.50 IS CODE =� UPS�'REAM NOE?£ 410.50 ELEVATIDN = 268.51 (FLOW I5 UidDER P�SSUREI CALCULATE FRICTION I,OSSES(LACFCD}: PIPE FLOW = 5.�0 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 11.Q0 �'EET MANI3ING'S N- 4.01340 SF=(Q/xj**2 = i( 5.00}/� }.05.0221)**2 = O.o0227 . • � HF=L*SF = ( �1.ODj*f0.00227? _ -^-_O+D25--- NODE 4i0.50 : HGL =< 271_025>;EGL= < 271.�49>;FLOWLINE= � 268.510� *rtr+t+twkfy*rtiti�+w+�**++*rtir*rtr**+��++t+**xr+**r+axx+t*rw�*t.rf�**xx*�++*�+ FLOW PROCESS FROM NODE 410.50 TO NODE 4�0.50 IS CODE = 8 UPSTREAM NODE 410.54 £LEVATION = 268.51 (FLOW I5 UNDER PRESSLTRE) ------------------------------------------------------------------------------ CAI�CUi,ATE CATCH SASIN E3dTRP.NCE LOSSES (�,ACFCBj : PIPE FLOW = 5.Q0 CF5 PIPE DIAt�ETER = 18.00 INCHES FI,OW VELOCITY = 2.83 FEET/SEC. VELOCITY HEAD = D.�24 FEET CATCIi BASIN ENERGX LOSS =.2*{VF,�,pCITX HEAD) =.2*{ 0.124} = 4.D25 • -----------------------------------------------------------______-----_____--- NODE 41D.50 : HGL =� 271.174>;EGL= a 271.174>;F'E,OWLINE= � 268.510> r*ry.tir+.++**w+rt►*x►r+xw**+++*wxr�xww*wwx*w*r*f+**r��+�i.r,r�y,*+y�a+sk:�xrta.+*t*rf UPS'i'i�EAM PIPE FLOW CONTROL DATA: NOAE Nf7MBER = 410.50 FLOWLINE ELEVATION = 268.51 ASSUMED UPSTREAM CbNTROL IiGi� = 269.37 �'OR DOWNSTREAM RUN ANALYSTS ��_____=�_________________________________________��_�_��_____=�=__��===_ END OF GRADUAZ,LX VARI�A FLOW ANALYSIS � • * Y� . ''�h ' . , e+ � , . w � , w. Y ., .� - u • �. '� 1 ' � •` . -! Y < � . - . . . ' . 1 4 �a t w�� • ��. •- ,.. J� � z - �. � . • -n i . .4 i �,� aa. _ r • �. ' -� � - � �.. � !* , R � � > > . ,� � ' � , � � J �. • ✓ � � ��` n 4 Z � _ � • �� . � ., f � f 1 � � . � - � • . ' . u _w.��„1.: 1� _�- .4 =s.�Js .1"� a . .. . `�f' -` T , - iu-3.�� , � . ? .T-. s « . .._ . x . . i • ... � x+*++**+x+tr*w***x�*rt+rs***�rt��tx**x+*x*t*+**+**++**�*r**+r*r�***rx*�x+sx*s*t+ PIPE-FLOW HYDRAULICS COMPiJI'EH PROGRAfi PACKAGE (Reference: i�ACFCD,LACRb, ��t3D OCEMA HXi3RAi3LIC5 CRITERION) fc) Copyright 1982-20D1 Advanced Engineering Software (aesl Ver. 8.0 Release Aate: 01/01/2D0J. License ID 1509 Analysis prepared �ry: Projec[Design Consultants 701 B 5treet, 5uite $00 San Diego, CA 92101 (619} 235-6471 +**+�..*.**.*�.*....*.�*:* bESCRIPTION OF STiTDY "+��.+*,.��,..x++w��+=+_*... * BRESST RANCH - ULTIMATE CONDITIONS * * SYSTEM 4�7 {TpWN Gp,RDEI3 ROAD : PA-� LATERAI, COI3I+i�CTION} * " ].4D-XEAR STORM EVk:NT * W.�*.t...,.....***�*...**+.*.**.+.,,.**....**..�.,*ft****�**�.:**,.�.,....,.***. FIE�E NAME: C : \2244\407 . DA'F TI3+iE/DATE OF STUDY: 16:29 10/23/2002 +,.«*«*„*.*.*...,.**.,.....�+�**.*��.+**.r��.«.+*r.**+«++**v.+w*�,rxt+v.*w..*.**.«+* GR�DUALLY VAAIED FLOW A23ALYSIS FOR PIPE SYSTEt+� ' NODAL POINT STATUS TABLE (Notie: '*' indicates nodal point data used.} i7PSTfiEAM RUN DOWNSTRF_Acd �tUN � NODE f-EODEL PRESSURE PRESSURE+ FL+OW PRESSURE+ NUi+IBER PROCES S HEAD {�'T } MOMENTUM ( POUNDS } DEPTH ( FT ) MOMENTT3M ( POUNDS ? 407.00- 6.13* 1091.55 0.82 24$.8$ � ) FFtTC'F'103d 407.10- 4.81• 832.34 0.82 249.24 } FRICTION+BEND } HYDRAULIC �7UMP 407.20- 1.23 33� 200.57 0.73* 279.47 } JLTNC'F' T 03d 407.34- 1.31 201.59 4.53* 410.54 } FRICTION 407.40- 1.23'Dc 206.57 i.23*Dc 200.57 } CA'I'CH BAS�N 407.40- 1.86* 112.90 1.23 Dc 67.88 ------------------------------------------------------------------------------ MAXIMUM NUMHER OF ENERGY BALP.NCES iiSED IN EACH PROFIL,E = 50 NOTE: STEADY FLOW T-iYDRAULiC HEP.D-LO55 COMPUTATIQNS BASED ON THE M05T CONSERWATIVE FORMUi�AE FROM TI-IE CURRENT LACRA, 7�ACFCD, ANp OCk�Z�SA DESEGI3 MA�ii7AE,5. ww*x�*+++*,t*ws+****xs�+x*��*�+�,rwrw�*+�r*r:rr*t**rwtw�*+***ir*�sritx+****x*k�k DUWNSTREAM PIPE FLOW CONTROL DI+�TA: NOi]E NUMBER = 407.00 FLOWLII�E ELEVATIO?�I = 264.07 P�PE FLOW = 11.$4 CFS PIP$ DIAMETER � 2k.00 I�ICHES ASSUMEA DOWNSTREAri CONTROI, HGL = 270.20a FEET NODE 4D7.00 : f3GL =< 2�0.200>;EGL= < 274.419>;FLOWi�I23E= c 264.070> ♦+*x++**rrrr**w+�*+*�++w**xr,w**+xw«+x****w*t**x*s****�****+*e►r�x*�+��+i.�r*+*yx* � Fi,OW PRpCESS FRpM NODE 407.00 TO NODE 4D7.10 TS CODE = 1 .� UPSTREA�I NODE 407.1D ELEVATTQN = 265.58 (FLOW IS UNDER PRESS[]RE) ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSESI�CFCD1: PIPE FLOW - 11.8Q CFS PIPE DiP.METER = 24.00 INCHES PIPE �ENGTH = 68.6� FEET MAI3NING'S N= O.D1300 SF={Q/Ki**2 = {( ' ��.80}/( 226.220})**2 = 4.D0272 HF=L*5F = ( 66.b1i*{4.00272} = 4.187 ------------------------------------------------------------------------------ NODE 4p7.1D : HGL =< 270.38?>;EGL= K 270.6D6>;FLOWLINE= < 265.580> +r�rw�+**+rtf*.r++rrti*sw++s�+x+*****y�*+r*+xr++x+****w*+*****rk***�r+wt*�rr**r FLOW PROCESS FROM NODE 4D7.10 Tp NQDE 407.20 TS CQDE = 3 UPSTREAAS NdDE 907.20 ELEVA7'ION = 270.44 {HYDAAULiC J[7MP OCCCTRSI ------------------------------------------------------------------------___---- CAI,CULATE P�PE-BEND LOSSESiOCEMA}: PIPE FLOW = 11.86 CFS PIPE DIANSETER = 24.00 �NCHES CENTRAL ANGLE = 41.500 DEGFLEES MA.NNING'S DT = 0.0130D PIPE LENGTH = 220.99 FEET ------------------------------------------------__-_--------------------------- HYDRALFL�C JUMP: DOWNSTREAM Ri.TN AI+�ALYSIS FiESULTS ------------------------------------------------------------------------------- NORMAL I3EPTH{FT} = 0.82 CRTTICAL DEPTIi(FT) = 1.23 _______________________________« T=-===_______________________=_=_=====�----_� UPSTREAM CONTRQL ASSiJMED FLOWDEPTH(FT) = 0.73 «<__===��T=====__________--=========-===�-��« ��_��___________�______= GRADUALLY VARIED FLOW PROFILE COMPLTPED TNF'OR3dATION: ---------------------------______---------------------------------------------- AISTAt3CE FROM FLpW DEPTH VELOCiTY SPECIFIC PRESSURE+ . CONTFtOL { g"I' ) { FT ) { �'T/ SEC ) ENERGY ( FT } MOMFNTUM ( PQUfFDS } 0.000 4.731 11.357 2.735 279.47 a.995 0.732 11.319 ' 2.723 27B.74 2.006 4.734 11.283 2.712 278.01 3.034 0.736 11.2k6 2.7p1 277.29 4.079 0.738� 11.210 2.690 276.57 5.142 4.740 11.173 2.679 275.86 fi.225 0.741 11.137 2.669 275.�5 7.32� 0.743 11.102 2.558 274.45 8.450 0.745 11.Ob5 2.647 273.75 9.595 D.747 ].J..031 2.637 273.06 10.762 0.748 10.995 2.627 272.38 J.3.954 0.750 10.951 2.b17 27�.70 13.171 0.752 10.925 2.507 27Z.02 �4.415 4.754 10.891 2.597 270.35 }.5.687 0.755 10.857 2.587 269.6B 36.9B9 0.757 10.823 2.577 269.02 i8.323 0.759 10.789 2.56B 268.37 19.689 0.761 10.755 2.558 267.72 21..D92 0.762 10.722 2.549 267.07 22.532 0.764 J.0.688 2.539 266.43 24.012 0.765 1D.6$5 2.530 265.79 25.535 0.768 1D.622 2.521 26S.J.6 27.105 0.770 10.589 2.512 264.53 28.723 0.771 10.557 2.5D3 263.41 30.395 0.773 10.524 2.494 263.29 32.124 0.775 10.492 2.485 262.66 33.915 0.777 10.4fi0 2.477 262.D7 � 35.774 0.778 10.428 2.468 261.47 u • � 37.7D6 34.718 41.817 49.014 46.319 48.743 51.302 54.013 56.896 54.976 63.290 66.873 70.77B 75.D73 79.851 85.240 9]..429 98.713 107.583 118.959 134.914 162.09D 220.990 D.780 D.782 0.784 D.785 0.787 0.789 0.791 0.793 0.794 0.796 0.?98 O.BflO 0.601 0.803 0.805 0.8�7 0.808 0.814 0.812 4.814 Q.815 4.81? 4.817 10.397 14.365 14.334 14.3D3 14.272 16.291 10.210 10.180 10.150 10.119 1D.089 10.06a 1p.030 10.D01 9.971 9.942 9.913 9.884 9.856 9.827 9.799 9.771 9.77D 2.460 2.451 2.443 2.435 2.427 2.41B 2.411 2.403 2.395 2.387 2.379 2.372 2.354 2.357 2.35U 2.342 2.335 2.32B 2.321 2.314 2.307 2.301 z.aoo 260.87 260.27 259.58 259.09 258.51 257.94 257.36 256.79 255.23 255.67 255.11 254.56 254.�1 253.47 252.93 252.39 251.86 251.33 250.81 25D.29 249.77 249.26 249.24 HYDRAUL,IC �7UMP: UPS'I'RE.�M Rf]N ANALYSIS RESiFLTS ___________________________________________��_==_==_=__==_=_===___=_===__��__ ___ _ ____.. _ __.._..__ __ AbWNSTREAM CONTROL ASSUMED PRESSUAE HEAU;FT) = 4.81 .--..-..�<<�_«��««��R�_______F___________________��«.-.�� :��__________ PRESSURE FLOW PAOFILE CQMPUTED INFORMATION: � ----------------------------------�------------------------------------------- DISi`ANCE FR0�3 PRESSLFRE VELOCi'i'1' SPECIFIC PRESSUR�f CON'I`ROL f�'T ) HEAD ( FT? ( FT / SEC } E?�iERGY ( FT } NIOMEIVT[]ly5 I POUNDS y D.400 4.807 3.756 5.426 832.14 147.216 2.�OD 3.756 2.219 28�.93 ----------------------------------------------------------------------------�_ ASSUMED DpWNSTREAi�1 PRE55URE HEP.DIFT} - 2.OU ====c=====ncncc==c===c=n=s_-x_--¢�a4an_�_____�a�__=xaa===vcv=as___ava___�n=c-= GRADUALLY VARIE� FLOW PROFILE COMPUTE37 INFpRMA'iIDsI: DISTIaNCE FROM FLOW DEPTH VELOC�?'Y SPECIFIC PRESSURE+ CONTRbL{FTi {FT) [FT/SECi ENERGY{FTJ MOMEN'T'CTMiI'OUNDS) 147.216 2.000 3.i55 2.219 2B1.93 147.9$2 1.485 3.759 2.2D4 279.02 148.722 1.9b9 3.767 2.190 276.20 149.445 1.454 3.777 2.176 273.44 �50.156 1.939 3.789 2.162 270.73 150.855 1.523 3.803 2.148 268.07 151.545 1.408 3.816 2.135 265.45 152.225 1.893 3.834 2.121 262.69 152.897 1.877 3.852 2.108 260.36 153.561 1.862 3.87i 2.095 257.67 154.217 1.847 3.892 2.D82 255.43 154.864 1.831 3.913 2.D69 253.03 155.505 1.816 3.936 2.057 25D.68 156.137 1.801 3.960 2.D44 248.3fi 156.763 1.785 3.985 2.032 245.09 157.380 �.77D 4.011 2.020 243.67 � 157.99a 1.755 4.D38 2.OD8 241.64 i58.592 1.739 4.467 1.996 234.55 �59.1B7 1.724 4.096 1.965 237.46 i59.773 1.709 . 4.327 1.973 235.42 360.351 1.693 4.159 1.962 233.42 �fi0.921 1.578 4.192 L 951 231.47 �51.482 1.663 4.226 1.940 229.57 �62.434 i.647 4.261 1.930 227.72 162.577 �.b32 4.Z98 1.919 225.92 153.i11 3.b17 4.335 1.909 224.18 153.fi34 Z.501 4.375 1.899 222.4$ 164.148 1.586 4.415 1.889 22D.83 164.550 1.571 4.457 1.879 219.24 165.�41 1.555 4.500 1.670 2�7.71 165.621 1.540 9.544 1.661 2�6.23 166.D88 1.525 4.590 i.652 214.81 166.542 1.5fl9 4.637 3.844 2�3.45 166.983 1.494 4.66fi 1.835 212.14 167.4Q9 1.479 4.737 1.827 21D.9D 167.820 1.463 4.769 1.820 209.72 . 168_2i5 1.448 4.$42 1.812 208.63 168.594 1.433 4.848 1.BD5 207.55 168.954 1.417 4.955 1.799 206.57 169_296 1.402 5.014 1.793 2D5.65 169.6i7 1.387 5.079 1.767 204.81 169.9i7 1.371 5.137. 1.782 204.D3 170.194 1.356 5.202 1.777 203.33 170.446 1.341 5.269 1.772 2D2.70 17D.672 1.325 5.337 1.766 202.15 . 17Q.870 1.310 5.409 1.765 201.67 171.038 1.295 5.482 1.762 201.26 17�.174 1.2B0 5:558 1.759 200.97 171.274 1.264 5.63fi 1.758 2DD.75 171.337 1.249 5.717 1.757 200.61 171.359 1.234 5.801 1.756 2D0.57 220.990 1.234 5.801 1.756 200.57 ------------------------END OF HXDRAULIC JUMP AI�P,LYSIS-___----____----___----- � PR�SSiTRE+�OMENT[iM HAL.a.NCE pCCURS AT 154.44 FEET UPSTREAM OF NODE 407.1D � � DOW1d5TREP.i�4 DEPT�-i = 1. B41 F£ET, UPSTREAM COI3JUGATE DEPTH = fl.799 FE�T � -------------------------------------_____------------------------------------- N4DE A07.20 : HGL =< 271.171>;EGL= < 273.175>;FLpWLTNE= < 27D.440> r* 1. ir+Yr�.� Yr* yrt+�.+�r ii! i�r+# ie r++rtw Yr xw# * ri* R rxx*s * x*x k+! rtw Yi xRir rw I.wlrvrYrk f wri w xw+xw# f#'F't♦ FLOW PRpCES$ FROM NpDE 407.20 TO NODE 407.30 IS CODE = 5 UF'S'T'REAM NODE 407.30 ELEVATION = 270.77 �FLOW I5 SUPERCRITICAL) CALC[TI�ATE JUNCTIOId LOSSES : PIPE FLOW DTAMETER AI3GLE FLOWLTNE CRT'I'ICAi� VELOCITY {CFSJ fINCHESf (DEGREES) ELEVATION DEPi'H(FT.} (F'i`/SECj UPSTREP.NS 11.8Q 24.00 47.00 27D.77 �.23 37.552 DOWNSTREAM 11.80 24.DD - 27D.44 1.23 11.360 I,ATERAI, #1 0. p0 0. 00 0. DO 0. DO 0. 00 0. OOD i�ATER.AL #2 O.OD 0.00 O.OD 0.04 0.00 O.00D QS 0.00===Q5 EQi3ALS SASIN INPUT=== LAC�'CA AND OCEi�IA FLOW JUNCTIOid FORML3LA� USED: � DY=(Q2*V2-Q1*V1*C05{DELTAI}-Q3`V3*C05{DELTA3}- � Q4"V4*COS{n�LTA4))/(fA1+A2}*16.1}+FRICTION LOSSES IIPSTREAM: MAi�TNING'S 13 = O.DZ340; FRIC'FION SLOPE = 0.11249 DOWNSTREAM: N3ANNING'S bI = 0.01300; FRICT�ON SLOPE = 0.03350 AVERAGED FRICTIpN SLOPE IN JUNCT�ON ASSUMED AS O.D7300 JiJNCTION LENGTH = 4.00 FEET FRICTIO[V LOSSES = 4.292 FEET ENTRAI3CE LOSSES = 0.40D FEET �TUNCTION L05S£S = (DY+Hl71-HV2 i + {ENTRAi�10E LQSSES} �TiJNCTION LC?S5E5 = I 2.912)+{ D.OQ4) = 2.912 ------------------------------------------------------------------------------ NODE 447.30 : HGL =< 271.303>;EGL= � 276.067>;FE�OWi�IN£= � 270.770> �ryr*+ysr+rf+x*sw*ty*+Ww+r*rr��iy.i�r**+y.tirrr�rw.+*xr*:s*x*�x+r�x,r***x**+**+s�t* FLOW PROCE55 FROM NODE 407.30 TO NODE 407.40 IS C�DE = i UPSTREA,M NODE 4D7.40 ELEVATION = 262.D2 (FLOW IS SUPERCRITICAL) CAi,CULATE FRICTION LDSSES(LACFCD}: PIPE FLOW = 11.B4 CFS PiPE DIAi�FETER = 24.00 INCHES PIPE i,�IGTH = 90.D0 FEET MP.NN�NG`5 N - 0.013D0 NOI�MAL DEP'T'H { FT �= 0. 52 CRITICAL DEPT�3 ( FT }= 1. 23 UPSTREAM CON'I'ROL ASSiJ2+SED FL(7WDEPT�-i { FT )= 1. 23 GRADUALLY VARi£D Fi,OW PftOFZLE COldPUTED INFORMA'I'ION: ----------------------------------------------------------------_--_------------- llTSTANCE FRpM FLOW bEPTH VELOCITY SPECIFIC PRESSiFRE+ CONTROL { FT } { FT y ( FT / S EC � ENERGY ( FT ) MdMENTUbF ( POLTNUS } Q.ODO 1.234 5.801 1.756 200.57 . 4.pD3 1.219 5.881 .1.757 200.51 4.�Z1 2.205 5.964 1.758 2D0.73 4.025 1.191 6.050 1.759 200.94 0.045 �.176 6.139 1.762 201.24 O.p74 �.162 6.230 1.765 201.52 0.108 i.148 5.324 Z.769 202.�� 0.151 �.133 6.422 1.774 202.58 0.2�1 3..119 fi.522 1.780 203.35 D.251 �.105 5.526 1.767 204.19 0.329 i.09Z fi.734 1.745 205.�3 D.408 1.076 fi.845 1.604 206.02 0.498 i.062 5.960 1.815 207.13 0.599 �.048 7.079 1.626 2D8.36 D.712 1.033 7.203 1.844 209.71 0.839 1.019 7.331 1.854 211.19 0.980 1.OD5 7.463 1.874 212.80 1.137 0.993 7.b01 1.688 21A.54 1.311 D.97b 7.743 ].908 216.43 1.5D2 0.962 7.891 1.930 218.47 1.714 D.948 8.045 �.953 220.fi7 1.947 D.933 8.204 1.979 223.02 2.204 0.9�9 8.370 2.008 225.55 2.486 0.905 8.543 2.039 228.25 2.796 0.891 8.722 2.073 231_i4 3.137 0.876 8.9R9 2.13D 234.22 3.513 0.862 9.109 2.J.5D 237.51 3.925 0.848 9.307 2.194 241.Q� 4.384 0.833 9.519 2.241 244.74 � 4.680 0.819 4.74a 2.293 248.7}. C� • 5.432 6.042 6.718 7.467 8.3Dd 9.230 10.271 11.442 12.76� 19.269 15.993 17.989 20.310 23.069 26:365 30.466 35.724 42.772 53.140 71.674 9D.000 �.$05 0.791 0.776 0.762 D.746 0.733 0.714 0.705 0.591 0.676 0.662 O.b48 0. fi33 0.619 O.b05 0.591 0.576 0.552 0.548 D.533 0.533 9.971 10.213 10.465 10.730 11.OD8 11.299 11.604 11.925 12.263 12.619 12.993 13.389 13.807 14.249 14 ..717 15.214 15.741 16.302 16.899 17.537 17.546 2.35D 2.411 2.478 2.551 2.630 2.717 2.611 2.914 3.427 3.150 3.285 3.433 3.595 3.774 3.970 4.287 4.425 4.591 4.985 5.312 5.317 252.93 257.41 262.16 267.24 272.52 278.33 284.40 290.$5 297.70 344.99 312.74 320.99 329.78 339.34 349.�.2 359.78 371.16 383.33 396.37 410.35 410.54 -----------------------------------------------------------------___-__--------- iJODE 4D7.40 : HGL =< 283.254>;EGL= < 283.776>;FLOWLINE= < 282.024> fYrYrkYrRf�FYrY� Y�YrfY� Y�Y� k*t k*YrY� fYrYrk Y� fiFY� MfY1r*i�*Y�Y�Y�'h Yr *YCYr fYrfY� MYr�M Yrfi�FYrYrY�YrYrYr*Yri� Y� fYrY� kYrY� f#fY�'lrtk FLOW PRpCESS Fi�OM NODE 4D7.4� TO NODE 407.40 TS CODE = 8 LiPSTAEAM NODE 447.40 EL,EVATION�= 282.02 (FLOW IS AT CRITICAL DEPTH� CAi,CULATE CATCH BASIN �NTRANCE IASSES(LACFCD}: PIPE FLOW = �1.Sa CF5 PIPE DIAMETER = 24.OD INCHES FLOW VELOCITY = 5.64 FEET/SEC. VELOCITY 13EAD = 0.523 F£ET CATCH SASIi3 FNERGY LOSS =.2*(VELOCTT`Y HEADj =.2*( 4.523j = 0.105 NODE 407.40 : HGL =< 283.8B1�;EGL= � 283.881>;FLOWLINE= < 282.024> *...,.*.**.***....�..,.,,***+**+.+�***+,�,.�.+v.+**�++.*�*.**.***�***..**.+�++�*�..>. UPSTR£.�M PIPE FLOW CONTROL DATA: - NODE IdtJMBER = 447.40 FLOWLINE ELEVATION = 282.02 • ASSUMED UPSTREAM CONTROL HGL = 283.25 FOA DOWNSTREP.I�3 RUN ANALYSTS ==-=====---===-=--=-==--=--=--==�__=��=��_====__===__==____=___===__===______ � OF GRADUALLY VARTED FLOW ANALYSIS • � � i � * * # 1 * k } } * � i k * * * * * * * f M k * * Y * k 1 * * * * * � i f * i * * * # * # * * * t # * t k 1 1 Y # 7 + Y t # Y i f Y W Y * * f * i � t Y ! i � P�PE-FLpW HYDRAULTCS CQMPUfiEF2 PROGRAM PACKAGE [Fteference: J�ACFCd,�ACRD, AND OCEMA HYDRAETLICS CRITEftI�Nj {c) Copyright 1982-2402 Advanced Engineering Software (aesl Ver. 8.0 Re�Ease Date: Oi/01/2002 License TD 1$Q9 Analysis �repared by: Pl2pJECT DESIGN CONSLTLTAl�iTS 74i 'B' STREET, SUiTE B00 SAN DIEGO, CA 92101 619-235-6471 �***�**+rt***w+*w**v,��st DESCRIPTIQN OF STUDY *+*+*�***�++*+�*�+*a***t** * BR�SSI 7�ANCH - ULTIMAT� CONAITZOFIS * * SYSTF.I�i 9],4 - PA-2 : 3'OWN GP.RDETF R�AD * * PiPEFLOW NODES 414.0 Td 922.3 * *.***,.*...**.**.**.**.*****�**...,.*�***�.+..***.**.*.*****��t*+�**++********* FILE NAME: L414.DA'i' TIME/DAT£ OF STUDY: 08:37 D1/17/2003 �w*rrt�w�r***wv.*x�wr�w**9r��***+�rw*+rxt+�*ry*wrr*ry,r*v�+v.++i.�,t++**a***�++***Ww*♦ GRADUALLY VARIED FLOW ANALYSIS FOR PZP� SYSTEM NdDAI, PO�NT STATUS TABLE (Note: •*' indicates noda� point data used.} UPSTREAM RUN DOWNSTREAM RiJAF NODE MODEL PRESSURE PRESSURE+ FLOW PRESSiJRE+ NUMBER PROCESS HEAD ( FT ) MOMEN�'UM ( POUI3DS } DEP'FH ( FT } i�70MEi3TlIP5 ( PC}UNDS j � 414.00- 5_76* 2362.61 1.31 1254.85 } FRICTION 414.10- 5.31* 2162.67 1.2$ 1262.21 } FRTC`i'ION+BEND 414.20- 3_45* 1342.42 1.26 1305.83 } FRICTION } HYDRAULIC JUTSP 415.D0- 2.11 Dc 952.74 1.33* 1239.90 } JUNCTYON 415.10- 2.17 Dc 1040.40 1.54* 1156.67 } FRICTIONtBEND 920.00- 2.17 Dc 1040.40 1.96' 1251.55 ) JUNCTIDN 92Q.90- 2.53 999.03 1.21+ 3236.62 ) FRICTION+BEND 422.D0- 2.07 Dc 887.70 1.22* 1231.93 ) FRTCTIOAI+BEND az2.�o- 2.a� pC sa�.�o i.z3* izz�.�z } �UNCTION 422.2D- 2.57 962.23 0.92* 1717.29 } FRICTION 422.40- 2.07 DC 887.7D 1.54• 996.85 } JUNCT�ON 922.50- 2.07 Dc 887.70 1.b5* 952.65 ] FRIC'FION 922.30- 2.07*Dc 887.74 2.07*Dc $67.70 ) CATCH BASIN 922.30- 3.9b* 67B.13 2.07 Dc 258.43 MP.XIMUM NUMBEfi OF ENERGY BP,I�ANCES 135ED IN EACH PROFIL� = 25 i ---------------------------------------------------------------------- NOTE: STEADY FLOW HYDRAUI,iC HEAD-LOSS COMPUTATIOiV5 SASELs OA3 THE MOST � CONSERVATIVE FORMULAE FROM THE CllRRENT LACRD,LACFCD, AND OCEMA DESIGN MAN�iALS . i i}�i�} f{� **iF1 *i�Yrk�cf �Ak�kiF*w+1 J f} y*y * f YkYcf Yr *ir**Yr# Y� *iY�*t 1�k#ti*yrMri iFy�*Y�k*� *****t**t* DOWNSTREA�S PIPE FI.,OW CONTROL DATA: NODE 13CFMBER = 914.OQ FLCIWF,INE ELEVATION = 262.37 PIPE FLOW = 42.04 CFS PIPE DIAi�1ETER = 35.Q0 INCHES ASSUN3ED DC�VNSTREAM CON'i`ROL HGL = 268.130 FEET NODE 414.d4 : HGL =� 268.130>;EGL= < 268.578>;FLpWLINE=�<+ 262.370> *�.«*+****++..w�ww****.*****�*****�t**�*f*+**��.*�*+**��*t***tt�.*.*+*w+w�**� FIAW PROCESS FROM NODE 419.00 Tp NODE 914.10 IS CODE = 1 UPSTR�P.M NODE 414.10 ELErIATION = 262.93 (FLOW IS UNDER PRESSURE} - ------------ CAi�CULATE FRICTI01� LOSSES ILACFCD) : PIPE FLOW = 42.00 CFS PIPE DIAME�'ER = 36.00 INCI3ES PIPE LENGTH = 26.91 FEET M.�NNING'S N= 0.41300 SF=(Q/K)*+2 = (( 42.00)/( 667_03Q})*�2 � 0.00396 HF=LwSF = f 25.91}*{Q.Q0396} = O.la7 NODE 414.1Q : HGL =� 268.237>;EGi.= < 266.7$5>,FLOWLINE= < 262.930> .**«*.**�***�******��.****�*..«***.*�******.**��**�.�.�******w.******t*+**+*** FLOW PROCE55 FRpM NOFE 419.10 'FO NODE 414.20 FS CODE = 3 UPSTREAM NpDE 414.20 ELEVATYON = 265.23 (FLOW IS UNDER PRESSURE) CAI,CUF,Ai`E PTPE--BEND EASSES(OCEMA) : �_�HR PIPE FLpW = 42.00 CFS PTPE pYAMETER = 35_00 INCI-iES CF�ITRAL ANGLE = 45.000 DEGREES MANfi�NG'S N= 0.013a0 • PIPE LF�7GTH = 66.34 FEET BEND CQEFFICIF.PIT{}(�} � Q. �7678 FLOW VELOCI'iY = 5.94 PEET'/S�C. VELOCITY HEAD = 0.5�16 FEE'P HB=KB"{�ELOCITY HEAD} �( 0.177J*( 0.54$) = 0.097 SF=IQ/K}**Z = i{ 92.00j/f 656.96911**2 = 0.00397 HF=L*SF = ( 8f.39)*{p,p0397) = Q.343 'POTAL FiEAD LpSSES = HB + HF =( 0.097)+( 0.343} - p.439 NODE 419.2D : IiG�, =< 268.b76>;EGL= < 2fi9_224>;F�,OWLINE= � 2b5.230>y` ^ +irir*ir**,F**#** ****i tf f **w*Yrwi.� �irir#*a***x+w *r * k x f *ir**irt*+y �*++*+irlr ir* * fr # * * �Irw �l.*,hi.* FLOW PROCESS FROM NODE 414.20 TO fIODE 9Z5.40 I5 CODE = 1 UPSTREANS NODE 415 . 00 ELEVATIOPi = 2 7 Q. 6 6 ( HYDRAULIC JLTp3P OCCURS } ------------------------------------------------------------------------------ CAi�CULATE FFL�CTION LOSSES {I,pCFCD} : PiPE FLOW = 42.40 CF5 P�PE DIAMETER = 36.00 YNCHES PIPE LENGi'H = 182'. 94 FEET MANNI23G' S N = 0. 01300 ------------------------------------------------_____--------------------------- HYDRAULIC JEJMP: AOWNSTREA� RUN ANAE,YSIS RESULTS ]30}2MAL DEPTH(FT) = 1.25 - CR��iCAi� DEPTH(FT} - 2.11 -- ---------------_-------------- UPS'I'REAM CflNTROL ASSUMED Fi,OWfaEPTH (FT) = 1.33 _ ------------------------ GFtADUALi�Y VARIED FLOW PRQFILE COMPUTED INFORM.�TION: DISTAi�ICE FROM FLOW DEPTH VELOCITX SPEC�FIC PRESSURE+ CONTROL ( F'i' } ( FT } ( FT / SEC � ENERGY ( FT } MOMF.NTUM ( POUDIDS j fl.d00 1.325 13.943 4.346 ?239.90 2.718 1.322 13.982 4.360 1242.55 5.565 J..320 19.02}. 4.374 1295_21 • 8.553 1.317 19.Ofia 4.389 1247.90 11.695 1.314 19.100 4.4Q3 12SQ.6Q � C� • 15.045 18.541 22.204 26.136 30.327 34.849 39.b22 44.$�6 50.452 56.646 63.379 70.904 79.346 88.965 �DD.12Q 113.374 129.569 Z50.773 180.657 i82.940 1.31� 1.308 1.30b 1.303 1.300 1.297 1.294 1.291 1.289 1.2B6 1.263 1.280 1.277 1.275 1.272 1.269 1.266 1.263 1.260 1.260 14 14 14 14 14 �4 19 14 19 19 14 14 14 1A 14 14 14 14 14 14 14D 180 220 261 302 342 384 925 967 548 55i 593 635 b78 72� 754 808 852 89b 89$ HYDRAULIC JUMP: UPSTREAM RUN ANALYSTS RESLFLTS 9.418 9.933 9.948 4.453 9.478 4.493 4.5�9 4.525 9.590 4.555 �4.573 4.589 4.645 4.622 4.639 4.656 4.673 4.690 4.7DB 4.709 1253 �25b i258 i261 1264 1267 1270 1272 1275 127B 1281 1284 1287 1290 J. 2 9 3 1296 1299 1302 1305 1305 32 06 82 50 44 21 05 91 79 68 50 54 50 48 98 50 59 61 69 83 DOWI�iS�'REAP4 CONTROL ASSUMED PRE55URE HF�D(FT} � 3.45 PRESSURE FLOW PROFTLE COMPUTED INFORMATION: DISTANCE FROM CON'I'ROL ( FT } a.000 �7.399 PRE$SURE VELOCI'I'Y iiEAD(FT) (FT/SEC} 3.�46 5.992 3.00D 5.942 SPECIFIC PRE55UR.E+ ENERGY ( F`I' f M03�1�NTUM S POUNDS ) 3.994 1342.D2 3.546 1145.23 ASSUMED DOWNSTAEFIM PFtESSUAE IiEAD(FT) = 3.40 GRADUALi,Y VA}2YED F'ii�C3W PR�FILE COMPUTED INFORMATION: DISTANCE FRQM C ON'I'ROL ( FT 1 17.349 18.532 19.826 20.969 22.058 23.111 24.127 25.108 26.053 26.964 27.839 28.679 29.481 30.245 3Q.969 31.651 32.287 32.877 33.415 33.$99 34.329 34.68b 39.979 Fi,OW DEP7'H ( FT) �.oaa 2.964 2.929 2.893 2.858 2.822 2.787 2.751 2.715 2.680 2.6A4 2.609 2.573 2.538 2.502 2.466 2.431 2.395 2.360 2.324 2.2$9 2.253 2.217 VELOCITY ( F'T/ SEC } 5.940 5.953 5.977 6.00$ 6.09A 6.aSb 6.133 6.�85 6.240 5.341 6.3b5 b.434 6.507 5.584 6.666 6.752 6.843 6.939 7.040 7.145 7.257 7.373 7.496 SPECIFIC ENERGY ( F`P ) 3.546 3.515 3.484 3.454 3.425 3.398 3.371 3.345 3.321 3.297 3.274 3.252 3.231 3.211 3.192 3.175 3.159 3.193 3.130 3.117 3.107 3.098 3.490 _ PKESSUAEfi MOMENTUM ( POITfdAS ] 1145.23 1130.61 1116.92 1103.88 109i.41 1D79.47 1db8.03 1Q57.08 1Q46.62 7.036.66 iaz�.�s 1018.22 1009.7b 1001.82 994.91 987.59 981.24 975.51 970.37 965.85 961.95 956.71 956.�4 � 35.198 2.162 7.524 3.085 954.27 35.335 2.146 7.759 3.082 953.12 35.383 2.111 7.904 3.08� 952.74 182.940 2.111 7.904 3.0$1 952.74 -------------�_____-----END OF HYDRACFLIC JUMP ANALYSIS------------------------ I PRESSURE+MDMENTUM BALANCE DCCURS AT 3.21 FEET UPSTR.EA�7 OF NODE 414.2� I DOWNSTREAM DEPTH = 3.354 PEET, UPSTREAM CONJUGATE DEPTH = 1.2b1 FEET � NODE 915_00 : HGL =< 271.985>;EGL= < 275.006>;F�OWLINE= � 270.66D> * * * * * * � Y f * t 4 # 1 # t ! t ! t * * i k * * k � * * # * * # * � * � * � rt t * i * * * * # k * * # * * � � * * * * i * � � � * � * * w w * * M f � * FLOW PROCESS FROM NODE 415.00 TO NODE 415.10 �S CODE = 5 UPSTREAM NOpE 4�5.10 ELEVATION = 271.16 {FLpW IS SUPERCRITICAL) CALCUI.ATE JUNCTION LOSSES: PIPE FLAW DIAMETER ANGLE FLOWLINE CRITICAL VELQCITY (CFS) (Ii�7CHES) {DEGREES} ELEVATION DEPTH(FT.f (FT/SEC) UPSTRF�Pr7 42.00 30.00 O.DO 271.16 2.17 12.348 DOW�ISTRF..AM 42.00 36.00 - 27D.66 2.11 � 13.947 LATERAL #1 0.40 0.00 4.D0 0.00 O.OD 0.44D LATERAL #2 0.40 0.00 O.bO 0.00 0.00 fl.040 Q5 a.00-=-Q5 EQUALS SASIN INPUT=== LACFCD AND OCEMA FLOW JLTNCTION FORMULAE USED: DX=IQ2*V2-Q1*V1*COS(f}ELTA11-43*V3iCO5i�ELTA3}- Q4"V4*COS{DELTA4}j/{{AZ+A2)*16.1}+FRICTION LOSSES UPSTREAM: MANNING'S N= 0.413�0; FRICTION SLOPE = 0.0180I DbWNSTR�A�3: MANNIAFG'S N= 4.OI300; FHTCTION SLdP£ = O.Q2440 AVERAGEA FRICTION SLpPE �N JUNCTION ASSUMED AS a.azizo JUNCTIQN I.,k.TIG'i'H = 4. d0 FEE'i ` � FRICTION LOSSES � 0.085 PEE'i' ENTRP.�iCE LC}SS�S = 0.000 FEET ,7i7NCTION LOS5E5 = (AY�HVI-i-I�l2} � {EA7TRF�ICE LOSSES} JLTNCi`ION F�OSSES =( 0. Z57? +{ p. pQD 1= 0.157 -----------------------------------_------------------------------_--�---------- NQDE 415.10 : HGL =< 272,795>;EGL= < 275.162>;FLOWLINE= < 271.16D> ***i1r*1r**##}}**1F 1'i+**Y�*�k i Y Y Yr* t�*�k ir�k *YrYr T**f+i �ilf *i�lY f# Y!*itt* �***#k # k Yr**f f ii+! Y� t FL4W PROCESS FROM NODE 415.1D TO NODE 420.00 IS CODE = 3 UPSTREAM NODE 420.�0 ELEVATION = 273.88 (FLOW IS 5i3PERCRITICAi) CALCLTf�ATE PIPE-BF.I3D LOSSES (OCEMAI : PIPE FLOW = 42.00 CFS PIPE DIAMETER = 30.00 INCHES CENT� ANGLE = 28. 650 AEGREES 3�3P,ATNING' S N= 0. 013fl0 PIPE LENGTH = 159.5� FEET ------------------------------------------------------------------------------ NpHMP.L DSPTHfFT) = 1.67 CR�TICAL DEP3'HSFTj = 2.17 UPSTAEAM CONTROL ASSUMED FLOWDEP'i`H{FTj = 1.45 GRADUALLY VARIED FLOW PROFILE COMPU'i'ED z�TFORN3ATI0N: DISTA�3CE FROM FLOW DEPTH VELOCITY SP�CIFIC PRESSUREt CONTROL(FT} (F`P} (FT/SECi ENERGX(FT) N30M�'NTUM(POUNDS} 0.40Q 1.465 14.a49 9.531 1261.55 4.188 1.473 13.956 9.499 1255.49 6.504 Z.481 13.864 9.968 1249.55 12.948 i.489 13.774 9.937 1243.73 17.545 1.497 13.685 4.907 1238.42 22.305 1.505 13.597 9.378 1232.42 • 27.29b 1.513 13.510 9.349 1226.94 32.387 3.521 13.425 4.322 1221.56 � 37.751 �.529 13.343 4.295 1216.29 43.366 �.53$ 13.258 4.269 121�_13 49.264 �.546 13.176 9.243 1246.07 55.485 i.554 13.095 Q.218 120i.1� 62.077 1.562 13.015 9.194 119b.26 69.099 1.570 12.937 4.1�1 1191.50 75.627 �.578 12.860 4.148 1186�84 84.758 f.586 12.7$3 9.125 1182.28 93.620 I.594 12.708 4_104 117�.8I 103.385 1.602 12.539 4.482 1173.43 114.295 3.610 12.56i 4.062 1169.15 126.705 �.619 12.48$ 4.042 1164.96 141.167 1.627 12.417 4.022 11b0.85 159.6D0 �.635 12.347 4.003 1156.89 159.510 i.635 12.394 9.002 115b.67 NODE 420.OD : HGL =< 275.345>;EGL= < Z78.411>;FZOWLINE= < 273.880� ��*��*�*...**�...*�**.****�***.+**.�*.*+***�.**.*�*..*�**+.*+.+++***+.**�**... FLOW PROCESS FROM NODE 420.00 TO NODE 920.90 IS CODE = 5 UPSTREAM NODE 420.90 ELEVATION = 274.23 (FLOW IS SUPERCRITICALj CAT.CiTLATE JUNCTYON LOSSES : ' PIPE FLOW DTA�+4ETER ANGLE FLOWLTNE CRIT�CAL VELOCITY {CFS) (INCHES) (DEGREESi ELEVATION DEPTH(FT.1 SF'd'/SEC) UPSTREAM 37.b0 30.00 Q.aa 279.23 2.07 15.935 DOWNSTREA.M 42.04 30.00 - 273.88 2.17 14.053 LATERAL #1 2.20 1B.00 90.00 279.88 D.56 3.655 LATERAL #2 2.24 18.00 9Q.00 279.88 0.56 3.655 • Q5 0.40===Q5 EQL3ALS BASIN INPUT=== LACFCD ATFD OCEMA FLOW JUNC2'ION FORMUI�AE USED: DY={QZ*V2-Qi�V1wCOSf�ELTA1}-Q3*V3*COSiDELTA3]- Q9�iI4*COS(DELTA4))/((A1+A2}*�f>.�)+FRICmTpN LOSS�S UPSi'AEAM: MP.NNI�IG'S N= O.fl].30D; FRICTION SI.APE = 0.03734 DOWNSTR�AM: MPNNIAiG'S N= 0.01340; FRICTION SLOPE = 0.025D0 AVERAGED FRICTION SLOPE IN JUNCTION ASSiJ�fED AS 4.43�17 JUNCTION LENGTH = 4.00 FEET FRICTION LOS5E5 = 4.125 FEET EA3'I'RANCE LOSSES = 0.000 FEET JUNCTION LOSSES = (DY+HVl-HV2}+(ENTRANCE LOSSES) JUNCTION LOSSES =( 0.973f+( O.00Q? = 0.973 NOI7E 420.90 : HGL =� 275.992>;EGL= < 279.385>;F'LOWLINE= < 274.230> ♦*i ## i�k�k1+`k+41! �Y�'k*# 4�#*YCYci� ## f� f#f#*f Y•#**'�*#*i## �k i�*+ti*4 t#1� # i� t i#**'F �k'F*�l*f YY�1 k#i PLOW PROCESS FROM NODE 424.9Q TO NODE 422.40 TS CODE = 3 UPSTREAM NODE 422.D0 ELEVATION = 275.73 (FLOW IS SUPERCRITICAL) ------------------------------------------------------------------------------ CAL,CUT.ATE P�PE-BEND LOSSES(OCEMAi: PiPE FLOW = 37.60 CFS PEPE DfAMETER = 3Q.40 INCHES CEN�'RAL ANGLE _?.100 BEGREES MANNING'S N= 4.013Q0 PIPE LENG'I'H = 39.5Ss �EET NORM.AL DEPTH(FT) = 1.21 CRITICAL D�P'I'H{FT) = 2.07 UPSTREAM CONTROL ASSUMED FLOWDEPTH(F'F') = 1.22 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------- GfiAl)UALLY VARIED FLpW PROFII.,E COMPLT'iED I13F'OR�SA'T'ION: • DISTP.PFCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT) (FT} {FT/SEC) ENERGY(FT) N30NSENTUM{PQi.TNDS) � o.aao 1.21b �5.856 5.123 123�.93 2.783 1.216 i5.663 5.126 1232.36 5.685 1.216 15.870 5.129 1232.78 8.719 1.215 15.675 5.132 1233.21 11.896 1.215 15.883 5.135 3233_63 15.230 1.214 15.894 5.137 1234.Ob 1$.738 1.214 15.89fi 5.140 3239.49 22.437 1.214 15.943 5.143 1239.92 2b.351 1.213 15.93Q 5.146 1235.34 30.504 1.213 15.9�6 5.149 2235.77 34.929 1.212 15.923 5.152 i23fi.20 39.540 1.212 15.930 5.155 Z236.62 ------------------------------------------------------------------------------ NODE 922.00 : HGL =< 275.946>;EGL= < 280.853>;FLOWLINE= < 275.730> *+********t***yrt**sr**f*��y�*ia�rfsr+*s*��**r**r++�++*xw**t*w**xx>*�w+�**+t+f FLOW PROCESS FROM NODE 422.00 TO N4DE 422.1p IS CODE = 3 UPSTAEAM NODE 922.10 FI.EVATION = 277.48 (FLOW I5 SUPERCAiTICAL} CALCULATE PIPE-BEND LOSSES{pC�); PIPE FI,OW = 37.60 CFS PIPE DIAMETER = 30.00 INCHES CENTRAL ANGLE = 29.340 DEGREES MANNING'S N= 0.0130D PIPE LENGTH = 46.0$ FEET -------------------------------------------------------------_------------------ I30RMAL DEPTH�FTj = 1.21 CRITICAL flEPTH(FT} - 2.07 ------------------------------------------------------------------------------- iJPSTREA�f CONTROL ASSUMF3� FLOWDEPTH(FT) = 1.23 -------------------------------------------------------�__-------------_____.�r GRADI3ALLY VARTEp FLOW PROFIE,E COMPU'fED �NFORMATEON: __-_�------------------------------------------------------------------------- � DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTRDI. { FT ) { FT ) ( F'i` / 5EC } ENEAGY { FT ] MQM�:N I'UI+S ( POUNDS 1 4.000 �_22� �5.640 5.452 1221.32 2.737 . 1_226 �5.709 5.Q57 1222.�7 5.594 1.225 15.717 5.Q63 1223.02 8.562 1.224 15.734 5.069 1223.87 11.713 1.223 15.744 5_074 1224.73 15.�02 1_222 15.757 5.080 1225.58 16.4fi3 1.222 15.771 5.086 1226.44 22_11fi 1.221 15.784 5.092 1227.30 25.989 1.220 15.796 5.09B 1228.17 30.�91 1.219 15.811 5.143 1229.03 34.469 1.238 15.$25 5.1fl9 1229.90 39.155 1.218 15.83B 5_115 1230.76 99.195 1.2Z7 15.852 5.121 123L 63 96.080 1.216 15.856 5.123 1231.93 NODE 922.10 : HGL =< 27$.7D7>,EGL= < 282.532>;FLOWI_,I�iE= < 277.480> f fiYr!*Yr#Yr�YYYY 144�i�#*i#�kiFf* }yr}*}**�FYriF* ki�Y�f *Yri�Yr*fi* kYrY•* *?Yr*Mk*�***�ctf*#*Y**�r* t*#iF FLOW PROCESS �'ROM NODE 422.10 TO I30DE 422.20 IS CODE = 5 UPSTi2EAT3 I+70DE 922.20 ELEVATIOI3 = 277.83 {gLOW IS SUPEI2CRITICAL) CALCiTLATE JUNCi`ION LOSSES: PIPE FLpW DIAMETER ANGLE FT,OWLTNE CRITICAL VELOCITY (CFS) (INCHES) (DEGREES) ELEVRTIOi�3 DEPTH(FT.) �F'F1SEC) UPSTREAM 37.60 34.04 45.00 277.83 2.07 23.035 DC1WN5'FREAM 37.60 30.04 - 2�7.48 2.07 15.695 LATEI�AL #1 0.00 a.oa O.DO 0.00 0.00 O.pDO � LATEFtAL #2 fl.Ofl 4.Q0 0.00 O.OD 0.00 0_000 Q5 O.DO===QS EQUALS BASIN IIJPUT=-= � LACFCD AND OCEMA FLpW JUNCTION FORI�ULAE USED: 17Y={�2*V2-Q1°V1*COS(DELTAI)-43*V3�COS(DELTA3}- Q4*V4*COS(DELTA4)�/I(A1+A2}*16.1}+FRICTION LOSSES UP5'i`RF�M: MPNNITdG'S N= 0.01300; FRICTION SLOPE = O.1Q186 DOWNSTREA3+3: MANNING'S N= 0_01300; FRxC`PION SLOPE = 0.03586 AVEiiAGED FRICTI013 SLOPE IN JUNCTIOid ASS[dMED AS 0.06886 ,7UNC�'IOI3 LEIdGTH = 4.OQ FEET FRTCTION LOSSES = 0.275 FEET ENTRn.NCE LOSSES = 4.000 FEET 3UNCTIOT3 X,QS5E5 = (DY+HV}-HV2j+(ENTRANCE LOSSES) JiJNCTIOI�i L05SES = f 4.455)+( 4.000} = 4.455 ------------------------------------------------------------------------------ NpDE 422.20 : HGL =< 27B.797>;EGL= < 28fi.986>;FLOWLTNE= < 277.830> **.�***tt+.*.**�*.�,,*..�.�*�**.**.w.��+.****+++.+***.�**.***�..*****,.**,.*.,,... FLOW PROCESS FROM NODE 422.24 TO NODE 422.40 I5 CODE = 1 iJPSTREAM NODE 422.40 ELEVATIO?�F = 2$8.54 (FLOW IS SUPERCRITICAL} ------------------------------------------------------------------------------ CALCUIJITE FRICTION LOSSES{�CFCD}: PIPE FLOW = 37.b4 CFS PIPE DIAMETER = 30.Q0 INCHES PI PE E�ENG'I'H = S D. 40 FEET MA?�TNING' S N = 0. 413 0 D NORMAE� DEPTH ( FT j= d. 85 CR�TICAI, DEPTH ( FT) = 2. 07 UPSTREAM CdN'PROL ASSUMED FLOWDEPTH(FT) = 3.54 GRADl1ALi�Y VARIED FLOW PROFILE COMPU3'ED IA1F'ORMATIOI3: ------------------------------------------------------------------------------ DISTAi�iC� FROM FLdW DEPTH VELOCITY SPECIFIC PFtESSURE+ . CONTROE� ( FT ) ( FT } ( FT / SEC J �.TIERGY ( F'T ) MOMEEdTCTM ( PO[7NDS ? O.OQO 1.538 �Z.870 3.727 996.85 0.561 1.5�Q 12.126 3.795 1010.1$ 1.226 1.483 22.395 3.870 1024.55 1.944 1.455 �2.678 3.953 1040.fl1 2.741 1.428 �2.975 4.043 1456.63 3.627 1.900 13.287 4.143 1074.4$ 4.615 1.373 13.616 4.253 1093.fi4 5.716 1.345 13.962 4.374 1114.18 6.947 1.318 14.326 9.507 1136.20 8.326 1.290 14.711 9.653 �]59.84 9.875 1.263 15.117 4.81� Z185.09 11.b22 3.235 7�5.547 4.991 i2�2.i8 Z3.599 �.208 16.001 5.186 �241.21 �5.849 1.180 16.482 5.401 1272.32 18.424 1.153 16.993 5.64� 134�.68 21..393 1.125 17.535 5.903 1391.47 24.846 1.098 18.112 6.195 1379.88 28.906 1.071 18.72b 6.519 1421.14 33.745 1.093 19.381 6.879 1465.50 39.617 1.01fi 20.Q8i 7.281 1513.24 46.916 0.988 20.829 7.729 1564.69 56.303 0.961 21.632 8.232 162a.16 b9.016 0.933 22.495 8.795 1660.10 80.400 - 0.917 23.028 9.156 1717.29 ------------------------------------------------------------------------------ NODE 422.90 : HGL =< 290.178>;EGL= < 292.367>;FLOWL�NE= < 288.640> +t++**.�+�t+**+*+..�..*�..*..�*..+�..�*.*..��+.*****.*�.**.++..*�**�*.***.�*�� FLOW PROCESS FROM NODE 422.94 TO NODE 422.SQ IS CODE = 5 • UPSTREAM NODE 922.50 ELEVATION = 2$$.97 (FLOW IS SUPERCRITICALJ ----------------------------------------------------------------------------- � CALCULATE JiTNCTION LOSSES: PIPE FLOW DTAMETER ANGLE FLOWLI[dE {CFS� {INCHES} (DEGREES} ELEVATION UPSTREAM 37.60 3D.b0 0.40 288.97 � DOWNSTREAM 37.60 30.Oa - 288.69 LATERAL #1 0.00 O.OD 0.00 0.00 LATERAL #2 D.00 0.00 0.00 D.DD Q5 0.0�==-QS EQUALS EASIN INPUT=== CRI'PICAL VELOCITY AEPTH{�'T.) (FT/SEC) 2.a7 10.954 2.07 11.$73 0.60 0.000 4.04 D.400 LACFCD AND OCEMII FLOW JUNCTION FORMULAE USED: 17Y=(42*V2-Q1*V1*C05(DELTA�]-Q3*V3*COS{DELTA3}- QA*V4}COS(AELTA4j}/{{}�1+A21*16.1}+FRICTION LOSSES UPSTREAM: MANNING'S N= 0.01300; Fi�ICTION SLOPE = 0.0141I DOWNSTREAM: MANNING'S N= D.Q13D0; FRIC'I'ION SLOPE = 0.0J.727 AVERAG�D FRICTION SLOPE IN JUNCTION ASSUMED AS D.01569 JUNCTIQN LENGTH = 4.00 FEET FRTCTIQN LOSSES = O.Ofi3 FEET FNTR�NCE L05SES = Q.000 FEET JC3NCTION i,USSES = (DY+HV1-HV2)+(ENTRP.NCE LOS5E5j JCTNCTIQN LOSSES =( O.lJ.S}+( 4.D00) = 0.115 NODE 422.50 : HGL =< 29a.618>;EGL- < 292.481>;FLpWLINE= < 288.970> «+..*******.+��+�*******...*********...****�*****++*��.*..«**+k�**,r+*++{t FLOW PROCESS FROM NODE 422.50 TO NODE 422.30 I5 CQDE _� UPSTREAM NODE 422.30 Ei,EVATION = 2$9.67 (FLOW IS 5UPE32CAITECAL) --------------------------_---------------------------------------------------- CAL.CULA'I'E FRICTTON LOSSES {LACFCD) : PIPE FLOW = 37.60 CFS PIPE DIATfETER = 30.00 INCHES PIPE I.�ENGTH = 35.4a FEET MPNNING'S N= 0.01300 � --NOItN3AL-DEPTHIFT?--=--=-=�=47==--=_--=-=CRITICAL-DEPTH(F"P�=-======2=07y"'=== __.... _.. _ .... �_ _ __ __ __ _ UPSTRE.�.�f CON'PROL ASSUMED FLOWDEPTH (�"I' )= 2. 07 GRAi7(3ALLY VARIED FLOW PRpFILE CO2+3PUTED INFORMATION: DISTANCE FROM FLOW p�PTH V�LOCITY SPECIF�C PRESSTJRE+ CONTROI, ( FT } { FT j ( FT / SEC ) FNERGY { F'I' } MpMEN'i'UM { POLTNDS j O.Q04 2.474 8.633 3.232 887.70 0.457 2.a50 8.726 3.233 8$7.B9 0.236 2.025 S.B23 3.235 888.43 0.544 2.001 6.924 3.238 889.36 0.995 1.977 9.029 3.243 890.66 1.642 1.952 9.139 3.250 892.37 2.3$0 1.928 9.253 3.258 894.48 3.348 1.9D4 9.372 3.268 897.01 9.528 1.879 9.495 3.260 899.96 5.945 1.$55 9.524 3.294 903.37 7.631 1.831 9.758 3.310 907.23 9.625 1.$46 9.897 3.328 911_57 , 11.972 1.782 �0.042 3.349 916.40 14.730 3.758 10.193 3.372 921.74 17.374 1.733 1Q.349 3.398 927.6� 21.797 1.709 10.513 3.425 934.03 26.324 1.685 10.682 3.458 941.02 31.725 1.66D 10.859 3.493 948.60 35.040 1.646 10.951 3.51i 952.65 ------------------------------------------------------------------------------ NODE 422.3Q : HGL =< 291.744>;EGL= � 292.902>;FL4WLII3E= < 269.670> • �F YriFtt# M-F#! * i*�k�F YrYrYrY� #Yci **}}*iit! i il i*f }#? k il #*i�Yi 1**t�r�hir �kYr***t�1�k� Y�t11�k*f�1il�*Yr* � FLOW PROCESS FROM NODE 422.30 TO NODE 422.30 IS C4DE = B UPSTREAM NODE 922_30 ELEVATION = 289.67 {��QW UNSEALS IN REACH) ------------------------------------------------------------------------------ CALCITLATE CATCH BASIN F�7TRANCE LOSSES(LACFCD}: PIPE FLOW = 37.60 CFS PIPE DIAMETER = 30.00 INCHES FLOW VEi�OCITY = $.64 FE�i'/SEC. VELOCITY HEAD = Z.15B FEET CATCH $ASIN ENERGY L05S =.2*{VELOCTTY HEAD} _,2'I I.15B) = 0.232 Y NODE 422.3Q : HGL =< 293_134>;EGL= � 293.134>;FLOWLINE= < 289.b70> �+t***..*�**�>*t�.+w*,.w*�*�t�.****��**+*+��*.*+*++�++ttt+*********,.**�**.w*** [3PSTFtEAM PIPE FLOW CONTftOL DA'i'A: NpDE NUMBEA = 422.3D FLOWLIAiE EL�/ATION = 284.67 ASSUMED LiPSTREAM CONTRdL HGL = 291.74 FOR DOWNSTREAM RUN ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS • ` J � APPENDIX 4.1�.6 SYSTEM SUO (EL CAMINO REAL} � �J . +wx*.tf*f��w++**+*+�**++�t*+�+++�w�y��***+*r****�**+�r*r�+*R**+**�**+*+�*ti*+ PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRD, ATFD OCEMA HYi3RAUT.,ICS CRI�ERION) fc] Capyright 1982-20a2 Advanced Engineering Sof�ware (aes) Ver. 8.0 Release Date: O1/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSUi�TANTS 701 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 619-235-647� '"`**********''"*w***"++**+* DESCRIP'FION OF STUDY *r+r�+***+ii*rrty*tt+t*+** " BRE55I RANCH - ULTYMATE CON�JiTION * * SYSTEM 800 {42" ALONG EL CAMiNd l2EAL): DOWNSTRF.AM OF CbS UNTT * * 1Q0-year storm event ` .**++**��t.�,�,..,.+�.��+t++t�+:.*.f**+�.:****..****:.,,.�.**..,.++.,.�**�,.�**�*.� FILE f3AME: L8QOA42.11AT TFME/DATE OF STUDY: 17:35 Q1/20/2003 yrlYYr f*� Yr***� *�1rf fi*Yrt'k# �k **�ki*t* ik tk tk M' k f**1r* **'k#Yr*1k 1tYyr4Y *fi11� * fY#YY*Y4*Y�#�1Y�k *** f**ir GRADUALLY VARIED FLOW ANAT.�XSxS FOR PIPE SYSTEM NODAL POiNT STATUS TABLE �Note: •"" indicates nodal poin� data used.) UPSTRE.�M RUN AC1WN5`i'REAM RUN NODE MODEL P}�SSIiRE PRESSURE+ FLOW PRESSURE+ NLTMBER PROCESS HEAD ( FT ) MOMEN'PUM { POLTNDS ) DEPTH ( F'I' I MOMENTUM ( POUNDS ) • 800.00- 3.00 2082.64 2.15' 2175.24 } FRICTIOA3 801.0�- 3.04 2101.16 2.47* 2225.56 } FR�CTION 8Q2.00- 2.B7 2097.34 2.03* 2259.73 } ,7UNC'i`IObI 802.90- 3.25 3924.95 1.65* 2207.72 } FRICTTON 803.00- 2.58*Dc ' 3737.13 2.58*Dc 1737.13 ) ,7urrc�zorr 603.90- 3.64* 2045.55 1.97 1655.07 } FRIC'f`ION BQ5.00- 3.65"' i929.61 2.12 1594.02 } MANHpLE 805.90- 3.48* 1829.28 2.98 Dc 1541.22 ] FFtICTION 810_04- 3.34* 1759.18 2.19 1575.'72 } MANHOLE 810.9Q- 3.19* 1692.14 2.98 Dc 1541.22 ) FRICTION 8J5.00- 2.87* 1591.27 2.19 1575.72 ) MA73HOLE 815.90- 2.48*Dc 1541.22 2.98�Dc 1543.22 ) FRICTION 819.00- 2.75* 1565.42 2.48 Dc 15A L 22 MP.XIAf[iNf I3i7MBER OF E�}ERGY BAT_�ANCES USED I1V EACN PROFILE = 25 -------------------------------------------------------------____-_------------- 130�'E: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASE17 ON THE MOST CONSERVATIVE FORMULAE FROM THE Ci3RREI3T LACRD,LACFCD, AND OCEMA . DESZGN NFANUALS. � t K # f � � i + } * * * * � * * � i t * * * M M * ? * * # * * * # i 1 1 Y k � k * f 4 f Y Y % * N � # W # * } * * w f * Y * * * * * * * * * * * * * # * * * DOWNSTREAM PIPE FLpW CONTRpL DATA� NODE NUMBER = 500.00 FLOWLINE ELEVATION = 278.67 PIPE FLOW = 72.00 CF5 PIPE BIAMETER = 36.00 ZNCHES ASSUMED DOWNSTREAM CpNTROL HGL = 28�.67Q FEE`I' -----------------�------------------------------------------------------------- NODE 800.00 : HGL =< 280.821>;EGL= < 283.557>;FLOWLINE= < 278.67�> *****.�*,�.*****t*+*+w.**��w*��**��***.��****k.,.�.��+�*+.�.+.��++�+�*** FLOW PROCESS FROM NODE 800.00 TO NQDE 801.00 IS CODE = 1 UPSTR� iJODE � 801.00 ELEVATION = 278.90 {FLOW IS SUPERCRITICAL) CALCULATE FRYCTION LOSSES(LACFC37}: PiPE FLOW = 72.p0 CFS PIPE DIP.METER = 36.04 �NCHES PIPE LENGTH = 23.3� FEET NSADiNIIVG'S N = O.OI30Q -__> NORMAL PIPEFLOW I5 PRESSURE F�,OW _-_____------------------------------------------------------------------------ NORMAI, DEPTH(FT� = 3.00 CRITICAI, DEPTH{�'�') = 2.68 UPS�'REAM CQNTROL ASSUMED FLOWDEPTH{FTJ = 2.67 GRFIDUALLY VARIEI7 FLpW P�dFILE CQMPUTED INFORMATIOid: ^" DISTANCE FFtOM FLOW DEPTH V�E,OCITY SPECIFIC PRESSURE+ CQN'PRpL{FT) (FT) (FT/SEC} ENERGY{FT) MOMENTLTM(POUNDS} 0.000 2.D72 13.619 5.04D 2225.66 7.2D6 2.Q97 13.642 4.988 2208.96 14.455 2.121 13.471 4.941 2193.1B 21.751 2.146 13.306 9.896 2178.28 23.30D 2.151 13.271 9.887 2175.24 . ------------------------------------------------------------------------------- NODE 801.00 : HGI� _< 280.972>;EGL= < 283.944>;FL�WLINE= < 27B.90p> *y�s*�+*sy�***+*�+*�*r+**a�**tt*�t*at*+*fw+++*+**r�frYw***i.*axxx**wx,o-,o-**rwx***� FLQW P32pCE55 FROM NODE 801.00 'i0 NODE SD2.00 IS COD� = 1 UPSTAF�A�i NODE $02.04 ELEVA'FION = 279.4fl (FLOW I5 SUPERCAITICAL) CALCULA�'E FRICTION LOSSES [7�ACFC1:l) : PIPE FLQW = 72.a0 CFS PIPE DIA.METER = 36.40 INCHES PIPE LENGTH = 3g.2Q FEET MAN3QING'S N- d.a1300 NORNSAL DEPTH ( F'i') = 2. 21 CRITIClaL DEPTH { F�' )= 2. 68 -----------------------------------__---_-_--___--------------------- ----------- UPSTRE.�M CONTROL ASSi.]MED FLOWDEPTH(FT) = 2.03 GR�iDUALLY VARIED FLOW PROFILE COMPEJTED INFOR�+IATION: __------------------------------------------------------------------------------ DZSTANCE FR0�3 FLOW DEPTH VELpCITY SPECIF�C PRE55i7RE+ CONTROL ( FT } { F`i' } { F�' / 5EC ) F�IERGY ( FT ) MOMENTUM ( POUNDS j 0.000 2.026 �9.169 5.145 2259.73 4.979 2.034 14.�12 5.128 2254.Q5 10_115 2.041 14.055 5.1�0 2248.A8 15.923 2.048 13.999 5.093 2242.99 20.9I8 2.056 13.943 5.076 2237.59 26.619 2.063 13.888 5.460 2232.27 32.547 . 2.070 13.839 5.044 2227.04 34.200 2.072 13.8�9 5.a40 2225.66 FIODE 8D2.00 : HGL = � 28�.426>;EGi,= a 284.546>;FLOwLINE= � 279.4DQ> � .�..**�*.*�*.+..**.��.+++++��..t.t+.��++...*�*a...t.«.+.*****++*.....*+..,++*� � FLOW PROCESS FROM NQDE $02.00 TO NODE 602.90 IS CpDE = 5 UPSTREAM NODE 802.94 ELEVATION = 279.73 {FLOW IS SUPERCAITTCALI ------------------------------------------------------------------------------ CAi�CULATE ,7UNCTION LOSSES : PIPE FLOW DIAMETER ANGLE FLOWL�NE CAI�'ICAL VELOC�TY {CFS? (INC3-IES} (DEGREES) EL�7ATION I3EPTH(FT.) (FT/SEC) UPSTR�AM 64.70 36.00 0.4Q 279.73 2.58 15.241 DOWNSTREAM 72.00 36.00 - 279.44 2.68 14.174 LA'FSRAL �1 3.70 18.00 90.OQ 279.73 0.73 2.094 LATERAL #2 3.60' �8.00 90.44 279.73 0.72 2.Q37 Q5 � 0.00---Q5 EQUAZ,S BAS�N II3PUT=== i�ACFCD AND OCEMA FLOW �TUNCTIbN FdRMUI,P.� USED: DY=(Q2*V2-Q1°V1*COS(DELTAI}-Q3*V3*COSIDELTA3)- Q4*tiI4"C�S{pELTA4}}/((A1+A21*16.1j+FRICTION LOSSES UPS'i'REAM: MP.Nt3ING'S N= 0.013b0; FRICTION SLOPE = 0.02725 DOWNSTREAM: MANNING'S I3 = 0.013Q0; FRICTION SLOPE = O.OiB3D AVERAGED FRICTIOt3 SLOPE IN 3iTNCTTON ASSUMED A5 0.02277 JUNCTION LENGTH = 4.00 FEET FREC'i'ION LOSSES = 0.091 FEET EEVV'i'RANCE LOSSES = 0.000 FEET ,7UNCTION LOSSES = (DY+}-N1-HV2j+(ENT}tANCE LOSS�Sa ,7L7NC`i'IQN i,QSSES = ( 0 . 913 ) + { Q . 400 } = 0 . 913 NbDE 8D2.94 : HGL =< 281.383>;EGL= < 2B5.459>;FLOWLINE= < 279,730> *** **� ktk * f YrYrYrk �R f*f1Yri� iF}ii Yr*}****# �f * k* 1YY�i �k * Y*i *!ti i*�! tY Y1! fYti4Yttf #*t t**'k'k*Yr�F FLOW PROCESS FROM T30DE 802.90 �'0 NODE 803.Q0 IS CODE = 1 iIPSTREAM NODE 803.00 ELEVATIQN = 282.79 (FLOW iS SC7PE12CRITICAL} CALCLTf,ATE FRICTION LOSSES(LACFCD): • P�PE FLOW = 64.70 CFS PIPE DIAME'I'ER = 36-00 INCHES P�PE LINGTH = 73 . 04 �'EET MANNIPIG' S N 0. 01300 NORMAL, DEPTH{FT} - 1.45 CRITICAL DEPTHSFT} = 2.58 UP5T32EAM CONTROL ASSUMED FI�OWDEP'1'H{F"I') = 2.58 GRADUAF.E,Y VA1tI£D FLOW PROFILE COMPUfiED TNFORMATTO�I: DISiANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL ( FT ] ( FT } ( F'I' / SEC i ENERGY I FT j 3�503�7ENTL�1 I POUNI7S ) 0.040 2.580 10.000 4.134 1737.13 0.051 2.535 �0.151 4.136 1737.94 0.252 2.490 34.312 4.142 1740_4D 0.581 2.445 �0.465 4.153 1749.57 1.063 2.400 i0.669 4.169 175D.49 1.713 2.355 1Q.866 9.189 1758.24 2.548 2.310 11.075 4.216 1767.90 3.590 2.255 ].1.297 9.248 1779.55 9.$66 2.220 11.534 4.287 1793.30 b.407 2.175 11.786 4.333 1809.24 8.250 2.130 12.053 4.387 1827.52 �a.Q42 2.085 12.337 4.450 1898.24 13.040 2.094 12.639 4.522 1871.57 16.115 f.994 12.96}. 4.605 1897.67 19.758 1.949 13.303 4.699 7.926.72 24.067 1.9Q9 13.6�7 4.807 1958.92 29.25& 1.859 14.455 4.929 �994.5D 35.481 1.819 14.970 5.Ob7 2433.69 43.055 1.769 14.912 5.224 2Q76.79 � 52.4�7 1.724 15.385 5.4Q2 2124.11 • 64.247 1.679 15.891 5.6�3 2175.98 73.OA0 1.653 1fi.196 5.729 2207.72 ----------------------------------------------------------------_-_____-__---- NODE 803.OD : HGL =< 265.370>;EG�= < 286.924>;FLOWLINE= a 282_790� - * * * * 1 i * * f } * * * * * * * * * * ! i * # * * * * t # Y * * w * t * i * # * � � * * * f * * * * i * * Y f Y * Y i Y � * Y * i 1 i 4 1 y i Y � Y f Y # FLOW PROCESS FROM NODE 803.40 Tp NODE 803.90 IS CQDE = 5 UPS'PREAM NObE 803.90 ELEVATION = 282.79 (FLOW UNSEALS IAi REACH) ------------------------------------------------------------------------------ CALCULATE JUNCTION LOSSES: PIPE FE�OW DIAMET�R ANGLE FLO'WLINE CRITICAL V�LOCTTY (C�'S} (INCHES) (��GREES) ELEVATION DEPTH(FT.� (F'T/SEC) UPSTREAM 62.b0 92.a0 0.00 282.79 2.48 6.507 DC�WNSTREAM 64.70 35.04 - 282.79 2.58 10.003 LATERAL #1 0..0o a.aa o.00 o.00 o.00 o.000 z.�TEx�, �2 a.oa a.00 o.00 a.00 o.00 o.oao Q5 2 . �4--=45 �4v�s eAS�N rrr�U'r=-= LACFCD AND OCEH3A FLOW JUNCTION FORMUL,AE USED: DY={Q2*V2-41*V1*COS(DEL'FA1J-Q3*V3*COSIDELTA3}- Q4"V4*COS(DELTA4Jj/{(A1+A2)*15.1�+FRECTION LOSSES UPSTREAM: MAIVNING'S N= 0.013D0; FRICTION SLOPE = 0.00387 DOWNSTREAM: M.a,NI3ING'S N= 0.01300; FRICTION SLOPE = 0.00871 AVEftAGED FRICTION SLpPE IN JUNCTION ASSUMED AS 0.00529 ,7UNCTION LENG'i'H = 4 . QQ FEE'F FRICTIpN LOSSES = 0.025 FEET FNTRANCE LOSSES = 0.311 FEET �UNCTTON LOSSES = (DX�HVI-HV2)�+(EN'FRANCE LOSSES} JUNCTION �.OSSES = I D.055)+( 0.311) = 0.356 ------------------------------------------------------------------------------ NODE 803.90 : HGL =� 286.632>;EGL= < 287.29Q>;FiOWLINE= < 282.790> � *+**w+w+*******f+t**tt++*w***yryrxtt�r++�Wx*t+t*+it*trf**s�rt�rr�r�**+rtrrtt*+s++*+ FF�OW P3tOCESS FROM NODE 803.90 TO AIODE 805.OQ IS C�]]E = 1 UPSTREAt+! i�IODE 805.Op ELEVATFpN = 283.00 {Fi�OW IS ii�iDER PRESSURE) CALCUL�ATE FRICTION LOSSES(LACFCD): PTPE FLOW = 62.60 CFS PIPE DIAMETER = 42.00 INCHES PIPE i,ENGTH = 4.36 FEET MANNiNG'S N- 4.01300 SF={{�/K) "'2 = ( ( 62.60} / ( �OD6.}.90j ) **2 = 0.00367 HF=L*5F = ( 4.35}*(0.00387) = 0.017 ------------------------------------------------------------------------------ NODE 8D5.00 : HGL = a 286.699>;EGL= � 287.307>;FLOWLI3dE= � 283.000> Y* iittYrt Y t i**Y� Yr* 1c �F tt#�kii fi # iFY� * rt4**i 4y 1YY i i 44*ikf iil�k�kiY�k *�i }}}# j� � i�.#+i�k�iY4i * fY i�k FLOW PROCESS FROM NODE 805.d6 TO NODE 805.90 IS CODE = 2 UPSTREAM NODE 805.90 ELEVATION � 283.20 (FLOW SEAi,S ZN REACH} CALCULATE MANHOLE LOSSES(I.ACFCDI: PIPE FE,pW = 62.60 CFS PIPE DIAI�fETER = 42.6Q INCHES AVERAGEA VELOCITY HEAD = 0.658 FEET HMN =.D5*{AVERAGED VELOCITY HF.�i) =.05*f 0.658} = 0.433 ------------------------------------------------------------------------------ NODE $05.90 : HGL =< 286.683>;EGL= < 287.39a>;FLOWL�NE= < 283.20D> �++**+W�+w**t*�*„��***.*.****.�..*�******�*.�**..*********�**�,.��.**********. FLOW PROCESS FROM NQDE 805.00 TO NODE 81Q.40 IS CODE = 1 UPSTREAhi NODE S10.Oa ELEVATION = 283.91 (Fi,OW IS SUBCRI'i�CAi,} CRLCULATE FRIC`FION LOSSES{LACFCDi: PTPE F�,pW = 62.60 CFS PIPE DIAMETER = 42.00 Ii�]CHES . PIPE LENGTH = 170.88 FEE'I' t�1ANNING'S 13 - 0.01304 � ------------------------------------------------------------------------------ NORMAL DEPTH(FT} - 2.77 CR�TICAL DEPTHfFT) 2.48 ------------------------------------------------------------------------------ DOWNS'i'RF.P.M CONTROL ASS�JMED FLOWDEPTH{F'Ti = 3.48 GRADUALLY VARIED FLOW PROFIL� C4MPUTEI7 INFpRMATIOi�i: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPiH VELOCiTY SPECIFIC PRE5Si3RE+ CON'I'ROL { FT ) ( FT ) { FT / SEC ) ENERGY [ FT ) Mpi+SF.�IT[7i+I ( POUNDS } 0.000 3.48i 6.SD9• 4.140 1629.28 95.193 3.453 6.522 4.114 1813.69 82.740 3.429 6.540 4.084 1798.73 1i6.150 3.395 6.562 4.064 1784.3Q 197.019 3.357 6.587 4.041 177D.32 170.880 3.343 6.b09 4.022 1759.18 ------------------------------------------------------------------------------ NODE 810.D0 : HGL =< 287.253>;EGL= < 267.932�;FLOWLINE= < 2B3.910> 1 Y�f Y i*## t t* f�r * i Y# i 1 i* 1 1 4 i rt Y Y i Y Y� Y# 1* Y# i Y Yi t i Yc t*** t* i t# f i i Y i i Y Y Y Y Y 4 1 4 4 i i Y Y t!# i t t f FIAW PROCE55 FROM NODE 810.OD TO NODE 81D.90 IS CODE = 2 UPSTREAM NODE 81fl.90 ELEVATTON = 284.D6 (FL,OW IS SUBCRITTCAL) CAi,CiJL�AT� MP.NHOLE LOSSES(LACFCD} ; PiPE ELOW = 62.60 CF5 PIPE DIAMETER = 42.00 I13CHES AVE32AGED VELOCITY HEAD = 4.694 FEET HMN =.D5*(AVERAGED VELOCITY HEAD) _.05"'{ 0.699) = D.035 ------------------------------------------------------------------------------ NODE 810.90 : HGL =� 287.248>;EGL= � 287.967>;FLOWLINE= < 284.06D> # i*ikf 4Y1�f Yf YYY� �i iFf # 1k Y�i� tkl� *#i#*tti� i i#ii# 1#}i�i *if f+4Ytk t�i iY �k1t*�k �Y�Ltt#*ii�i� # f*�i **1*�ii 1• FLpW PROCESS FROM NODE 810.90 TO NObE 815.00 TS CODE = 1 � UPSTREFII�4 NODE 815.DU �LEVATION = 285.45 (FI,OW IS SLiBCR1TTCALj ------------------------------------------------------------------------------ CALCiJLATE FRICTION L05SES{LACFCDy: PIPE FLOW = 62.64 CFS PIPE DIAMETER = 42.fl0 ENCHES PIPE LENGTH = 335.53 FEET M.�NNII3G'S N= 0.01300 ----------------------------------------------------------------------------- �FORMAL DEP'i'H{F";') - 2.77 CRITICAL DEPTH{F'�') - 2.48 ------------------------------------------------------------------------------ DQWAIS?'REAM CONT'ROL ASSUMED FLOWDEP'I'H ( FT} � 3. 19 ------------------------------------------------------------------------------ GRADUALLY VARTED Fi�OW PROFILE COMPLPFED INFORM.�TION: ------___----------------------------------------------------------------------_ DiSTANCE FROM F%OW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTRO�., ( FT ) ( FT } ( FT/ SEC ) ENERGY { F'7' ) MOMENTUM ( POUNDS } O.a00 3.188 6.Bfl9 3.9a7 1592.10 15.073 3.171 6.829 3.896 1685.56 30.157 3.159 6.855 3.8$4 1679.15 45.2B5 3.137 6.882 3.$73 1672.86 60.491 3.121 6.949 3.862 1666.70 75.810 3.3Q4 6.937 3.852 166Q.b8 91.28D 3.d87 6.956 3.841 1.654.79 1Q6.944 3.D70 6.996 3.831 1649.02 122.847 3.454 i.026 3.821 1643.94 139.091 3.037 7.458 3.811 1637_90 155.588 3.020 7.090 3.BD1 1632.54 172.557 3.OD4 7.122 3.792 7.627.31 190.D35 2.987 7.156 3.782 1622.23 2a8.124 2.970 7.19D 3.773 1617.27 226.953 2.953 7.225 3.769 1612.46 • 246.6$6 2.937 7.261 3.75b 1607.79 � 257.536 2.920 7.298 3_747 1603.26 289.741 2.9D3 7.335 3.739 1598.88 313.B52 2:886 7.374 3.731 1594.64 335.53Q 2.873 7.906 3.725 1591.27 NQDE 815.00 : HGL =< 288.323>;EGL= � 289.175�;FLOWLINE= � 2B5.450> *+t*+*��*�***��x*****+��a�w�trtitrf**++*+�**�*x*x*x**x�***xx*++*+*+*+++��s+syy♦ FLOW PROCE55 FROM NODE 815.00 TO NODE 815.90 FS CdDE = 2 UPSTREAM NODE 8I5.90 E�EVATION =. 2$5.60 {�LOW iS RT CRITICAL DEPTH) CALCULATE MAI3HOLE LOSSES{LACFCD}; PIPE FLOW = 62.64 CFS PIPE DIPiME'I'ER = 42.00 INCHES AVERAGED VELOCITY HEAD = Q.999 FEET F�IIrII�1 = .05* {AVERAGED VELOCI'E`Y HEAD} - .45* ( 0.999j = 0.050 NODE 8�5.90 : HGL =< 288.080�,EGL= < 289.225>;FLOWLINE= � 285.600> *wYc *k�Mtk�lrkYriF*YrYrYrfYrY�ri i�*#1 rt#*f kM#iiikf*1Y#it#*****YiYrkYri�Y�Yri�YrY�YrYrff iFrikY�k f**i**if �kik}*f FLOW PROCESS FROM NODE 815.90 'I'0 NODE 819.00 IS CODE = 1 E3P5TREAM NQDE 819.00 ELEVATION = 286.98 (FLOW IS SUBCRITFCAL} ------------------------------------------------------------------------------ CALCULATE FRICTIOP] LOSSESILACFCDy: PZPE FLOW = 62.60 CFS PIP� DIAMET'ER = 42.00 TNCHES PIPE LENGTH = 330.73 FEET MAAFNING'S 3�1 � 0.01300 �70R[�4AL DEPTH ( FT )= 2. 7 6 CRITICAL 1�EPTH ( FT )= 2. 9 8 DOWt3STREAM CONTROL ASSCFMED FLOWT7EPTH ( FT) = 2. 4 B ------------------------------------------------------------- --- -- � '-GRADi3ALLY VARIED FLOW PROFILE CbMPEiT�D INFORMATIOI3_ -------------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRE55URE+ CpNTROL ( F'P ) ( FT } ( FT / SSC ) ENERGX ( FT ) MpME:NTiTM f POi7ND5 } O.DOD 2.480 $.586 3.625 1541.22 �.087 2.491 8.545 3.625 1541.26 0.359 2.502 8.5D9 3.626 154 L 40 0.833 2.513 8.463 3.626 1541.62 1.530 2.524 8.423 3.627 1543.93 2.471 2.536 B.383 3.628 1542.33 3.6$2 2.547 8.344 3.629 1542.82 5.196 2.558 B.306 3.63a 1543.39 7.D46 2.569 8.266 3.631 1544.D5 9.277 2.580 B.230 3.633 1549.79 i1.938 2.592 8.193 3.635 1545.61 15.090 2.6�03 B.156 3.636 1545.51 18.609 2.614 8.120 3.639 1547.50 23.].88 2.625 8.085 3.641 1548.57 28.343 2.636 8.050 . 3.643 1549.71 34.427 2.646 8.015 3.646 155D.94 41.639 2.659 7.96fl 3.648 1552.24 50.247 2.67D 7.947 3.651 1553.62 60.631 2.583 7.913 3.654 1555.06 73.34b 2.fi92 7.880 3_657 1556.61 89.252 2.703 7.848 3.660 1558.22 109.789 2.715 7.815 3.664 1�59.90 137.b61 2.725 7.764 3.667 1551.66 178.942 2.737 7.753 3.671 I563.49 253.122 2.79$ 7.722 3_675 �5b5.39 � 33D_730 --`+ 2�748« '_--7-721----------3_675----------�555.42Ny'-- -------------------- . NODE 819.00 : HGL =< 2$9.72$>;EGL= � 290.655>;FLOWLYNE= < 28b.9$0> �****��w.*ww+*w*�w+*x�**��+�+�w+w�.**�>***t*�***t*�****+*.�*tt*ti+�.*+...*t***. UPSTREAM PIPE FLOW CONTROL DATA: NQDE NiTMBER = 819.00 FLOWLFNE ELEVATTON = 2B6.98 ASSiJMEA UP$TREAM CON'I'ROL HGL = 289.46 FOR DOWNSTREAM RUN AidALYSIS END QF GRADUALLY VARIED FLOW ANALYSIS � • � * � * * * * * w k * k * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * t * t * * * * * * * * * * * * PIPE-FE,04V HYDRAi]�ICS COMPUTER PROGf2AM PACKAGE {Reference: LACFCD,LACRD, A�iD OCEMA �-IYDRACTLICS CRITERIOiV) {c) Copyright 1982-2042 Advanced Engineering Software (aes} Ver. 9.a Release Date: O1/O1/2002 License ID 1509 Ana3ysis prepared by: Pi�pJECT DESIGid CONSULTAN'i'S 701 'B' STRE�T, SUITE $04 5AN DIEGO, CA 92101 619-235-5471 +s+rrW*s�*w*,r,r************ �ESCRIPTIOid �F STLFDY �*************w*wa*�w**�*� * BR�SSI RANCH - UL'i'IMATE CONDI`FZONS * * EL CAMYNO REAI� SYSTEM - UPSTREAM OF CDS UI3IT * * 104-YEAR STORM EVENT * ***«***********+*+*t****+*+**t******,.***�*+*„t*****�****f:�+*w**.**f*�*f�+ FILE NAME: L800US42.DAT TIME/DATE QF S`I'UAY: 14:35 D2/13/2003 *****�*********�***«****«***********�***�**++****��*x*�*,.***********..********* GRADUALLY VARIEd3 FLdW ANALYSIS FOR PIPE SYS'FEM NODAL POINT STATUS TASLE (Note: "�" indicates nodal point data us�d.) UPS'i'REAM RUN DOWNSTREAM RUN NODE MODEL PKESSURE PRESSiTRE+ FX�OW PRESSURE} NUMBER PROCESS HEAD ( F'i' } MOMENTUM ( POi71QDS ) DEP'i'H { FT) MOi]ENTUM [ POUNDS } � 819.9D- 4.27* 2302.21 2.48 Dc 154�.22 ) FRICTION 824.04- 4.27* 2304.09 2.48 Dc 154i.22 } ,NAICTION 821.00- 4.58* 831.90 ]..37 Dc 263.96 } FRTCT�ON 825.00- 4.52* 820.26 3.37 Dc 263.96 } ,TLTNCTIOi�I 825.00- 4.68* 821.68 �.28 Dc 223.10 } FRICTION 925.10- 4.58� 800.66 �.za r,c zz�.io } ,TUNCTIOi�7 825.10- 4.72* 801.73 �.�.$ Dc ].SQ.62 } F12ICT'ION 826.00- 4.45* 749.23 1.18 Dc 184.62 } 3[jNCTION 826.10- 4.64* 787.09 1.Q2 186.17 } FRICTION 827.00- 4.47* 754.03 1.18 Dc 180.62 } CATCH BASIi�1 827.00- 4.70* 724.71 1.1& Dc b1.69 MAXINiLTM NUMBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEADY FiAW HYDRAULIC HEAD-LOSS CO2+IP[T`i'A'i'FONS BASED ON TH� MOST CONSERVA`i'IVE PQF2.MULAE FROM THE CURRENT LACRD, LACFCD, AND OCEi�A DESIGN MANUAZ,S _ �*********.*********+*�**.***++*.*�*+****+*+.*+*******+***+*t+�++.*�******.�** DdWNSTRF.AM PIPE FLOW CONTROL DIaTA: � NODE NiTMBER = $�9.90 FLOWi,INE ELEVATION = 287.03 PIPE F�dW = 62.60 CFS PIPE DIAME�`Eft = 42.p0 INCHES � ASSUMED DQWNSTRFAM CON�'ROL HGL = 291.300 FEET NODE 819.90 : HGL =< 29�.300>;EGL= < 291.957>;FLdWLINE= < 2g7.03D> �r�***+*Www�**************f**:**�***+s*******rww��********+**t**t*****r***ww* FLOW PROCE55 FROM NODE 819.9D TO NOAE 82Q.OD I5 CODE = 1 UPSTREAM NQDE 820.00 ELEVATION = 287.08 (FLOW TS UNDER PRESSURE) CALCLTLATE FRICTIOI3 LC7SSES {J,ACFCD} : PIPE FLOW = 62.6D CF5 PiPE DIAMETER = 42.Oa rNCHE5 PIPE E,Ei4G'l'H � 12.00 FEET MANNING'S N = 0.0134Q SF=(Q/IC)**2 = (( 62.fi0)/( lOQ6.146))**2 = 0.00387 HF=L*SF = { 12.00f"(0.003B7} 4 Q.046 NODE 820.Q0 : HGL =< 291.346>;EGL= < 292.004>;FLOWLINE= < 287.080> **�**�v.,r***+*******f*****+r�x*�*w**w,r,r***x#**v.****+**«+***r**t*t+***w,r�,�,+v�wwv.vr FLOW PROCE55 FROM NODE 620.00 'd`0 I30DE 821.00 I5 CODE = 5 L7PSTREAM NODE 821.00 ELEVAT`xON = 287.29 (FLOW IS UNDER PRESSI7RE} CALC[iLATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWI�INE CRI`£ICAL VELOC�'I'Y (CFS) (INCHES) (DEGRE£S) ELEVATIpN AEPTH{�'T.} (FT/5EC) UPSTRFArs 14.5D 24.OQ O.OD 287.29 3.37 4.b�5 DOWNS'PHEAPS 62.60 42.00 - 287.OB 2.48 6.507 LA�'ERAL #1 48.10 30.OQ 60.00 287.58 2.27 9.799 LATERAi� #2 O.dO 0.00 0.00 0.00 b.00 D.a04 Q5 a.oa===4s EQUALS BASIN It3PUT=== LACFCD AND OCEMA FLOW J(JNCTION FORMULAE USED: � DY=(Q2'*V2-QZ*V1*COS(DEE,TAZ]-Q3*V3*CQ5{DELTA3)- Q4*V4*COS(DELTA4})/((A1+A2)*16.1)+F'RZCTION L055E5 UPSTREAi+]: MANNIiJG'S N= 0.01300; FRICTIOE�F SLOPE = O.Q0411 DOWNSTRE.�,M: MANNi?3G'S N= 0.01300; FRICTION SLdPE = 0.40387 AVERAGED FRICTTON SLOPE IN �UNCTION A55UMED AS 0.00399 JUNCTI0�3 LFNGTH = 4.00 FEET F1�ICT'ION LOSSES = 0.016 FEET FNTR�NCE LpSSES = 0.000 FEET JiJNCTION LASSES = (DY+HVl-HV2)+{ENTRAi�10E LOSSES} JUNCTION L05SE5 =( 0.199)+( 0.004) = D.i99 NODE 821 .00 : HGL =< 297.. 672>; EGL= < 292 .203>; FiOWf,irF�= < 287 .290> # tt***Yr�k* f*yr1�Y yr yr#**Yr **** ik tk iFyrtkik ik k Ir�F*tk*'ktktkt*i*tt i t i f i iFY �Yyr *** **#** f** ik Yr Yr**iFYr* *** * FLOW PRQCESS FROM NODE 82�.04 TO i�IODE 825.b0 IS CODE = 1 UP5'£REAM b30DE 825.OQ ELEVATION = 287.fi4 (FLOW IS UNDER PRESSURE} CALCUI�ATE FRICTION LQSSES (I�ACFCD) : PIPE FLOW = 14.50 CFS �IPE DIANIETER = 24.00 INCHES PIPE LENGTH = 61.Od FEET MANNING'S �1 - O.D1300 SF=(Q/Kf**2 = i( 14.50)/( 226.221))**2 = 0.00411 HF=L*SF = S 67.00f*50.00411� = 0.251 ------------------------------------------------------------------------------- r�017E 825.00 : HGL =< 292.123�;EGL= < 292.453>;FLOWLINE= < 287.604> *�*,.******:**t.,�+��*+***+***,�*��**��..*��*.*t�***��.*..»**�**+***�+�***�.*w� FLOW PROCESS FROM NODE 825.00 �'0 AiODE 825.D0 IS CODE = 5 UPSTREAM NODE 825.04 ELEVATIOI3 = 287.60 {FL4W IS UI3DER PRESSURE) CALCTJ�,ATE JU�+ICTION LOSSES : � PIPE FLOW DTAME'I'ER ANGLE FLOWF,INE CRTTTCA� VELOCITX (CFS) (INCHES) (DEGREES} �LEVATION DEPTH(FT.) (FT/SEC} � UPSTREAM 12.70 24.40 0_00 287.6D 1.28 4.042 DOWNSTR.EA.M 14.50 24.04 287.60 1.37 4.615 LATERAL #1 1.80 18.00 90.00 287.95 D.54 �.0�9 LATERAL #2 Q,00 0.60 D.00 O.OQ 0.04 4.D00 45 . 0.00===Q5 EQUAi,S BASIN INPUT=== � • LACFCD AI3D OCEMA FI,OW JUNCTION FOR�+fULAB USED: DX=(Q2*V2--Q1*V1*COS(DELTAlf-Q3*V3*COSIDELTA3}- Q4*V4*C05SDELTA4y)/({A1+A2j*16.1}+FRICTIpN LOSSES UPSTREA2+I : MAi3AiId+}G' S 13 = �. 01300 ; FRICTIOId SLOPE = 0. 00315 DpWNSTRFAM: MANI3I2JG'S I3 = 0.41300; FRICTIOid SLQPE = D.00411 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS O.D0363 �3UNC`i'IOI�F LENGTH = 2.00 FEET FRICTIOI3 LOSSES = 0.007 FEET ENTRAl3CE LOSSES = 0.040 FEET �7UNCTIOI3 L{?SSES = fDY+HVl-HV2)�(EDITRANCE LOSSESI JUNCTION LOSSES =( fl.084j+( 0.0001 = 0.084 NdDE 825.4Q : HGL =< 292.284>;EGL= < 292.538>;P'LOWLINE= < 287.500> *******+*+*****t+++,r�*wwr�w�wv.wwwwww,rwww+�v�*,ra*xv�***,r,r,rr**++�****************�* FLdW PROCESS FRpM NODE 625.00 TO ?�iODE 825.16 IS CODE _� i3PSTfLEAM NQDE 825.10 ELEVATiON = 2B7.89 (FLOW IS UNDER PRESSURE) CALC[TLATE FFtICTION LOSSES (LACFCDJ : PTPE FLOW = 12.70 CF5 PIPE DIAMETER = 24.OD INCHES PIPE LENG�'H = 58.40 FEET MAI3NING' S N = 0.01300 SF=(Q/K}**2 = (( 12.70}/( 226.219}}*�� = 0.00315 HF=L*SF = ( 58.00)*ffl.flp315j = 0.183 NODE 825.10 : HGL =< 292.467>;EGL= � 292.721>;FLOWLINE= � 287.890> *****++*******„**********t****��+tf,.***�**�.��***t�+*+****.��*��,��.*****f FLOW PROCESS FROM NQDE 825.10 TO NODE 825.10 IS COD� = 5 UPSTREAM NODE 825.10 ELEVATION = 287.89 (FLOW IS LTNDER PRESSURE) CALCiTLA`d'E JUNCTION �,OSSES: PTPE F�,OW DIAMETER ANGLE FLOWLINE CRITICAL i7ELOCI'FY (CFS) iINCHES� (DEGAEES} ELEVATION DEP`PH(F7'.) {F"P/SECi iJPSTREAM 10.90 24.00 4.00 287.89 1.}.8 3.470 DCIWNSTREAM 12.70 24.00 - 287.89 1.28 4.042 LATERA.L #1 1.80 1$.00 90.00 288.14 D.50 1.01.9 LATERAL �2 O.Oa O.Ofl a.ao 0.00 0.04 a.aao Q5 0.00===Q5 EQUALS BASIN INPUT=== LACFCD AND OCEMA FLOW JUNCTION FORMUi�A� i3SED: I}Y-{Q2*V2-Q�*V1*COS(DELTAI)-Q3*V3*COS{DELTA3j- Q4*V4*COS(DELTA4)�/{{A1+A2}*36.1)+FRICfiION LOSSES UPSTREAM: �A�VPIING'S N= 0.4134Q; FRICTION SLOPE = O.Od232 DC}WNSTREP.M: P#A�iNING'S N= a.o�3aa; FRIC`I'�ON SLpPE = D.00315 AVERAGED FRICTION SLOPE IN JUNCTION ASSL7�SED AS 0.0027� JUNCTION LENGTH = 2.p0 FEET FRICTION LOSSES = D.005 FEET ENTRANCE L055E5 = 0.000 FEET �7UNCTTON LOSSES = {DY+HV1-HV2)+{ENTRANCE L055ES} JUi�7CTI0N i�055E5 =( 0. 0721 +( 0. 000 )= 0. 072 ------------------------------------------------------------------------------_ I30DE 825.10 : HGL =< 292.6Q6>;EGL- < 292.793>;FLOWLINE= < 267.890> +*******+*****��***�*.«*�**�*************«*.*t**++*+++��*w��w«��.�,****** FLOW PROCESS FROM NODE 825.10 TO NODE 826.Od IS C�DE = 1 UPSTREAM NODE 826.Q0 ELEVATION = 288.39 (FLOW IS UI3DER PRESSURE� � CALCULATE FRICTZON LO$5E5(LACFCDj: PTPE FL4W 10.90 CFS PIPE DIAMETER = 24.40 INCHES PIPE LENGTH = lap.00 FEET t+jANNING'S N= 0.01300 5F=(Q/K)**2 = (L 10.90}/{ 226.227i?**2 = O.Q0232 HF=L*SF = ( ioa.aaf*fD.002321 = 0.232 NODE 826.00 : HGL =< 292.838>;EGL= � 293.025>;FLQW�INE= � 288.390> ************+**t+**wrwww�*wwr+****+*��w�*t*+*+*+*�+*�x*********f**+++*++****** FLOW PROCESS FROM NODE 826.D4 TO NODE 826.10 IS CODE = 5 UPSTRF.AM NODE 626.1D ELEVATIDN = 288.58 (FLOW IS UNDER PRESS�RE} ------------------------------------------------�___-------------------------- CALCULATE JUNCTIpN LOSSES: PIPE FI,OW DIAMETER ANGLE FLOWLINE C�tITICAL VC:LOCITX (CFS) (Ii3CHE5) (DEGREES) ELEVAT�ON BEPTH(�'T.) (FT/SEC) UPSTREAM 10.90 24.OD 90.00 288.58 1.18 3.470 DOWNSTREAM 10.90 24.�0 - 288.39 1.18 3.470 LATERAL #3 0_00 0.00 0.00 O.OD O.OQ 0.000 LATERAL #2 0.00 0.00 p.00 4.00 O.DO O.D40 Q5 0. 00===45 E4uas,s aasz�r INPL7T=== LACFCD AND OC�MA FLOW JUNCTIO�I FORhf[FLAE USED: AY=(42*�2-41*vl*COS(DELTAI}-Q3*V3*COS(DELTA3i- Q4*V4*COS(DELTA4�}/((A1+A2)*16.1}+FRICTION LOSSES [3PSTREP.M: MAi�FNING'S N= 0.01300; FRICTION S7,OPE = D.Q0232 I7QWidSTREAM: MANNING'S N= 0.01300; FRICTXOI�i SLdPE = 0.00232 AVERAGED FRICTION SLOPE IN J[TNCTTON ASSUMED AS 4.00232 ,TCTNCTION LENGTH = 4. DO FEET FRICTIpN LC}SS�S = D.409 FEET EN�`RANCE L055E5 = 0.000 PEET +IUNCTXON LOSSES = {DYtHVl-HV2}+(ENTRANCE LOSSESj � --JLTNCTION LC}SSES = { D.3$3}�{ 0.000} = 0.363 --------------__________________--_----------------------------------- NODE $2b.10 : HGL =< 293.221>;EGL= < 293.408>;F�,OWLINE= < 288.5$0� �**�rW+,,***�******+******+******�**+*.�f****++�*t*t*****..�w************�***,r** FLOW PFtOCESS FROM NODE $26.�0 TO NQDE 827.00 IS CODE = 1 UPS`i`REAM NODE $27.Oa EI,E[lA'i`ION =. 2B8.80 {FI,OW IS UNDER PRE55URE) CALCUL�TE FRICTIQN LOSSES{i,pCFCD): � PIPE FLOW = 10.90 CFS PIPE DIAMETER = 24.00 IPFCHES PIPE LENGTH = 22.11 FEET MAi�IN�NG'S N= 0.01300 SF={4/K1"`*2 = ({ 1D.94i/( 226.221))**2 = 0.00232 HF=L*SF = ( 22.11)*(0.00232) = 0.051 �TODE 827.Q4 : HGL =< 293.273>;EGL= � 293.459>;FLOWLINE= � 288.800> +*+*,rr******+rtx**+++��v.++++i.t*w�w+*v.w*w*+fi�****+*+s,r*«,o-*****+t**++��*tw++*++ FLOW PROCESS FRO[+I t30DE 827.00 Tp N017E 827.00 IS CODE = B LFPSTREAM NODE 827.00 ELEVA'I'�ON = 288.80 (FLOW I5 UNDER PRE55URE} ---------------_--__------------------------------------------__--____---------- CALCC7LA`i'E CA'I'CH BASII+i ENTRANCE LOSSES (LACFCD) : PIPE FLOW = 1fl.90 CFS PIPE DIAMETER = 24.Q0 �NCHES FLdW VELOCITY = 3.47 FEET/SEC. VELOCITY HEAD = 4.187 FEET CATCH BASIN F.i�iERGY LOSS =. 2*( VELOCITY I-IEAD j=. 2*( 0. 187 �= d. 037 NaDE 827.00 : HGL =< 293.497>;EGL= < 293.497>:FLOWI��NE= < 288.8D0> *�1r***�k********Y� �k ie�Y�Y �Y�kW **#�k * ** * * * *f * * * Yr * * * ********** iF * �k **�k***** iF i��lriri**�ktt�lr �Ic **** UPSTREA�S PIPE FLOW C4NTROL DA'�'A: � NODE [ffi7[�BER = 827.00 FLOWLINE ELEVATION = 288.80 ASSi3MED UPSTREAM CONTROL HGL = 289.98 FOR DOWNSTREAM RUN ANAL,YSIS i*,.y*�,��*.,*�.�,�.*,�,,,.�,�*��.w..��*�..,�.*..**.*.,*.�x.��.,*�*��**,�**�,.� PIPE-FLOW HYDRAULICS COMPUTER PROGAI�hS PACKAGE lReference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION} Ic) Copyright 1982-2002 Advanced Engineering 5oftware {aes} Ver. B.0 Re3ease Date: 4�/41/2002 License ID 1509 Analysis prepared by: Pi20JECT 17ESIGN CONSULTAN'I'S 701 'B' STREE'I', SUITE B00 SAN DIEGO, CA 92101 519-235-6471 +*�w�***w.,ra*��***�*v�**+++ I)$SCREPTION OF STUDY +�r*raw,r****aa******+i*+** * SRESSI RANCH - UI,TZMATE CONDITIdNS * * EL CA�iINO REAI, - PA3 30' CONNECTION TO DESILT BASIN * * 100-YEAR STORM EVENi * t**.*�+.*:+***�.,**.+**+t.*�t��+**.*+...t�+*,��rwt**...:.�t+**..**�+*�**++*** FILE NAME: 840C.DAT 'I'IME/DATE OF STUDY: 17:58 01/20/2003 *+-�*�.**«�*+*t+**+*w+�**�**+.****.��***.*****�**.*��*v,*******.,*t***.**t***.+* • GRADUALI�Y VAftIED FLOW ANALYS35 FOR PIPE SYSTEM NODAE, POINT STATUS TABLE {Note: '*" indicates nodal point data used.) UPSTREAM RUN DOWNSTREAM RUAI NODE MOD�L PRESSURE PRESSURE+ FLOW PFtESSURE+ N[7Mi3EA PROCESS HEAD ( FT 1 A4dMEN'I`UM ( POE1ND51 DEPTH ( FTi Mp2+3ENTUM ( POUNDS ) � 809.00- 4.15 1832.29 1.30� 1883.�2 } FRIC�ION 80B.40- 2.29*Dc 1303.21 2.29*Dc 1303.2t } CATCI-i BASTN � 808.40- 4.30* 933.79 2.29 Dc 318_14 ------------------------------------------------------------------------------- MAX3MUM NU[+SBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 • NO'£E: STEADY FLOW ]iYDRAiTi�IC HEAD-LQSS COt�SPUTATIO�iS BASED ON THE MpST C�NSERVATIVE FORMULAE FRpM THE CURRFsiT LACRD,LACFCD, AND OCFMA D�SIGN M.AN[JALS . i� i�*YriF*!*YriFiFk f� t t**i* f� t yr*# **}**Yr*iY **1r!!# il Y� Yr* *ikfttti * t1Yyr�kyr*i*Y� *�F **Yrf***YrfYrf }Y� Y� f DOWNSTREAM PIPE Fi,pW COI�FTROL DAi'A: NODE NLTMBER = 809.00 FLOWLINE ELEVA'i'ION = 287.85 PIPE FLOW = 48.9p CFS PIPE DIAMETER = 30.00 iNCHES ASSUMED DOW135TREAM CONTROL HGL = 292 . Q00 FEE`F' ---------------------_---------------------------_-_---------------------------- NODE 809.00 : HGL =< 289.152>;EGL= � 294.715>;FLOWLINE= < 287.85d> r�*+f.w+*++�*�.�.**►��**t+...r...y.M**r+++**+**...***f�+++*�rtti�riwtt**t*�t+*.�w. FLOW PROCESS FROM NODE 609.0� 'i'O NQDE 8p8.40 I5 CODE = 1 UPSTREAM NODE 809.40 ELEVATION = 292.06 {FLOW TS SUPERCRITICAL} --------------------------------------------------_-_--------------------------- CALCULA'FE FRICTION LOSSES{LACFCD): P�PE FL4W = 46.9Q CFS PTPE DIA?�SETER = 3Q.04 INCHES PIPE I�EIVGTH = 39. 45 FEET MP.NNING' S N = 0. D1300 ------------------------------------------------------------------------------ NO�L DEP3'H (FT) = 1. 04 CRITICAL DEPTH q F'F) = 2. 29 ------------------------------ • UPSTREAM CONTF20L ASSUMED FLOWDEP'iH(FTj = 2.29 � __________________�-==_______________________�,�_ � GRADUALLY VARIED FLQW PROFILE COMPLJ'I'ED INFORMATIpN: DISTANCE FROM FLOW DEP'I'H VELOCITY SPECIFIC PRESSURE+ CONTRQL(FT} (FT) {FT/SEC) ENERGYfFTi MOMk.NTUM(PQUNDS) O.00fl 2.2B5 10.392 3.963 1303.21 D.039 2.235 �0.556 3.967 1309.29 0.159 2.1B6 �Q.740 3_978 1307.51 D.364 2.136 10.944 3_997 1312.90 0.660 2.087 11.166 4.025 1320.51 1.D56 2.037 11.414 4.051 1330.41 1.562 1.987 }.1.682 4.1Q8 1392.72 2.193 1.938 11.974 4.155 1357.56 2.9b9 1.888 12.291 9.235 1375.08 3.897 1.839 12.634 4.319 1395.47 5.035 1.789 13.006 9.4i7 14i8.93 6.350 1.739 13.409 9_533 1445.69 7.939 1.690 13.646 9.b59 1A7b.03 9.833 1.640 19.321 9.827 1514.27 12.092 1.590 14.636 5.011 1548.74 14.799 1.541 15.397 5.224 159�.86 18.061 1.491 16.00B 5.973 164D.15 22.428 1.442 16.675 5.762 1694.11 26.909 1.392 17.404 6.099 1754.39 33.016 1.342 18.205 6.492 1821.74 39.450 1.302 18.923 6.865 1883.12 NQDE 808.4Q : HGL =< 299.345>;EGL= < 296.023>;FLQWLTNE= < 292.D60� *#i *#+�1�{ W �{*#**#**i�Y�f ** i� k Y� ** * *#**#f ***i # *# �; *! * *****YriF***YrYrk kYr * �lr ***YrYr# Yc Y� 1� i�Yr ir * FLOW PROCESS FROI�S NODB 848.4D TO I30DE 808.40 IS CODE = 8 --UPSTREAM NODE 806.4� ELEVATION = 292.46 (FLOW UNSEALS IN REACH} � ------------------------------------------------------------------------ CALCULATE CATCH BASIN ENTRANCE L055E5(LACFCD}; PIPE FLOW = 48.90 CFS PIPE DIAMETER = 30.00 INCI-4ES FE,OW VELOCITY = 10.40 FEETISEC. VELOCITY HEAD = 1.678 FEET CATCH BASIN EC�iERGY LOSS =.2*(VELOCIi'Y HEAD) _.2*( 1.678) = 0.336 �O�E 808.90 : HGL =< 296.359>;EG�- < 296.359>;FLOWLINE= < 292.460> *,..**.*x*�,.***.*�.x*.****.**.***,...x****.**�..*.,...*�«*.,�t�+**+***tt��*******,.* UPSTREAM PIPE FLOW CONTAdL DATA: NODE NUMBER = 8a8.9a FLOWLINE ELEVATION = 292.66 ASSUMED UPSTREAM CONTROL HGL = 294.35 FOR DOWNS�'RF.AM AUN ANALY5I5 END OF GRADUAE,LY VARIED FLOW AI�IAiYSIS � � * * * * * * * * * t t t * + * * k * * * * * * * * * * * * * * * i * # * * * W * # * # } * * � w * * * * * * * ! + t * * * * i + Y t � * i f f * + + t * * * PIPE-FLOW HYDRAULICS COMPUTER PROGRAI� PACKAG� {Reference: LACFCD,LACRIJ, AND OCEMA HYDRAi3LIC5 CRITERION) {ci Copyright 1982-2002 Advanced Engineering 5oftware {aesl Ver. 8.0 Release Date: O1/O1/2002 License ED 1509 Anaiysis prepared by: PROJEC`F` DESIGN CONSUL'PAN'PS 741 'H' STItEET, SiiITE 800 SAN DIEGO, CA 921D1 619-235-6471 **+w***+*++**t*+**++rt***** DESCRIPTION OF' STUi?Y w**,t*�***«*******:****t*** * BRESSI RADFCfi - ULTIMATE COND�'i'IONS * * 5Y5TEN5 800 - EL CAMxNO AEAL A'I` GATEWAX ROAD - LAT. 1 PER SHEE?` 3 * " �40-YEAR STORM EVENT * *W�****w,t+*********«***w*********************+*****+**>sWw*�r+**�v�v�*��rw FILE NAf�7E: L800-1.DAT TIME/DATE OF STUDY: 14:47 02/13/2063 t***+++**+f+***f***,r,+*,t***v�*�*********,tw*w,t*v��,�**,ra*«*«�********t****t:+f**** GRAD[7ALiY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POINT STATi3S �'ABLE (Note: •*" indicates nodal point data used.) UPSTREP.M i3UN DQWNSTR�AM RUN NODE MOBEL PRESSURE PRESSURE+ FLOW PRESSURE+ NUMBER PROCESS HEAL) ( FT j MOMEN'rLTDS ( P013NDS ) DEPTH ( FT ) MOMENTUM { ppTJND$ } �� 822.00- 4.45* 412.83 0.28 39.59 } FRICTION B22.90-- 3.39* 296.13 0.55 Dc 22.94 } CATCH BASIN 622.90- 3.42* 294.2a Q.55 Dc 8.27 MAXIML7M NUMBER OF ENBRGY BP,T�ANCES USED IN EACH PROF�LE = 25 ------------------------------------------------------------------------------ NOTE: S'I'EADY FLOW HYDRAi]LIC HEAD-LOSS COMPUTATIONS BASED ON THE MQS�` COATSEFtVA'�`IVE FORMiJLAE FROM THE CURRE[QT LACKD, LACFCB, AND OCFMA D�SIGN MANUALS. ****+�*,r*****.,.*******+*�**+**��t,..*r+**+*t*+++.r�**��*,r�*****x***********�*�* DOWNSTREAM PIPE FLOW COId'I'ROL DATA: NODE NUMBER = 822.00 �'LOWLINE ELEVATTON � 287.85 PIPE FLOW = 2. 10 CFS PIPE i�iANSETER = 18 , 00 INCHES AS5lJ2+iED DOWidSTREAM CON'I'ROL HGI, = 292.3Q0 FEET ------------------------------------------------------------------------------ NODE 822.00 : HGL =< 292.300�;EGL= < 292.322>;FLOWLIi�FE= < 287.850> ******,r**+,r,r++***+***,r****+*f+***�*****ftt****��**+,r*w,rw*ww,r,t**,r*+�*,r*+w*wrft* Fi,OW PROCESS FROM NODE 822.D0 TO NODE 822.90 IS CODE = 1 UPSTREAM NOBE 822.90 ELEVATIQN = 288.g1 (FT10W IS LiNDER PRESSURE} ------------------------------------------------------------------------------ CA�CULATE FRTCTxON LOSSES(LACFCD): PTPE FLOW = 2.10 CF5 PIPE DIAMETER = 18.00 INCHES PIPE LENG�H = 4.24 FEET 2+3ANNING'S N= 0.01300 SF=(Q/K)**2 = ({ 2.1D)/( 105.547J}+*2 = p.00040 HF=�*5F = ( 4.241*(D.00a44) = 0.002 • NOD� 822.9D : HGL =< 292.342>;EGL= < 292.324>;FLQWLINE= < 2$8.910> � ftet+t**t+***t+��**��**�+wtw**�*�*��***w*w**wW�+*f��+***+*x***++******x++*+*** FLOW PROCESS FROM NOD� 822.90 TO NODE 822.9Q iS CODE = 8 UPST�AM NODE 822.4D ELEVATION = 288.9� {FLOW IS UNllER PRESSURE) CAI,CULAT$ CA'I'CH BASiN E3JTRANCE LOSSES (L:ACFCD) : PIPE FLOW = 2.1D CFS PYPE �3�AME'FEFt = 1B.Op TNCHES FLOW VELOCITY = �.19 FEE'3'/S�C. VELOCI`d`Y HEAp = 0.022 FEET CATCIi BASIN ENERGY LOSS =.2*(VELOCITY HEAL�) _.2*{ 0.022) = 0.004 --------------------------------------------------------------------------_--_-- NOD£ 822.90 : HGL =< 292.328>;EGL= � 292.328>;FLOWLINE= < 28B.910> *****�*******+�**+**********************,r***�********t*++***rrr***ww*v.*w,r*rf*** UPSTREAM PFPE FLOW CONTROL �ATA: NODE NUM$ER = 822.90 FLOWLINE ELEVA7`I4N = 288.91 A$SUMED UPSTREAM CONTROL HGL = 269.45 FQR DOWNSTREAM RUN ANALYSIS END OF GRP.DUAi�LY VARIED FLOW ANALYSIS � • � * * * * * * * * * * * * # * * * * * f * # * f * * # t t * t # i * * * * * t # t * * # * * t * # # * # t f # w # w f w W w * * * * * * # i * * * i * W 4 � t PIPE--FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRD, AND OCENIP� HYDRAULICS CRITERIOi3) (c) Copyright 1982-2Q02 Advanced Engineering Software faes} Ver. 8.Q Release 1]ate: 01/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGI3 CONSULTANTS 701 'B' STREET, SUITE 600 SAN DIEGO, CA 92101 619-235-6471 ***v.+*�*+**�***�a*ww«*,r**• BESCRIPTIOT3 OF STEIDY r*s*++++r++****ww*++****** * BR�SSI RANCH - ULTIMATE CONDITIONS * * SYSTEM SQQ - EL CAMINO REAL AT GATEWAY ROAD. LAT. 2 PER SHEET 3 * * * ***++++*****+*+*rt**wv.w,tv.*�,�*w*+rwtw�*w*,r*r�*wwv.*******,*�****�*+,r*,r******* FILE NAME: L800-2.DAT TIME/DATE OF STUAY: 14:49 a2/13/2003 *****,r********,r**,r***************++*+++++**+****,r**t*s+*+x*wwxww*rww*�wwwW>*w# GRADUALLY VARFED FLOW A�}ALYSIS FOR PIPE SYS'TE2+9 NQDAL POIAI'I' STATi}5 TABLE (Note. "*" indicates nodal point data used.l UPSTREAM RiR+� DOWNS7'REAM Ri3DI NODE NiODEL PRESSURE PRESSi_FRE+ Fi,OW PRESSUR£+ NUMBER PROCESS HEAD ( FT J MOMEi�PI'UM ( POiJNDS } DEPTH ( FT J MOMENTUM { ppLTNDS ) �� 823.00- 4.46* 413.94 0.21 57.93 } FRICTION 823.10- 1.89* 130.5� 0.55 Dc 22.94 } CATCH BASTi� 823.10- 1.92* 128.61 0.55 Dc 8.27 ------------------------------------------------------------------------------ MAX�MLTM AFi3MBER OF E33ERGY HP.LANCES USED I�I EACH PROFILE = 25 -------------------------------------------------------------------------------- NOTE: STF�iDY FLOW HYDRAULIC HEAD-LOSS COMPiT�'ATIONS SP.SED ON THE N505T CONSERVATIVE FORMUL.�E FROM THE CURREN'I' LACRD, L,ACFCD, AND OCEI�iP, DESICN M.�NCTALS . t�rv.wrs**��r,ry��sy��,ry�**+**+***r++************«x***+x+****,r**a*rt+t**fttt++*r****+ DdWNSTRE.�M PIPE FLOW CONTROL DA'i'A: I3pDE NUMBER = 823.D0 FLOWLiNE ELEVATIOI3 = 288.14 PIPE FLOW = 2.�d CF5 PIPE DIAMETER = 18.Ofl II3CHES ASSUMEA F?OWNSi`REAM CONTROL HGL = 292.500 FEET -----------------------------------------------------------____________--__----- NODE 823.00 : HGL =< 292.600>;EGL= < 292.b22�;F'LOWLINE= < 2$8.140> *+�*t+*+***r*+x+,..��.**v.+,r�***��+*******,r*.**�**+****�x****+.*+******.*,.�*+�*+* FLpW PROCESS �'FtOM NODE 623.00 'i`0 NODE 823.10 IS CODE = 1 UPSTREAM NODE 823.10 ELEVATION = 290.71 (FLdW IS UNDER PRESSUREf ------------------------------------------------------------T___---_----------- CALC[FLATE FRICTION LOSSES{�CFCD]: PEPE FLOW = 2.10 CFS PIPE prAMETER = 18.00 INCHES PIPE LENGTH = 10.27 FEET i�7ANf�iIDiG'S N - O.00QOQ SF=fQ/x}**2 - (( 2.lOj/{ 212.816}}**2 = O.fl0410 HF=L*SF = ( 10.27}*(p.000101 = 0.001 � NdDE 823.30 : HGL =< 292.600>;EGL= < 292.622>;FLOWLINE= < 29fl.710> � * * * * W # w * # * * * * * * * * * * # * * * t * t t * * * # * * i i # # * i t t * * * * * t * * i L Y w * w * * * * * * * * * * * * * * * * * * * � * * # FLOW PROCESS FRpM NODE $23.14 TO NODE 823.1Q IS CODE = 8 UPSTREAM NODE 823.10 ELEVATION = 290.71 {FLOW IS UNDER PRESSURE) ------------------------------------------------------------------------------ CALCULATE CATCH SASIN ENZ'RP.NCE LC?SSES(LACFCDj: PIPE FLOW = 2.10 CFS PIPE DIAMETER = 1$.00 INCHES FLOW VEi,OCITY = 1.19 FEE'I`/SEC. VELOCITY HEAD = 0.022 FEET CATCH SASIN EI�ERGY IASS =.2*(VELOCITY HEADa =•2*( 0.022) = 0.004 -----------------___----------------------------------------______________---___ NODE 823.10 : HGL =< 292.626>;EGL= � 292.626>;FLOWL�NE= < 290.73Q> *+f***+�***t+t«��+,�.,�**+***************************+*,.*�*�**�***«**�,��***>*�*� UPSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = $23.10 FLOWLINE ELEVATIO�I = 290.71 ASSUMED UPSTREAM CONTROL HGL = 291.26 FOR DOWIQSTFtE,AM RUN ANAi,YSiS ------------------------------------------------------------___---------------- ---------------------------__--------------___--____—__----------------------------- EAID OF GRAf�UALLY VARI�D FI.OW ANALYSIS s �: ! APPENDIX 4.1.7 SYSTEM 2000 {jF' STREET, PA-5) s � . # � * * Y Y i Y t W 1 ! * f � + f * * x * * f f fi * * * * * * f i * * * f i � + + � t + + i � Y + rt Y f + M * # * ? r # * 1 * k f f * Y � } * * * * * f + + PIPE-FLOW HYDAAULICS COMPUTER PROGRAM PACKAGE {Reference: i�ACFCD,I�ACRD, AND OCEMA HYDRAi7LICS CRITERYQN] ;c) Copyx-ight 1982-2042 Advanced Engineering Software (aes) Ver. 8.4 Re�ease Date: 01/01/2b02 License ID 1509 Analysis prepared by: PR0.7ECT DESIGN CONSULTAN£S 701 'B' STAEET, SUITE B04 SAN DIEGO, CA 92101 619-235-6471 *+***w«***�*,r****f**s****+ DESCRIPTIOA3 OF STUDY x*****�****t+*+ts++++*iit� * BRESSI RANCH - ULTIMATE CONDITIONS * * SYSTEM 2040 - GATEWAY CENTER COURT {pA-5} • * 100-YEAR (1 * v.v.*+*w*��r**#w�r*�*************�++�*,r�*�,�w*r*:i***s�v.�r+*+�a**********,r***�+* FI�.E NAM.E: P2aD0.DAT TIME/DATE OF STUDY: 17:�3 Q1/16/2Q03 ******************+****+*�*******+*****,.�++»*,.�*�*******+*+tt++t***+*��,.t*+*« GRADUAi,LY VARIED FLOW ANALYSIS FOA PIPE 5Y5TEM NODAF, POINT STATUS TABLE (Note: •w" in�icates nodal point data used.} DPS'T'4ZEPM RUN DOWNSTREAM AUN P}ODE MODEL PRESSURE PRESSURE+ PLpW PRESSURE+ NCFIySBER PROCESS HEAD(FT) MOMENTUM(POUNDS} DEPTH(FT) MOMENTi7M(POUNDS? • 2000.00- 6.65* 5191.79 1.97 4382.63 } FRICTION 2000.20- 5_79* 4762.00 2.04 4257.49 } FRICTION+BEI3U 2000.5fl- 4.73� 4294.03 2.25 3923.13 } FRICTION 2040.60- 3.76* 3867.79 2.b7 357�.28 } ,7UNCTION 20Qa_60- 3.97* 3883.16 2_49 3593_92 } FRICTION 244I.00- 3.62* 3724.SZ 2.90 Dc 3439.34 ) JUNCTION 2Q01.94- 6.63* 2894.93 1.25 1698.65 ) FAICTION _ • 2001.91- 5.37* 2339.05 �.23 1730.25 } FRICTION-rBEND ) HYDRAULIC 3UMP 2002.00- 2.2b Dc 1142.47 1.91* 1492.37 } F'RTCTTON 2003�.00- 2.26 Dc 1142.47 1.58� 1393.40 } M.�,i@7�i0F.E 2003.90- 2.26 Dc 1�92.47 1.66* 1292.25 } FRICTION 20Q5.00- 2.26 Dc ZZ42.47 1.73� 1251.$3 ) ,IUNCTION 2405.90- 2.19 Dc 1043.58 1.58* �393.12 ] FRICTION+BEND 2006.00- 2.16 Dc 1043.58 1.49* 1256.06 ) FRICT�ON 2010.00- 2.18 Dc 1043.58 1.93* 13Q5.11 : } ,717NCTIpN 2010.90- 2.23 Dc 1147.99 1.85* 1204_56 • } FRICTION 2011.00- 2.22 Dc 1147.99 1.86* 1241.98 } FRICTIQNtBEND 2a15.D0- 2.22*Dc 1147.99 2.22*Dc 1147.99 } JUNCTION 2015.Ofl- 2.51* 1153.52 1.91 1151.76 } FRICTI4N+BEN'D 2016.00- 2.57* 1171.73 1.87 1151.33 } FRICTION ) HYDRAULiC JL7MP 2017.00- 2.21 Dc 11�7.25 1.76" 1198.19 } MANHOLE 2017.10- 2.21 Dc 1117.25 1.95` i142.30 } FRICTION 2020.00- 2.21*Dc 1117.25 2.21*Dc 11�.7.25 } CATCH BASTN 2420.00- 3.93* 824.66 2.21 Dc 296.29 ------------------------------------------------------------------------------ MAXIMUM NUMBER OF ENERGY BALANCES USEI? IN EACH PROFILE = 25 ' NOTE: STEADY FLOW HYDRAUL�C HEAD-L055 COMPUTATIONS BASED 023 THE MQST CONSERVATIVE FORMULAE FROM TiiE CURREN� LACRD,LACFCD, AND OCEMA DESIGN N3ANiJALS . *�h #*'F *f'M'ktttt'k%i# i tk1� * i�'k *'hY�1t1tY.1N�1t*'t 1 Y 4**t # fYr***�FYrYi yrtkYrlr�k* YrYr*Yr**�r'k****i k�k *l��k 1�'Yr'I� *!* DOWNSTRE71.t+] PIPB FLOW CONTROL I7ATA: NODE fiC7MBER = 2 D Q 0. 0 D FLOWLINE ELEVATIOAI = 3 8 3. 2 5 PIPE FLOW = 102.32 CFS PTPE DIAMETER = 36.00 INCHES ASStJMED DOWIVSTREAM CONTROL HGL = 389.90d FEET --------------------------------------------�___----_-______--_---___------------- NODE 2000.00 : HGL =� 389.904>;EGL= < 393.154>;FLOWi,INE= � 383.25fl> • **.*tti+��*�*��t....*...*...�...�*�+x+.***.*�*,.*...,.rt,..x,,...*.******.+***.****� FLOW PROCESS FRQM NpDE 2400.a0 TO NODE 2000.2Q IS CODE = 1 UPS'T'REAM 130D8 2400.20 EL�VATION = 384.85 (FLOW IS UNDEit PRESSURE� --------------------------------------__-_------------------------------------- CALC[JL�ATE FRFCTION LOS5E5 ( LACFC!}? : PIPE FLOW - 102 . 32 CFS PIPE i}IAMETEFt = 36 . d0 INCI-3ES PiPE LF�IGTH = 31 . 40 FEET MP.NNII3G' S�I = 0. 013D0 SF=iQ/K} "2 = ;( 102.32)/( 666.987??**2 = 0.02353 HF=L*SF = { 31.401*(O.D23531 = 0.739 N4DE 20D0.2a : HGL =< 390.639>;EGL= � 393.893>;FL(3WiINE= < 384.850> ***.��*f*++++*�*�+t�*++.�*��+.tw.�..,��*.�.**�*+*****��**+*t**�t*****+.*.*�.��* FLOW PROCESS FROM NODE 2000.2a TO NpDE 2000.50 IS CODE = 3 UPSTREAM NOD� 2000.50 ELEVATZON = 387.65 (FLC?W I5 UNDEFt PRESSURE} ------------------------------------------------------------------------------- CALCULATE PIPE-BE[3D LOSSESfOCEi�IA) : PIPE FLOW = 102.32 CFS PIPE �IAl4$TER = 36.00 INCHE$ CENTRAL ANGLE = 26.330 i�EGREES MPNNING'S N= 0.01300 PIPE LENGTH = 55.20 FEET BF�iD COEFF�CIENT(KB} = 0,13522 FLOW VELOCTTY = 14.98 FEET/SEC. VELOCITY HEAD = 3.254 FEET HB=KB*(VELOCITY HF.Ai}) _( 0.135)*( 3.254) = 0.990 SF=(Q/K)*•2 = {� �42.32)/{ 666.986)1�*2 = 0•Q2353 HF=L*SF = f 55.20)*(0.02353} = 1.299 TOTAL HEAD LOSSES = HB + HF =( 0.440�+( 3.299) = 1.739 NODE 200�.5a : HGL =< 392.378>,EGL= < 395_632>;FLOWL�NE= < 3$7.650> •�Jryr�YY! * f i�k 1� k# f**##******#***Yr*** k k k k i� Y� iF **## f*}}# # i}#}yri f� J*f i t*�{ #i i�lyr**�klik4 t t � FLOW PftOCESS FROM NODE 2000.50 TO NO�E 2000_64 IS CODE = 1 UPSTAEAM NODE 2000.60 ELEVATION = 389.49 (FLOW IS UNDER PRESSL7RE) ------------------------------------------------------------------------------ CALCULATE FR�CTION L055ESiLACFC�): � PIPE FLOW = 1d2.32 C�S P�PE DIAMETER = 36.00 INCHES PTPE LENGTH = 35.OQ FEET MANNING'S N- 0.41300 SF=(Q/K)*'2 = f( 102.321/( b66.9B8}j�*2 = O.D2353 HF=L*SF = ( 35.QOj*(0.42353) = 4.824 ------------------------------------------------------------------------------ NODE 2000.60 : HGL =< 393.202>;EGL= < 39fi.455>;F'LOWLINE= � 389.444> * k * 1 * Y w f 1 1 1 f t ! w � i t # * # f t # # * * t A * # } * # * # � f � ti i + M w # � # � # # * * # * * * # * * * * w * f * w * 1 * # * k + + f � * f F�OW pROCESS FROM NODE 2QOO.bO TO NODE 2004.60 IS CODE = 5 UPSTREAM NODE 20DQ.60 ELEVATIQN = 389.44 (FLOW IS LlNUER PRESSURE? ' ------------------------------------------------------------------------------ CALCULATE JUNCTION F,pSSES: PIPE FLOW bIAME�'ER A�IGLE FLOWL,INE CRITICRL VELOCIZ`Y (CFS) (INCHES) (DEGREESj ELEVATION DEPTH(FT.j (FT/5EC} UPSTREAM ZdQ.93 36.D4 0.46 389.44 2.90 14.279 DOWNSTREAM �02.32 36.04 - 369.44 2.90 14.975 71ATERAL #1 1.39 18.OQ 90.00 390.20 0.49 0.787 TIATERAL �k2 O.DO a.OQ O.U4 0.00 0.00 o.aao Q5 0.00===Q5 EQUAiS BASIN INPUT=== LACFCD AND OCEMA E'FAW JUNCTION FOT23�7ULAE USEB: DY={Q2*V2-Q1*V1*COS(DELTAI)-¢3*V3*COSf�E�TA3j- Q4*V9*COS(DELTA4jj/I(A1+A2)*16.1}�+F}ZICTIOI�i L05SES UPSTREAM: MANNING'S N= D.Q1300; FRICTEQN SLOPE = 0.0229Q DOWNS�REAM: MANNING'S N= 0.01300; FRICTION SLOPE = 4.02353 AVERAGED FRIC'PiON SLOPE Ii�7 JUNCTION ASSUMED IaS 4.02321 J�JNCTIQN iENG'i'H = 1.50 FEET FRICTION LASSES = fl.035 FEE'P ENTRANCE I,OSSES = O.OQp FEET • JUNCTION LOSSES = (DY+�-TV1--HV2}+(E13TRANCE L059ES} JUNCTIQN LOSSES =( 0.1231�( 0.000} = 0.123 ___---------------------------------------------------------------------------- NODE 2000.64 : HGL =< 393.412>;EGL= < 396.578>;�'LOWLI23E= � 389.440> 1r'kk tk'k'k1r'kYrYr*'M **�t**i *� �k ** f i� 4�k �k �k �k i4#*t1� tti t**# ***** * tt t**** t YrYttf t�Y�Y ff i i� **1r*it*t� FLOW PROCESS FROM NODE 2000.60 TO NODE 2D01.00 I5 CODE = 1 UPSTREI�t�f NODE 2001.00 ELEVATION = 390_07 (FLOW IS 1JN17�R PAESSURE) CALCCTL,.�TE FRICTTON LQSSES(LACFCD}: PIPE FLOW = ��4.93 CFS PZPE DIAMETER = 36.QQ INCHES PIPE LFNG'I'H = 12 . pQ FEET MANNING' S I3 = 0. 013 00 SF=(Q/K)�*2 = ({ 1.OQ.93?/f b55.9881)'*2 = 0.02290 HP=�*SF = f I2.001*Ia.a229D? = 0.275 ------------------------------------------------------------------------------ NODE 2001.00 : HGL =< 393.687>;EGL= < 395.853>;FLOWLINE= < 39Q.070> *t*tt*ikikYrik*** ** t t*tt**Yi i 1 i YYr**i! Y�! #YrYrYtk tYYiYrYr **Yrtt t Yr Y�k Yr#* Yl�f 1 Y Y1 f Y+4iki 1 Y Y 1�41* FLOW PROCESS FROFII30DE 2001.00 TO NODE 24Q1.90 I5 CODE = 5 UPSTRF.Ar3 i�iODE 2001.90 ELEI1ATIpN = 390.40 IFLpW IS UNbER PRESSURE) CALCULATE JUNCTTON LOSSES: PIPE FLOW DIAMETER ANGLE FLOWL�NE CRITICAL VELOCITY iCFS} {INCHES} (DEGREESJ ELEVATION DEPTH(FT.} (FT/SEC} UPSTREAM 4$.QO 36.00 d.00 394.40 2.26 6.791 DQWNSTREAI� �OD.90 36.00 - 39b.07 2_90 f4.274 LA'PERAI, #1 50.40 30.00 45.00 390.90 2.30 10.267 LATERAL �2 2 SO 18.00 90.00 391.90 0.60 1.415 Q5 0.00===Q5 EQUALS HASIN INPUT=== � T�ACFCD AND OCEMA FLOW JLTNCTIQN FOT�MUI.AE USED: (� DY=(42*V2-Q1*V1*COSIDELTAI)-Q3*V3*CbSIDELTA3)- Q4*V4*COS(DELTA4}}/{(A1+A2)*16.1)+FAICTION L05SES UPSTREAM: MANNTNG'S N w 4.01304; FRTCTION SLOPE = O.OQ5�8 DOWNST�EAM: MP.i�IING'S N= 0.6130Q; FRICTION SLOPS = 0.02288 AVERAGED FRICTION SLOPE IN JUNCTION ASSUI+FED AS 0.01403 JUNCTION LENGTH = 4.00 FE�T FRIC'I'ION LOSSES = 0.05b FEET ENTRANCE LOSSSS = 4.4Q0 FEET . JiJA3CTI0I3 LC35SES = ( DY+HV�-HV2 ) + ( ENTRANCE LOSSES ) 3UNCTIOI3 LOSSES = t 0.896J+( O.00b1 = 0.896 NODE 2001.90 : HGL =< 397.031>;EGL= < 397.747>;FLOWLINE= < 390.40D> *Yri Yt t tYr * t t ttt*1 tf Y Y f i Y i!li�i#�Y Y#i 3 Y#i y f*ti t#*f i Y444ti*�.## }# i�*�F#*Yr*YrYr**A i* i�+}� FLOW PROCESS FRQM NODE 2001.90 'i'0 NOBE 2401.91 IS COI�E = 1 UPSTREAM NO17E 2Q03..9� ELEVATIO� = 391.87 (FLOW IS UNDER PRE5Si3RE} ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSES(LACFCD}; PIPE FLOW - 98.00 CFS PIPE DIAMETER = 36_Od INCHES PIPE LFNGTH = 90.5b FEET MANNING'S t3 = 0.01300 SF=fQ/K}**2 - {{ 48.00)/f 666.992j}**Z = 0.00518 HF=L*5F = I 4Q.50)*(p.00518} = 0.210 NODE 2da1.9� : HGI1 =< 397.241>;EGL= < 397.957>;FLOWLiNE= < 391.B70> �*x�**t*�*��+**«.,...*�«..**.***+*.*.�,.***,.***,,*,.,.*..*�++*t*�t**++*++�*++*+��*�* FLOW PROCESS FROM NODE 2001.91 TO NODE 2002.00 I5 CODE = 3 UPSTREAM I30DE 2002.00 ELEVATIOid = 40D.27 (HYDRALILIC JTJfSP OCCUR$) -----------------------------------------------------------_------------------- CALCUL.�TE PIPE-BEND E,OSSESfOCEMA): PIPE FLOW = 48.00 CFS PEPE DIAMETER = 36.0� II3CHES � CENTRAL ANGLE = 34.500 AEGREES MANNING'S N= 0.01300 PIP� L�FGTx = 191.90 FEET ------------------------------------------------------------------------------ HYDRAULIC JlJN3P: DOWNSTRE.n.M RC7AI A�]ALYSIS RESUI,TS ------------------------------------------------------------------------------ NORMAL DEPTH(FT} - 1.21 CRITYCAL DEPTHfFTj = 2.2fi ------------------------------------------------------------------------------ LiPSTREAM CONTROL ASSUM�D FLOWDEPTH{FT} � 1.41 ------------------------------------------------------------------------------ GRADUALLY �IARI� FLOW PROFILE COMPUTED INFORMATION: ------------------------------------------------------------------------------ DISi'ANCE FROM FLC}W DEPTI-E VELOCITY SPECIFIC PRESSURE+ CONTROL(FT) (FT) (FT/5EC) ENERGY(F�`} MOMENTUM(POLTNDS} 0.000 1.4a7 14.742 4.789 1492.37 2.307 1.399 14.848 � 4.829 i500.63 4.742 1.391 14.955 4.866 15D9.04 7.317 1.364 15.063 4.909 1517.60 1fl.046 1.376 15_173 4.953 1526.32 12.943 1.368 15.285 4.998 1535.19 15.027 7..360 15.396 5.045 1544.22 39.31$ 1.353 15.513 5.092 1553.92 22.839 �.345 15.630 5.141 1562.78 26.620 1.337 15.748 5.191 1572.32 30.693 1.33d �5.868 5.242 1582.02 35.1OQ 1.322 35.990 5.294 1591.90 39.891 1.314 i6.119 5.348 160Z.96 45_127 1.306 16.239 5.904 1612.21 5�.887 1.299 16.367 5.4b1 1b22.64 57.271 1.291 ' 16.496 5.5�9 1533.26 � 59.412 1.2B3 16.527 5.579 ]fiAg.07 72.489 1.275 16.760 5.640 ib55.08 � � 81.753 1.268 15.896 5.703 1666.29 92.573 1.260 17.033 5.768 1677.71 ZQ5.539 1.252 17.172 5.B39 1689.34 12�.547 1.244 17.314 5.402 1701.1B 142.452 3.237 17.456 5.972 1713.24 172.261 3.229 17.604 6.094 1725.52 191.900 I.226 17.560 6.072 1730.25 ------------------------------------------------------------------------------ 1-iYDRAULIC Ji.R+1P: UPSTREAM RIFN ANALYSIS RESULTS --------__�___--_�_--------- DOWNSTREANi CONTROL ASSUMED PR�SSURE HEAD(FT) = 5.37 --------------------------- PAESSURE FLOW PROFILE CO�fPUTED II3FORMATION: DISTAriICE PROM PRESSURE VELQCI7'Y SPECIFIC PRESSURE+ CONTKOL ( F3' ) [iEAD ( FT ) ( F'F 1 SEC ) E13ERGY ( FT 1 MO[+SENTUM ( POUNDS 1 0.000 5.371 b.791 6.087 2339.05 63.0$0 3.D00 6.791 3.716 1293.27 ---------------------------- ASSUMED DOWNSTRF.AM PRESSURE HEADS�'T) = 3.00 ---------------------- GRADiJALLY VARIED FiAW PAOFILE COMPUTED IhIFORMATION: DISTANCE FRONi FLOW DEP'i'H VELOCITY SPEC�FEC PRESSUREt CON'I'ROL ( FT ) ( F'T } ( FT / SEC ) ENERGY { FT ) MOMF�ITLJM ( POUNDS ) b3.fl80 3.004 6.789 3.716 1293.27 63.787 2.970 b.840 3.689 �281.21 64_436 2.990 6.82i 3.663 1270.06 65.Q50 2.931 6.848 3.639 1259.53 65.639 2.$81 6.880 3.616 1249.53 . 66.192 2.851 6.916 3.594 1240.01 66.726 2.821 6.957 3.573 1230.95 67_238 2.792 7.fl01 3.553 1222.32 67.728 2.7b2 7.050 3.534 1214.12 68.196 2.732 7.101 3.516 1206.34 68.643 2.702 7.157 3.498 119B.98 69.068 2.673 7_215 3.4$2 1192_04 69.970 2.643 7.277 3.466 1185.52 69.85Z 2.613 7.343 3.451 i179.43 �a.zaa 2.583 7.412 3.437 1173.77 7Q.542 . 2.554 7.48A 3.424 1�58.54 70.857. 2.524 7.560 3.412 1�63.76 71_134 2.494 7.640 3.403 1159.43 71.391 2.A64 7.723 3.391 1155.57 71.619 2.435 7.810 3.382 1152.16 71.817 2.405 7.901 3.375 1149.27 71.9$9 2.375 7.995 3.366 1146.86 72.118 2.345 $.Q94 3.363 1144_96 72.216 2.315 8.197 3.359 I193.59 72.277 2.286 8.3D4 3.357 3192.75 72.298 2.256 8.4J.5 3.35b 1192.�17 291.900 2.256 8.415 3.35b 1i42.47 ------------------------END OF HYDRAULIC JUMP ANALYSIS-------------------------- I PRESSURE+MOMENT(JM BAI,ANCE OCCURS AT 37.45 FE�T' UPSTREAM OF NODE 2001.91 � DOWNSTR�',AM DEPi'H = 3.963 FEET, UPSTREAM CONJUGATE DEPTH = 1.234 FEET f NODE 2002.00 : HGL =< 4Q1.677�;EGL= < 405.fl54�;FLOWLINE= <� 400 274> J+ ***+*ttit**+*+*�+***�*++w*�*+**+******+****it�+w+i.w+i�*�*++x*�+****+*�*+*+t+t,�♦ : FLOW PROCESS FRO[y1I�ODE 2002.4Q TO NODE 20D3.OD SS CODE = 1 iiPSTREAM NODE 2003.00 ELEVATION = 4D2.66 (FLOW IS SUPERCRY'i3CAL} � --------------------------------------------------------------------�--------- CALCULATE FRICTION LOSSESILACFCD}: PIPE FLOW - 48.00 CFS PIPE DIAi�7ETER = 35.00 �NCHES PIPE LENGTH = 76.99 FEET MANNING'S N= 0.0130Q NORMAL DEPTH(FT} = 1.33 CRITICAL DEPTH(F`i') = 2.2b ------------------------------------------------------------------------------ UPSTR�AM CONTROL ASSiiM�A PLOWDEP'I'H(FT} = 1.58 GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: DISTANCE FROM FLOW DEPTH VELOCITY SPEC�FIC PRESSiFRE+ CONTROL { F";' } ( FT ) ( FT / SEC } ENERGY ( F"i' } MOMENTi1M I POUNDS ) 0.400 1.578 12.739 4.099 i343.4d 2.207 1.568 12.839 4.129 1350.42 4.548 1.558 12.941 9.160 1357.fi1 7.035 1.54& 13.099 9.192 2364.97 9.685 ]..538 13.149 4.225 1372.5J. 12.5i3 1.529 13.256 4.259 �380.22 15.535 1.519 13.365 4.299 Z388.22 18.775 1.549 13.475 4.330 �396.20 22.258 1.499 13.587 4.3b8 Z404.4$ 26.6I3 �.489 13.701 4.406 Z412.94 3Q.077 1.479 13.8i$ 9.446 1421.b0 34.491 1.970 13.936 9.487 1430.47 39.3�0 i.h60 14.056 9.�29 1439.54 44.599 3.450 14.�78 9.$73 1448.81 50.439 �.440 14.302 4.6i8 i456.3� 56.938 I.430 14.928 9.565 �468.Q2 64.234 3.421 14.557 9.713 1477.96 . 72.518 1.411 14.688 9.763 I4$8.12 76.440 i.407 14.742 9.7$9 �492.37 ------------------------�T_--------------------------------------------------- NODE 2003.OQ : HGL =< 404.238�;�GL= < 90fi.759?;FLOWLTNE= < 402.fi6d> ******** *i� *****Yr***Yr�1rYr�Flr k1r**Yrri Y� Yr#�YrYri� k �k*1ri# *i� *i1r ****Yr * *** ** *-!r*W �M Ycrt Yr iF ***k ****i�# # FLOW PROCESS FROM NQDE 2003.00 TO NODE 2443_90 IS CODE = 2 LiPSTREAM NODE 2003.94 ELEVATION = 4Q2.99 (FLOW F5 SUPERCf2ITICAL) ------------------------------------------------------------------------------ CALCU7IATE MANHOLE LOS5E5(LACFCD): PIPE FLOW = 46.00 CF5 PIPE DIAMETER = 36.00 INCHES AVERAGED VELOCITY HEAD = 2.37b FEET HMN =.45*iAVERAGED VELOCTTY HEAD? _.05*{ 2.376i = 0.119 NODE 2Q03.90 : HGL =< 409.647>,EGL- < 406.878>;FLpWLTi�1E= < 402.990> ****+*��*****++*�,r****�*.**.*.«**.+***.*+*�+�.*+�*+++*++****..****.**t�.++*W� FLOW PROC�SS FROM NODE 2043.90 TO NODE 2005.OD IS CODS =� UPSTREAM NO]}E 2005.00 ELEVATION = 407.21 (FLOW IS SUPERCRITICALf ------------------------------------------------------------------------------ CALCi7L,ATE FRIC'I'�ON LOSSES {�,pCFCD) : PIPE FLOW = 98.OQ CFS PIPE DIAMETER = 36.00 INCI-EES PIPE LENGTH = 281.70 FEET MANNING'S N= 0.0130a ------_------------------------------------------------------------------------ NORMP.L DEPTH ( FT )= 1. 6 5 CRI'I'ICAL DEP`i'H { FT )= 2. 2 6 UPS'i'REAM CONTROL ASSUMED FLpWi�EPTH (FT) = 1.73 ------------------------------------------------------------------------------ GFtADUALLY VARIED FLOW PROFILE COMQUTED IiVFORMATION: ------------------------------------------------------------------------------- � DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ � CONTROL { F'i` } ( FT ) { FT / SEC ) EPiERGY ( FT } MOMENTUi�] ( POl3�iD5 ) O.00Q 1.734 11.335 3.730 1251_83 2.8D7 1.731 � 11.361 3.736 1253.36 5.754 1.728 11.386 3.792 1254.69 $.85I 1.724 11.912 3.748 1256.44 32.1�9 3.721 11.938 3.759 1256.01 15.559 i.71$ 11.464 3.760 1259.59 39.209 1.715 11.490 3.7Gb 1261.18 23.071 1.712 11.516 3.772 1262.78 27.185 3.7D8 11.542 3.778 1264.4� 31.577 �.7D5 11.569 3.785 1266.03 36.282 1.702 11.596 3.791 1267.68 41.344 i.694 11.622 3.797 1269.34 46.816 1.696 11.649 3.804 1271.01 52.762 1.692 11.676 3.8�1 ].272.74 59.267 1.689 11.703 3.8�7 J.274.40 66.437 1.686 11.730 3.824 1276.12 74.412 1.683 11.758 3.831 1277.$5 83.382 1.68fl 1�.785 3.838 1279.54 ' 93.614 1.676 �1.813 • 3.845 1281.36 J.05.496 1.673 Z�.8Q1 3.852 1283.34 119.64D 1.670 II.869 3.859 1284.93 137.053 1.667 Z�.697 3.$66 1286.73 154.638 1.669 11.925 3.873 1288.55 191.668 1.66Q i1.953 3.88Q 129fl.39 246.$49 1.657 11.962 3.888 1292.24 281.700 1.657 11.962 3.888 1292.25 NO]]E 2005.Op : HGL =< 408.944>;EGL= < 410.940�;FLOWLINE= < 407.210> . ��.**+*****+*****%..��*+t*�t*t*++*��...*+�********.*t+*..,�..*.�*.*t>+�*�.��**.* FIAW PRDCESS FROM NODE 2005.00 TO NODE 2005.90 IS CODE = 5 UPS�'AF�M NQDE 2005.9fl ELEVATION = 407.54 (FLOW IS SUPERCRiTICAL) CAi�CULATE JLTNC'i`ION LOSSES _ PIPE FLOW l3�Ai�1ETER ANGT,E FLpWI,Ii�IE C32ITICAL VELOCITY {CFS) {INCHES) (DEGREES} ELEVATION DEPTH(FT.) (FT/SECi UPSTREP.M 99.92 36.D4 0.00 4fl7.54 2.1$ 11.876 DOWNSTRF.ANS 48.00 36.04 - 4fl7.21 2.26 11.339 LATERAL #1 I.56 18.40 90.00 408.29 0.47 1.786 LATERAL #2 1.52 18.00 90.Ofl 408.29 0.4fi 1.740 Q5 0.00===Q5 EQUALS SASIN INPUT=== LACFCD AND OCEMA FLOW ,TTJNC'1'ION FORMULAE CJSED: Dy={Qz*V2-Q1*V1*C05(DELTAI}-¢3+Z73*COSIDEL`FA3)-- Q4*V4*COSfDELTA4)j/((A1+A2)*36.1f+FR�CTTON i3OSS�5 UPS�`REAM: MAN'NTNG'S N= 0.013Q0; FRICTION SLOP� = 0.01515 DpWNSTREAM: MANNTNG'S N= D.013E}D; FRICTION SLAPE = D.OZ289 AV�F�AGED FRTCTTON SLOPE IN �UNC?'ION ASSUMED A5 0.01402 3UNCTION �,ENGTIi = 4.00 FEET FRICTION LOSSES = 0.056 FEET ENTR�33CE LOSSES = 0.000 FBE�' J[iNCTIOl�7 LOSSES = {DYtHVI-HV2}+(ENTRANCE LOSSES� JiTNCTION L055E5 =; 0.373)+( O.pDO} = 0.373 ----------....�----------------------------------------------------------------- NO�?E 2005.90 : HG� _< 409.Z23>;EGL= < 9�1.313>;FLOWi,INE= < 9a7.540> ...**.****+��.*t*�..++�+��+�+.*+.�t*�+*.�,�t..�,+.*t��t,�+«.�w****,,*****�***,,�**+ FLOW PROCESS FROM d30DE 200S.9D TO NODE 20Q6.da IS C4DE = 3 . UPSTitEAM NODE 2006.00 ELEVA'�ION = 411.29 (FL�W IS SUPERCRITICAL} � --------------------------------------------------------------------------- CALCULATE PIPE-BEND L05SES(OCEMAJ: � PIPE FLOW = 44.92 CFS PIPE DIAT3ETER = 3fi.00 INCHES CENTRRL ANGLE = 11.840 DEGREES MANN�NG'S N= 0.01300 PIPE LFNGTH = 250.11 FEET NORMP.L DEPTK(FT) = 1.59 CRITiCAL DEPTHIFT} = 2.�8 ------_____�------------------------------------------------------------------ ------------------------------------------------------------------------------ LTPS�'REAM CON'PROL ASSUMEI7 PLOWDEPTH (F'T) = 1.49 GAADUALLY VARIED FLOW PROFILE CO[�fPU�ED IIdF'Oi2MATIpA3: • DISTANCE FROM FLOW AEPTI-4 VELOCITY SPECIFIC PRESSURE+ CONTROi ( FT ) . { F"i` ) ( FT / SEC ) EI3ERGY ( FT } MOMFN3'[JM { pp�DS ) 0.000 1.487 12.845 4.051 1255.08 3.775 3.991 12.800 4.037 1253.11 7.6B4 3.995 12.757 4.024 125Q.17 11.740 3.999 12.713 4.011 1297.26 15.957 1.543 12.670 3.997 1294.38 20.349 1.507 12.627 3.985 1241.53 24.935 1.511 12.584 3.972 1238.71 29.736 1.515 Z2.542 3.959 1235.91 34.777 �.519 12.500 3.9�17 1233.15 40.086 i.523 12.458 3.935 123D.41 45.700 1.527 12.416 3.923 1227.69 51.b59 �.532 12.375 3.911 1225.01 58.Qi5 1.536 �2.334 3.899 1222.35 5Q.832 1.540 12.293 3.888 1219.72 72.19� 1.549 12.253 3.876 1217.12 $0.192 1.548 12.213 3.865 1214.59 88.975 1.552 12.173 3.854 �2].].99 � 98.723 1.555 12.133 3.843 1209.45 1Q9.695 1.550 12.099 3.832 1206.96 122.269 1.554 12.054 3.821 1204.99 137.033 1.56$ 12.ai6 3.811 1202.44 154.969 1.572 11.977 3.801 1199.62 177.923 1.5'76 11.939 3.79D 1197.22 210.037 1.580 11.9Q1 3_760 1194.85 250.110 1.583 11.873 3.773 1193.12 NODE 2006.D0 : HGL =< 412.777>;EGL= < 415.341>;FLOWLIiVE= < 411.29D> ++}�F�F1 *rt ti i Y�* Y 4�k4i ***# i� * Y* i! iFYr*****# # i**iY i� i1 ir **Y� iFY�iFf ** *}Y� YrfYrYr�k*'kt'M �** � ir ***iF*�*# * FLOW PROCESS FROM NODE 2406.00 TO NOD� 2010.00 IS CODE = 1 UPSTREAM NQDE 20�p.00 ELEVA'i'ION = 41,1.97 (FLOW IS SE3PERCRITZCAL� -------------------------------------------------------------------------------- CAI,CUi.�ATE FRICTION LOSSES (LACFCDj : PIPE F�,OW = 49.92 CFS PIPE DIAi�SETER = 36.00 INCHES PIPE LENGTH = 45.58 FEET MANidING'S N= 0.01300 NOR2�7Ai� DEPTH(FTj = 1.59 CRITICAL DEP'PH(FT) = 2.18 ------�----------------------------------------------------------------------- UPSTRE.�M CONTROL ASSUMED FLOWDEP'I'H(FF) = 1.43 GRADUALLY VARIED FLOW PROFILE COl�fPUPED INFORMATION: DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ C�NTROL(FT) {FT) (FT/SEC) ENERGY(FT} t402�F�ITUMIP0UND5) 0.000 1.426 13.557 4.282 1305.11 • 4.170 1.433 13.477 4.255 1299.50 B.474 1.434 13.398 4.228 1293.97 • 12.922 1.446 13.320 4.202 128$.54 17.530 1.AS2 13_292 9_177 1283.19 � 22.313 1.454 13.166 4.�52 1277_92 27.288 1.465 13.090 4.I28 �272.74 32.478 1.472 13.016 4.104 1267.54 37.9a6 1.474 12.942 4.081 1262.62 93.64f 1.485 12.669 9.058 1257.b9 95.58Q 1.467 12.645 4.45] 1256.D8 NODE 2Q10.40 : HG� =< 413.396>;EGL= < 415.252>;FLOWLINE� � 411.970> *****�*�t+t��«��w+�+��*��*�.**��w**�*�*�*�****..**+�*+�***>*.*�*** « **+*** FLOW PROCESS FROM NODE 2010.00 TO NpDE 201D.9D IS CODE = 5 UPSTRF�IM NQDE 2Q10.9� ELEVRTION = �12.47 {PLQW IS SUPERCRITICAL} ------------------------------------------------------------------------------ CALCUi�ATE JTJNCTIQN LOSSES: P�PE FLOW DIA3�fETER ANGLE FLOWI.INE CRI'i`ICAi� VELDCITY {CFS) {��7CHES) (DEGREESj ELEVATION DEPTHSFT.} (FT/SECj UPSTREAM 44.92 30.00 a.oa 412.47 2.22 11.531 DQWNSTREAM 44.92 36.00 - 411.97 2.18 13.561 LATER.AL �1 4.00 0.00 Q.04 D.DO 0.44 O.OflO LATERAL �2 0.00 0.00 0.4Q 0.00 O.DD O.Ofla Q5 6.OD===Q5 EQUALS BASiN INPUT=== LACFCF AND OC�.MA FLpW JUNCTION FOFZMULAE USED: DY=(Q2*V2-Q1*V1*COS(DELTA3)-Q3*V3*COS{DELTA3}- Q4*V4*COS(DEI.�TA4jj/((A1+A2)*1b.1)+FRTCTI�N LOS5E5 UPSTAEAM: MANNING'S N= 0.0].3�4; FRTC'I'TON SLOPE = 4.01488 DOWNSTREAM: MANNING'S N= 0.0130D; �'A�CTI03�I SLOPE � 4.02158 AVERAGED FRICTI4N SLOPE YN JUNCTION ASSUMED AS D.01823 ,7UNCTION LENGTH = 4.00 FEET � FRTCTION LOSSES = 0.073 FEET EN�RA23CE LOSSES = O.D00 FEET , J4JNCTTON LOSSES = {DY+HV3-HV2i+(ENTftANCE LOSSESi JUNCTI�N LOSSES ={ 0.133)+{ D.00Q1 = Q.133 NODE 201D.94 : HGL =< 914.32D>;EG�,- < 416.385>,FLOWLINE= � 412.470> .+tt*****.*.*.*..******t***.*..��..***.*.*****�+****#**++*�t***+tt.,*��+�tt** FLOW PROCESS FROM NODE 2410.90 TO NODE 2011_00 IS CODE = 1 UPSTRERM NODE 2011.00 ELEVA'i'ION = 413.61 (FLbW IS SUPERCRZTICAL} CALCL7LA'FE FRiC`I'iQN LOSSES {LACFCD? : PIPE FE.OW = A4.92 CFS PIPE DIAMETER = 30.00 IAFCHES P�PE LENGTH = 76.23 FEET MANNIAiG'S N= 0.01300 NORMAL DEPTH{FT) _ �.65 CitITICAL DEPTH(FT) = 2.22 ---_----------------------____-------------------------------------------------- ----------------------------------------..___---------------------------------- UPSTREAM CONTRdL ASSi7MED FLOWDEPTH(F'P) = 1.8fi -------------�____________.._�..__--_____---------------------------------------- GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATiON: ------------------------------------------------------------------------------ DTSTRNCE FROt+1 FLp4J DEPTH VELdCITY SPECIFIC PRESSURE+ CONTROL(FTa (FT} (FT/SEC) ENERGY(FT) MOMENFUMSPOUNDSj 0.000 1.859 11.475 3.905 1201.98 2.749 1.858 11.476 3.905 1202_13 5.614 1.858 11.4B1 3.90b 1202.28 8.619 1.857 11.4B4 3.906 1202_43 11.7fi3 1.857 11.488 3.907 1202.58 Z5.05S 1.856 11.491 3_906 1202.74 }.8.590 1.856 11_994 3.906 1202.89 22.207 1.855 11.997 3.909 1203.04 . 2b.088 1.855 11.500 3.910 1203.19 30.209 1.854 11.503 3.910 1203.35 � 34.602 1.859 1L 50b 3.911 1203.50 39.304 I.853 11.509 3.911 1203.66 44.360 1.853 11.512 3.912 1203.61 49.82� 1.852 ��.516 3_913 12D3_96 55.777 1.852 11.519 3.9�3 32p4.�2 fi2.342 �.851 11.522 3.914 ]209.27 59.524 1.851 11.525 3.915 1209.43 75.23D 1.850 �1.528 3.9�5 12D4.56 NODE 2011.OQ : HGL =< 415.469>;EGL= < 417.515>;FLOWLiNE= <^y413.610> * * * * t * * Y f * * � * } * i f � 1 k * # x * t i * Y rt 4 k f t * f f * * * } k * f � * * * i i f 1 f * } * * * f * * * * * * i f * * f k * 1 Y f # i # # FLQW PRpCES5 FROM NODE 2011.Oa TO NODE 2a15.00 IS CODE = 3 UPSTR�AI'4 NODE 20�5.00 ELEVATYON = 915.1D (FLOW IS SUPERCRITICAL) -------------------------------------------------------------------------------- CALCULATE PIPE-BEND L05SES(OCEMA]: PIPE FI,OW = 44.92 CFS PIPE DIAMETER = 30.00 INCHES CE�ITRAL ANGLE = 16 . 0 0 0 DEGREES MANNING ' S i�i = 0. D 13 0 0 PIPE LENG'�'H = 95.00 FEET - --------------------- NO}�Mp.i, D�PTH { FT )= 1. 81 CRITICAL DEP'I'H ( FT )= 2. 2 2 ------------------------------------------------- UPST}tEAM CONTFtOL ASSUMEI] FLOWDEP�'H {�') � 2, Z Z __ __---------------------------------------- GRADUALLY VARIEb FLOW PROFIi,E COMPiT£ED INFORMATION: ------------------------- DISTANCE FFtOM FLOW DEPTH VELOCITY SPECIFTC PRESS[,FREt COI3TRpL{FT) (FT) (FT/SEC) ENERGYfFT} MOMENTUM{ppUNps} a.00� 2.221 9.794 3.fi95 1197.99 D.097 2.205 9.799 3.697 1k48.13 0.342 2.188 9.857 3.698 1].48.47 0.745 2.172 9.917 3.700 1149.02 , 1.315 2.Z55 9.978 3.702 1149.77 2.065 2.139 1p.042 3.706 1150.72 3.011 2.123 la_108 3.710 1151.89 4.169 2.106 10.176 3.715 3153.26 ' S.562 2.09Q 10.29b 3.721 1154.85 "7.2i5 2.073 10.318 3.727 1Z56.66 9.158 2.D57 10.392 3.735 1158.69 11.934 2.041 Z0.469 3.743 1160.94 �4.Q76 2.029 10.547 3.753 1163.41 17.154 2.Q0$ 1d.628 3.763 1166.11 20.737 1.991 1Q.711 3.774 1169.05 24.420 1.975 10.797 3.786 1172.23 29.827 1.958 10.885 3.799 3175.65 35.625 �.942 ifl.975 3.819 1i79.31 92.556 1.92b Z1.Q68 3.829 1183.23 50.963 1.9a9 2�.164 3.846 1187.41 61.3BB 1.893 11.262 3.863 119L 84 74,733 1.876 11.363 3.882 17.96.55 92.695 1.660 11.466 3.903 1201.53 95.00Q 1.859 11.475 3.905 �201.9$ NODE 2015.00 : HGL =< 4�7.321>;EGL= < 418.796>;FLOWi�ENE= < 415 100>` ^ +f**+*�,,,.�**+�*t.*��+*.**��*******...+.,�,�t+�f++++,.,�.�+�*.+.��t��»..**.**�+**+ FLdW PROCESS FRp�7 NODE 2015.D0 TO 230bE 2015.00 IS CODE = 5 iiPSTAEAM i�10DE 2015.00 ELEVATION = 415.10 (FLOW UNSEALS IN REACH? ------------------� ' CALCZiLAT� JUNCTION LOSSES: • PIPE FLOW DIAMETER ANGLE FLOWLTNE CRI'I'ICAI, VELOCITY • • C � i3PSTRERM DOWNSTRF�TaNf LATERP.L # 1 l,A'Y'�RAL # 2 Q5 (CF5) (INCHES} (DEGREES) ELEVATION 94.10 30.DD D.00 415.10 44.92 30.00 0.82 18.00 o.00 a.00 O.OD===QS EQUALS - 415.1p 90.40 415.66 o.oa o.00 SIaSIN INPUT=== DEP7'H(FT.) {FT/SECj 2.21 8.984 2.22 9.737 0.34 0.464 a.00 a.000 LACFCD AND OCEMA FLOW JUNCTIQN FORM[FLA$ USED: DY=LQ2*V2-Q1*V1*COS[DELTAI}-Q3*V3*C�S(DELTA3j- Q9*V4'CQS(D�LTA4j}/{{A3+A2J*36.1)+FRICTEpN LQSSES UPSTREAM: MANNING'S N= O.Q13Q0; FRxC'I'�ON SLQPE = 0.03155 AOWNSTR.EAM: MAI3NING'S N= a.Q130q; FRICTI4N SLOPE = O.OlOb7 AVERAGED FRICTI0I3 SLOPE TN JUNCTION ASSUMED A5 O.D1111 JUNCTION LENGTH = ]..50 FEET FRICTION IASSES = Q.017 FEET ENT}tANCE LOSSES = d.Q00 FEET JIJAiCTIpN LOSSES = {DY+I-IVl-HV2 j + (ENTRASiCE LpSSES) ,7[TL�FCTiON LOSSES = i 0. 0661 +( 0. 000 )= d. 066 NODE 2015.Ofl : HGL =< 417.609�;EGL= < 416.863>;FLOWLINE= < 415.100> **..**.***t..+t*..��.+.+****�*...*...**..***�*.+t**+.*��**.*w*w.*....**�++**��. �'LOW PROCE55 FROM I30DE 2015.04 TO NODE 2D15.00 �S CODE = 3 UPSTREAAf 330DE 2016.00 ELEVA�'ION = 415.29 (FLOW IS [RJDER PRESSCTRE} CALCiJi�ATE P�PE-BF�ID LOSSES{OCEMP.) : PTPE FLDW = 49.1Q CFS PIPE DIAMETER = 3D.00 INCHES CEA7TRP.I, ANGLE = 2.800 DEGREES MANNING'S N= 0.01300 PIPE LENG1'H = �b.80 FEET BEND COEFFICIENTfKB} = Q.04410 FLOW VELOCITY = 8.98 E'EET/SEC. VELOCITY HEAD = 1.253 FEET HB=KB*(VELOCITY HEAI)) _( O.D44�*f 1.253) = Q.055 SF={Q/K)**2 = {( 44.10)/{ 410.158))**2 = 0.01�56 HF=L*SF = ( �.6.80}*(0.01156? = 0.�94 TOTAL HEAD LOSSES = HB + HF ={ O.fl55j+( 0.194) = 0.249 NpD� 2016_QO : HGL =� 417.859>;EGL- < 419.112�;FLOWF.,I13E='< 415 290>M � *iFY� f YrYr*iFYr fi k�k*****1 y� * y f�***1r f*YrYr*YrYrYrYr**YrYr*'M k*tktk*ir�k *tt�!#*1�Yy.}***Y� �kiF�kM Yr*'k*tktM Yr*'kt* FLOW PROCESS FROM NpD� 2016.00 TO NODE 2D17.00 I5 CODE = 1 UPSTREAM NODE 2017.00 ELEVATION = 418_43 (HYbRAULIC JUMP OCCURS} --------------------___-------------------------------------------------------- CAI,CULP.TE FR�CT�ON LOSSES(LACFCDj : PIPE FLOW = 44.10 CFS PIPE DIAMETER = 30.00 �NCHES PIPE i,FNGTH = 227.00 FEET MJ�NNTNG`S N = O.D1300 HY77RAULTC JUMP: DpWNSTREAM RUN ANALYSIS RESUI,TS ----------------------------�-_----------------------------------------------- NORMAI, DEPTH(FT} - 1.86 CRITICAL DEPTH(FT) = 2_21 - ----------------- UPS�'REAAf CONTROL ASSiTI+3ED FLOWDEPTH(FT) = 1.76 _-- �---------------------- GRADUAi�LY VARIEA FLOW PROFILE COMPUTEF] INFORMATION: DISTAI�CE FROM FLQW DEPTH VELOCTTX SPECIFIC PRESSURE+ CONTROL(FT} (FT) (FT/S�C) EI3ERGY(iT) MOMENTUM{POUNDS) 0.00� 1.764 11.906 3.967 1198.19 3.948 1.769 11.873 3.959 1196.38 7.009 1.773 11.840 3.951 1194.61 2fl.692 1.778 1L $D7 3.944 1192.$5 19.510 1.783 11_779 3.935 1191.12 7.8.475 3.787 �1.741 3.929 11$9.4I 22.603 1.792 Z�.709 3.922 11$7.73 � C� S 25.911 31 .419 36.153 41.140 46.417 52.026 56.020 64.466 71.451 79..088 87.531 96.996 107.799 120.429 �35.708 �55 . J�74 182.285 227.040 1.79b 1.801 �.806 �.810 �.$15 1.819 i.824 1.829 1.833 1.838 1.842 1.847 1.851 7..856 1.861 1.865 1.870 1.874 11 11 11 11 11 11 11 �1 11 11 11 11 11 11 11 11 11 11 677 645 614 582 551 520 490 959 429 399 369 340 310 281 252 224 195 158 3.915 3.906 3.901 3.894 3.$$$ 3.881 3.8"l5 3.869 3.663 3.857 3.851 3.895 3.839 3.834 3.82$ 3.823 3.817 3.812 �186.D7 ZI84.43 ZI82.62 I181.23 1�79.66 �178.12 1176.60 1175.]0 1173.62 �172.16 2170.73 1169.32 1167.93 1166.56 1165.21 1163.89 1162.58 1161.33 HYDAAUL3C JUMP: UPS'�'REA�7 R[1I3 ANALYSTS RESi.TLTS ------------------------------------------------------------------------__�--_-- ---------------------------------------.._�__-___------------------------------ D4WNSTRE.�M CON`I'ROL ASSi7�7ED PRESSURE HE.AD{�'T) = 2.57 ---------------=------------------------------------_-------------------------- __---___________--___�---------------------------------------------------------- PR�SSUAE F�,OW PRQFILE COPSPUTED INFOFiMATION: ----------------------------------------------------------------__---_-_--------- DISTANCE FROM PRE55i3RE VELOC�TY SPECIFIC PRESSITRE+ CONTROLSFT) HEAD(FT} {FT/SEC) ENE3tGY(FT) MOMENTUM(POC]NiIS) o.oaa 2.569 8.984 3.822 1171.73 30.267 2.500 8.984 3.753 1150.56 ==ASSLFMED-DOWNSTRF.Al�-PRESSURE-HEADSFTI---==--2=50-----________________________ GRADUALLY VARIED FLOW PROFILE CQMPiJ�'ED INF'ORMATION: -------------------------------------------------------------------�....-------- DISTANCE FROAf FLOW DEPTH VELOCITY SPECIFIC PRESSUR�+ CONTROL(FT] {��) (F'T/SECi EN�RGYf�"P) MOMENTUM(POUIVDS} 30.267 2.500 6.981 3.753 1150.66 34.�47 2.488 6.986 3.743 114'J.52 37.Z55 2.477 B.995 3.734 1144.72 39.753 2.465 9.005 3.725 1192.14 42.064 2.454 9.020 3.718 1139.75 49.153 2.442 9.035 3.710 1137.53 4fi.Q6Q 2.430 9.�52 3.703 �335.45 A7.811 2.419 9.071 3.697 I�33.5D 49.425 2.407 9.090 3.691 113L fi9 50.917 2.395 9.I�2 3.fi85 1129_99 52.297 2.389 9.134 3.680 1126.41 53.573 2.372 9.158 3.675 1126.95 54.752 2.361 9.183 3.671 1125.fi0 55.838 2.349 9.209 3.667 1124.35 5b.835 2.337 9.236 3.663 1123.21 57.745 2.326 9.264 3.659 1122.17 58.571 2.314 9.294 3.656 1121.23 59.313 2.303 9.324 3.653 1120.39 59.973 2.291 9.355 3.651 11Z9.66 60.550 2.279 9.388 3.b49 11�9.02 b1.044 2_26$ 9.92}. 3.547 i1�8.48 61.452 2.256 9.456 3.b95 z718.04 61.�75 2.295 9.491 3.644 �117.70 62.010 2.233 9.528 3.b43 1117.45 52.153 2.227. 9.565 3.643 1117.30 � 62.201 2.210 9.643 3.643 1117.25 227.000 2.210 9.643 3.643 1117.25 ------------------------ENd OF HYDRAULIC JUMP ANALYSIS---_________--_-----____ I PRESSURE�MOMEN�UM SALANCE OCCURS AT 14.37 FEET UPSTRERM OF NODE 2016.OD � I DOWNS�REAM DEPTH = 2.536 FE�T, UPSTKEAM CONJUGATE DEPTH = 1.873 FEE� � NODE 2017.04 : HGL =< 42Q.�94>;EGL= � 422.397>;FLOWLINE= < 918.43D> �w+*��*�***ti**t��t�r**++***s*+**w++***�****��*r+r*t*tt+ttfr*y�:w��*�rrtitirt�rt+*f FLOW PROCESS FROM NODE 2Q17.40 TO NOD£ 2017_10 IS CODE = 2 UPSTREAM NODE 2017.10 ELEVATIpN = 418.76 (FLOW IS SUPERCRITICAL) CALCULATE MANHpLE LOSSES(LACFCD): PIPE FLOW = 44.1Q CF5 PIPE DIAhFETER = 30.00 �NCHES AVERAGED VELOCITY HEAD = 1.993 FEET HMN =.D5*(AVERAGEFI VELOCITY HEADi =.05*( 1.993j = 0.100 ------------------------------------____-_-_----------------------------------- NODE 2037.1D : HGL = � 420.714>;EGL- � 422.495>;FLOWLINE= < 918.760> 1tYr1F*'k'ky� 11'h***i**i�i �Yr**i1 *YrY� YrY� �k�M Y� Y� k kY�'k'kY� �M �k'kY� tM * tk �*** it* f Y*tYY! Y�lllttt* �l �1 t*t * 11'k*ttf FLOW PROCESS FROM NODE 2017.1D TO NODE 2020.40 IS CODE _� UPSi'RF.AM NODE 2024.00 ELEVATIOAi = 419.2� (FLOW IS SUPERCAI'i'ICAL) ------------------------------------------------------------------------------- CAY,CULATE FRICTFdN E�OSSES ILACFCD} ; PIPE FLOW - 44.10 CF5 PIPE DTAME�'ER = 30.00 INCHES PIPE LENGTH = 30.00 FEE'I' MANNZNG'S N= 0.0�34D NORMAL DEPTH{F�') = 1.82 CRITICAL DEPTH(FT} - 2.21 ------------------------------------------------------------------------------- UPSTREAM CONFROL ASSUMEB FLOWDEPTH{FT) = 2.21 • ________________________________________________________�Tf�r��===____==-��f�, GRADUALLY VARIED FLOW PFtOFIL£ COMPUTED INFORMATION: DISTANCE FROM FLpW DEPTH VELOCITY SPECIFIC PRESSURE+ CONT320L { FT ) ( FT } ( F�' / SEC ) • ENERGY i FT 1 MOMENTUM ( PO[]�IDS ) Q.000 2.21D 9.603 3.693 1117.25 a.069 2.194 9.657 3.b43 1117.34 0.280 2.17B 9.712 3.b44 1117.62 0_643 2.163 9.770 3.b46 11J.6.47 1.168 2.147 9.829 3.648 1118.71 1.867 2.131 9.89fl 3.651 �1119.53 2.755 2.115 9.953 3.654 �120.54 3.850 2.100 10.017 3.659 Z121.73 5.172 2.084 10.084 3.664 1Z23.12 5.745 2.068 10_152 3.670 1�24.74 8.601 2.p52 1.0_223 3.676 1126.48 �d.776 2.037 1Q.295 3.684 1128.46 13.314 2.421 1Q.37Q 3.592 1130.64 16.271. 2.005 10.446 3.70i 1133.�2 19.720 1.969 1D.525 3.73i 1135.62 23.750 1.974 10.606 3.721 1138.42 2B.483 1.958 10.689 3.733 1141.44 30.OQ0 1.9�4 10.711 3.736 1142.30 ----------_-------------------------------------------------------�------------ NODE 2D2D.06 : HGL =< 92�.920>;EGL= < 422.853>;FLOWLINE= < 914.2�0> Yr Yr * * * �lr * * * * t * * Yi Yr * t t i Y �k �k * �k # i i } * f f f # # # tt f * # i yr'k * `k * * * # } * * # i Yr M Y� # k �h f �lr * * * * * * * t * # * * * t * Yr'k FE�OW PFtOCESS FI20M NODE za2a. ao TO NODE 2D20 . DO IS C�DE = $ UPSTREP.M NODE 2020.D0 ' ELEVATION = 419.21 [FLOW UN5EAL5 IN REACH} • "'------------------------------------------------------------_____-___.._______ CALCUl�ATE CATCH BASIN E13TRANCE L05S�S(LACFCD}: . PIPE FLOW = 99.I0 CFS PIPE DTAMETER = 30.00 �NCHES FLOW VELOCITY = 9.61 FEET/SEC. VELOCI'I'Y HEAD = 1.433 FEE'f' CATCH BASIN ENERGY LOSS =_2*{VELOCI'i'Y HEAD) =.2*( 1.433} = 0.2$7 NODE 2420.00 : HGL =< 423.139>;EGL= < 423.139>;FLOWLINE= < 419.210� Y� i� *i i� *f'k�r M##'k *'if f'Fi #*f }#}iik**+�iyr jrf�L * Y Y* Y#!f Yi if �it*#f Y#i ti #4i �k Y* f 1 Y Y# Y#ii i tf �r *# UPSTREAM PIPE FLOW CONTROL DATA: I30DE NUMBER = 2020.04 FLOWLINE ELEVATION = 419.2� ASSUMED UPSTREArS CQN`I'RpL HGL = 42Z.42 FOR DOWNSTRE�S RUN ANALYSIS EI�FD OF GRADUALLY VAAIED FLC?W ANALYSIS • • � +++�r��r��ra*artrw��x*+**:x,�**ww�r++*+*x�w*+xx*+***r**+**+++r�wiy�iYtY�**�r**t PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRF], AND OCEMA HYDRAULICS CR�TERION} fc) Copyright 1982-20fl2 Advanced Engineering Software faes} Ver. B.0 Release Date: 41/O1/2D02 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSiJI,TANTS 7D1 '�' STREE7', SiIITE 800 SAN DIEGO, CA 92101 619-235-6971 • • *...*****�+**++*.�..*.�..+ DESCRIPTION OF STUDY ••*•*:*•+*�+�****+*�*.*++* � BRESSI F2ANCH - ULTIMATE COND�TTONS * * SYSTEM 2000: LINE k 30" RCP SN0.7 PER SHT. 8 OF AWG 4008D) * * 100-YEAR STORt�f EVENT * **'!r#**#'k*#*�F*YrYrY� Y� fi fi fYrlr�ki �********Yr**yriFYr'k frYrYrYc 1'kiF'k*Yr�k k t****1*#i i�! �k! i! Y�t �k�k4#i FILE NAME: P2000-I.DAT TIME/DATE OF S4'UDY: 17:19 O1l16/2D03 i f*t�!*ti #t*YY i i Y1 f f f4�Yiki# # i##*M*#}f y}#ti++*iti�i 4*iF�kt yrt }#*�{* #* iY� Y� Y� Yr Y� Yi Yr k Y� Yr Y� **}YrY� * GRAbUAF�LY VARIED FLOW AA3ALYSIS FOR PIPE SYSTEt4 NODAL POINT STATUS TAI3i,E (Note: •*' indicates nodal point data used.) UPSTREAM RCJI3 DOWIVSTFtE.n.M RUN NODE MODEL PRESSURE PRESSUItE+ FLOW PRESSU�2E+ NLFNlBER PROCESS HEI�D { FT } MOMENTUM ( POIFAIDS } DEPTH ( FT ) MOMEN�'UM { POUNDS ) 2001.70- 6.�0* 2695.92 1.73 }.810.72 } FAICTION 20D1.80- 4.93* } CAT'CH BASIN 2003.80- 7.30* 2336.40 3852.26 2.3b Dc 2.36 Dc 1578.09 339.6}. _____-------------------------------------------------------------------------- MAXZMUM NLTMBER OF ENERGY BALANCES [7SED IN EACH PAOFILE = 25 ----------------------------------------------------------------__-_______..____ NOTE: STEADY FLOW HYDRAI3LIC HEAD-LOSS COMPUTATIONS BASED pN TH� MOST CdNSERVAT2VE FORMULAE FROM T1iE CURRENT LACRD,LACFCD, AND OCFMA DESIGA3 MANUALS. ****t*ttttx+y�t��r>ir��++**+t*++*+*r++��k*i.*�i.+w,r+�+i.�twrf*+i.w**,ir****+*wtw*w**+� DOWNSTREP.NS PIPE FLOW CON'i'ROL DATA: NODE NUAfBER = 24p7..70 FLOWLTN� ELEVATION = 390.90 PIPE FLOW = 55.37 CFS PIPE DIAMETER = 30.00 INCHES ASSUMED 170WNSTAEAM CON'i'ROL HGL = 397_ODO FEET ___-______-------------------------------------------------------------------- NODE 2Q02.7p : HGL =< 397.400>;EGL= < 39$.976>;FiOWI.�NE= t 390.900> Y�fi*f *!*yr*�F**Yr****#t�l�k4Y* ik*4�kY�k�F+y�Jr11 *Y�YY��kYr�kYYYf 1�r 1 iYl�Yl�i�k**#**i�**�k#*Y�***** #*i�* FLOW PROCESS FROM NQDE 2001.7Q TO NQDE 2Q0�.80 IS CODE = 1 UPSTREAM NODE 24QJ.SQ �LEVATION = 393.24 (�'LOl^1 IS UNDER PAESSURE} ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSES{LACFCDj: PIPE FLOW = 55.37 CF5 PIPE DIAMETER = 30.4Q I�ICHES PIPE LENGTH = 64.00 FEET MANNING'S �= o.ol3aa 5F={Q/K}��z - {( 55.37)/( 41p.173))**2 = O.D1822 HF=L*SF' _ { 64.00}*{0.01822} - 1.166 -------------------------------------------------------------------------------- NODE 2001.8D : HGL =< 396.165>;EGL= < 9�0.142>;FLOWLINE= < 393.240> * * # f * � * Y i � � � * k Y + f * W 1 # i i } * * f Y * i 4 * i # * � ti * * * * i # � 4 * t Y # i f * * � i � M f * * * * * # * # 1 * � * k * * i # f � i FLOW PROC�SS FROM NODE 2fl01.60 TO NODE 2001.80 TS CODE = B UPSTREA2+] NODE 2003.80 ELEVATION = 393.24 (FLOW I5 UNDER PRESSURE) CALCULA'�'E CATCH BASFN EidTRANCE LOSSES{�CFCD) : PIPE FLOW = 55.37 CFS PIPE DIAMETER = 3Q.00 INCHES FLOW VEL,OCITY = 13.28 FEET/SEC. VELOCITY HEAD = 3.976 FEET .CA'I'CH BASIN �NERGY LOSS = .2*IVE�,OCITY H�? _ .2*i 1.976) = 0.395 ------------------------------------------------------------------------------ NODE 2QQ1.80 : HGL =< 940.537�;EGL= r 40Q.537>;FLdWl,INE= < 393.29Q> ******+*.,****�t*��**�*�*��**�,,**�*�*+*+�+*w**+*+****++****.**.++***.**«.�.* UPSTREAM PIPE FLOW CONTROL DATA: N4DE NUMBER = 20Q1.80 FLOWLINE ELEVATION = 393.24 ASSUMED L7P5TREAM CONTROL HGL = 395.b0 FOR DOWNSTREAM AiJN ANP.LYSIS END OF GRADUAi.LY VARIED FLAW Ad3ALYSIS i�r #* Yr **** w*** t i* t i i f* i* i!! t Y 1 i* Y* i**! t f i! t t# i� **�k i� �r *# t t i f? f t�i **** f*� i 4 Y f f Y Y i Y f PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCB,LACRD, AND OCEMA HYDRAULICS CRTTERION} (c} Copyright 1982-2042 Advanced Ei�gineering Software (aes) Ver. 8.0 Release Date: 01/01/2002 License ID 1549 Anaiysis prepared by: PR0.7ECT DESIGN COSISULTAN'f'S 701 ' B' S'i'RE£T, SUITE 84b . SAN DiEGQ, CA 921b1 6�9-235-6471 ++�*ft.++�++**+�,r,.*****�.. DESC�2IP3'i0N OF S'Ti]I)Y **�**..,*.,..*.*t�.****:**�x * BRESSZ RANCH - ULTIMATE CONDITIONS * * SYSTEM 2000: LINE 1 34' RCP (N4. 8 PER SHT. B OF BWG 440-BDf * * 100-YEAR STORM EVEtdT * *«+�*+++**+�*+�++***.***....�..*.:ttt+��*�+t+*+�*.**+:.,�...�++�++*�,��**�+ FILE NAME: P2000-1.bAT TIME/dATE OF STIJDY: 17:19 01/16/20D3 • ) FRICTION 2001.80- 4.93* ) CATCH BASIN 2041.84- 7.30�" **+.***��+�+.+if+++***x**�,,,,.*rt+.,r�++f*++.**wr++:i+++*+.,..*��..,.,.�..**..,.*..**� GRADUALLY VARIED FLOW ANALXSIS F4R PIPE SYSTEM NODAL POI3d'I' S'i'ATUS TABLE {Note: '*' indicates nodal point data used.} iJPSTRF.7iM R[J�1 DOWNSTREAM RUN �IODE MODEL PRE55URE PRESSUAE+ FLOW PRESSEJR_E+ NETMBER PROCESS HEAD(FT) MOMENTUM(POUNDSj DEPTHfFT} MOMEN'I'UMfpOUNDS) 2001.70- 6.�Ow 2695.92 1.73 181a.72 ------------------------------------------------------------------------�..__-- MAXIMUM NUMBER OF ENERGY �ALANCES USED IN EACH PRpFILE = 25 NOTE: STF.ADY FI,CiW HYDRAULIC HEAD-LOSS CQMPUTAT�ONS BASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, AND OCET3A DESIGN NiAN[JAi�S. +�rti�**+wa��a�*ra�x+r*r�+�*�t+�tyw*�wra*r**:++a*+*++rr+�ai++ay,w+a+..++t+++�rat+t 2336.40 1B52.26 2.35 Dc 2.36 Dc 3578.�9 339.61 � � f i�F * i� * * ri ri -Fri # ir * �lr*# i Y� # tY*Y Y �k *Yr * �M ik�i %ti* *Y y�Yi�Jr}#�YY 4 �iyr#�i �e y' *{� k *1riF# �M * Yr * ****Yr*YrYY�1ti tY�t ' P�PE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, RND OCEMA HYDRAULICS CRIT�RION) (c) Copyright 29$2-2002 Advancad Engineeri.ng Software (aes} Ver. 8.0 Aelease �aCe: a1/01/2402 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULT�NTS 741 'B' STAEET, SUFTE SOa 5AN DIEGO, CA 92101 619-235-647I � • a+*�**�r**��++a�***��+w�*�* DESCRIPTION OF STUDY +ttt*�+w+**+*�*�w�****��k� * BRESST AP.NCH - ULTIMATE CONDITIO�iS * * SXSTEM 2600 - LATERAL 2(NO_ 9 PER 51-IT. 8 OF DirdG 440-8D) * "' 100-YEAR STORM EVEN�' t 1�'Yr1riFYrtkYrYr***Yr�*ity Y Y# f yr4}f�k%ti}*#; **** #'k f* i�**i� ****YrY� **YrtM iM * Yr***iY �kY��k i i*Y� ti' �'y'1# FILE NAM£: P2000--2.bAT TIME/DATE pF S7'UDX: 17:17 O1/16/20Q3 'tY�tt'k ��**i�if ** i*Yr Yr�h iF Yr9riklr t*# ** Y i� �k t# t#! Y Y!*Y! Y#ttf ##tYY1 yr#y �# ***Y� �h k Yrf��k k YrY� t***yr1� ** GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL PpIN'i' STATUS TABLE fNote: "'" indicates nodal point data used.} Ul'S`i'R�M RUN DdWNSTREAM RUN NODE MODEL PRESSURE PRESSURE+ FLOW PKESSURE+ NUMBER PROCESS HF,AD ( FT) MOAfEN'I`lJM ( POLFNDS j DEPTH ( FT i MQM�ITIJM ( POUNi7S j 20Db.60- 3.20* 276.96 0.28 55.31 ] FRICTION 20D0.7a-- 1.39• ) CATCH BASIN 2fl00.70- 1.43* 77.97 73.99 0.60 Dc 0.60 Dc 28.53 10.23 ------------------------------------------------------------------------------ MAXINSUM NiFMBER OP ENERGY AALANCES L35ED IN EACH PROFILE = 25 NO'i'E: STEADY Fi,OW HYDRAE3LIC HEAD-L05S COMPi7`�'ATIONS BASED ON THE MOST CDNSERVATIVE FOR�IULAE FROM Tl-IE CURRENT LACRD, LACFCD, ANn OCF.�7A ]7ESIGN MANUAE,S . .**+�..++*+**�*,...****+*t*+�+wt**+..**.+..+�*f.��,�s+.�******�.*.******+.�**�** DOWNS'E`REAhf PIPE Fi,OW CON'FROL DATA: NOn� NUz�3ER = 2000.60 FLOwLINE ELEVATZON = 390.20 PIPE FLaW = 2.49 CF5 PZP� DIAMETER = 18.Q0 I13CHE5 A55i7i�iED DOWNSTREAM CONTROL HG� = 393.90d FEE'i' NODE 2000.60 : HGL =< 393.400�;EGL= < 393.431>;FLOWLINE= < 3g0.200> YY1��Y t 1 Y Y� Y 1�k tii i#*}# * iF *YrYr}Yr�kYrYr� *�****i * �# f i*}*t * f t�li �k i 1+�k�ki # yr **** k*Yr*�k? *YrY� *# *?#'F FLOW PROCESS FROM NODE 200D.60 TO NODE 2000.70 IS CODE = 1 [3PS'I'i�EAM NODE 2000.70 ELEVATIQN = 392.01 {FLOW SEALS IN REACH� -----------------------------------__�--___------------------------------------- CALCULATE FRICTTpN LOSSES(�.ACFCDj: PIPE FLOW = 2.49 CF5 PIPE DIAMETER = 1$.d0 INCHES • PIPE LENGTH = 7.25 FEET M.�NNING'S N= 0.013fl0 DOWNSTREA3�i CONTROL ASSUMED PR�SSURE HEP,D(FTj = 3.20 PRESSURE FLOW PROF��,E COMPUTED INFORMATION: �^ 1WL4N� �'~�yY� � DISTANCE PROM PRESSURE V�LOCITY Sp�C�FIC PRESSURE+ CONiROL { FT ) HEAD i F'3' }� ( FT / SEC 1 EI3ERGY ( FT ) MOMEI3TUt4 I POIJIdDS ) O.ODD 3.200 1.909 3.231 276.96 6.825 �.500 1.909 1.53J. 89.50 ------------------------------------------------------------------------------ AIOR3�lAi DEPTH (FT) = 0.22 CRI'i'ICAL DEPTH { FT} = 0. 60 -------------------------------------------------------------------__________-_ --------------------------------------------------------__-_-------------------- ASSUMED DOWNSTREA4�7 PRESSURE HEAD(FT) = 1.50 GRADUAi�LY VARIED �'I,OW PROFILE COMPUTED INFQR�fATIO�I: DISTANCE FROM FLdW DEP'I'H VELOCITY SPECIFIC PRESS{3RE+ CONTROL ( FT 1 ( Fi' ) ( FT / SEC 1 E�3ERGY ( F�' 1 MpME�I'I'UM ( POUNDS } 6.825 l.$a4 1.409 1.531 69.50 6.968 1.464 1.416 1.495 85.57 7.110 1.928 1.434 1.460 81.72 7.25D 1.392 1.455 1.425 77.97 ------------------------------------------------------------------------------ I30DE 2000.70 : HGL =< 393.902>;EGL= � 393.435>;FLOWLINE= � 392.010> yk �k Y ti1�1�YY*f i�**f *f�F*# *f#f yr*�F#yr# yF LL yr�k41�W �k1 Y#i##Yi * fYYti � f�iYyr*#y�i***i� *# i� i� h*** *f* ** FLOW PROCESS FRpM NOB� 2pOD.70 TO NpDE 2000.70 TS C017E = 8 UPSTREAM 730bE 20D0.70 ELEVATIpN = 392.01 {FLpyJ IS SUBCRI'i'ICAL) CA.LCULATE CATCH BASIN ENTRANCE LOSSES(LACFCD): PIPE FLOW = 2.49 CFS PIPE DIAMETER = 1B.flQ INCHES FLOW VELOCI'iY = 1.46 FEET/SEC. VELOCITY HEAD = 0.033 FEET CATCH SASIN ENERGY L055 =_2*(VELOCITY fiEAD) _.2*i 0.033) = 0_007 NODE 2000.70 : HGL =< 393.44I>;EGL= < 393.441>;FLOWLINE= < 392.OiQ> � ****v��,�+v�++�****+*,r****«�*�,.*,.*****+***�***t��**+�****+�«****.,,*+**********.t� LTPSTREAM PIPE FLAW CONTROL DATA: NdDE NLIMSER = 20Q0.?0 FLOWLINE ELEVATION = 392.01 ASSUMED UPSTRF�FIM CONTROL HGL = 392.61 FOR DOWNSTREAM RUN ANALYSIS ------------------------------------------------------------------------------ ------------------------------------------------------------------------_____----_- END OF GRADUALLY VARTED FLQW ANALYSIS � • r*y*:+w+�w*�****i�tv�f**�w+++�*+v�tti*�r+i+*�rt.��s*��*+�at:*+t*+*****r**w+***,t**+x PIPE-FLQW HYDRAULICS COMPU'�'ER PROGRAM PACKAGE iRe#erence: LACFCD,LACRD, AND OCEMA HYDRAiJLICS CRITERIQN) (c} Copyright �982-2002 Advanced Engineering Software (aes) Ver. 8.0 Re3ease Date: ��/O1/2002 License ID 1509 Analysis prepared by: PROJECi' DESIGN CONSULTANTS 701 `H' STREET, SUITE 800 SAN DFEGO, CA 92101 6i4-z3s-64�1 • • ''''**"`•"+*•**•"'**""''**+**** DESCRIPTION OF ST[JDY *+•+.*t+Y+...*.++*�++*.+*+ * SAE55� RANCH ULTIMATE CONDITIONS * * SYSTEM 2400: LATERAI. 3{�7p. 7 PER SHT 8 OF DWG 400-SD) * * Z60-YEAIt STORM EVEN'P * �**+tt*t*f.*�+..*v.****,r+*++***+*+**��+�*+*+a+w**+++****.****.**++**+****++ FILE NAME: P2000-3.DAT TIME/DATE OF STUDY: 17:16 al/16/24Q3 **,ir,irr***r*r***��+*++i*+tr*+tyrt*++++***++��+*ta*r+t*rs++�v.��+i.i.**��*,tt�*�*****♦ GRADUALLY VARIED FLOW A�iALY5I5 FOR PIPE SYSTEFS PTODAT., POINT STATUS TABLE (Note: "*" indicates nodal point data used.} UPSTREAM RUN DOWNSTRF.AM RUN NpDE MODE� PRESSURE PRE55URE* FLOW PRESSURE+ ATiTMBER PROC ESS !-IEAI} ( F'i' } MOMEI�iTUM { pp��5 ) DEPTH ( FT ) MOMENTUM ( POUNDS ) 2001.J0- 5.i4* 486.47 0.50 29.91 } FRECTION 2001.2fl- 4.69* } CATCH BASIN ZOD1.20- 4.73* 441.74 439.Q2 fl.60 �c 0.60 Dc 28.53 10.23 MAXIMUM NUMBER OF ENERGY BAiANCES USED I13 EACH PROFILE = 25 ------------------------------------------------------------------------------- NOF'E: S3'EADY FLOW HYDRAULIC }{EAD-LOSS COMPUTATIONS BASED pN �'H� MOST CONSERVATIVE FOFiMULAE FROM THE CUARENT LACRD,LACFCD, AND OCEMl�, D�SIGN MANUALS. ********rs�t***at*++***y+++�+ri�MfY#*4li�fltYY#iY�fiFi�yl�r�r�ra+�+*k*a**w****x***,t*�f DOWNSTRF� PIPE FLOW CON'1'ROL DATA: NODE NUMBER = 2001.10 Fi,OWLIN� ELEVATiON = 391.90 PIPE FLOW = 2.49 CFS PIPE DIAMETER = 18.00 INCHES ASSlJ1+iED DOWNSTREAM CONTROI.� HGI.� = 397.000 FEET ------------------�-_--------------------------------------------------------- NODE 2flflL 10 : HGL =< 397.040>;EGL= < 397.031>;FLOWLINE= < 391.900> *xx+*+x*+t�x,k++**+*tr*tt**tt***t+*+++*+**xr+*++x*****y�rr+�+*+*+t�*+*++*+ti�+�t+ FLOW PROCESS FROM NdDE 2001.10 'i'O NODE 2001.20 IS CODE = 1 UPSTRER.M NODE 2001.20 ELEI7ATYQN = 392.33 (FL�OW IS UNLIER PRESSiTRE) CALCUT.I�TE FRZCTION LOSSESILACFCD): PTPE FLOW - 2.49 CFS PIPE DIAMETER =�8.Dfl iNCHES PIPE LENGTH = 43.25 FEET MANfVING'S N= 0.p1304 SF=IQ1Ky**2 =(I 2.99)/{ 105.000})t�2 � D.Od055 HF=L*SF = { 43.25J*{Q_p0056} - 4.p24 NODE 2dp�.20 : HGL =� 397.Q24>;EGL= < 397.055>;FLdWLINE= < 392.330> * # * * � * * * * * * # * k * * + i * M * k * * � # * * # w f # # * * f * � * t * * * # * * * * # � � * * * r + * * * # * � * * * * � + * * Y i Y * 1 + i # .FLOW PROCESS FROM NODE 2001.20 TO NODE 2001.20 IS CQDE = 8 UPSTREP�M N6DS 2001.2Q ELEVATION = 392.33 (FLOW IS UNnER PRESSUftE) CALCULATE CA'I'CH BASZN ENTRAPICE LOSSES(LACFCD} : P�PE FLOW = 2.49 CFS PIPE DIAMETER = 18.00 zNCHES FLOW VELOCITY = 1.41 FEET/SEC. VELpCITY HEAD = Q.031 FEET CATCH BASIN ENERGY LOSS =.2*(VELOC7TY HEADj =.2*S 0.031} = 0.446 NODE 20Q1.20 : HGL =< 397.Ob1>,EGL= < 397.Q61>;FLOWLINE= < 392.330> ♦**fs�Y*t*r*y��+,�*++i.**+******xxx�***�x***i�x*wwx**t+*t+trt*ti*�*t*t+W�*i***ti.+ UPSTi3EAM PIPE FLOW CONTROL DATA: NOD� NUMBER = 2001.20 FLOWI�YNE ELEVATION = 392.33 A55UMED UPSTREA�i C013TROL HGE� = 392.93 FQR DpWNSTR.EAM RUN ANALYSIS END QF GRADUALLY VARIED FE�OW ANALYSIS ^ �^^^� . � • . � Y Y i 2 Y Y Y Y t t i f * � � 1 * * M * � i � � k w i * * * * * * # i f i k * � * * * � * * * * * * i 1 4 � w � # * i f f f * f * * * * k * fi * ? * ! i i PIPE-FLOW 4�YDRAULICS CQMPUTER PROGRAM PACKAGE ;Reference: I,ACPCD,LACRD, AND OCF�iA HYDRAULICS CRITERION} Sc1 Capyright 1982-2002 Advanced Engineering Software (aes} Ver. 8.4 Release Date: O1/O1/2002 License ID 15fl9 Analysis prepared by: Proj�ctDesign Consultants 701 a Street, Suite 80D San Diego, CA 92101 *+"*"`+t*��*"�*"'�`�"**�`* 1?ES�R�PF'I�N QF STUi7X *�*Yrk�M***tti*f*Yfi*t*yYtfY * BRESSI RANCH - i1LTI2dATE CONf1ITIONS * * SYSTEM 20d0 LATERAL 4(N0.7 PER SHT. 9 DWG NO. 400-$D} * "` 100-YEAR STORM EVENT * # i�k Y� i� Y� * i� * kYrYrYrYr}1� tktkYr�k*# t*##tYY**YY*YYft f Y Y*Y # YtYY t yr f Y{ *****!! /r!r* �r*YrYr*Yr k f Y� f• FILE NAME: P2D00-4.DAT TIME/DATE OF STCTDY: 16:01 12/23/2002 f t! # 4 Y fY } 3�}y}+4iF�Y y��# ty yr**�h Y� Y� *f *YrYrri }*i� Yrf k* f* rtY,YriF*Y *yri** f i* YY**iF**f+f �L# W y�iF*ii Y4 GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POINT STRTUS TASLE �Nate: '*' indicates nodal point data used.) UPSTREAM RUN bOWNSTREAM RL7AI NODE MODEL PRESSURE PRESSllRE+ FI,OW PRESSURE+ NUMBER PROCESS HEAD {�) MOMEN'PUM ( PQUNDS } pEPTH ( FT j MONfEt3TUM ( POUNDS } � 2005.10- Q.83 34.23 D.40* 35.26 } FRICTION 2005.20- 0.60*Dc 26.53 0.60*Dc 28.53 ) cA�cH sAszrr 20D5.20- 0.87* 15.25 0.60 Ac 7.0.23 ------------------------------------------------------------------------------ M.a.XIMUM NUMBER OF ENERGY EALANC�S USED IN EACI-E PR4FII,E = 25 ------------------------------------------------------------------------------- NO'f'E : 5TF�1DY FLOW HYI7RAULTC HEAD-I,OSS C4MPUTA'I'IONS BASED ON 7'HE MOST CONSERVATIVE FORMUT.,AE FFtOM THE CURRErPI' %ACRD, LACFCD, AND OCEMA DESIGN MANUALS. �.**.�+�.***.�,�..�**++****..*,..,..�*..****�**.*«.�***+**+*.�.�w�s**t*�++�v�.�..** DOWNSTREANF PTPE FLOW CONTROL DATA: I30DE i�FL7MBER = 2005.Z4 FLOWLINE ELEVATION = 408.29 PIPE FLOW = 2.49 CFS PIPE DIAMETER = 16.00 INCHES ASSUMED DOHaNSTREANi CONTROL HGL = 4D9.120 FEET ------------------------------------------------------------------------------- NODE 2045.10 : HGL =< 408.b94>;EGL= < 409.347>;FLOWLINE= < 408.290> **+******�**��++*+,,��*w.*wt***�****+***+..�*+..*.*..**.�****t*�*�.�,�*�.�*�*�,.* Fi�OW PROCESS FROM NODE 2005.1D TO�NODE 2005.20 I5 CODE = 1 UPSTREAM �]ODE 24a5.2fl ELEVATION = 4Q9.33 (Fi�OW �S SLIPERCRITICAL} ------------------------------------------------------------------------------ CALCULATE FRICTION LQSSES;LACFCD}: PIPE FLOW = 2.49 CFS P�PE DIAMETER = 1B.00 INCHES PIPE LENGTH = 43_25 FEE'i' MANNING'S N= 0.0130a NORMAI� DEPTH(FT} - 0.4Q CRITICAi., DEPTH(FT} = 0_60 • UPSTRE7IM COId'I'ROL ASSUMED FLOWDEPTH (�'TI = 0. 6d � --G12.ADUALLY VARIED FLOW PR4FILE COMPUTED iNFORMATION: , DISTANCE FROM FLOW DEPTH VELpCT`T'Y SPECIFIC Pi�ESSURE+ � f COhITRpL ( FT ) ( F'I' ) ( FT/ SEC ) ENERGY ( FT j MOMENTUM ( POUNDS } 0.000 D.597 3.792 0.821 28.53 D.011 0.5B9 3.862 D.821 28.54 0,047 0.581 3.934 0.822 28.57 O.lOB 0.573 9.408 0.823 28.61 0.199 0.565 4.085 0.825 28.67 . D.323 0.557 4.165 0.$27 28.76 0.482 0.599 4.246 0.830 28.86 O.b83 D.�41 4.333 0.833 28.98 D.928 0.533 4.422 D.837 29.12 1.225 Q.525 4.515 4.842 29.29 1.581 0.517 4.611 4.947 29.48 2.445 Q.509 4.713 0.854 29.7tl 2.507 0.501 4.815 0.861 29.93 3.100 0.493 4.923 D.869 30.20 3.801 0.4B5 5.436 0.879 30.49 4.632 0.4�7 5.i53 O.B$9 30.$1 5.621 0.469 5.275 0.90i 3�.17 6.806 0.461 5.403 0.414 31.55 8.242 0.453 5.537 0.929 31.96 10.409 0.445 5.676 � 0.945 32.41 12.227 0.437 5.622 fl.963 32.90 15_109 0.929 5.975 0.983 33.43 19.d25 0.42� 6.135 1.Qa5 33.99 29.858 0.412 6.303 1.030 34.5� 35.383 4.404 6.479 1.057 35.26 43.250 ------OT404 --`-Y5-480----------1_057-'-Y--------35_26----- . TNODE` 2005 20 HGL =< 409.927>;EGL= < 410.151>;FLOWLII3E= � 409.330> *.****�*��***�+.,�w+�+�,..,.«..****+****�**++�tt��*.+++**�+**«*+*+*t***�*.*w*�++w FLOW PROCESS FROM A30DE 2005.20 TO NQDE 2d05.2p IS CODE = 8 UPSTREAM NODE 2005.24 ELEVATIOTI = 409.33 (FLOW IS SUBCRTTTCAL) ------------------------------------------------------------------------------ CALCULA�`E CATCI-I BASIN ENTRANCE LOSSES(LACFCDj: PTPE FF�OW = 2:49 CFS PIPE DIAf�SETER = 18.04 INCHES FLOW VELOCITY = 3.79 FEET/SEC. VELOCITY HEAD = 0.223 FEET CATCH BASIN ENERGY LpSS =.2*(VELOCITY HF�D) _.2*( 0.223) = 0.045 NODE 2005.20 : HGL =< 410.196>;EGL= < 910.196>;FLOWLII3E= < 909 330> T^ tr++***ft�**rr**r�rw�i�*i��*****+*rri*+++**y+*:f�r�r�ft+*w*w+*r**rti***s*r�rtit****,r*,t C3PSTREAM PIPE FLOW CONTROL DATA: I+FODE NUMBEi2 = 2045.20 FLOWT.,TNE EL�7ATION = 949.33 ASSUMED UPSTRF..At�7 CONTROL FfGL = 4D9.93 FOR DOWNSTftEAM R[TN ANALYSIS --------------------------------- END OF GRADUALLY VAI2IED FLOW ANALYSIS � � * * * * t * * * # * # i i Y * Y Y M # i # # � * # f f � f * f * * * f * * * # * * * * * * * * * * k ti � i * # i * * * Y * * w k * * * # t * � # # R * * t * PIPE-FLOW HYDRAULICS COMPUTER PROGRA3�f PACKAGE (Reference: LACFCD,LACRD, AND OCEMR HXDRAiTLICS CRITERTONj (c) Copyright �982-2002 Advanced Engineering Software (aes) Ver. 8.0 Release Date: O1/D1/2002 License ID 1509 analysis prepared by: ProjectDesign Consultants 701 B Street, Surte 800 San Diego, CA 92101. *****+*��****«wa*t++**+*** DESCRIPTIOi+I QF STUDX *w***�++r*�**,r,r+*�*�+�*++* * BRESSI RANCH ULTIMATE CONDFT�QNS * * SYSTEM 2000 LATERAI� 5(N0. 8 PER SHT 9 OF DWG N0. 4D0-9D) * * 100-YEAR STORM EiIENT * +.,**:ti.*t...�:t�.*+�*,.,..,.*.***�*.*.*�*.�.***+�+**.v.�**+***,.*++*tt�+�**.+��t FILE IdAME: P2000-5.DAT TIt�f�/AATE QF STLTDY: �6:06 12/23/2002 i� *�k Y� Yrk �M Yr Yr k*1*****Yr�Y t�Y Yf �f ik iY #*iif*t## #**#}*f*iYr*Y� Yrk Ir* tt f y fyr�Jr# *i� i� * iF *YrYr}Yr}fY� * iFf * ik GRADUAI,LY VARI�A FLOW ANALYSIS FOR PIPE SYSTEM NODAL P�IN'I' STATUS TABLE (I3ote: '*" indicates nodal point data used.) UPSTRF.AM RUN DOWNS'I'AEAM RUN NQDE MOAEI. PRESSURE PFiESSURE+ FLOW PRESSURE+ NUMBER PROCESS HEAD ( FT) MOMENTLibf ( PpUNDS J DEP�`H S PT) Mp2+SFNT[)M ( POiINDS ) • 2a0S.50- 0.83 34.23 Q.26* 59.51 } FRiCTION 2D05.6fl- 0.60*Dc 28.53 0.60*Dc 28.53 } CAi'CH BASTN 2005.b0- 4_87* 15.25 0.6D Dc 10.23 ------------------------------------------------------------------------------- MAXIMt7M NUMBER OF �NERGY BALANCES USED IT3 EACH PROFILE = 25 NOTE: STEADY FLOW HYDRAULIC HEAU-LQSS CO[�4PUTATIONS BASED ON THE MOST CONSERVATIVE FORI�F{3LAE FROM THE CUR32�NT LACRA,LACFCD, AND OCEMA ]�ESIGN N3AiJIJALS . ikikiA'Yr'k'k*rt'kYr'k1� tk * * * �k f 1�! �kf f i}*** * * * # i�* *#!r*#�k Y� iF iF kYr�M Yr **** f � �Yfi * * * * k f * *yr****t �**** t* DOWi�ISTRF�M PEPE FLOW CONTRO� f]ATA: NODE NUMBE�L = 2dQ5.50 FLOWLINE ELEI7ATIpN = 448.29 PIPE FLOW = 2.A9 CFS PIPE DIAMETER = 18.00 INCHES ASSUMED DOWNS`i'RF�M CON'i'ROL HGL = 409.120 FEET -----------------------------------------------___--__--------------__�-_--__---- NQDE 2005.50 : HGL =< 408.552>;EGL= < 410.806>;FLOWLINE= < 4D8.290> Yr}*i� Yi?Yr�kY� *Y�kYiFirkk**�1� #Yrlik�k�i *i�*#t#*i�*#f*f*#**YrMY�kkYrYrtk*�*�4�k�k*��***i ***Yr*riYr* fY��lr * FLOW PROCESS FR4M PFODE 2Q05.5Q TQ NODE 2005.6Q iS CQDE _ � UPSTREAM NODE 2005.60 ELEVATION = 410.35 {FLOW IS SUPERCRITICAL) ----------------__------------------------------------------------------------- CALCULATE FRICTION LOSSES(LACFCD): PxPE FLOW - 2.49 C�'S PXPE pzAMETER = 18_00 INCHES PIP� LENGTH = 5.25 FE�T 2+�ANNING'S �7 = 0.01300 -----------------------_---------------------------___------------------------- � NOR3+IP.L DEP7'H[FT) = 0.20 CRITICAL DEPTi�i(FT) = 0.50 ------------�__--__------ • UPSTR.F_.AM CONTROL A5Si.7MED FLOWDBPTH { F"I') = 0. 64 � --GRADUAL,�,Y VARIED FLOW PROFILE COMPUTED II3F'ORMATIpI+I: DISTANCE FROM FLOW AEPTH VELOCITY � SPECIFIC FRESSURE+ CO1dTROL ( F'!' } • { FT ) { FT / SEC ) ENERGY ( FT ) M�MENT[3M ( POL7ND5 } O.ODO 0.597 3.792 D.82i 28.53 0.002 0.582 3.932 0.$22 28.56 D.409 0.556 4.082 0.825 26.67 0.022 0.550 4.242 0.$29 28.85 0.091 0.539 4.4�5 0.837 29.11 O.Ob7 Q..51$ 4.601 0.847 29.96 O.ZQ2 0.502 4.$42 0.860 24.90 0.147 D.48b 5.019 0.877 30.45 0.204 Q.970 5.255 0.899 31.11 0.276 6.954 5_512 0.926 31.89 0.364 0.438 5.792 Q.959 32.80 0.472 0.422 6.099 1.000 33.8b 0.606 0.4D6 b.435 1.050 35.09 D.770 0.390 5.807 1.110 36.51 Q.972 0.375 7.218 1.164 38.14 1.222 0.359 7.574 1.274 90.Q2 1.533 0.343 8.185 1.384 42.17 1.923 fl.327 8.757 1.518 94.64 2.421 0.311 9.4a4 1.685 47.49 3.D55 0.295 10.138 1.892 50.78 3.920 0.279 10.978 2.152 54.60 5.093 0.263 iZ.947 . 2.A$1 59.06 5.250 0.262 12.044 2.5t6 59.51 -------------------------------------------_____------------------------------- NODE 2045.6d : HGL �< 43.0.947>;EG�= < 411.171>;FLOWL,INE= < 410.350> �rs�r*s**r*Y*s��+��i.t****w�****t�wr**�**'*a*w*+**+*f***+�r*rt�**�+*****x**�**�+t • FLQW P3tQCESS FROI� NODE 2005.6Q TO NODE 2005.56 IS CRDE = S UPS'FREAM NODE 2005.60 Ei,EVATIO�I = 410.35 (FLpW �S SUBCR3TICAL? ------------------------------------------------_------------------------------- CALCULATE CATCH BASIN ENTRANCE LOSSES{LACFCT?): PIPE FLOW = 2.49 CFS PTPE DZAMETER = 18.Q4 INCI-iE5 FLOW VELOCITY = 3.79 FEET/SEC. VEi,OCITY HEAD = 0.223 FEET CATCH BASIN ENERGY LOSS =.2*(VELOCITY HEAD) =.2*� 4.223) = 0.095 NODE 200$ . 60 : tiGL =< 411 . 216> ; EGE�= < 411 . 216> ; FLOWLI�TE� < 41 Q. 3 50> ***i�'f{ #'f i# #*1r*1r**i1 iFYrYrYr7r** t* t*�k i�k t*it*t*#t#�kY#f i YY�Y�!! iY i y�} #***f*f *YrYr*ik fr*Yr�kY� Y� Y�YriFk UPSTREAM PIPE FLOW CONTRQL DATA: � NOD� NUMBER = 2005.6D FLOWLINE ELE�IA'i'TQN = 410.35 ASSUMED UPSTREAM C�NTROL HGL = 410.95 FOR DOWNSTREP.M RUN ANALYSIS END OF GR�DUALLY VARTED FLOW ANALYSIS • ! *.***�**t�***.*�*******,��**x�****.***�*}*�,*.*.*.*..****.*��..��.�**,*..*. PIPE-FLOW HYDRAULICS CDMPU'PER PROGRP.M PACKAGE � {Aeference: LACFCD.LACRD, AND OCEMA HYDRAULICS CRITERIO�ii (c? Copyright 1962-2002 Advanced Engsneering Software (aes) Ver. 8.4 Re].ease Date: Ol/O1/2002 License ID 15D9 Analysis prepared by: ProjectDesign Consultants 741 B Street, Suite 800 San Di.ego, CA 92�OZ ****"**•***+••***•*•i+'`"'** DESCRIP'i'ION dF STI7C}Y ��•'*•*•+++++.****+++..**� * BRESSI RA.NCH iTL,TIMATE CONDITIOI3S � * SYSTEM 2046 : LATERAF, 6(NO. 9 PER $HT. 9 OF DWG. 400-9D) � ' 1D0-YEAR 5�'ORM EVENT ' **w++�t+++;*+*�******�*��.��**�***�,.�*�*t��*t*t�*******.*******.v..t�t..**++ FILE NAME: P2000-6.DAT TIME/AATE OF STUDY: �5:10 72/23/2002 *�k1�! * fir*'kYrYr***i� *i'1� # tk'ty Yt t* i*� 1� ih #*# ir*`t*y t**ikY� fi**i**#****'k #�'�'i *tt�i tk tklrYrY� *M3'Y�!#f�k* GRADUALLY VARIED F7�f}W ANAi,YSIS FOR PFPE SYS'I'EM NODAL POINT STATUS TABLE tNote: '*" indicates nodal point data used.) l3FSTfiEAM R[7N DOWl35TREAM RUN AiOD� MODEi PRE55UR� PRESSURE+ FLOW PRE55URE+ NS3MBEf2 PROCE55 I-3EAD(FT) MOMENTUM(POUNDS} DEPTH(FT) MdM�NTUM(POUNDS} 2015.�4- 1.69* 105.37 0.27 15.61 } FR�CTION 2015.10- d.67* 17.56 O.A2 Dc 11.84 } CA'i'CH BASIN 2015.10- a.72* 14.70 0.92 Dc �•3z MAXIM13i�4 ld[3MBER 4F ENERGY SALANCES USE[} IN EACH PROFILE = 25 NOf`E: STEADY FLOW HYDRAl3LIC HF:All-LOSS COMPTJ'I'ATIONS BASED ON THE MpST CONSERVA'FIVE PORMULAE FROf�S THE CUFtAEN'I' LACRi3, LRCFCD, AND OCEMA DESIGA3 MANiiALS . +*t*+x*r**w,r,t***w�*�w*w+*+xwta+*,rw�+i.++*�rfi*+**x*x++**a*+*wy.ra*+*w****Y�t+i+* DOWNSTREAi�7 PIPE FLpW CONTROL DATA: NOQE NUMBER = 201S.a0 FLOWLYNE ELEVA'i'�ON = 935.52 PTPE FLOW = 1.25 CFS P�PE DIAMETER = 18.00 INCHES ASSUMED DOWNSTREAi+] CONTRQI, HGL = 417.2I0 FEET ------------------------------------- AIODE 2035.00 : HGL =< 417.210>;EGL= < A17.218>;FLOWLINE= < 415.520> .*****.***+*�.�wt+.*+*+**..**..**+v.��+++�**,..�.++��w�*******.****+,**+**+* FLOW PROC�SS FROM NODE 2015.Q0 TO NODE 2015.10 IS CQDE = 1 UPSTAEP.I�1 NODE 2015.10 ELEVATION = 416.51 (Fi�OW SEALS IN REACH) CALCULATE FRICTION LOSSES(LACFCD}: PIPE F�,QW = 1.25 CFS PIPE DIAMETER � 18.d0 I�FCHES PIPE LENGTH = 3D.81 FEET I�4ANNING'S N= 0.01300 --------------------�--__----------------� _ DOWNSTREAM CQN'FROL ASSUME3� PRESSURE HEAA(FT] 1.59 ------_ ___ � --PRESSURE FLQW PROFILE COMPiJTED �NFORMATION: BISTANCE FROM PKESSURE VELOCITY SPECIFIC PAESSURE+ � CON�ROLIFT) HEAD(FT) {FT/SEC1 ENERGY(FT) MOMENTUM{POUNDS} O.ppp 1.b96 0.707 1.698 1Q5.37 5.939 1.500 Q.707 1.50B 84.42 ------------------------------------------------------------------------------ NORMAL DEP`I'H ( FT) = Q. 2 6 CRITICAL DEP'I'H I FT j= 0. 42 ----------------...._____-- ASSiJi+]ED DOWNSTREAM PR�SSURE HEAD(FT) = 1.50 ----------------- GRADiDALLY VARIEE? FLOW PROFILE COI�PUTED INFORMATION: DISTAPICE FROM FI,OW DEPTH VELOCITY SPECIFIC PRESSURE+ CQNTRQL(FT) (FT} (FT/SEC) ENERGY{�} MOMENTl36f(POUNDS) 5.939 1.5fl0 �.707 1.508 84.92 7.287 1.457 0.713 I.455 79.67 6.632 1..413 0.724 1.422 75.00 9.973 1.370 0.738 1.379 70.42 11.3�2 I.327 0.756 1.336 65.94 12.b99 1.289 0.776 1.293 61.58 13.984 1.240 O.B00 1.250 57.36 15.315 1.�97 0.826 L 208 53.27 15.644 1.154 0.857 1.165 49.33 17.968 1.111 Q.891 1.123 95.55 19.289 1.067 0.929 1.OB1 41.93 20.604 1.024 0.972 1.039 38.49 2�.913 0.9B1 1.02Z 0.997 35.22 23.215 0.937 1.476 0.955 32.13 24.507 0.894 1.138 0.914 29.23 - 25.788 0.85� 1.208 0.$74 26.52 27.453 0_808 1.288 0.833 24.0� . 2B.300 0.769 1.381 0.794 21.70 29.521 0.721 �.487 0.755 19.66 30.748 Q.b78 i.611 4.718 17.72 30.810 Q.b74 t.623 0.715 17.55 ------------------------------------------------------------------------------ NODE 20i5.10 : HGI, _< 417.164>;EGL= < 417.225>;FLOWLINE= � 415.510� �rry,*yt*rw*tt*i�x�x*wt�it*t****�r*wY*v.**rtt*ttyaaayi+rtx+�*w**,rw*wfs*rs*Yf***�r*** FLOW PROC�SS FROM NODE 2015.10 TO NODE 20�5.10 IS CODE = 8 UPSTR.F.RM NODE 2015.10 ELEVATION = 41b.51 (FLOW I5 SUBCitITTCAL) CALCiJE,ATE CA�`CH BASTN ENTRANCE LOSSES (E.ACFCD) : PIPE FLOW = 3.25 CFS PIPE DIA�7ETER = 18.00 I�JCHES FLOW VELOCITY = �.62 FEET/SEC. VELOC�TY HERI? = 0.041 FEET CATCH SASIN Ei3ERGY �.OSS =.2*[VELOCITY HEADf =.2*I 0.041} - fl.008 ------------------------------------------------------------------------------ NODE 2Q}.5.10 : HGL =< 417.233>;EGL= � 417.233>;FLOWL�NE= � 416.510> f i#iF* f'k�kiF*#}# Y� i�#**YrYc# *** t#*f1 �i 1�L4ti *�ktt*1� �Fir}� f i i� **** * i� wiF�kYr*#*t f i k! # i i* 14*f f! �kti UPSTREAM P�PE FLOW CONTROL DATA: f�10A� NUMBER = 2015.�d FLOWLINE ELSVATION = 416.51 ASSUMED UPSTREAM CONTROL HGL = 416.93 FOR DOWNSTREAI�f R[)N ANALYSIS ----------------- END OF GFtA,DiJALLY VARIED FLpW ANALYSIS . � APPENDiX 4.1.8 SYSTEM 3000 (`D' STREET AT EL FUERTE) i • • Y** i f Y t w� 4 r t* w* i* f ** rt* 4 t i i� i i* f x f fi**# R x� t�+� i� x� f rt* k f* k k*�* w# t t Y t** k Y t Y f Y i i y i PiPE-FLOW HYDR.AULTCS COMPUTER PRbGRAM PACI{AGE � �Reference: LACFCD,LACRD, A23D OCEMA HYDRAULTCS CRITER�OI3i ' � {c) Copyright 1982-2001 Advanced Engineering Software {aesi Ver. 8.0 Release Date: O1/OZ/20D1 License Ip 1509 Analysis prepared by: PROJECTDESIGPI CONSULTANPS 701 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 519-234-0349 • �ttYrYyi*y#1l1�Y�*#1t�Y�Y�#ftY�1t DESCRIPTION OF STUDY +*••"**•"+**t++*..*�+.*.** * BRESSI RANCH - ULTTMATE CONDITiODIS * "� SYSTEN4 3040 � * 100-Y� STORM � ***.w..��v.*,r�*w+�„r+*t*ww+***v,+**�,.*��x**v�«*,..*.wx««+...*+*+**t�+++*.+*+*+�.. �zz�� r�r�: P3ooa.DA� TIME/DAmE OF STUDY: 15:06 09/2fi/20D2 xxw*w�*******+**++**+*+frwrrt*+ww**++++�+*+**r*tsy**�rrr*tii**rytt+r**+�+r+r�t♦ GRADZiALLX VARIED FI,pW ANALYSIS FQR PIPE 5Y5TEM I30IlAL �OYNT STATUS TABLE {Note: '*" indicates nodal point data used.� UPSTREP.M RUN DC?WNSTREAM RUN NODE MO17EL, PRESSUFtE PRESSiiRE+ FI,pW pRESSURE+ NUMBER PROC£S5 HEAD(FT) t�40MENTUM(POUNDSj DEPTT-i(FT) MOMENTUM(POLTNDS) 1QD6.OD- 8.65* 905.52 6.46 138.12 H1.74 • 1006.50- 3.94* 35i.75 0.67 Dc f3.43 t+SA}CIMLiM NUMBER OF ENEi3GY B71L.�NCES USED IN EACH PROF�i�E = 25 ------------------------------------------------------------------------------- i30TE: STEAbY �'LOW HYDRAULIC HEAD-LOSS COMPL7TATTONS BASED ON THE MOST CONSERVATIVE FdRMULA£ FROM THE CURRENT L�ACRD,LACFCD, Ai�TD OCEMA DES�GN MAt+n7Ai,5. *+tti***W*ry,�wtaaxrwa�**wx*+*+t�s+r++**.�1.+*++w*�****�****w******r***w:*wxx,rw*sw DOWNSTREAr7 PIPE FLOW CONTAOL DATA: NODE N[.iM.HER = 1046.00 FI,OWL,�NE ELEVATION = 365.25 PIPE FLOW = 5.60 CFS PIPE DIAMETER = 18.D0 INCHES ASSUMED DOWNS�'REAM CONTROi� i3Gi� = 394 .$00 FEET -------------------------------------------------------------------------------- NODE 1006.00 : HGL =< 344.90D>;EGL= < 395.056>;FLOWLIidE= < 386.250> ) FRICTION 1006.30- 5.20* ) JUNCTIQN 1006.�0- 5.19" ) FRTCTIQN 1006.50- 3.88� ) CATCH $ASIN 529.95 499.92 355.97 0.91 Dc 4.34 a.67 Dc 55.06 37.82 *+***rx*y****t+++**+**++**+****r**x**+*rar+ryt*++ti*+y****r�ts�r***y**rt***+tr� FLOW PRpCESS FRaM I30DE 1p05 . DD 'i'0 �IODE 1D06 .30 �S CQDE = 1 UPSTREAM NODE ia06.30 - ELEVATION = 389.85 �FLOW IS UNDER PRESSUREJ CALCULATE FRICTION L05SE5(LACFCB): PIPE FLUW = 5.60 CFS PIPE DIAFIETER = 18.00 INCHES PIPE LENGTH = 52.33 FEET MANNII3G'S N= 0.0�300 SF=(Q/K}**2 = {( 5.60)/f 105.099}1**2 - D.Q0284 HF=L*SF = ( 52.33)*(D.002$91 = 0.149 NODE 104b.30 : HGL =< 395.449>;EGL= < 395.2D5�;F'LOwLINE= < 389.850> +*+�++.***.:�*.*.**.**+t******.***�.**��**..w*.�,�.twt.f*.***�*..w**+f*+.�,��..* FLOW PROC£SS FROM NOAE 30D6.30 Tp I30DE 1006.40 IS CODE = 5 UPSTREAM I�QDE 1006.40 ELEVATION = 390.18 IFLOW IS L7NDER PRE55URE) CALCCTLA'I'£ .7UNCTION i,O55E5: PIP� FLOW DIAI�SETER ANGLE FLOWLIbiE CRITICAL VEI,C7CITY � (CFSj (TNCHES] {DEGREES} ELEVATIpid DEPTH{�'�'. ) (F'T/SEC) ' UPSTREAM 3.10 18.00 90.D0 390.18 0.57 1.754 D04JNSTREA2� 5.60 18.00 - 389.85 0.91 3.169 LATERAL #1 2.50 18.00 90.4D 390.18 0.60 1.415 L�ITERP.L #2 0. DO 0.00 0.00 4.00 0.00 �.000 Q5 O.Oa===QS EQUALS HASTN ZI+�PUT=== LACFCD A3�Ii? OCEMA FLOW JiJNCTION FORMi.Ti,AE USED: . AY=(Q2*V2-Q1'V1*COS(DEi,TAl}-Q3*V3*COSIDELTA3]- Q4*V4*�C05{DELTA4})/((A1+A2)*16.1)+FRICTION LQSSBS UPSTREA1+f: MANNING'8 N= 0.013�4; FRICTION SLpP� = D.D0087 Dt?WNSTP.EAM: MANNING'S N= 0.41300; FRICTION SLOPE = D.60284 AVERAG£D FRICTION SLpPE 3N JUNCTION A5SiJ3dED A5 0.003$6 JUNCTION LENGTH = 4.D0 FEET FRICTION I.,OSSES = 0.007 FEET ENTRANCE LOSSES = 0.000 FEET J[JNCTIpN LOSSES = (DY+}IVi-HV2)+(ENTRAf10E LOSS£S} JUNCTION LOSS�S = i 0.211j+f D.000} = 0.211 ------------------------------------------------------------------------------ NODE 1006.44 : HGL =< 395.368>;EGL= < 395.4�6>,FLOWLINE= � 390.180> ♦**�**xwy�*wy*+*rrrr*rrrir**�rsr*r**rs�r+wxwxtw+x�,rx+*s*t*+*y*******tt*rts***t*r ' FLOW PROCESS FROM NODE 1006.40 TO NODE 1046.50 IS CODE = 1 UPSTREAM NODE i0p6.5D ELEVATZON = 391.49 (FLOW ?S UNDEFt PRESSCTREj . CALCULATE FRICTIODI L055E5[LACFCiI): PIPE FLpW = 3.10 CFS PiPE DIAMETER = 38.D0 INCHES PIPE LENGTH = 5.25 �'EET MPNNING'S N= 0.�1300 S�'=I¢/K}**2 - (( 3.10}/( 104.98311**2 = O.DOa87 H�'=L*SF = ( 5.25}*{0.00067) = 0.405 -------------------------------------______-_---------------------____-_____-_-_ NODE �406.5D : HGL =< 395.373>;EGL= < 395.A20>;FLOWLINE= < 391.490> � � » t+rrxrs*rx*,r�***w*w*xxw*x*****w*wwtw******tvrxr*yr+**:+*+rtrtrxx�*+x**e***,rw FLOW PROCESS FROM NODE 1D06.5a Tp NQDE ].006.50 IS CODE = 8 UPS�`REAM NODE 1DOb.50 ELEVATION = 391.49 {FZ,pW I5 T3NDER PRESSiTRE) CALCi3LATE CATCii SASIN ENTRP.NCE L(?SSES (LACFCD) : P�PE FLOW = 3.10 CF5 PTPE DIAMETER =�8.00 INCHES FI,OW VELOCITY = 1.75 FEET/SEC. VEL,OCiTY HEAD = 0.048 F�EI' CATCH $ASTPI ENERGY LOSS =.2*(VELOCITY HEAD} =.2*( p.D981 = 0.01Q ----------------..________________________------------------------------------- NODE 1446.54 : HGi, _<_395.430>;EGL= < 395.430>;FLOWLINE= < 391.490> tr�k�k* M�k## *!�I***�F4 yry� *tt *%'f tt'F tk* tt'F Y�kY� *�4�r1 y� �Y**t/*Yc* k YrYrlrYryrlr** *Yrt #1Y�Y #Yf *Y � f# f itt*tyr* UPSTR£AM PIPE FLOW CODiI'ROL DATA: NODE 13U23BER = 1 p 0 6. 5 0 FF,CfWi�INE ELEVATION = 3 91 . 4 4 ASSUMED UPSfiREAM CON'TROL HGL = 392.16 FQR pOWNSTF2EAM RiJN ANALY5I5 _______=-==�T «__��_=_=��_�__�«��____________________�,t�_=�,�,�-�«-_� E� OF GRADUALLY VAFtIEi] FT,OW ANALYSIS • xt*wt.+>**rx*.+**+y.r**ratr+�<..w.**rw*xy**x*yr*+rar**w*rx*+xx+t*.�r•*x.:r.*.r PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACICAGE � (Reference: LACFCD,LACRD, AND OCEMA HYDR.ALTi�ICS CRITERION) ' {cj Copyright 1982-2401 Advanced Engineering Software (aes} Ver. 8.0 Release Date: �1/O1/2001 License xn 1509 �+nalysis prepared by: PAOJECTbESIGN CONSULTAN'I'S 7U1 'B' STREET, SiJITE BDO SAN DIEGO, CA 42101 619-234-0349 �v.**��*****x***�+*w*****� DESCRIPTION OF STUDY *+*x�*******r***«***r++**� ' BRESSX RANCH - LTLTIN9ATE CONFITIONS * * SYSTEM 3000 - T�ATERAL * ' 100-YEP.�t STpRi�7 * ♦wx**w***+aw*+**�r*++*att:yxk*tttrtf**++*xrt*trt*�*rx*r***x**t***+a*+�*r�• FIiE NAME: P3DOOL.DAT TII�3E/DATE dF STUDY: 15:07 09/26/2002 **�***.+**v.w+*********+*.***�**+*+***�**�+�****..*«+..t.**.�.**...>*..r�++w+..,. GRADUALLY VARIED FLOW ANALYSIS FQR PIPE SY5'I'EM NODAL PtIINT STATUS TABLE INote: "*" indicates-nodal point data used.) UPSTREAM RUid DOWNSTREAM RUN NODE MODEL PRESSURE PRESSURE+ FL�C?W PRESSUAE+ Nt7MBER PROCESS HEAD ( FT) MOMENTUM ( POUNDS f DEPTH { gm } MOMEN'T'UM I POUN]?S } 1406.80- 5.19* 496.45 4.37 3B.64 } FRICTION 1d06.90- 3.7�* 332.65 0.60 D� 28.68 . _}-CATCH BASIN ^_3006_90- ----------3-�¢*------------329_90^,------Q`60-Dc-----------10_2$+ MAXIMUM NUMBER OF ENEi2GY SP.LAidCES iJSED IN-EACH PROFILE = 25 -------------------------------------------------------------------------------- NOTE: STEADY FLOW �iYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVA�`IVE FORMULAE FAOM THE CURRENT LACRD,LACFCD, ANp OCEMA DESEGN MP.NUALS. � +*.*+**t*.***wv�.+..+*w*+*++*�v.*�++.+�**�*+***x..«««.*+**++x***.�**t++**�..*... DOWNSTREAM PIPE FLOW CONTROL DATA: I30DE NUMBER = ].005.80 FiAWE�INE ELEVATION = 34d.18 PIPE FLOW = 2.50 CFS PTPE D3AMETER = 18.00 INCHES ASSL32�EI? DOWNS'iREAM CONTROL HGL = 395.370 FEET 3dODE 1Db6.80 : HGL =< 395.370>;EGL� < 395.441>;FLOY7LINE= � 390.1$0> �F tY *Yrti 44 iF i�Ktk1�! Y• iFiFYr N 1rYrYr YrYr} *Y� k ri*Yr iFik*Yrf Yr Yr1rYrY� Yr** * f f Y i f* t*ik f�t }*it�lr#Y�* *�/�ki4f *f W+�li FLOW PROCESS FRQM NODE 1006.80 'T'0 NObE �406.90 I5 CODE = 1 UPSTREAM NODE 1006.90 ELEVATIOt�i = 391.64 (FLOW IS UNDER P�SSi7RE) CALCULATE FRICTIpI3 LQSSE$(LACFCDJ: PIPE FLOW = 2.50 CFS PIPE IITP.METER = 18.44 Ii�ICHES PTPE LENGTH = 43.25 FEET 2+4ANNING'S N= p.Q1304 SF=(Q/K)**2 = (( 2.5D1/f 1D5.027}}**2 = D.00057 HF=L*SF = ( 43.25)*(D.00a57) = Q.�25 ----------------_________________..-------------------------------------------- NODE 1D06.94 : HGL = � 395.395>;EGL= < 395.425>;FLOWLINE= < 391.644> >:.w...*.w�.....*...«+...tw*..«.*.�.**�.+*:t*..*�ti.�,..�+.*.�.....+�,�.*+,.*..*.* FLOW PROCESS FROM NpDE 100fi.90 TO NODE 1045.9D IS CODE = 8 UPSTREAM NODE 1006.90 ELEVATION = 391.59 (FLQW IS UNDER PRESSURE} --------------------------------------------------------------�--- • CALCUi�A'I'E CATCH $ASIN £NTRANCE LQSSES(LACFCD): PIPE FLOW = 2_5a CF9 PTPE DIAMETER = 18.00 YNCHES FLOW VELOCITY = 1.42 FEET/SEC. VELOC3TY HEAD = D.031 FEET CATCH BAS�N ENERGY LOSS =.2*(VELOCITY HEAF}j =.2*( 0.03�} = 0.006 NODE lOD6.90 : HGL =< 395.432>;EGL= c 395.432�;FLdWLINE= � 391.690>"`+ � ♦�******.swrw*>+*+x*w�*xf*xrw.ixxs�x�*x�**Rx**x*y*rr*x+>sw***x*xwr++rww**w*s*� UPSTREAM PIPE FT,OW CON'I'RQL DATA: NODE NUMBER = 1d06.9p FLOWLFNE ELEVATION = 391.69 ASS[]MED UPSTREAM CONT'ROL HGL = 392.29 FOR DOWNSTREAt+I RUN ANALYSIS ____....-------------- END OF GA,ADUALLY VARIED FLOW ANALYSIS � � • � APPENDIX 4.1.9 SYST'EM 4000 {�C' STREET AT EL FUERTE) � � • ��*w�»****..****�.**.*>*...*.*�**.*..*.*�,.,.*.*«*.*�**��*.��..�,��*******.* PIPE-FLOW i�iYDR.AUI.ICS CbMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION) ic) Copyright 1962-2041 Advanced Engineering Software {aesl Ver. 8.0 Release Aate: 41/O1/2001 License ID 1509 AnaZysis prepared by: PROJECTDESIGN CONSULTAN'f5 701 'B' STREET, SUITE 800 SAN DIEGO, CA 921D1 619-234-D349 *****..s*+tv.*t+.�w:�w,.«..� DESCRIPTION OF STL3DY •"'«�**+**++**+********+*+* * BRESS� R�NCH - ULTIi�1ATE C033DiTI0N * "` SYSTEM 4000 - GARAENGATE ROAD * * 10 0 -YEAR STQRt+S * w*ww*rs*t*r****.t*x**r******x►*yrtr***s�xtyt**r+r**�r►�xw*rt�xwww*�*ww*ww*x• FILE NAME: P4000.DAT TIME/DATE OF STUDY: 16:21 09/26/20D2 ♦*ti�*ar�rstw*+�,r**�w*,rx*ww++x*+wx***�*,r,r�s*wxw**wwrt,***ssttr*ryyr*rtsi**rt***rtx**r GRAUUALLY VARIED FLOW ANALYS�S FQR PIPE SYSTEM AIODAL POINT STATUS TABLE (Note: '*• zndicates nodal point data used.f ' UPSTAEAM RiJ3�1 DOWNSTRE.�hf RUN N0�1E P40DEL PRESSURE PRESSURE+ FI,OW PRESSURE+ NUMBSR PROCESS HEAD(Fi`) MOMENTUM(�OUNDS) DEPTHfFT) MOMENFUM{POUNDS) • 4000.00- 8.�6* 2734.44 1.64 i055.88 } FRICTI013 4000.50- 7.92* 2672.83 •1.b2 1064.70 } FRICTION aaos.ao- �.��* 2546.84 1.53 �110.02 } JUNCTION 40D1.70- 6.96* 1820.14 1.28 iD38.07 ) FRICTION 4001.90- 5.A4* 1521.27 1.67 �247.02 ] FRICTION-rBEND } FiYDRAULIC JUMP 4002.00- 4.40 1316.79 0.69* � 2135.9�7 } 34ANHOLE ' 40D2.14- 4.16 1270.39 0.68* 2169.69 } FRICTION - 4002.50- 1.90 Dc 840.53 1.58* 88b.76 } MAI3HOLE 40fl2.51- 1.9� Dc 84D.53 1.77* 847.56 } FRICTIpN 4a42.52- 1.40*Dc 840.53 1.90*Dc 644.53 } CATCH BAS�N 4002.52- 3.97* . 582.56 i.90 Dc 175.73 ----------------------------------�---_-___-_---------------------------------- MFLXIP3i7M NLTMBER OF ENERGY BALP.NCES USED II3 EACH PROFILE = 25 NDTE: STEADX FLOW HYDRAULIC HEAD-LOSS COMPUTA'FIONS BASED ON THE MOST CO3dSERVATIVE FQRMUL.�E FROM THE CURRENT LACRD,LACFCD, AND OCEMA DESIGN IrfANUALS. ***wr*r+*�rt+*+t+w+***wrr**r�*rrtr*ry,r*rrar��*++***+*+**,r*,wr**rx*****t,***+x►*� DOWNSTitEP,M PIPE FE,OW CONTROL DATA: NOI3E NUNffiER = 4400. DD FLOWLINE ELEVATIOI3 = 336.70 PIPE Fi,OW = 39.94 CFS PIPE DIAME�'ER = 30.40 INCH£S � • ^-ASSUMED_DOWNSTREAM CONTROL HGL = 344.760 FEET NODE 400Q.Op : HGL =< 344.750>;EGL= < 395_786>;FLOWLINE= < 336.700> ! Y ► # t * * f * � * r * * rt * R * f * * f f * * � * * f � * # * * t y * * * * * f * } * * * * � M k M * # * * � * * # * Y # * * i Y f * * ► M Y # t * * f F�OW PROCESS FROM NODE 4000.00 TQ NpDE 4pDD.50 IS CODE =� UPSTREAM NODE 4000.50 ELEVATION = 337.08 (FLOW IS UNDER PAE5Si7i3E} CALCULATE FRICTION LOSSES{I,pCFCD}; PIPE FLOW = 39.90 CFS PIPE DIAMETE}t = 30.OD INCHES PIP� F,ENGTH = 25.B0 FEET MP.NNiNG'S N= Q.613Q0 SF={Q/Kf**2 = (( 39.901/f 9].0.169??*"'2 = 0.0099fi HF=L*SF = ( 25.80j�'{O.a0946) = 4.244 NODE 4000.50 : HGL =< 345.044>;EGL= � 346.030�;FLOWLINE= < 337.08D> .rry.**�iw+*+**w�w+*+*w*rt*rxwyk*+*�+sw**w+rt+*+*r*wix**rxr+***r*ytrt►tr**i��***r♦ Fi,OW PROCESS FROM NODE 4000.50 TO ?dODE 4001.00 IS CODE = 1 UPSTREAM NODE 4041.00 ELEVATION = 338.20 SFLOW IS UNbER PRESSUFtE1 CALCUi�ATE FRIC'T'ION T,OSSES (LACFCD} ; PIPE FLOW = 39.9D CFS PIPE DIAi�fETER = 30.40 INCHES PIPE LENGTH = 74.68 FEET MP.NSIING'S N= U.01300 SF={Q/K1**2 = (( 39.901/f 910.174}}**z = p.40945 HF=L*5F = ( 74.88)'{0.00946f = 0.709 � NODE 4D01.00 : HG� _< 345.713>;�GL- < 346.739>;FLOwLINE= < 338.204> ♦w � w*ww}xa �1r7rr*iri. y.t x* y �-*i x++y**+*w+f w# tir+ic r f t* r f* r r yr'*Y�w+wY�+wy1. s+*+*# ##trt *� #ariti. FLOW PROCE55 FROM N�DE 4001.00 TO NOA�. 4041.7b IS CODE = 5 .` UPSTRE.�M NODE 4001.70 ELEI/ATION = 338.72 (FLOW iS iJDiDER PRESSURE) � -----------------------------------------------------------______--------�-- CAx�CULA'i'E JUNCTION LOSSES: PiPE Fi,OW DIAM�TER ANGLE FLOWLINE CR�TICAL V£LOCITY {CFS1 (TNCHES) (DEGRBES} E7�,E�TATION DEP'i'H(FT. j (FT/SEC} UPS'i'FtEAM 32.50 24.OD 0.00 338.72 1.9D 10.345 DpwNSTREA,M 39.90 3D.00 - 338.20 2.13 8.128 i�ATERAL #1 4.70 18.00 90.a0 339.2a 0.83 2.66D F�ATERAL #2 2.70 16.00 90.00 339.2D 4.62 i.528 4� D.OD===Q5 EQURLS BAS�N �NPUT=== LACFCD P.I3D OCEMA FLOW ,7TINCTION FORMUL.�E i7SED: DY=IQ2*V2-Q1*V1*COS{DEiTA1}-Q3*V3*C05{a�,�p3�- Q4*V4*C05{iJELTA4j)/[{A1+A2}*16.1j+FRICTIO�i L05SES UPSTREA�1: MANNTNG'S N= 0.0130fl; FRICTION Si3OPE = D,02064 M}WNSTR�AM: MANNING'S N= 0.0�3D4; FRICTI013 S�OPE = 4.00946 AVERAGED FRTCTION Si.OPE IN 3UNCTION ASSUtYIEA A5 0.01505 JiJNCTIOIV LENGTH = 9.00 FEET FRICTION L055ES = b.060 FEET EN'PRn.PICE L05SES = D.Q00 FEET JUNCTTON LpSSES W (DY+H[71-HV2)+(ENTRP.NCE LOSSE51 JUNCTION i3OSSES =( 4.604y+( O.DQO) = 0.604 NODE 4001.7a : HGL =< 345.6B1>;EGL= � 347.343�;FLOWLINE= < 338.720� �r�rrr�r:�*.wx�t.*�+wrtx+*+,rxtw++x+++s+�+f**►wx***w*r+rr�*+*+*r***twy*+y*x*wt�+++♦ FLOW PROCESS FRON3 NQbE 900�.7D TO NpDE 4441.90 IS CODE = 1 UPSTREAM NODE 4001.90 Ei�EVATION = 342.79 (FLdW IS UNDER PRE55URE) ------------------------------------------------------------------------------- CALCU�ATE FRICTION �,OSSES(LACFCD): PIPE FLOW = 32.50 CFS P�PE DIAMETER = 24.00 INCHES PIPE LENGTH = i23.33 FEET 2+L�NNTI3G'S N= 0.�1300 r� �J . SF=(Q/K)**2 = {( 32.50j/{ 226.224}}*+2 = 0.02D64 HF=L"S� _ ( 123.33}*(0.02054) = 2.545 ---------________________-------------- -------------------------------------- NODE 4001.9D : HGL =< 348.227>;EGL= � 349.$88>;FL,OWL�NE= < 342.790> ****f++*t*rtf+tr**+*Wr►rr:wyx*yx*+*ay*srt*r�rrtrsf�+w*txw+***�++*fw++t*++t*++kxax FLOW PROCE55 FROM NODE 4401.90 TO NODE 4Q02.00 xS CODE = 3 UPSTREP.Nf NODE 4002.00 ELEVATIaN = 346.35 (HYpRAULIC JLTMP bCCURS} CALCUI�ATE PIPE-BEND LOS5E5(OCEMAj: PIPE FLOW = 32.50 CFS PIPE DIAMETER = 24.Q0 INCHES CENTRAL ANGLE = 47.500 DEGREES MANidiI3G'S I3 = D.01300 PIPE LEI3GTH = 107.82 FEET ------------------------------------------------------------------------------ HXDRAULIC JUMP:�DOWNSTREAM RUN A23ALYSiS RESULTS �IORMP.L bEPTH[FTj = 1.34 • CRIT�CAIJ DEP'i'H(FT} = 1.9D �====--====----�___�____---_--_-_---___-____=====ccv�car�s4x_-xc_acx�s4�====__ CTPSTREPM CONTROL ASSUMED FLbWD�PTH(FT) = 0.59 GRADUALLY VARIET7 FLOW PROFILE COMPUTED INFORNSATTQN: D�57'ANCE FROM FLAW DEPTH VEi,OCTTY SPECIF�C PRESSURE+ CONTAOL { FT } ( FT } { FT / 5EC � FNERGY ( FT ) I+IOMENTLTM { pQ�7D5 j Q.000 0.593 33�.629 18.264 2135.97 6.421 0.719 3�.986 16.516 2034.].1 12.925 0.745 34.486 15.185 1941.24 19.524 D.771 29.110 13.937 1656.35 26.217 0.797 27.846 12.844 1778.55 33.028 0.823 26.681 11.893 1707.a7 • 39.9b9 0.848 25.5D4 11.435 1641.27 47.�58 0.874 24.507 10.283 1580.56 54.315 0.900 23.582 9.615 1524.46 b1.76A 0.92fi 22.822 9.Q19 1472.53 b9.436 0.952 22.421 8.487 1424.39 77.3b7 0.9']$ 21.273 B.Q09 1379.70 85.5a0 1.D04� 20.574 7.5$1 1338.17 94.190 . 1.030 19.919 7.195 1299.53 103.246 1.D55 i9.3D5 6.847 1253.55 �07.820 1.069 19.022 6.691 1247.01 HYDRAULIC JUMP: UPSTRF.AM RUN ANALY5I5 R£5[7i�T5 . �_��__��____________________________________________________________________ DOW135T`REAM CONTROL ASSUMED PRESSLiFlE HEAD(FT) = 5.44 _C_______��___�___��_�_�____��_��_�� :�.�t PA�SSURE FLbW PROFILE COMPUTED INFORMATION: ---------------------____--___-------------------------------------------------- DISTANCE FROM PRESSURE VELOCITY SPECIPIC PRESSiTRE+ CON'I`ROL 1 FT } HEAD ( FT } ( FT / SEC ) ENERGY { FT } MONSENTUM ( POUAiDS ) Q.000 5.437 1D.345 7.098 1521.27 147,B20 4.904 1fl.345 6.�65 137.8.79 -----------------------END OF Hl'E1RA[7i�IC JUi�SP ANALYSIS-______..____----___----- � PRESSiJRE+M4MENTiJM BALANCE OCCLTRS AT 41 . 42 FEEi UPS�'REAM OF NODE 400� . 40 � DOWNSTREA.M DEPTH = 5. D40 FEET, UP5`i'REAI� CON3iJGATE DEPTH = 0. 942 FEET I -----------------------..________-------_____..-------------------------------- idODE 4002.00 : HGL =< 347.043�;EGL= � 364.614>;PLOWLINE= < 346.350� y.r*�*�y*t�*y,�y,y,y,x*r*x�x*+r*a*+*+trxr+rrswxs*+*iywr**rrrsry.y.+w+fas+w.rrf+�*ri*.s FLOW PRQCESS FROM NODE 40fl2.D4 TO NODE 4002.10 IS CODE = 2 UPSTREAM NODE 4002.10 ELEVATTON = 346_68 (FLOW IS Si7PERCRITICALj i • CP.LCULATE MANHQLE L055ES[LACFCD): PIPE FLOW = 32.50 CFS PIPE DIAMETER = 24.OD INCHES AVERAGED VELOCITY HEAD = 17.657 FEET HMN =.05*(AVERAGED VELOCI'�'Y I3EAD} =.05"(17.857} � p.�93 �IOI7E 4D02.10 : HGL =< 347.365>;EGL= < 365.506>;FLOWLINE= < 346.fi80> 'f ** **! iFY� Yr 1rYr yrYrRt f tt1� #**R*Ii k iFYrYr YrYrf YrYr IrY� YrYrY�* *4k*} Myr! *# i y y� *i� *M*'R#* 44 Yr*1r # Yr *** iF * M*� M} FLpW PFtOCESS F3tOM NODE 40D2.10 TO NODE 4002.50 IS CODE _� UPST'REAM NODE 4D42.54 ELEVATION = 389.29 (FLOW IS SLiPERCRITICAL} CALCUL.�TE FRIC'?'ION LOSSES (LACFCD] : p�pE FLOW = 32.50 CFS PIPE DIAMETER = 24.p0 INCHES PIPE LENGTH = 106. 00 FEE'P M.�NNING' S N = {} . D1300 NdRMAL DEPTH{FTj = O.fi5 CRITICAL DEPTH[FT) = 1.90 �____________________�______-_____________��_____-____��---_-__-_-_-_------__ _ __.. _ _ _ .. __..___ UPSTREAr7 CD�ITROL AS S�1MED FLOWDEPTH {�} = Z. 5 B __====�T��__��=_�4�______________�_��_��=_=____==_=�____________________ GAR.Dl3ALLY VARIED FLOW PROFI�E COI+iPUTED Ii�IF'ORMATION: ----------------------------------------------------------------------------__--- DISTANCE FROM FLOW DEPTH VELOCI'FY SPECIF�C PRESSURE+ CONTROL{�} (FT] {FT/SEC) ENERGY(FT) MOMENTUM{ppL7r7D5) D.000 1.583 12.1$1 3.889 886.76 0.193 1.546 12.969 3.962 898.80 0.418 1.5Q8 12.782 4.447 912.45 0.678 1.471 13.118 4.145 927.82 0.979 1.434 13.482 4.258 995.01 1.325 1.396 13.874 4.38'7 954.1'i 1.724 1.359 14.298 4.535 985.46 � 2.182 1.321 14.755 4.704 1D09.a4 2.749 Z.284 15.249 4.897 1035.11 3.317 �.2A6 15.784 5.117 lOfi3.92 4.038 i.209 16.3b4 5.369 1095.71 4.831 1.171 �6.993 5.556 1130.80 5.777 �.134 17.b77 5.489 11b9.52 6.883 3.097 I8.422 6.37� 12�2.28 8.�84 1.Q59 19.237 6.809 1259.55 9.725 i.Q22 20.Z28 7.317 1321.86 11.5b8 0.984 21.1p8 7.907 1369.8'] 13.798 0.947 22.186 8.595 1434.32 16_535 0.909 23.379 9.402 15a6.10 19.955 0.872 2A.702 �4.352 1586.29 24.33'7 0.834 26.176 3I.480 1676.17 30.149 0.797 27.925 }�2.827 1777.30 38.276 0.76p 29.682 14.448 1891.59 5a.7D9 0.722 31.781 16.416 2D27..40 73.851 0.6B5 34.172 18.828 2169.69 . 106.000 0.685 34.172 18.828 2169.69 NODE 4002.50 : HGL =< 390.8�3>,EGL= < 393.179>;FLbWiJII�= < 389.290> sx+*��**y.�+xx+*****+*xrt*+�x*w+xR*x**+xx**r�*�>++*r**yt*f**�r*yti*ryr+++ty+f++*+ FLOW PROCESS FRQM NpDE 4D02.50 Tp I30DE 4002.51 I5 CODE = 2 UPSTRE.�.M NODE 4002.51 ELEVAT30Di = 389.62 (FLOW IS SUPERCRITICAL) � CALCULATE MANHOLE LOSSES(LACFCDj: P�PE FLOW = 32.50 CPS PIPE DIAMETER = 24.Oa �NCHES AVERAGED VELOCI7`Y HEAll = 2.097 FEET I3MN =.05*(AVERAGED VELOCiTY HEAD] _.05*( 2.097a � 0.105 r 1 L J � NODE 4D02.S1 : HGL =< 391.395>;EGL= c 393.283>;FLOWL�NE= < 389.620> �*x*:rxx**wr*w****x+�x+�wx+++ws��x**++x*xxrr*�>+�sye�++*x**rtwe�**rt*ar**t***a• FLOW PROCESS FRDM NODE 4002.51 'T'0 NODE 4402.52 IS CODE = 1 UPSTREAM NODE 4042.52 ELEVATION = 390.02 {gLOW SS SUPERCRITICAL) ------------------------------------------------------------------------------ CAi�Ci3LATE FRICTION LOSSESSLACFCbi : PYP$ FLDW = 32.50 CFS PIPE DiAMETER = 24.OD INCHES PiPE LENGTH = 20.D0 FEET MANNII3G'S N= 0.0�300 --------------..__ NORi+iAL DEPTH{FT} = 1.67 & 2.00 CRiT2CAL DEPTHIFT} - Z.9D NOTE: SUGGES'i' CONSIDERATION OF WAVE ACi'ION, LTNCERTAINTY, EfiC. ��___________________��_��_-��--=�=_=___===____ « «__��==____===_=___=_=__ UPSTR.EAM CONTROL ASSUMED FI,OWDEPTH(FT� = 1.90 _ ---------------------------------- GRa.DUALLY VARIED FLOW PROFILE COMPUTED INFORMATTON: ---------------------------------------------------__------------------------- DISTANCE FROM FLOW f]EPTH VELQCITY SPECIF�C PRESSLTRE+ CON'IFtOL ( FT ) ( FT } ( FT / 5EC ) ENERGY ( FT } MOMENTUM { pOUNI�S J 0.000 1.896 10.552 3.b26 840.53 D.102 2.887 10.580 3.526 840.57 0.403 1.B77 1D.610 3.527 840.69 0.942 �.858 10.641 3.626 840.90 1.599 1.659 10.672. 3.629 841.18 2.497 }..850 10.7Q5 3.631 � 841.55 3.b06 1.641 10.74D 3.633 841.99 4.934 1.832 10.775 3.63fi 842.51 6.49B 1.823 1fl.811 3.639 843.10 8.315 1.814 10.849 3.643 843.77 �0.410 1.805 10.887 3.647 844.51 : 12.813 1.745 ].D.927 3.651 845.33 15.561 1.787 10.968 3.656 845.23 18.703 1.778 1i.010 3.6b1 847.20 20.Op0 1.775 I1.025 3.663 847.56 NODE 4002.52 : HGL =� 391.9167;EGL= < 393.646>;FLOWLINE= < 39D.020> **Yr�* f Y YY ** i ty�}# *y y.* *yr �y rtYi Y k krt Yr# f# Yi irlrYryrYriM*iF tYr #Y ti YYti f yr�kt> {� *** 4* ri YrYrYrf Y� YrYrYrYrYr M1i*YrYr FI,OW PROCESS FROM NODE 4002.52 'FO I30DE AOD2.52 IS CODE = B UPSTREAM NDDE 40D2.52 ELEVA�IODi = 390.42 (FLOW I5 AT CRITICAL DEPTH} CAi,CLiLATE CATCH BASIN ENTRANCE LO$5E$(LACFCD): PIPE FT,{}W = 32.50 CFS PIPE DIAMETER = 24.OQ INCHES FLOW VELOCITY = 10.56 FEET/SEC. VELOCIi`Y HEAD =�.730 FEET CATCH BASIN El�TERGY L05S =.2" (V'ELpCTT'Y HEA[}) =, 2* { 1.730i = 0.346 ---_-__------------------------------------------------------------------------ NODE 4002.52 : HGL �< 343.992>;EGL= < 393.992>;FLOWL�NE= < 390.D2D> +rti**i.*++�,r�*r*s+t++*a*tyti**i*rt�r*rt*r+*��ff�r+y,�xrtw**r*rsttx*xrrrsrrr+rr�rr+**+ UPSTREAM PIP� FI,OW CONTROL DATA: NdDE 3�IUMBER = 40D2 . 52 FLOWLINE ELEVATI0i�1 = 390 . D2 ASSUMED UPSTREAM CONTROL HGT., = 391.92 FOR DOWI35TFtEAM RUN ANALYSTS _________��,�__��=--====---===--=--=---=====t��==______==_____=_==_=_==___== END OF GRADL3ALLY VARIED FLOW ANALYSIS � �J � e*w**w****rtrr�***�**twr*r*�xs:yrt++*�***s**t*rrr*r*.*e*w�r*+*.r++�+>+x***xxwww PIPE-FLOW HYDRAiJLICS COMPUTER PFcOGRAM PACKAGE (Reference: LACFCD,LP.CRD, AND OCEMA HYDRAULICS CRZTERION) � (c} Copyright 1982-2001 Advanced Engine2ring 5oftware (aesl Ver. 8.0 Release Date: D1/41/2DOi License iD 15D9 Analysis prepared by: PROJECTDESIGN CONSULTAN'f5 701 'B' STREET, SiJITE 800 SAN DIEGO, CA 921.D1 619-234-4349 �v..»x�,**..�.++..*...,,.*... DESCRIPTION OF STUDY +...+.+�**+*.**.**,.x*�w*�* * SRE55T RANCH - ULTTMATE CONDITTONS � * SYSTEM 4D00 - LATERAL 1 ' * * 10D-YEAR STORM EVENT * ♦rrr*txr*+*wrt*e+***�s*xw*r++++**+r+*+xxrtw**�**,i.**xw**wryw*r�i.�rrrwrti*+y.*rr FILE NAi+3E: P4000L1.DAT TIME/bATE OF STUAX: 1b:24 49/26/2002 # f k R�F!l1rYr ** #t t f Y#f t*t1*! #*tf ##tt Yrt #t*t #tYY Yf i f f f t*yr�k**i* f�k*#*k Yri�Yr Y� f Yr *Y�YrYr*i�Yr1 f Yr GitADUA�LY VARIEA FLOW ANAI.,YSIS FOR PIPE SYSTENS NpbAL POIN'I' STATUS TABLE {Note: "*" indicates nodal point data used.} UPSTi�EAM RLiN DC}WNS'T'REAM RUN NObE MQDEL PRESSiFRE PRESSURE+ FLOW PRESSURE+ NUMBER PAOCESS HEA�! ( FT) M034ENTi3M { pOUNDS ) DEPTH ( F'P) MOMENTUM ( POUNDS j 4001.50- b.49* 715.95 0.65 2].2.99 � } FRICTION 4Q01.60- 5.24* 577.67 1.14 Dc 147.79 } .CA'I`CH BASIN 4QD1.60- 5.69* 544.47 1.14 Dc 45.17 MAXIi�SiJM NUMBER pF EI3ERGY BALANCES iiSED IN EACH PROFIiE = 25 ------------------------------------------------------------------------------ 13pTE: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASED QN TF3E MOS'T' CO?�ISERVA'�`iVE F4RMU�AE FROM THE CURRENT LACRD,LACFCD, AND OCEMA DESIGN MPNUALS. Y� Yr*MrKY� i� Yr�* rtYrYrYriFY� YriYrM *** i�rtf tkY�Yr*�F *Y� iYr *� if YrttiY YY *f y*f * f yriF#�Lyr **Yr k Y� *�k iF iF�k #* Yr**# f M*t� DOWNS�'REAM PIPE FLOW CONTROL DA�'A: NODE NUMBER = 4001.50 ' FLOWLINE ELEVATTON = 339.22 PIPE FLOW = B.70 CFS PIPE DIAMETER = 18.00 TNCi�1ES A55UMED T)UWNSTREA2+f CONTROL HGL = 345.710 FEET - ------------------------------------------------------------------------------ NpbE 400�.50 : HGL =< 345.7i0>;EGL= < 346.086>;FLOWLINE= < 339.224> ♦ **** * YYt Y!lYYi *r*** f i ** yr* �4�k*tM4 *t *+*� #{}; k #Yck f *Yr iFi� iFYrk * *i**t**#*t * ii*t*t#1t*Y� �k �'LOW PROCESS FROM NODE 4D01.50 TO �iODE 40fl�.60 2S CODE = 1 UPSTREAM NODE 44D1.60 ELEVA'I'ION = 340.51 (FLOW i5 UNbER PRE9SURE) CALCCTLATE FRIC'FION LOSSES(LACFCDI: PIPE FLOW - 8.70 CFS PIPE DTAMETER = 16.OD I13CHE5 PIPE LENGTH = 5.25 FEET - MANNING'S N= 0.0�30D SF=(Q/K)**2 = (( 8,70}/{ 105.047?1**2 = 0.00686 HF=L°SF = ( 5.25}*(O.DD686) = 0.�36 -----------------------T--____-__�________-_----------------------------------- N�AE 4001.60 : HGL =< 345.746>;EGL= < 346.122>;FLOWLINE= < 340.510> C � �♦**rxwtw*.:s*rx..+�rr.�++r.r*rt.rr*sr+w*rxax*+s�x**xwxwr***xr.ywy+tr*rr�xrW�+r* _ FLOW PROCESS FRQM NODE 4001.50 �'O NODE 4d01.5D IS CODE = B UPSTREAM NODE 4d01.6fl ELEVATION = 390.51 {FLC}W IS U�DER PRESSURE} ------------------------------------------------------------------------------ CAi,CULATE CATCH BASIN £NTR.AiQCE LOSSES{��FCD) : PIPE FF,OW = B. 70 CFS PiPE DiA2+�ETER = 1B . 04 IPICHES � FLOW VELOCI'iY = 4.42 FEET/SEC. VE�,OCITY HEAD = 0.376 FEET � CATCH BASIN ENERGY L�55 =.2*{VELOCITY HEAD) _.2*( 0.37{>) = D.D75 ------------------------------------------------------------------------------ NODE 4041.50 : HGL =< 346.198>;EGL= � 346.196>;FLOwLINE= < 340.51D> *+**y�***ir*ry.�y,�k*wv.+:+*�+++v.+*t*+�v.+Rx**r*�**�+*tx*rrr*rW+*+v.t++*+tv.**i.r+**Ww UPSTREAM PIPE FLOW CONTROL DATA: NODE NLIMBER = 4001.50 FiUWLINE ELEI7ATION = 340.51 ASSUMED UPSTREAM COi�i'TROL HGL = 341.65 FOR DOWS�1STFtEAM RUN ANALYSIS __C__________�_____C________________�=��=�:T��`______________________________ ENA OF GRP.DUALLY VARIED FLOW ANP.i,YSIS • i C� � +s*�+x**x*r**.w�r*t**str*�*�*xr*r�**rrrt�f++r►++xx+**r+:wx*wrrrr�r*r*rrt++wt+* PIPE-FLOW i�iYDR.AULICS COt�SPU'T'ER PROGRANI PACKAGE {Reference: LACFCD,LACRD, PND pC�MA HYDRAULICS CRITERI023} (c1 Copyright 1982-20a1 Advanced Engineering Software {aesl Ver. 8.0 Release Date: Dl/01/20D1 License ID 1509 Analysis prepared by: PROJECTDESIGN CONSULTANT'S 701 'B' STREET, SUITE 800 5AN D�EGO, CA 42101 6�9--234-4349 **..**�.++*.*..*..«x*....*. DESCRIPTION OF STUDY ,•***••**�+•***�•*•**�••••• * BRESSI RANCH - ULT3MATE CONDIITpNS * * SYSTEM 40�4 - LATERAL 2 + * 100-YEAR STORM y tYr#! Y!*1*ttlktkt�ri Y� hY� �k #*Y•Y Y�*iiF�k f!*M Yr*Y� Y�Yrk kri Yr*M�k##�ltW *�'kf k**Y�Yr# **Yrri f YrYCYr *f*** kriYr FTLE NAME; P4000L2:DAT TIME/DATE OF S'I'LTDY: 1fi:26 49/25/2Dp2 f!r'X'kRir ** Y� *yr YrlYr �kt M# #Y f Y** t* * fY�t# Yi iYrt Y#YYii yrk *yr***#Yr *}I� �F tk Yr *** *** i tt*# Yi**t *tYrY♦ GR.ADUALLY VARIED FiOW ANALYSIS FOR PTPE SXSTEM NODAL PUTNT STATUS TASLE fNote: "*" indicates nodal point data used.) UPSTREAi� RUI3 DbWI35TREA�3 RUN NODE MpDEL PRESSURE PRESSUR�+ FLOW PR�SSURE+ NUMBER PROCESS HEAD(FT} MQM�NTUM(POUNDS) DEP�'H(FTj 3�SpMEN'I`UM(POUNDS} � 4041.J.D- 6.51' 662.57 0.52 96.74 } FRICi'ION 4041.24- -4.6$* 482.6� 0.86 bc 70.41 } CATCH BASTN 4Q01.24- 5.03* 471.64 0.66 Dc 24.19 MAXIMLiM NUMBER dF ENERGY �ALANCES USED IN EACH PROFILE = 25 NOTE: STEAI]Y FLOW HYDR7aULIC HEAD-L05S CO2+FPUTAT'TONS BASFD OI3 THE M05'i' _ C0335ERVATIVE FORM�,AE F�t01� 'I'HE CURREN'P LACRD, LACFCD, AND OCRMA AESIGN MAI3[7Ai�5. r+►*r*w+�xk**w***w+x*r*x+s*y+**+tt*x++**i**r+++��*****�rr**w+t++xrw***i+*+**** DOWNSTREAiQ PIPE FL,OW CONTROL AATA:� ' NODE NUMSER = 40fl1.10 FLOWLTNE ELEVATION = 339.20 PIPE FLOW = 5.00 CFS PIPE DIAME'I'ER = 18.40 INCHES A55UNFED DOWNS'I'RE.�t4 CONTROL HGL = 345.710 FEET NODE 40p�.10 : HGL =< 345.7i0>;EGL= � 395.$34>;FLOWf,2NE= < 339.200> «+«*.+**�+.*t*r...*wv.++v.**�+v.+++**��+**+�***«*�««...f*�***.w+*,�+.**,��*�*+*�fv... FLOw PROCESS FROM idODE 4D01.10 'I'0 NODE 4001.20 IS CODE = 1 UPSTREAM NODE 4001.20 ELEVATION = 340.93 (FLOW IS UNDER PRESSi3REy CALCULA'FE FRICTION LOSSE$(I,ACFCDI: PIPE FLOW = 5.Q0 CFS PIPE DIAMETER = 18.�0 INCHES PiPE LENGTH = 43.25 FEET MAAINTNG'S N- D.413D0 SF=(Q/Kj**2 = (( 5.OD)/I 105.043)}**2 = p.00227 HF=L*SF = S 43.251*(0.00227) = 0.098 NpDE 40D1.2a : HGL =< 345.808>;EGL= < 345.932>rFLOWLII3E= � 340.430> C J � +rx�**+w*yax*sr�*��r++rrtr+tw:t+**�ar*t�x*r**a**rw+*+xw**+**+***++*+x*w*t*�r+�� FLC7W P�OCESS FROM NODE 4fl01.20 TO NODE 40�1.20 i$ CODE = 8 UPSTREAM NODE 4001.20 ELEVATION = 34D.93 {��,pW IS UNDER PRESSURE) ------------------------------------------------------------------------------ CAiaCLFLATE CATCI-i BASIN ENTRANCE LOS5E5{�,ACFCDj : PIPE Fi�OW = 5.OQ CF5 PIPE DIAMETEI� = 18.00 INCHES FLOW VE�OCITY = 2.83 FEET/SEC. VEI,OCITY HEAD = D.124 FEET CATCH HP.SIN ENERGY L�SS =.2*{VELOCITY HEA�?f =.2*( 0.124} = 0.025 NODE 40D�.20 : HGL =< 345.957>;EGL= < 345.957>;Fi,OWLiNE= < 340.93D> •wxt+trtt*yrr�*r+�++.+i.r*+*W*rW*+rrrrt+try.r***,r+�*****f*r+***t+**r*yrr*+**+++*t UPSTREAM PIPE FLOW CONTROL DATA: NODE Ni7MBER = 4�d1.24 FLOWLINE ELEVA'T'IpN = 34�.93 ASSITMEb UPSTREP,M CONTROL HGL = 341.79 FdR DOWN5TF2EAM R[fiT APL�LYSTS _��_______________________________________________��=_==_==__==___=_=___=__ END OP GRAAiiALi�Y VARIED FLOW A.NALYSIS i � � � APPENDZX 4.�.10 SYSTEM 5004 {`B', `P', `Q' STREETS) � C� .] � ; • � � NODE NUMBER COIUIPARISON SYSTEM 5404 AES Pi eflow AES Ratianai Met�od AE5 Pi flow AES Rational Meth�d SOOO.OQ 1080.00 501020 5�57.00 5001.00 5�95.00 50102i 5057.00 500120 5095.00 501 D.22 -- 5001.30 5091.00 5010.23 5057.D0 5001.40 5091.00 5D1024 5057.00 5Q01.50 -- 5010.30 -- 5001.6a 5095.04 5010.3i -- 5001.7a 5094.00 5010.32 -- 5001.90 5095.00 5d10.40 -- 5002.00 5090.00 5D10.50 5060.00 5002.20 5490.00 5410.50 -- 5002.30 5086.63 5010.60 5d62.30 5602.9D 5090.00 5010.70 SQ62.30 5003.Oa 5085.00 �o� a.so 5062.3a 5003.1 Q 5085.00 5010.90 sosa.oa , 5DD3.2a 5085.30 5011.Op 5040.Od 5043.50 5085.pQ 5011.10 SQ40.00 5003.60 , 5085.40 5011.20 5038.30 50Q3.90 50$5.00 5011.50 5040.00 5044.OD -- 5011.60 5039.30 5004.90 -- 50i 1.90 5040.00 5005.00 5081.00 5012.00 5437.00 50D5.10 5081.00 5012.50 5037.OQ 5005.20 5081.10 5012.60 -- 5005.90 5061.DQ 50i 2.90 5037.00 5006.00 5080.00 5013.DQ 5025.60 5406.i 0 5060.00 50� 3.10 5025.60 5006.20 5078.00 50� 3.2b SD25.20 5006.30 5078.04 504 3.90 5025.60 50D6.40 -- 5014.OQ -- 5006.50 5079.00 5015.Od 5030.00 5006.60 5a79.00 5015.5b 5D30.00 5006.90 5080.00 5015.60 5028.80 5007.00 5075.00 5015.90 5030.00 5007.10 5075.00 5Q2p.00 5025.00 5007.54 5075.d0 5Q20.90 5025.00 5047.60 -- 5Q25.00 5025.40 5008.00 5070.00 5030.00 5016.00 5008.90 5070.OQ 5030.90 5016.00 5009.00 5065.00 5031.00 5015.00 5009.10 5065.00 5031.10 5415.00 5009.2D SQ61.24 503120 5012.30 5009.50 5065.00 5031.50 5015.04 5009.60 5062.34 5031.6Q 5013.30 5009.9Q 50fi5.OD 5031.90 5015.00 5410.00 50fi0.00 5032.OQ -- 5010.00 5060.00 5032.90 -- 501 �. i 1 -- 5035.00 -- • * * * * * } * # # ti � * * * * ? * M � * * * f * � x * * * 1 * k f * f t f i # f * Y ti Y � k i k t + � t � � + Y 1 * i * 4 } # * * � * # * t � k # * * * * ♦ PIPE-FLOW HYDRAULICS COMP[FI'ER PROGR.A�1 PACKAGE fReferencE: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION) (c}-Copyrigh� 1962-2002 Advanced Engineering So€tware {aesl �Ier. B.0 Release Date: D1/07./2002 License ID 1509 - Analysis prepared by: PRU7ECT DESIGIV COAISULTAN'i'S 703 'B' STREET, SUITE B00 SAN DIEGO, CA 92101 ' 619-235-6471 �s�+*+ti+*t+t+**+*+*t++a++t D£SCRIPTION OF S'PUDX ***�*x*****************r*� * BRESSI RAfdCH - ULTIMATE CONDITIONS '` • Hydraulic Analysis System $OOQ " * 100-YEAR STORM EVEIdT * *+*,rw�,r+*�+�x*+R►+*x+xk++i�+*s**+tf*++rrr**�r****x++t+y*farx*srr***f+**�+*r FILE NAME: L500Q.DAT TII+SE/DATE OF STUDY: 10:26 OI/�7/2D03 ir+*v�++w++*��+�i+rr*tti+r*s*y�r+**+t*t+**t*www**�*xw+*x��*+*�wxr**x*>t+t+�ty**r GRADIJALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAI, PdINT STATUS TABLE (Note: "*• indicates noc3al point data used.} UPSTRF.AM AUN DOWNSi`RE.�.M RUN NODE MODEL PRESSURE PRESSURE+ FLOW PRESSURE+ NUiYFBER PROCESS HEAD(FTi MdMENTiJP7(POUNDSI DEPTH(FT) MQMENTUM{pOUNDS) • 5000.00- 8.59* . 6686.79 2.17 7126.98 } FRICTION 5001.00- 6.27* 7068.43 2.38 6499.28 } JUIdCTION • 5001.90- 6.56' 7053.74 2.12 6831.14 } FRICT�QN } HYDItAL7L,IC 3UMP 5042.00- 3.59 Dc 4916_59 2.95* 5201.42 } ,NNCTf�N � 5Q42.90- 4.71 4361.75 1.89* 4988.Sa } FRICT�ON SOQ3.OD- 3.20 Dc 3590.14 1.95* 482Z.53 ) ,nmrc�riar� 5003.90- 2.93 9c 3962.07 2.1i* 4707.i8 } FR�CTIOI3 5009.00- 2.93 Dc 3962.07 1.75* 5667.�3 ) MANHOLE ' 5009.90- 2.93 Dc 3962.07 1.74* 5716.75 ) FRICTTpN 5005.OD-- 2.93 Dc 3962.07 1.52* 5�76.14 ) JUNCTION 5005.90- 2.93 Dc 3925.78 1.59* 6240.82 } FRICTION - 5006.00- 2.93 Dc 3925.78 I.74" 5643_35 } ,�[FNC�'ION 5006.90- 3.13 3829.29 1.65' 5682.20 } FRICTION � 5Q07.00- 2.92 Dc 3753.05 1.90� 4883.70 } JUNCTION 54q7.90- 9.Q3 3647.82 1.58' 4894.70 . } FRICTION • 5aQ8.OD- 2.88 Ac 3175.29 1.?B* 9306.89 • } 1�ANHOLE 5008.90- 2.88 Dc 3175.29 1.77� 4319_76 } �'RICTION 5009.00- 2.86 Dc 3175.29 1.79* 9291.22 } ,TUNCTION • 5009.90- 2.87 Dc 3106.27 1.74� 4293.4b } FRICTION 5010.00- 2.87�Dc 3106.27 2.87*Dc 3�06.27 } ,TUNCTTON 5010.90- 5.55* 2782.44 1.28 2598.56 } FRICT�ON ) HXDRAULIC Ji1P7� - 5011.04- 2.52 Dc 1570.37 ].75• 1897.78 } JUNCTi4N 5011.90- 2.92 1455.78 1.48* I8Q5.50 ) FAIC'i'ION 50�2.00- 2.40*Dc 1372.31 2.4D*Bc 1372.32 � ) JUNCTION � 5012.90- 3.12 �253.73 1.41* 1284.97 ) FRICTI013 5a13.OD- 2.17*Dc 1024.05 2.17*Dc 1024.05 } ,7UNCTION 5013.90- � 3.65* i495.4� 1.50 1238.17 } FRICTION 501A.00- 3.17' 1286.65 L 50 124D.93 } FRICTION+BEND } HYDRAULFC .7iJMP 5015.00- 2.17 Dc 104�.00 1.46* 1268.48 } J[TrFCTION 5015.9a- 2.5? 956.41 1.23* 1246.55 } FRICT�ON+BEND 5020.00- 2.09*Dc 904.51 2.09*Dc 904.53. • ) JUNCTION 5020.90- 3.14* 888.73 1.54 627.63 ) FRICTION+BEND } HYDRAULIC ,TUMp 5Q3a.00- I.82*Dc 6fl4.6Q 1.82*Dc 504.60 } 3-idNCTION 5030.90- 3.02* Sb2.95 1.52 632.52 } FRICTIO?�I 5031.00- 2.56' 720.81 1.45 648.70 } Ji]23CTTON 5031.90- 1.76 Dc 550.81 1.62* 555.43 } FRICTION 5032.00- 1.75*Dc 550.78 1.75*pc 550.78 ] J UNC'3'ION 5032.9a-- 3.59* 681.73 1.53 565.32 } FRICTION 5035.00- 3.48w 854.27 ],.75 Dc 550.78 MAXIN3CTM NUMbER OF ENERGY SALANCES USEI} IN EACH PRQFILE = 25 NO3'E: STEADY FLpW HXBRAULIC HEAD-LOSS COMPUTATIONS BASED ON 1'HE MOST CONSERVATIVE FORMLTLAE FROM THE CURRENT LACRD,LACFCD, AND pCEMA DESFGN MANY7ALS . *'t*11t# 1*## **** f rt!r***t##Y! *i�k+4 ik �l Y*#411�kikY4*4 iFi �k f�kik ##**# 1 iF f*fYrk �***tti i Y?Yr**iri • DOWNSTREAM PIPE FLOW CONTROL DATA: i30DE EdU�7BER = 5000.00 FLOWLIIVE ELEVATYON = 174.74 PIPE FLaW = 155.30 CF5 PIPE DIAMETEA = 98.00 INCHES ASSU33ED DOWiJSTREP,M CONTROL HGL = 383.330 FEET NODE 50DO.fl0 : HGL =< 183.330>;EGL= < 185.702>;FLOWLINE= < 174.740> • ******+*�*+***+,,ww�,��,,�*.«+**.***x.�****��.***�**.�.�.�*�.**�*,,�..�++++��*f� � FLOW PROCESS FROM NODE 5000.00 TO NOBE SOO1.Q0 I5 CODE = 1 UPSTREAM NODE SDO�.OD ELEVATION = 177.62 (FLpW TS UND�R PRESSURE} CALCi7L�TE FRICTION LOSSESfLACFCDf: PIPE FLOW = �55.30 CFS PIPE DIAMETEA = 48.00 INCHES PIPE LENGTH = 48.00 FEET M�iNxNG'S N= 0.013QD SF=fQ/K)**2 = [f 155.301/f 1436.432})**2 = 0.01169 HF-L�SF = ( 48.40j*(fl.Qllb9) = 0.561 . NODE 50D1.OD : HGL =� 183.891�;EG�= < 186.263>;FLOWLINE= < 177.620> *�***�ww.�*��*.w�*.*�*��*w��+��+w*�*.**t********+*tt�*f�*��*.��.��.**��tt�t* FLOW PROCESS FRpM NObE 54a1.40 TO NODE 50D1.90 IS CODE = 5 UPSTREAM NODE S�OZ_9D ELEVATION = 177.95 (FLOW TS iJNDER PRESSLTRE) ------------------------------------------------------------------------------ CALC�ATE Jlii�7CTI0N L055ES : • PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCITY {CFSj (INCHES} (DEGREES) ELEVATIOAI DEPTHfFT.) (F'T/5EC1 UI'STREAM 199.90 4$.00 20.00 177,95 3.59 11.924 • DOWI3STREAM 155.3D 48.00 - 1'77.62 3.63 12.358 I�ATERAL #1 2.1D 34.40 50.00 179.15 0.47 0.428 LATERAL #2 3.30 18.OD 90.dD �80.45 0.69 1.867 Q5 Q.QO===QS EQUALS BASIN INPUT=-- LACFCD FLND OCEM7� FLOW JUNC�`�ON FORMUZJaE USED: DY=(Q2*V2-Q1'V1*C05(DELTA�]-Q3*V3*CQS(DELTA31- Q4�V4*COSfDEL�A4)j/ffA1+A2)�16.1}+FRICTION LOSSES UPSTREAl�S: P4ANNING'S N= 0.01300; Fi2ICTI0N SLOPE = 0.010$9 DOWNSTREAM: MANNTNG'S i�I = 6.D1300; FRFCTION SLOPE = 0.01159 AVERAGED FRTCTION SLOPE ZN JUNCTION ASSUMED AS 0.01129 JUNCTION LENGTH = 4.OD FEET FRICTIOA} LOSSES = 0.�45 FEET ENTRANCE LOSSES = 0.�40 FEET JUNCTION LOSSES = (DY+HV�-HV2)+(E?�7'I'RANCE LOSSES} JLTNCTION LOSSES =( 0.473)+( O.00D) = 4.473 ------------------------------------------------------------------------------ NODE 5001_90 : HGL =� 184.526>;EGL= � 186.736>;FLOWi�I�7E= < 177.950> ****siaatri+rfa++f�t**++*�f*�*+++,t++*+a�r***tiyr�+�rttf**r*s�*ti�*r�+*+++iti**a** FLOW PROCESS FR4M I3017E 5d01.90 TO NODE 5002.00 IS CODE = 1 UPSTAEAM NODE 5002_00 ELEVATZON = 187.36 {HYDRALTI.7C JUMP OCCURS) CAi�CULATE FRFCTION L05SES(LACFCD}: PIPE Fi,OW - 149.90 CF5 PIPE DIAME'TER = 48.00 Ii3CHE5 PIPE LEATGTFi = 221.b3 FEET NSP.NNTNG'S N = 0.01340 ------------------------------------------------------------------------------ 1�iYDRAULIC �3UMP: DOWNSTREAM RUN ANALYSIS RESULTS ------------------------------------------------------------------------------ NORt�AI� DEPTH ( FT i= 2. 02 CAI'9'ICAL DEPTH { FT f= 3. 59 ------------------------------------------------------------------------------ ----------------------------�--_w_-_--------------------------------------------- UPSTR�AM CON'1'ROL ASSUMED FLOWDEPTH{�'} - 2.95 ------------------------------------------------------------------------------ GftADUALLY VARIED FLOW PROFILE COMPUTEE} INFOFtMATION: ------------------------------------------------------------------------------ DISTANCE FROM FLpW DEPTH VELOCITY SPECIFIC PRESSURE+ CdNTROL(F�'} (FT) (FT/SECJ ENERGY(FTj MOMEN'TUM{pOUNDSf O.OaO 2.947 15.097 6.469 52Q1.02 2.060 2.910 15.301 6.548 5237.25 9.332 2.873 15.512 5.512 5276.06 b.938 2_$36 15.732 6.661 5317.56 � 9.641 2.798 15.960 b.756 5351.B4 12.648 2.761 16.197 b.837 5409.00 i 16.011 19.726 23.836 26.394 33 .460 39.109 45.432 52 . 541 60.581 69.735 60.247 92.446 106.794 123.969 145.022 171.715 207.352 221.630 2.729 2.666 2.644 2.612 2.575 2.537 2.500 2.463 2.425 2.388 2.351 2.314 2.276 2.239 2.202 2.364 2.127 2.117 16.443 15.699 16.964 17.291 �7.528 17.827 �8.138 18.46� 18.798 Z9.149 19.519 19.$95 20.293 20.70$ 21.14� 21.593 22.06b Z2.204 6.925 7.D19 7.121 7.230 7.34$ 7.475 7.611 7.758 7.916 8.085 8.268 8.464 8.675 8.902 9.146 9.409 9.693 9.774 5459 5512 5568 5628 5692 5759 5830 5905 5984 5067 b156 b249 5347 6450 fi560 6b75 6796 6831 16 44 95 84 26 35 za 22 37 93 1� 15 30 $2 00 17 64 34 IiYDRAULIC JLTMP: UPSTREAM RiJri ANALYSIS RESULTS llUWNSTREAM CONTROL ASSi3I�4ED PRESSURE HEAD(F'1'1 = 5.58 PRESSURE FLOW PROFILE COMPUTED IPiFORMATION: DISTANCE FApM CONTROLSFT) a.aoo 81.6�6 PRESSURS VELOCITY H�b(FTJ (FT/SECf 6.576 11.929 4.00Q 11.929 SPECIFIC PRESSL7RE+ ENERGY ( FT ) MOMENTl3M ( POUt3DS ) 8.786 7053.74 6.210 5033.43 ASSUMED DOWNST3tEAM PRESSURE HEAD(FTjR� 4 00 ` . ________________________________________�_��------------- GRADUALLY VARIED FLOW PROFILE COMPUTED INFORrSATIOfV: • DISTAi�ICE FAOM CONTROL ( k'T ) 81.616 82.066 82.459 62.817 B3.149 83.456 B3.742 84.D08 84.257 84.489 84.704 84.904 85.086 85.256 85.414 85.556 85.684 85.798 85.899 85.986 86.060 86.120 86.158 8b.201 86.222 FT,OW DEPTH I �"i' 1 4.a00 3.984 3.968 3.951 3.935 3.919 3.903 3.$86 3.87D 3.854 3.838 3.&22 3.805 3.769 3.773 3.757 3.741 3.724 3.708 3.692 3.675 3.659 3.693 3.627 3.621 VELOCITY (FT/SECi 11.925 11.930 11.940 11.952 11.967 11.983 12.Dfl2 12.022 12.043 , 12.066 32.09fl 12.Z1b i2.�43 12.171 12.200 12.231 12.262 12.295 12.328 12.363 12.399 12.436 12.474 12.513 12.553 SPECIFIC EAIERGY ( FT j 6.2�0 6.195 6.183 6.�71 6.1b0 6.15D 6.141 6.132 6.124 6.116 6.109 6.103 6.096 6.d91 6.Q86 5.081 6.a77 6.073 5.470 5_067 fi.464 6.062 6.061 6_060 6.059 PRESSURE+ MOMENTU#�I ( POLTi�iDS � 5033.43 5022.24 5012.30 5603.20 4994.77 4986.93 4979.63 4972.81 4966.46 496D.55 4955.06 4949_97 4945.27 4940.95 4937.00 4933.42 4930.i9 4927.31 4924.79 4922.b0 4920.75 4919.25 491B.09 99J.7.25 9916.75 � 86.22B 3.595 12.593 6.D59 4916.59 221.630 3.595 12.593 6.059 4916.59 ------------------------END OF HYDRAULIC JUhIP ANALYSIS------------------------ I PRESSURE+MOMEN�'lJM BALANCE OCCURS AT 9.97 FEET UPSTREAM OF NODE 5001.90 � I DOWNSTREAM DEPTH = 6.262 FEET, UPSTREAM CONJUGATE DEPTH = 2.�24 FEET � -------------------� NO�E 5002.44 : HGL =� 190.307>;EGL= < 193.849>;FLOWLINE= <�87.3bQ> **+++*�a�rt*�r*+ti++**sw*��*�**++s�+ia++r*�t*a+t+*��***+riiy*++++++*+x**rwr*att FLQW PROCESS FROM NODE 5402.00 TO NODE' S002.90 IS CODE = 5 UPSTREAM NODE 5002.90 ELEVATION = 187.86 {FLOW IS SUPERCRITICAL� CALCULATE �IUI3CTION L055ES : � �� W� PEPE �'LOW �IAMETER ANGLE FLOWLINE CRTTICAE, VELOCI'I'Y ICFS) (INCHES} (DEGREES} ELEVATION DEP'i'H{FT.) (FT/SEC] UPSTREP,M 113.70 42,00 4.00 187.86 3.2D 21.426 DOWNSTREAAf 149.90 48.00 - 187.36 3.59 15.102 LATERAL #1 35.2p 30.00 90.00 188.86 2.04 8.�442 LATERAL �2 0.00 0.00 0.00 Q.00 0.00 0.400 Q5 4.00===Q5 EQUAI,S SP.SIN INPiJ'I'=== �ACFCD A?+TD OCEMA FLOW JUNCTION PORMi7T,AE USED: DY={Qz+V2-Q1*V1*CQS(DELTAI}--Q3*V3*COSIDELTA3}- Q9*V4*COS(DELTA4))/f(A1+A2)*16.1}+FR3CTION LOSSES UPSTREAM; N3ANNING'S N= 0.0130d; FRICTION SLOPE = O.fl3939 DOWNSTREAM: M.�NNING'S N= �.01300; FRiCTION SLQP� = q.01366 AVERAGED FRICTI4N SLOPE EN JTJI3CTION ASSUMED A5 0.02652 JUNCTION LEI�FGTH = 4.00 FEET ' FRICTION LOSSES = fl.1D6 FEET SN'I'RANCE L055E5 = O.Q00 FEET JUNCTION LOSSES = { DY+HV1-HV2 ? + ( �1'1'F2ANCE LOSSES ) � --JUNCTIOi�I LOSSES = i 3.D32f+( 0.000} - 3.032 NQDE 50D2.9p : HGL =< 1$9.752>;EGL= < 195.$81>;Fi�OWLINE= < 187 8b0> +�++e**>x++��*r*trat*r***++*xxw*r*r�*t+ft+t+it*r*�*y�t*++*,rr*r**ittfrt**ys**�r�r� FI.,OW PROCESS FROM NODE 50Q2.90 TO NODE 5003.00 �S CODE = 1 UPSTREAM NODE $D03.00 ELEVATION = 192.68 {g�,pW I5 SUPERCRITICATJj CALCULATE FRICTIOi1 LOSSES{I,pCFCD}: � �� PiPE FLOW = 1�3.7D CFS PTPE DIAMETER = 42.OQ INCHES PYPE LEr3G'1'H = Z14.77 FEE'T' MANNING'S 3J = 0.013aQ -------------------- NORMAL DEP'T'H(FT} = 1.86 CRITICAL DEP'�'H(FT) = 3.20 -- ----------------------------- UPSTREP.2�7 CONTROL ASSEJMED FLOWDEP`I'H S FT} = 1.95 ------------------------------------- GRADi}AI�LY VARiED FLOW PROFILE COMPUTED INFdRMATI4N: ------------------------------------------------------------------------------ DIS'PANCE F3tOM FE,OW DEPTH VELOCITY SPECIFIC PRESSLIAE+ CONi'ROL ( FT } ( FT } ( FT / SEC 1 �NERGY ( FT ) MpME1V"PUM ( POCTNDS ) 4.000 1.955 20.569 8.528 � 4822.53 • 4.502 1.951 20.52D 8.558 4832.59 9.215 1.947 20.672 8.587 • 4842.b1 14.157 1.943 20.725 8.616 9852.75 19_351 1.939 20_777 8.695 4862.96 29.820 1.935 20.830 8.675 4873.22 30.592 1.931 20.883 8.707 4883.56 36_702 1.927 20.936 8.737 4893.96 43.1B7 1.923 20.990 8.7b8 4904.43 50.094 L 9I9 21.�44 8.800 4914.96 • 57.4'75 1.91� 21.098 8.831 4925.55 � ` � • 65.398 1.911 21.152 73.943 1.9Q7 21.207 63.209 1.9Q3 21.262 93.322 1.899 21.317 104.444 1.895 21.373 114.770 1.892 21.420 8.863 993fi.23 8.895 9995.97 8.927 9957.77 $.960 9958.64 8.993 4979.59 9.421 498$.80 NODE 5003.00 : HGL =< 199.535�;EGL= < 201.208>;FLpWLINE= <�92.680> �w�t+**.**t+*��*��t�*t.��**�.*+t****.*��*****.�*****.********��******�**�**** FLOW PROCESS FRpM NObE 5003.00 TQ �ODE 5003.90 IS CODE = 5 UPSTKFA� NOD� 5003.90 ELEVAT�O� = 193.18 (FLAW IS SUPERCRTTTCAL) -----------------------------------------------___---------------------------- CALCULATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CFtITICAL VELOCITY (CFS} {I�C�ES} (DEGREES) £LEVATION DEPTH(FT.} (FT/5EC} UPSTREAM 109.9Q 36.00 0.00 193.18 2.93 20.644 DOWNSTR.F.Al+f 113.7Q 42.00 - 192.68 3.20 2Q.575 LATERAL #1 2.94 18.40 90.00 194.68 0.59 3.751 LATERAL #2 1.9Q 18.00 90.00 194.6$ Q.44 3.205 Q5 0.00===Q5 EQUALS BASIN iNPUT=== LACFCD AND OCEMA FLOW JUNCTION FORI+fU�LAE USED: DY=(Q2*V2-Q1•V1"COSIDELTAIJ-Q3*V3*COS(DEL�'A3)- Q4wV9*COSIDEF,TA4})/{{A1+A2}*16.1)+FRICTIOI�i LOSSES UPSTREAAS: MANNTNG'S N= 0.01300; FRICTION SLOPE = Q.03806 DOWNSTRF'.AM: 2YIANNZNG'S N= 4.U�30fl; FRICTIOPF SLOPE = 0.03542 AVERAGED FRICTION SLdPE IN JUNC'I'ION ASSUMED AS 0.03579 J[i�iCTI03�F LSA3GTH = 9.OQ FEE7' FRICTION L055E5 = 0.197 FEET SNT�P,I+7CE LOSS�S = Q.60D FEET JUi3CTION L055ES = IDY+HV1-H}l2}+(ENTRAFVCE LOSSES) JUNCTION LOSSES = I a.7a3?+{ 0.000} = 0.703 ------------------------------------------------------------------------------ NODE 5043.40 : HGL =< 195.294>;EGL= < 201.9�Z>;FLOWLYNE= < 193.Z$6> **x+.*�**+.>.{.*****.***�***«.****++.+++�t...��..��*.*�.��.*,.�v.*+��...*s*.++** FLOW PROCESS FROM NODE 5043.90 �'0 NOAE 5004.04 �S CODE = 1 UPSTREAM NODE 5009.00 �f,EVA3'ION = 200.49 {FZ�OW IS SUPERCRITXCALJ CAI,CULA'I`E FRiCTION LOSSES {LACFCD} : - PIPE FLQW - Z09.90 CFS P�PE D�A3�7ETER = 36.Oa INCHES PIPE LENGTH = 222.00 FEET MANNING'S N- O.D1300 ------------------------------------------------------------------------------ NORMAL DEPTH(FT} - 2.24 CFtITICAi� DEPTH(FT) = 2.93 -------------------------------------------------------------------------__--__-- --------------------------�--____---------------------------------------------- UPSTREAM CONTROL ASSITMEIJ FLOWDEPTFi(FT) = 1.75 ------------------------------------------------------------------------------ GRADUALLY VARIED Fi,OW PROFILE COMPUTED TNFORMATION: DISTANCE FROM FLOW DEPT'H �7ELOCITY SPECTFIC PRESSLTRE+ COE�ITROL(FT} ;FT} (FT/5EC1 ENERGY(FT) MOMENTUMfPOUNDS) O.ODO �.751 25.655 11.977 5667.13 8.004 �.770 25.312 11.725 5599.30 16.217 1.790 24.979 11.4$4 5533.65 24.658 1.SQ9 24.655 11.254 547D.04 33.-351 1.829 29.39D 11.D34 5408.56 92.322 1.849 24.035 10.824 5348.97 51.60d 1.868 23.737 30.523 5291.2$ 61.220 1.888 23.448� 10.93I 5235.42 71.222 ]..908 23.ib7 10.247 5181.32 Sl.fiS& 1.927 22.894 I0.07� 5128.93 � . � 92 104 116 129 192 157 173 191 210 222 577 05b 175 D93 788 58i b95 283 918 040 1 1 1 2 2 2 2 2 2 2 947 967 986 OOfi az� 045 065 085 104 li9 22 22 22 2i z� 2� 2i 20 20 24 628 369 ii� 872 634 402 176 956 742 637 9 9 9 9 9 9 9 8 S 8 903 741 5B7 439 298 162 032 908 7B9 731 5076 5D29 4961 4935 4890 4847 4805 4765 4726 47D7 20 47 50 43 82 64 8A 37 21 1$ -------------------___-------------------------------------------------____--_-_ NOBE 5004.00 : HGL =< 202.241>;EGL= < 222.467>;FLOWLINE= < 200,490> �*...*.*�,.�****�*+ttt��**�.��*.********.,.*.��**.*...�.,...�t,.,...****.*�**�*... FLOW PROCESS FROM 230DE �004.Q0 TO NODE 5044.90 IS CODE = 2 UPSTREAM NODE 5004.90 ELEVATION = 204.82 (FLOW IS SUPERCRITICAL} CJ�I..CiJLATE MANHOI.,E LOSSES {7,pCFCD) : PIPE FLOW = 109.90 CFS PTPE DIAMETEi2 = 36.Op INCHES AVERAGED VELOCITY HEAD = IQ.327 FEET HMAT = .05*{AVERAGED VELOCI�`Y HEAD) = .Q5kI1�.327j = 0.516 -------------------=---------------------------------------------------------- NODE 5004.94 : HGL =< 2Q2.557>;EGL= < 2i2.984>;FLOWLINE= < 240.820> �k y� WiiFikfll � 4*�lYi**i�F�F�F�i f�Y �# t yiikik yryli* #Y*#�k*t� **!i *Yr***t�r***Yr#ti t! i4if #t� Y! Y�**#i Fi,OW PROCESS FROM N011� 5004.90 'FO NODE soos_oa IS CODE = 1 UPSTREAM NObE 50Q5.00 ELEVATTQN = 224.29 {FLOW I$ SUPERCitITICAL} CALCULATE FRICTION Lb55ESILACFCD): PIPE FLOW = 309.9Q CFS PIPE AIAMETER = 36.00 INCHES PIPE LENGTH 294.9$ FEET MANNING'S N= 0.01304 ------------------------------------------------------------------------------ NORMI�L DEPTH(FT} - 1.75 CRITICAi� DEPTH(FT) = 2.93 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------- UPSTREP.M CONTROL ASSUMED FLpWDEP'T'H{�') _ . 1.62 ------------------------------------------------------------------------------ GRADUALLX VARIED Fi,OW PROFILE COMPi7TED TNFORMATION: DIS'i'ANCE FROM FLOW DEPTH VELOCITX SPECIFIC PRESSURE+ CON'I'ROE, ( FT f ( FT f ( FT / SEC } ENERGX ( FT t MOMEN'PLTM ( POUNDS j Q.000 1.621 2B.200 13.977 6176.�9 5.157 1.626 28.091 13.887 6154.2Q 10.5�7 1.631 27.984 13.798 6132.46 16_068 1.635 27.877 13.710 6110.9Q 21.860 1.641 27.7�0 13.623 6069.52 27.905 1.695 27.6b5 13.538 6068.33 34.230 1.651 27.5b1 13.453 6047.32 40.86$ 1.656 27.457 13.359 602b.49 97.845 1.b61 27.359 13.287 60fl5.84 55.212 1.56& 27.252 �3.205 5985.36 63.017 1.571 27.151. 13.125 5965.06 7�.321 1.676 27.050 23.095 5999.94 8d.196 l.bel 26.951 12.967 5924.98 89.736 1.b86 26.852 � 12.889 5905.19 100.055 1.69� 26.753 12.812 5885.57 111.304 1.696 26.656 12.737 5866.12 123.67$ 1.701 26.559 12.662 5846.83 137.444 1.706 26.464 12.588 5827.70 152.973 1.711 26.36B 12.515 580$.74 170.813 1.717 26.274 12.442 5789.93 191.809 1.722 26.18fl 12.371 5771.28 � 217.38Q L 727 26.087 12.301 ' 5752.79 250.1B5 1.732 25.995 12.231 5734_46 294.980 1.737 25.9D& 12.164 5726.75 � C J NODE 5005.00 : HGL =< 221.911>;EGL= � 234.2b7>;FLOWI,INE= � 224.290> * k * � f * * # # } { # # } # � * � ti * # # # } } ! 1 * � 1 W * * f # * * * w � * * * * i 1 * � * 4 * i * Y * * * * * ; ! * M * * * i f # * # * * i } * i i FLOW PROCESS FROM NODE 5Q05.00 Tp NODE 5045.94 IS CODE = 5 UPSTREAM NODE 5005.90 ELEl7ATI0N = 220.62 {FLOW IS SUPERCRITICAL} CAI,CU�ATE JT7�CxI0N LOSSES : - PIPE FLOW DIAMET�R ANGLE FLOWI�INE CRITICAL VIIACI'I'Y (CFS) (INCIiES) SDEGI2EESf ELEI1ATIpN DEP�'H(FT.) (FT/5EC1 iFPS�'REAM 109.30 36.QQ D.00 220.62 2.93 28.'7Q2 DOWNSTREAM 109.90 36.OQ - 220.29 2.93 28_209 LATERP.� #1 0.60 18.00 90.00 221.95 Q.29 2.539 LATERAL �z o.00 o.00 o.00 o.00 o.aa o.aao Q5 0.00===45 EQUALS BASIN INP[TF=== LACFCD AND OCEMA FLOW �TUNCTION FORMULAE USED: DY=(Q2*V2-Q1*V1*COSSDELTA�)-Q3"V3*COS(DELTA3}- Q9*V4*COS(DEI,TA4)i/{{A�+A2)*16.1)+ERIC`I'IQN LOSSES �7PSTREAM: P4P,NNING'S N= Q.01300; FRICTTON SLpPE = D.OB813 DOWNS'TFtEAI�S: MANNING' S N= 0. 01300 ; FRICTION SLOPE � 0_ OB390 AVERAGEA FRiCTION SLpPE TN JUNCTION ASSUMED AS D.DB601. JUNCTION LENGTH = 4.Q0 PEET FRICTION LOSSES = 0.349 FEET £NTR.AI3CE LQ55ES = 0.000 FEET JUNCT30N iASSES = (DY+HV�-HV2j*(EN'i'RANCE LOSSES} NNCTION LOSSES =( 0.737}+( O.00Of = 0.737 ------------------------------------------------------------------------------- NpDE 54Q5.90 : HGi� _< 222.211>;EGI,=.< 235.OQ4>;FLpWf�INE= � 22Q.620> *******# tk i�*}y� *#yr* y��*'k#�1tY�'k #**Y! fi ttt*'k k Yr *Yr*fi*iYi� i� *Yr****iF******i�***i #�r *#*f f� tt#* FLOW PROCESS FROM NODE 5fl05.90 TO riODE 50D6.fl0 IS CODE _]. iTPSTREAM NODE sao6.aa ELEVATI03�F = 247.29 (FLOW IS SUPERCRITICALI ------------------------------------------------------------------------------ CALCIFLAfiE FftICTION LOSSESILACFCDj : PIPE FLOW - 149.30 CFS PZPE DIAMETER = 36.dd INCHES PIPE LENGTH = 297.4$ FEET MANNING'S rr = o.ai3aa ------------------------------------------------------------------------------ NOR3+iPi, DEPTH(FT} - �.5$ CR�TICAL BEPTH(�'T`) = 2.93 LL4i7PSTREAM�CONTROL ASSUMED FLOWDEPTH(FT) _ � 1.74 � GRAAUALLY VARTED FLOW PAOFILE COMPUTED II+FFORMATION: DISTANCE FROM FI..C1W DEP'i'H VELOCITY SPECIFIC PRESSURE+ CONTROL(F'i`} (FT} (�'T/SEC) ENEAGY(FT) MOMENTUMIP�UNDS) 0.000 1.74� 25.697 12.60Q 5693.35 3.526 1.734 25.810 12.D89 5665.65 7.432 1.728 25.924 12.17Q 5688.18 11.433 1.722 26.039 12.257 5730.96 15.647 1.715 26.Z56 12.345 5733.97 20.097 1.749 26.273 12.434 5757.23 24.805 1.703 26.392 12.525 5780.73 24.$00 1.696 26.512 12.617 5804.49 35.116 1.690 26.fi33 12.711 5828.49 40.79D 1.684 26.755 12.806 5852.76 46.871 1.677 26.878 12.902 5877.28 53.413 1.671 27.Q42 13.00Q 54Q2.07 6D.486 7..655 27.128 13.104 5927.12 � 68.176 1.659 27.255 13.200 5952.44 76.589 1.652 27.363 �3_3D3 5978.03 85.864 1.646 27.513 13.407 6a03.90 96.184 1.640 27.699 13.513 6030.05 107.796 1.633 27.77b 13.620 6055.48 121.045 1.627 27.909 13.729 60$3.20 136.439 1.621 26.044 13.840 611p.21 154.764 1.615 26.180 13.953 6137.51 177.337 1.608 28.317 14.0b7 6165.11 206.629 1.602 26.455' 14.183 6193.02 � 248.169 1.596 26.596 14.301 6221.22 297.480 1.591 28.694 14.384 6240.82 ------------------------------------------------------------------------------ NODE 5006.00 : HGL =< 249.030>;EGL= � 259.290>;FLOWLINE= � 247.290> ♦*+**y+*tix+ytyty��+w*rrw**�w�f*+r***y*�*t*t**iif*yiyrtirti�rz*�t+wf�i�++*rti+i FLpW PROCESS FROM NODE 5006.Oa TO NODE 5006.9Q IS CODE = S UPSTREAhI NpDE 5006.90 ELEVATZON = 297.62 (FLOW TS SUPERCRITICAL) CALCUT�ATE JEJNCTION L05SE5: PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCITY {CFSj (INCH£5i (DEGREES} ELEVATION DEP3'H(FT.) {FT/SECi UPSTREA�i Z06.40 36.00 4.Q0 247.62 2.92 26.706 DOWNSTREAM 1d9.30 36.00 247.29 2.93 • 25.705 LATERAL #1 1.80 16.00 9Q.OD 249.12 0.50 3.445 LATERAL #2 1_10 16_00 90.a0 249.12 0.39 2.996 Q5 0.00=-=45 E4Z7ALS HASIN iNPUT=== LACFCD AND DCEMA FLOW JiTNCTION FbRMLiLAE i3SED: DY=(Q2*V2-4�'V�*COS(DELTAI)-Q3*V3*CbS�DEI,TA3)- � 49 *ti74 *COS {DEE,TA4 y ) / ( (A1+A2 ) * 16 . 1) +FRICTIOI3 E,OSSES UPSTREAM: MRNNIlJG'S N= 0.01300; FRICTION,SEAPE = 0.07415 DOWNS'�'AEAM: MANNII3G'S N= 0.01300; FRICTION SLOPE = 0.466D5 AVERAGED FRECTION SLpPE �N JUNC'I'ION ASSUMED AS 0.07010 JUNC'i'IQN LENGTH = 4. fl0 FEET FRIC`i'FON LOSSES = 0.280 FEET �'Ni'RANCE LOSSES = 0.000 F�ET Ji7NC'�'IaN LOSSES = ( DY+HVl-HV2 } �+ ( �'RANCE LOSSES ) JLTNCTION LOSSES =( 1.055)+( O.QOD? = 1.055 ------------------------------------------------------------------------------ NODE 5006.90 : HGL =< 249.27Q>;EGE,= < 260.345>;FLOWL�NE= < 247.620> *tf**r,o-+w*t�a*+****�*t*t**tt*+tt+tft***++,tt*+*ia+rt**x��*tt+*ty++*f++a+�**vrr*w* FLOW PROCESS FROM NODE 5006.90 TO NODE 5007.40 IS CODE = 1 UPSTRF�t4 NODE 5007.Oa ELEVATION = 259.83 {FLOW IS SiTPERCRITICAL} ------------------------------------------------------------------------------ CALCULATE FRICT30N �ass�st�c�cD1: PIPE FLOW = 1d6.4p CFS PIPE DYA�fETER = 36.00 INCHES PIPE LENGTH = 145.42 FEET MANNING'S N= O.D130fl NORMAL DEPTH(FT1 = 1.59 CRITICAI. DEPTHfFT) = 2.92 UPS'I'REAM CONTROL ASSUMED FLOWDEPTH(FT) = 1.90 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------ GRADUALLY VAI2IED FLOW PROFTLE COMPUTED INFORi�iATION: DISTANCE FR02�4 FLOW DEPTH VELOCITY SPECIPIC PR�SSURE+ CONTROL(FT) [FTi {FT/5EC} ENERGY(FT) MOMFNI`UMIPOUI3D5} 0.000 1.904 22.482 9.757 4881.70 3.067 1.891 22.657 9.$67 4914.01 • 5.308 i.879 22.835 9_980 4947.01 9.7A1 1.8b6 23.016 10.097 4980.64 � �3.384 1.653 23.200 14.216 5015.49 17.255 1.841 23.388 10.340 505�.22 21.384 1.628 23.579 14.466 5086.08 25.749 1.816 23.773 10.597 5122.74 30.519 1.803 23.972 10.732 5160.09 35.600 1.79a 24.174 10.870 5198.28 91.081 1.778 24.379 11.013 5237.27 97.020 1.765 24.589 11.150 5277.10 53.4B5 1.753 24.803 11.311 5317.77 60.562 1.790 25.020 11.467 5359.31 68.357 '1.727 25.242 11.628 5401.73 77.010 1.715 25.4fi8 11.793 5445.07 . � 86.703 I.702 25.699 11.964 5489.34 97.682 �.690 25.934 12.140 5539.56 110.293 1.577 26.173 12.321 5580.76 125.045 1.664 26.418 12.508 5627.96 142.722 �.652 26.667 i2.701 5676.19 145.420 1.650 26.69$ 12.725 5682.2Q ------------------------------------------------------------------------------ NODE 5007.00 : HGL =< 261.734>;EGL= < 269,587>;FLQWLINE= < 259.830> *+tt�r�s*r*tzz+t+i*t�****�*******�+tt�*+�*r+a*t+iw+*s*ww*x****ww**++t+rr�sYi+* FLOW PROCESS FROM NODE 5007.D0 TO NpDE 5007.90 i5 CODE = 5 UPSTREAM NQDE 5007.90 ELEVATION = 260.16 (FLOW I5 SUPERCRITICAL} CALCULATE JUNCTIpN T,OSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CRFTICA� VELOCITY ICFSj (INCHESi IDEGREES) ELEVATION DEP`FIi(FT.) (FT/SEC) UPSTREAM 96.10 36.a0 O.DO 260.1b 2.88 25.429 DOWNSTREAM 106.40 36.a0 - 259.63 2.92 22.489 LATERAL #1 10.30 24.aD 90.00 261.16 L 15 5.515 � LATERAL �2 0.00 a.d0 D.00 0.00 D.00 0.000 Q5 D. 00===Q5 EQUALS �ASII3 IbIPUT=== LACFCD ANA OCEMA FLOW 3UNCTION FORMUI,AE USED: DY=fQ2*V2-Q1*V1*COS(DELT'A1)-Q3*V3*C05SDELTA3}- 44*V4*COS(I}Ei,TA4))/({A1+A2)*16.1}+FRICTION LOSSES IiPSTREAM: MANNING'S N= 0.0�300; FRICTION SLOP� = 0.06951 DOWidSTREA�7: MP.NNING' S N= 0. Q1300; FRICTIOid SLOPE = 0. �4765 AVERAGED FRIC'�'IQN SLOPE IN JUNC'I'IOPi ASSUMED AS 0. D5659 JUNCTION LENGTH = 4.00 FEET FRICTION LOSSES = Q.234 FEET ENTAANCE L055E5 = O.00fl FEET �ITNCTION L055ES = (DY+HV�-I-i�72}+(Ei3'I'RANCE L055ESj J[7t3C'PION LOS5E5 =( 2. 1951 +( 4. Q00} = 2. 195 I30DE' S007.40 : HGL =< 251.742>;EGL= < 271.783>;FLOWLINE= < 260.1bQ> 1 t * ri #'/rY�'k * }*** # # #i#**#*#*i###4fY!*****k i� *�1riF* **i* f ii#+iF*if *iY�f4Y Y4#Yr�t***ir ir f **if+ FLOW PiZOCESS FftOM NODE 5oa�.9a TD NODE saos.oa IS CODE = 1 UPSTREAM NODE 5008.OD ELEVATION = 280.96 (FLOW IS SUpERCRITICAL) -----------------------------------------------------------------___----------- CALCiJI,F1T£ FRICTION L055ES (LACFCD) : PIPE FLpW = 96.10 CFS PIPE DTAMETER = 36.00 INCHES PIPE I,ENGTH = 292.96 FEET I�iANNTNG'S N= 0.01300 ----------------------------------------------------------___-_---------------- NORMAL DEPi'H(FT) = 1.57 CRITICAL DEPTH(FT) = 2.88 UPSTREAM CONTROL ASSIJDSED FLOWDEP'T'H(�"i') = 1.78 GRALIUAL�,YYVA�tIED FLOW PROEILE CO3+3PUTED INFORMATIOAI: � ------------------------------------------------------------------------------ � DISTANCE FROM FLOW DEPTH VELOCITY SPECiFIC PRESSURE+ CON'iAOL{FT} (FT) SFT/SECj ENERGY{FT) MOMENTLT�7(PQUNDS) 0.000 1.779 21.996 9.297 43D6.89 3.339 1.771 22_120 9.374 4327.75 b.852 1.763 22.246 9.452 4348.93 10.555 1.754 22.373 9.532 937Q.40 14.456 1.746 22.5a2 9.5i3 9392.�9 18.607 1.738 22.632 9.697 9419.29 22.999 1.73Q 22.764 9.781 9936.7D 27.672 1.721 22.898• 9.8b8 4459.44 32.657 1.7�3 23.034 9.955 4482.51 37.993 �.705 23.171 10.047 4505.92 43.�26 1.596 23.310 10.139 4529.56 49.909 Z.588 23.951 10.233 A553.74 56.b12 1.580 23.593 1D.328 4578.18 63.937 �.57� 23.73$ 10.426 4602.97 71.929" 1.663 23.884 10.526 452B.13 80.785 1.655 24.032 10.628 4653.65 90.663 1.646 24.182 i0.732 4679.54 101.805 1.638 24.334 i0.839 4705.62 114.550 1.630 24.488 10.947 4732.48 129.395 1.621 24.644 1�.Q58 4759_54 147.110 1.613 24.$03 i�.171 A786_99 168.986 1.605 24.963 11.287 4814.85 197.442 1.597 25.125 � 31.405 4843.12 237.914 1.58B 25.240 11.526 4871.82 292.960 1.582 25.421 13.623 4894.70 NODE 5aa9.00 : HGL =< 282.739>;EGL- < 294.257>;FLOWL�NE= < 2$Q.96Q> � **********��**�+W++*w*��+.*+****+++*****�x+***+*+++�W+w�**�W�+��*W��**++*.* FLOW PKOCESS FRpM NObE 5006_00 TO NODE 5D0$.90 IS COpE = 2 UPSTREAM NODE 50D6.90 ELEVATION = 281.29 (FL�OW IS SUPF�tCR�TICAL? ------------------------------------------------------------------------------ CALCUi�71TE [�ANHOLE LOSSES(LACFCA) : . PFPE FLOW = 96.10 CFS PIPE DIAMETER = 36.00 INCHES AVERAGED VELOC�i'Y HEAD = 7.549 FEET HMN =.Q5*(AVERAGED VELOCITY I-EEAD) _.05"{ 7•544} = 0.377 NODE 5Q08.9D : HGL =< 283.464>;EGL= � 290.634>;F'LOWLINE= < 281.290� *ii* * **Yr * ***iY� # *** # ***i#f i'F }y f *i!t � * # tYr}1rY� YrYr Yr Yr * iF1r*Y� �k �k �k*** **# i **#i� # #! *YY? Y tYt** FLOW PROCESS FROM E�30DE 5006.90 TO NODE 5009.6D IS CODE = 1 UPSTREAM NODE 50�9.00 ELEVATIdN = 295.54 IFLOW IS SUPERCRITTCAL} ------------------------------------------------------------------------__------ CAi,CULATE FRICTION LOSSES(LACFCD): PIPE FLOW - 96.10 CFS PIPE DIAMETEA = 3b.40 INCHES PIPE LENGTH = 295.96 FEET MANNING'S IV = 0.01300 --_--_-----------------------------------�__-__-------------------------------__ NORMP.L DEPTH {FT} = 1. 77 CRITICAi� DEP`!'H ( FTj = 2.$8 UPSTREA2+5'CONTROL ASSUMED FLOWDEPTH(FT) = � 1.79 GRADUALLY VAFtIED FLOW PROFILE COMP4JTED INFORMATION: DISTAi�ICE FROM FLOW DEPTH VELOCITX SPECIFZC PRESSURE+ CONTROL(FT) 1FT} (FT/5EC} ENSRGY(FT) MOMENTUM{pOUNDS) 0.000 �.786 21.9D2 9.239 A291.22 4.452 1.7$5 21.910 9.244 9292.44 � 9.695 1.7$5 21.917 9.248 9293.66 13.948 �_7$4 21.924 9.253 9299.88 • 19.Q29 1.784 21.932 9.257 4296.10 24.36Q 1.783 21.939 9.262 4297.32 29.968 1.783 21.99b 9.266 4298.54 35.883 1.782 2�.953 9_271 4299.76 42.138 1.782 21.961 9.275 4300.98 48.777 1.781 21.968 9.28D 4302.21 55.847 1.783 21.975 9.284 4303.43 � 63.410 1.7$0 21.963 9.289 A304.66 7�.537 1.780 21.990 9.293 4305_E9 80.320 ��.779 21.997 9.298 4307.12 89.872 1.779 22.fl05 9.302 4308.35 100.340 1.778 22.012 9.3fl7 4309.58 111.919 1.778 22.019 9.3�� 4310.81 124.868 1.777 22.027 9.31b 4312.d4 139.557 1.777 22.034 9.324 4313.28 156.523 1.776 22.041 9.325 4314.51 176.599 1.776 22.049 9.329 4315.75 201.182 1.775 22.056 9.334 4315.98 232.892 1.775 22.063 9.338 4318.22 277.611 1.774 22.071 9.343 43�9.4b 295.960 1.774 22.072 9.344 4329.7b ------------------------------------------------------------------------------ NODE 5009.00 : HGL =� 297.326>;EGL= � 304.779>;FLOWLINE= < 295.540> * * W f i i # * # i * f f Y t i t * * * * * * f i i * * * * * * * ! # # i i # f * � * Y � i 1 i * f Y * * i � � � * i Y 3 1 i f * Y Y ! rt * * t * * * * * w Fi�OW PROCESS FROM NODE 5009.D0 TO NODE 5009.9D IS CODE � 5 UPSTREAM NODE 50d9.90 ELEVATIdN = 295.67 (FLOW IS SUPEFtCRITICAL) CRLCULATE JUNCTION LQSSES: PIPE FLOW DTAMETER ANGLE FLOWI,INE CRi3'ICAI, VEI��OC�TY • {CFS) (INCHES) (DEGREES} ELEVATION DEPTH(FT.} (FT/SEC) UPSTREA[�F s9.sa 36.aa a.00 295.B7 2.s� zz.ass DOWNSTREAM 96.10 36.OD - 295.54 2.88 21.909 LATERAL #1 a.ao 18.00 90.00 297,09 0.33 1.922 i,ATERAL #2 4.50 1B.Q4 96.00 297.04 0.26 1.201 Q5 d_QO===Q5 EQUALS BASII� INPUT-== LACFCD AND OC�IA FLOW JUNCTIQN FORMU7yAE i35ED : DY=(42*V2-Q1*V1*COS{DELTAI)-Q3*V3*COS(DEE�TA3f- 44*V4*COSIDELTAA))/((A1+A2)*16.I)+FRICTION L05SE5 UPSTREAM: MANNING'S N= 0.01300; FRIC�IOI3 SLOPE = 0.04953 DOWI3STREAM: MANNING'S N= 0.01300; FRICTION SLOPE = 0.04733 AVERAGED FRICTION SLOPE II+3 JUNCTION A55L734EB AS 0.04$38 JUNCTION LENGTH = 4.00 FEET FRICTIOI3 LOS5E5 = a.194 FEET FNTRANCE LOSSES = 0.000 FEET JUNCTION LOSSES = {DY+HV1-HV2�+(ENTRANCE LOSS�S} �'UNCTI013 LOSSES = S 0.5431+( O.ODO) = 0.5A3 ---------------------------------------------------�--_____-____--___----------- i30bE 5009.90 : HGL =< 297.611>;EGL= < 305.323�;FLOWLINE= < 295.870> Yrf�k�Mi��k***Yi�**** *}*i**}*#i�i�*#***�'F*4 ti i 1 f t**1rt1i*****�***k*Yr*Yr***1rf�FYrYr�k�k##f i#'4y't FLOW PROCE55 FROPf NODE 5009.90 TO A30DE 501fl.Q0 IS CODE = 1 UPSTRE7IM NODE 5010.00 El,EVAT1013 = 309.92 {FLQW I5 SUPERCRITICAL) CAT.CULA'i'E FRTCTION LOSSES (LACFCD) : PIPE FLOW = 94.$0 CFS PIPE DIAMETER = 36.04 INCHES PIPE LENG'I'H = 259.55 FEE?' MANNING'S N= O.Q�344 NOAMAL DEPTH ( FT} - },( g CRiTTCAL ]]EY'I'H { F`1') = 2. 87 ----------------------------- - • UPSTREAM C0�1'PROL ASSUMEB FLOWDEPTf-I ( FT) 2. 67 • • G}�ADUALLY VA12I�D FLOW PROFTLE COMPUTED INFORMATION: DISTANCE FROP4 FLOW DEPTH VELOCITY SPECIFIC PRE55URE+ CONTROL(F"I'j (FT) IF'F/SEC} ENERGY(FT} MdMENTUM(POUNDS) D.OQO 2.672 Z3.607 5.749 3106.27 0.125 2.B25 13.729 5.754 3108.25 D.490 2.778 13.870 5.767 3113.98 1.�87 2.731 14.029 5.789 3123.23 1.91B 2.684 Z4.206� 5.619 3135.90 2.994 2.637 Z4.399 5.658 3151.95 4.328 2.590 �4.609 5.906 3171.38 5.944 2.542 19.837 5.963 3194.26 7.867 2.495 15.082 6.030 3220.b6 10.131 2.44B 15.3A5 6.1D7 325D.58 12.781 � 2.401 15.627 6.195 3284.45 15.B69 2.354. 15.928 6.296 3322.14 19.461 2.307 I6.250 6.410 3363.93 23.641 2.260 16.593 6.53B 341D.02 28.517 2.212 �b.959 6.661 3460.64 34.226 2.165 17.349 6.842 3516.05 40.954 2.116 J7.765 7.022 3576.5$ 48.951 2.071 18.20$ 7.222 3642.52 58.57fl 2.024 18_6B1 7.446 37k4.25 70.329 1.97? 19.1B5 7.695 3792.1$ 85.035 1.930 19.723 7.974 3876.77 1D4.041 1.882 24.29$ 8.2B4 3968.53 129.886 1.835 20.913 8.631 4466.09 168.279 1.788 21.572 9.019 41'75.93 237.547 1.741 22.278 9.452 4292.95 259.560 ------1_74].---- 22.279 9.453 _^-4293_Ob-- NODE 5010.00 : HGL =< 312.792>;EGL= < 315.669>;FLOWLII�i�= < 3Q9.920> f Y#Y#**ittt#tt*Y� i�k�kttt it�ktYtY�kttt**!**t'Mkir*�kk�kYr**YrYr*Yr�k*YriFiFYrYiiMiMl�kf f*?*f#Y�ik*I�#+�F FLOW PROCE55 FROM NODE 5010.00 3'Q NODE 5010.90 I5 CODE = 5 UP5`PREAM NODE 5410.90 ELEVATION = 314.25 (FLOW,UNSEALS IN FtEACH) ___-----------------------_----____----------------------------------------------- CALCULATE �UNCTTQN I,OSSES: PZPE FLDW DIAMETER A�1GLE FLpWLII3E CRITICAL VELOCI�'Y {CFS) (INCHES) (AEGREES} ELEVA"I'ION DEPTH(FT.} (FT/SEC) iJPS�REP.M 60.30 3&.00 0.46 310.25 2.51 8.531 DOWNSTREAM 94.80 36.�� - 3D9.92 2.$7 13.bZ1 LATERAL #1 32.5D 30.0� 6Q.00 310.42 1.94 5.b21 LATERP.L #2 2.4Q 24.00 64.00 310.75 0.49 0.537 Q5 4.OQ===Q5 EQUA�,S BASIN INPUT=== LACFCD AND OCEMA FE�OW JUNCTION FORMULAE USED: DY={aZ*V2-Q1*V1*COS(DELTAI)-Q3*V3�COS{DELTA3)- (24*V4*COS(DELTA4))/((A1+A2)*16.1)+FRICTIOd3 LOSSES UPSTAEAM: MA�Ii�ING'S N= 0.0130p; FRICTION SLOPE = d.00817 DOWNSTREAf4: MANNING'S N= D.01300; FRICTTOid SLOPE = Q.01757 AV�RAGED FRICTION SLOPE IN JUNCTION A55UMED AS a.42287 3UNCTION LENGTH = 4_00 FEET FRICTIpN LOSSES = 0.051 FEET ENTRAIVCE LdSSES = 0.000 FEET ,7UNCTTON LQSSES = (DY+HV1-HV2)+(EN'PRAI�CE L05SES) Ji1NCTI0N LOSSES =( 1.260}�I O.Opp) � 3.2fi0 NpDE 5010.9Q : HGL =< 315.799>;EGL= � 315.929>;FLOWLINE= < 31fl.250� • +r*�i+tr+tft+farri.t****+xx++�xx��+k��*t++**�*r�*tfiaxww��+�w�*�r++++» r*rr*�* • FLOW PROCESS FROM NODE 5030.90 TO NODE 5011.00 IS CO�E = 1 UPSTREAM NODE 5fl11.00 ELEVATION = 328.50 (HYDRAULIC J[7[�SP OCCUR5) -----�-----------------------------------------------------------�------------ CP.i�CULATE �RICTIpN LOSSES(LACFCD): PIPE FLOW = 60.30 CFS PIPE DIAMETER = 36.fl0 INCHES P�PE LEI3GTH = 302.57 FEET NSANNING'S N= D.Q�3Q0 HYDfZAULIC Ji.Jt+4P: DC}WNS'PREAM RLFN ANALYSIS RESUL�'S NORMAI, DEPTH(FTj = �.26 CRITiCAL DEPTH(F'T) � 2.51 UPSTREAMJCONTROLTASS[7MED FLOWDEPTHSFT} � 1.75 'TGRADUALLY VAFtIED FLOW PROFII.�E COMPUTED INFORMATION: ------------------------------------------------------------------------------- DISTANCE FROM FL,OW DEPTH VEi,OCTTY SPECIFIC PRESSURE+ CO�TI'ROL ( FT 1 ( FT } ( F'�' / SEC } Ei�3ERGY { FT ) MOi+fEf7TiJM ( POUAIDS ) O.Q4D 1.750 39.OB6 4.832 1847.78 1.63b 1.730 14.280 4.898 1865.21 3.397 1.71fl 14.479 4.966 1883.40 5.297 1.641 14.664 5.041 1902.35 7.344 1.671 14.896 5.119 1922.12 9.569 �.652 15.114 5.201 1942.72 11.977 1.632 15.339 5.288 1964.18 7.4.593 1.612 15.572 5.380 � 1986.55 � 17.4A2 1.593 • 15.811 5.477 2049.84 20.556 1.573 16.a58 5.584 2a34.11 23.969 1.554 16.3�3 5.689 2459.39 27.725 1.534 16.577 5_804 2485.72 31.878 1.514 16.$49 5.926 2113.Z3 36.493 1.495 17.131 b.055 2141.69 . • 41.654 1.475 17.422 6.191 2171.93 47.467 1.456 17.723 6.336 220Z.42 54.074 1.436 18.039 5.489 2234.74 61.666 1.417 18.356 5.652 2268.33 7Q.513 1.397 18.69p 6.825 2303.37 B�.OQ6 1.377 19.036 7.00$ 2339.90 93.755 1.358 �9.395 7_202 2377•98 �D9.784 1.338 �9.767 7.409 2417.68 i31.Q47 1.319 20_152 7.629 2459.09 161.732 1.299 20.553 7.862 2502.29 215.'179 1.279 20.969 8.111 2547.37 302.570 1.279 20.980 8.118 2548.56 HYDRAULFC JUMP: UPSTREP.M RUN ANAI�XSIS RESULTS ----------------------------- _ DOWPFSTREAM CONTROL ASSiJ�7ED PRESSURE HEAD ( FT j 5. 5 5 PRESSURE FLOW PROFTLE COMPUTED INFORMATION: - DISTANCE FRdM PRESSURE VELOCITY SPECIFIC PRESSURE* CQ�1'PROL { gT ) HEAD ( F'T } { FT / SEC j EIVERGY ( FT ) MOMEN7'UM ( PQUNDS i d.a00 5.549 8.531 6.679 2782.94 48.891 3_000 $.531 4.134 1b58.47 ASS[,TMEi] DOWNSTREAM`PRESSURE HEADIFT] = 3.00 GRADUALLY \TARIED FLOW PROFTLE COI�SP(]'I'ED INFORMATION: -------------�---------------------------------------------------------------- . DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROLIFT) (FT} SFT/SEC) �'NERGY(FT] 3�70MENTUM(PpUNDS1 � 48.891 3.000 8.52B 4.130 1558.47 49.230 2.980 8.536 4.112 1650_67 49.533 2.961 8.55D 9.096 1b43.53 44.814 2.941 8.568 9.Q81 1637.34 50.477 2.921 8.590 9.058 1630.98 ' S0.325 2.941 8.614 4.059 1625.22 50.558 2.882 8.542 4.042 1619.61 50.779 2.862 8.671 4.030 1614.72 50.987 2.842 8.7Q4 4.019 1609.92 51.182 2.$22 B.738' 4.009 1605.42 51.367 2.$03 B.779 3.999 1601.21 51.540 2.783 B.8�3 3.990 1597.27 51.702 2.753 8.853 3_9B1 1593.60 51.852 2.743 6.895 3.973 1590.20 51.992 2.724 8.940 3.966 i587.07 52.120 2.704 8.987 3.959 1584.21 52.237 2.684 9.035 3.953 1581.61 52.343 2.665 9.065 3.947 1579.28 52.437 2.645 9.137 3.942 1577.21 52.520 2.625 9.191 3.938 1575.42 52.591 2.605 9.247 3.934 1573.89 52.650 2.586 9.304 3.931 1572.b3 52.696 2.566 9.364 3.928 1571.65 52.729 2.546 9.426 3.927 1570.99 52.750 2.525 9.489 3.925 1570.52 52.757 2.507 9.555 3.925 1570.37 302.570 2.5a7 9.555 3.925 1570.37 ------------------------END QF H7CDRAULIC JUMP ANALYSIS------------------------ I PRE55URE+MOMENTUM BA�NCE pCCURS AT 10.20 FEE'I'[JPSTREAM OF NODE 501D.90 -DOWNSTREAM DEPTI-f = 5.418 FEET, UPSTRSAM COI3JUGATE DEPTH = 1.279 FEET . ------- --------------------------------------------___--__-__-------------- NQDE 5031.60 : HGL =< 330.250>;EGL= � 333.332>;k'LOYTI,I23E= < 328.500> **yr** # i� # 14'k#'f'1iF�Y*i � *Y Y***rt * *i * � **Y� 1� * Y� #* f'�y'� t f'tt t**�r*�k1rA �rtkYr*Yrf YriFYriF! y * *#*'�'�+Y�#t t Fi,OW PROCESS �'ROM NODE 5012.00 TO NODE 5Q11.9Q IS CODE = 5 UPSTREAM 3�IODE 5011.9Q ELEVATION = 328.83 (FLOW IS SUPERCRITICAL} CALCULATE JUNCTIOIV T,QSSHS : PIPE FLQW DIAMETEFt ANGLE FLOWLINE CRITICAL VELOCITY (CF5) (INCHES) (DEGRE�S) ELEVATION DEPTI-4{FT.? �iFT/SEC) UPSTREAM _54.80 35.00 0.60 328.83 2.40 15.711 DOWNSTREAM 60.30 36.00 - 328.50 2.51 14.090 LATERAL �1 3.00 18.OD 9D.00 330.33 0.66 4.D18 LATERAL �2 2.50 18.00 _ 9D.00 334.33 0.6Q 3.798 Q5 0.00===Q5 EQUALS SASIN INPUT=== �,ACFCD AND QCEMA FLOW J[3NCTION FORMULAE USED: aY=f42*v2-41*V1"COS(DEL'PA1}-Q3*V3*COS{p��,TA3)- Q9 * V4 *COS ( I]ELTA4 } ) / ( (A1+A2 f *16 . 1 } +FRIC'i'IOi�1 LdSSES i7P5TREAM: MANNING'S N= Q.01300; FRICT�ON SLUFE = Q.02797 DOWNSTREAM: MPNNING'S N= D.0130D; FRICT�ON SL(}PE = 0.01977 AVERAGED FRICTIOi3 SLOPE IN JiFNCTIpT3 ASSiJr3ED AS 0.02387 ,JiJNCTION LENGTH = 4.40 FEET FRIC'i'�ON LOSSES = 0.095 FEET EN'T'RANCE LOSSES = D.4Q� FEET JUNC'FION LOSSES = (DY�-HVl-HV2f+IF�7TRANCE LOSSES) Ji7NCTION LOSSES =( a.815}+( 0_OOOi = 0.815 ' NODE 5011.90 : HGL =< 330.315>;EGL= < 334.148>;FLOWI.�NE= � 328.83D> ��*********+*.t�+�ti+,��.,*+*.�*.***.**��*�*�+�.*��,�..*********�.*�*�.**+,�*��«.+ • FLOW PROCESS FROM NODE 5031.90 TO NODE 5012.OQ T5 CODE = 1 � --UPSTREAM NODE 5012.00 ELEVATION = 337.12 (FLOW IS SUPERCRITICAL) CA�CULATE FRICTIDN LOSSES{LACFCD): PTPE FLOW = 54.B0 CFS PiPE DIAMETER = 36.00 INCHES PIPE LIIdGTH = 271 .74 FEET MATFNING' S N = 0.0134Q TNORMAL DEPTH(FT) = 1.45 CRITICRL DEPTH(FT� = 2.40 UPSTREAM^CONTROL ASSiJ�7ED FLOW3?EPTN(FT� = 2.40 yYGRA�UALLY VARIED FLOW PROFILE COI�fP1JTED INFORMATION: -------_----------------------------------------------------------------------- DISTANCE PROM FLQW DEPTii VELOCI'I'Y SPECIFIC PRESSURE+ COd3'I'ROL ( F'i'? { F'T } ( FT / SEC f EE'IERGY � FT j MOME�7TL7t�7 ( POUTFDS } O.QQO 2.399 9.042 3.6b9 1372.32 0.470 2.361 9.182 3.67a 1372.93 0.253 2.322 9.330 3.67� 1374.57 0.59Q 2.264 9.A86 3.682 1377.28 1.066 2.246 9.650 3.693 1381.11 1.707 2.208 9.822 3.707 1385.09 2.529 2.170 �0.444 3.725 t392.29 3.557 2_132 �O.Z95 3.747 2399.74 4.819 2.Q94 10.397 3.774 1408.52 6.333 '2.Q56 14.509 3.805 �416.68 8.150 2.0�8 10.833 3.841 1430.30 1d.310 1.980 11.068 3.884 1443.49 •. i2.869 1.992 11.317 3.932 1�458.20 15.895 1.909 11.579 3.987 1474.65 Z9.477 1.$66 11.855 4.Q50 1492.92 23.728 1.82$ 12.147 4.�20 1513.09 � 28.797 1.790 12.455 9.20Q 1535.28 34.866 1.752 12.7B2 4.290 1559.63- 42.282 1.719 13.127 A.391 1586.27 51.403 1.b76 13.493 4.544 1615.36 b2.898 Z.638 13.BBi 4.631 1647.08 77.857 Z.60fl 14.293 4.779 1681.62 98.324 1.562 14.731 4.933 17�9_19 128.896 1.524 15.197 5.112 1760.02 1$4.320 1.4B5 15.694 5_312 1804.36 27J..740 1.485 15.706 5.318 1805.5D ------------------------------------------------------------------------------ NODE 5012.Q0 : HGL =< 339.519>;EGL= < 340.789>;FLOWLIPIE= � 337.120> fit+�tt*t*****+s„�x+*k***+*x*++�*+*ssf+**tr*s�**x+*++++*+v.�rv.v�tWsf*sf**f**+**+*+ FLOW PROCESS FROM NODE 5012.OQ TO NQDE 5012.9D IS CODE = 5 UPSTREAM NODE 54t2.90 �LEVATIQN = 337.45 (FI.,OW U3�SF.AIsS IN REACH) (NOTE: POSSISLE JUMP IN OR 43PSTREAM OF STRUCTURE) -------------------------------------------------------------------------------- CA.IICULA'i'E ,7lR3CTYON LOSSES: PxPE FLOW DIAt�ETER ANGLE FLQWLII3E CRITICAL V�LOCITY {CFS} (II3CH£S) (DEGREES) ELEVATIODI DEPTH(F�'.) (FT/SEC} UPSTREAM 44.30 36.OQ 4.00 337.45 2.1'7 13.623 BOWNSTAEAM 54.80 36.00 - 337.12 2.4fl 9.030 LATERAL #1 14.5Q 24.00 9D.00 338.45 1.16 5.553 -i.ATERAL #2 a.ao 0.04 0.00 0.00 0.04 6.000 Q5 0. dQ===(25 EQUAE�S BASIN INPUT=== LACFCD AND OCEMA FiAW JUNCTTON FORMUi�E USED: 1]X=iQ2*V2-Q1*V1*CQS(DELTAIJ-Q3*V3'CQS(DELTA3)- � Q9*V4*C05[DELTA4))/ffA1+A2)*16.1)+FRICTIOI+1 L055E5 UPSTREAM: MPNNING'S N= 0.01344; FRICTION SLOPE = O.Oz206 � DQWNSTREAM: MANNING'S N= 0.013flD; FRICTION SLOPE = O.Q0705 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS �.01955 JUPiCTION LENGTH = 9.00 FEET FRICTION LOSSES = 0.058 FEET ENTRANCE LOS5E5 = 0.000 FEET J[ii�iCTIQt�F LOSSES = (DY+HV1-HV2j+(ENTRANCE LOSSESj J[if�3CTI0PI LOSSES =( 0.9A9j+( 0.000} = 4.949 NODE $012.90 : HGL =< 338.856>;EGL= < 341.738>;FLOWLINE= � 337.450> .*.++++*��,.***.+**,.+.**.*****++*�w.*��.��***.*+**.+,��*�*.*.*.***.�:«�****++.. FLOW PROCESS FROM NOBE 5Q12.90 TO AiODE 5D13.00 IS CODE = 1 UPSTREA�1 NODE 5013.00 ELEVATIOA3 = 343.53 (�'LOW IS SUPERCRITICAL) CALCi7LATE FRICTION LOSSES (i�ACFCD) : PIPE FLOW - 44.30 CFS PIPE DIAMETER = 36.00 INC�3ES � PIPE LENGTH = 255.03 FEE'i' MANNING'S N= 0.01300 ------------------------------------------------------------------------------- NOAMAi� DEPTH {FT) = 3.37 CRITICAL DEP'PH ( FT) = 2. 17 UPSTRF'.P.M'CON'I'ROLRASSUMED FLOWDEP'FH(FT) = 2.17 . GRADUALLY VARIED FLOW PROFTLE COMPUTED INFORMA3'FON: ------------------------------------------------------------------------------ DIS7`ANCE FROM FLOW DEPTH VELOCI7'Y SPECIFIC PRE55URE+ CON'F'RdL { F'T ) ( FT ) { g'�' / S�C ) ENF3tGY ( FT ) MOMENTUM { POl7NDS ) O.DOD 2.168 8.096 3.186 Ia24.05 0.053 2.136 8.225 3.187 1Q24.37 0.219 2.105 8.359 3.190 1Q25.35 6.509 2.073 8.500 3.I95 1027.b1 0.936 2.041 $.646 3.2Q3 1Q29.37 � 1.515 2.010 8.799 3.213 1Q32.47 2.264 1.978 8.959 3.225- 1035.34 3.203 1.946 9.Z27 3.240 1091.aa 4.355 1.914 9.301 3.259 1045.49 5.750 1.8B3 9.984 3.284 1052.86 7.422 1_851 9.675 3.3Q5 lOfi4.13 9.412 1_619 9.876 3.339 1D68.35 11'.771 1.7B7 30.485 3.368 1077.56 14.563 1_756 10.305 3.4Db 1087.83 17_868 1_724 10.535 3.448 1099.19 21.789 1.692 14.777 3.497 ].111_72 26.462 1.660 11.031 3.553 1125_47 32.D79 . 1.629 11.297 3.6�2 1140.51 38.883 1.597 11.578 3.584 1156.9i 47.271 1.565 I1.873 3.755 1174.77 57.830 1.534 12.�83 3.844 1194.1b 71.552 1.502 i2.511 3.934 1215.Z9 90.296 1_470 �2.857 9.038 1237.97 118.244 1.436 13.222 9.155 1262.64 166.811 1.407 13.b08 9.284 1289.23 255.03D 1_4p6 13.619 9.288 1289.97 ------------------------------------------------------------------------------- NODE 5013.OD : HGL =< 345.698>;EGL- < 346.715>;FLOwLINE= < 343.530> ,.,,+*,,**.+***.*��+�t+***t��w��*�.**+**.**�**.+++++t..��..+.�t�+ww*t**�**.��* FLOW PROCE55 FROM NODE 5013.Dfl TO NODE 5013.90 IS CODE = 5 UPSTRF�IM NODE 5013.90' ELEVATI4N = 344.43 ;FLOW UNSEALS IN REACH) -----------------------------------�------------------------------------------ CALCULATE JUNCTION LOSSES: • PEPE FiAW DIAMETER ANG�E FLOHTL�NE CRITICAL VELOCITY ICFS} (INCHES) (DEGREES} ELEVA`FIQN I]El�'I'I-i{FT. j [F'�`/SECj � � C J UPSTREAM 42.10 30.00 90.00 344.03 L70WNSTREAM 44.34 36.OD - 343.53 LA`rERAL #1 2.20 18.00 9Q.D0 345.03 LATERAL #2 b.Q4 0.00 4.00 0.00 Q5 Q.00==-Q5 EQUALS BA5�N TNPUT=== 2_17 2.�7 0_5G 0.00 $.577 8.096 1.245 O.ODO E�ACFCD AN3? OCFMA FLOW JUNCTION FORMULAE USED: �y�{Q2*V2-Q1*V1*COS(17ELTA1)-Q3*V3"'COS(DELTA3}- Q9*V4*COS(DELTA4�j/(fA1+A2?*16.li+FRICTT033 LOSSES UPS'FREAM: MANI3ING'S �I = D.0134Q; FRICTION SLOPE = 0.01453 DOWNSTREAM: MP.i�IIdI?3G' S i�7 = 0.01300; FRICTION SLOPE = 0.00580 AVERAGED FRICTION SLOF'E IN JUNCTFON ASSUMED AS D.00817 JUNCTION LENG'FH = 4.Oa FEET FRICTION i10SSES = 4.033 FEET �ITRRNCE LpSSES = 0.000 FEET JE7I3CTION �OSSES =( DY+HVl-HV2 j+( ENTRP.NCE i�OSSES j JLFNCTIaN LOSSES ={ 2.303}+( 0.0001 = 2.343 ^ NODE 5013 90 � HGL^='� 347 $78>;EGL= < 349.02Q>;FLOWLIN�= < 344.43D> *!****'k+�'y' Y Y 1*�r#i t1�'k k k�'kk'k'k *#'k'k1 * t***i� *'M k'k'k ** ***'t Y' �4 Y t i*i**i k*Yr*}# **tt4! Y* t*k *1r'k Fi�C)W PROCE55 FROM NODE 50I3.90 TO NODE 501A.00 YS COD£ = 1 UPSTREAM NODE 5414.00 EI,EVATION = 345_29 {�'I,pW IS UNDER PRESSUREj CALCULATE FATCTION LOS5E5(LACFCI3): PIPE FLOW = � 42.10 CFS PIPE DIA�fETER = 30.D0 INC3-lES PIPE LENGTH = 54.91 FEET MANNING'S fi = 0.01300 S�'=iQ/K1**z = i( 42•101/i 410.177))**2 = 0.01053 HF=L*SF = ( 54.91)*(Q.01053} = D.578 --------------------------�-_--_----------------------------------------------- fVOAE 5014.00 : HGL =� 3A6.456?;EGi�= � 349.599>;FLOWLINE= < 345_29Q> i*'k'Ir*Yr**#***'t YY� Y i i Yt iY� *+t *! f�MYrYr**i�*'F �� t t* *!� f� yr k*#**** *#`�tt**i t Y***�k �M i'RY� * f*Yr �rt*'t* FLOW PROCESS FROM NODE 5014.Q6 TO P10DE 5015.D0 �S CQI7E = 3 UPSTREP.M NODE 50�5.00 ELEVATION = 348.90 IHYD�AULTC JUMP OCCURS) CAF,CULATE PIPE-BEND LOSSES{pCEMAj; PIPE FE.4W = 42.10 C�'S PTPE DIAME'I'ER = 30. �0 INCI-IE5 CENTRAL ANGLE = 34 . 500 rJEGREES MAi�T�I35]G' S N= 0. 01300 PI PE L�TdGTH = 15 6. 7 6 FEET I-EYDRA[7�YC �3LJ3+]P: DOWNSTREANf RUN ANAE�Y5I5 RES1Ti.TS -------------------------- NQFtMAL DEPTIi(FT) 1.51 CRITICAL DEPTHSFT? = 2.17 ------------------------------------___ UPSTAEAM CONTi20L A55LT�5ED FLOWDEPi'H(FT1 = 1.46 ---------------- GRADUALLY VARIED FLpW PROFILE COMPUTED INFORMATION: �DTSTANCE FFtdM Fi,OW DEP'1`H VELOCITY SPECIFIC PRESSURE+ C4N'FROL ( FT ) ( FT) { F'I`/ SEC ) ENERGY ( FT ) MOMENTiTM ( POiJi�FL1S ) o.aaa 1.463 19.105 4.554 126B.48 3.340 1.465 39.685 4.547 1267.14 6.813 1.466 14.Q64 4.5A0 1265.81 10.431 1.468 14.a44 4.533 1264.49 19.246 1.A70 14.Q24 4.525 1263.17 18.154 1.472 19.004 4.519 1261.86 22.293 1.473 13.989 9.512 1260.55 26.5A3 1.475 13.9b9 4.SQ5 1259.25 31.229 1_477 13.949 4.498 1257.95 36.080 1_4�9 13.929 9.493 125b.66 41.23Q 1.480 13.909 9.489 1255.38 � 46.719 1.482 33.889 4.477 1254.10 � 52.598 1.484 13.865 4.471 1252.82 58.930 1.486 13.895 4.464 1Z51.56 65.794 1.487 33.82b 4.457 125D.29 73.291 1.489 �3.806 4.451 1249.04 81.555 1.491 �3.787 4.444 1247_78 90.767 1.493 Z3.7b7 4.438 1246.54 1O1.1B0 1.494 33.798 4.431 1245.29 113.166 1.496 Z3.729 4.425 1244.06 127.305 1.498 13.71Q 4.41B 1242.83 144.557 1.500 i3.690 4.Al2 124L 60 156.760 1.501 13.580 4.4flB 124fl.93 ------------------------------------------------------------------------------ f3YDRAULIC JUMP: UP5'FREAM Ri]FF ANALYSiS RESULTS ------------------------------------------------------------------------------ --- ------------------------------------------------------------___-______----- DQWNSTREAM CONT3�OL ASSUMED PRESSUAE HEAD(FT} - 3.17 ------------------------------------------------------------------------------ PRESSURE FLOW PFtOFILE COMPFJ'I'ED INFORMATION: DISTAPICE FROM PRESSi3RE VEIACITY SPECFFIC PRESSURE+ CONTROLIF'T} HEAD(FT} {FT/SEC) ENERGY(FT} MOMENTUM(POLTNDS} ' 0.444 3.166 8.577 4.30B 1285.65 62.23b 2.500 8.577 3.642 1082.60 ------------------------------------------------------------------------------ A$Si.7MED DpWNSTREAM Pi2ESS[iFtE HEAI){gT) = 2.50 ------------------------------------------------------------------------------ GRADi3ALLY 1iAR�ED F7,C)W PROFILE COMPUTED II3FOHMATiON: --------_---------------------------------------------------------------------- DISTANCE FROM FLOW DEPi'H VELOCITY SPECIFIC PRESSUAE+ CONTROL{FT) (FT} (FT/SECy ENERGY(F'i') MOt+3ENTUMfPOUNDS) 62.236 2.5Q0 6.574 3.692 ' 1082.60 �' 63.144 2.487 6.579 3.631 1079.03 63.931 2.974 8.589 3.620 3075.B5 . 69.648 2.461 8.603 3.6Z1 3.p72.91 65.310 2.448 8.518 3.602 Z070.17 65.924 2.434 8.636 3.593 1057.62 66.49B 2.421 S.b55 3.585 IOb5.22 67.034 2.408 8.57b 3.578 I052.9$ 67.536 2.395 8.699 3.57� 1050.88 66.005 2.382 8.729 3.569 1058.92 68.443 2.369 $.749 3.558 1057.09 6B.851 2.356 $.777 3.553 1a55.39 69.234 2.343 8.805 3.547 1053.81 59.582 2.33fl 8.835 3.542 1052.35 69.9Q5 2.316 8.867 3.538 1051.0� 70.2Q1 2.303 8.899 3.53A 1049.80 70.471 2.290 8.933 3.530 1048.70 74.713 2.277 8.968 3.527 1047.71 70.928 2.269 9.005 3.524 1046.84 71.115 2.251 9.042 3.521 1046.a9 71.275 2.238 9.081 3.519 1045.46 71.408 2.225 4.121 3.517 1044.93 � 71.511 2.27.2 9.162 3.516 1D49.53 71.586 2.198 9.204 3.5�5 1094.23 71.632 2.165 9.248 3.5�9 1044.06 71.697 2.172 9.293 3.514 }.044.00 155.7b0 2.172 9.293 3.519 �OA4.pp ------------------------gND OF HYDi�AULIC JU1�4P ANALYSIS------------------------ � PRESSURE�MOM�NTUM BAT.,ANCE OCCURS AT 13.71 FEET UPSTREAM OF NODE 5019.40 � ' � DOWNSTREAM DEPTH = 3.019 FEET, UPSTRF.AM CONJLTGATE DEPTH = 1.499 FEET � . ------------------------------------------------------------------------------ � NODE 5415.00 : HGL =< 350.363>;EGL= < 353.454>;FLOWLINE= < 348.900> �x*+att****y*s*s*it*t++***sf*+++ys�f+a+t*+++*+tt��*�*.****�**rr+r++��****�*a*� FLOW PAOCESS FROM NODE 5015.4a TO NODE 5015.90 IS CODE = 5 UPSTREAM NODE 5415.9D ELEVATION = 349.23 (FLOW IS S�PERCRITZCAi,) CALCULATE 3UNCTION LOSS�S: PIPE FLOW DIAMETER ANGLE FLOWI�INE CRITICAL �iELOCIT'Y fCFS) (INCHESj (DEGREES) ELEVATION 1�EPTH(FT.) (F'�`/SEC) i7PS'rRF.ars 3$ .10 34 . QO 0. 00 349 . 23 2. 09 15 . 821 DOWNSTR� 42.10 30.Q0 - 348.90 2.17 14.109 LA�'ERAL #1 4.00 18_OQ 90.00 350.23 0.77 A.412 LATERAL #2 D.00 o.aa 0.00 0.00 0.04 0.000 Q5 O.Op=--QS E4L7ALS BASIA3 IIdPU'r=�= LACFCD P.iJD OCEMA FLOW JU13CT'ION FORMI.FLAE USED: DY=(Q2*V2-Q1''V1*COS(DELTAI}-Q3*V3*COS(DELTA3�- Q4*V4iCOS(DELTA4})/((A1+A2)*16.1)fFRICTION LOSSES LFPSTFtEAM: M.a,NNING'S N= Q.0130fl; FRICTION SLOPE = O.Q3631 D(7WNSTRE.n,M: MANNENG'S N= Q.013D0; FRICTIpsi SLQPE = O.D2522 AVERAGED FRTCTIQN SLOP� IN JL3NCTION ASSUM�D AS 0.03Q76 JUNCTION LENGTH = 4.00 FEET FRICTI03+i LOSSES = 0.123 FEET ENTRANCE LOSSES = O.D�O FEET JlJi+7CTI03�F LOSSES =( DYti-IVl -HV2 )+( EN'i'RANCE LOSSES j JiFNCTIOFI LOSSES = ( 0 . 894 } + ( 0 . 000 } - 4 . 899 ------------------------------------------------------------------------------ NODE 5015.90 : HGL =� 350.462>;EGL= � 359.34$>;FLOWi�INE= � 349.230> t�} �k �1! y 1 t ir YiYY�YY 3!Y*yr4�iYiy� # M#*+�+�F�Y #yYy y�yryriF�fi1 yrfYli}#*}}{� ****i� * iY**�F Yc f***iF***Y� #* i PLOW PROCESS FROM NObE 5015.90 TO NOD� 5ozo.aa IS CODE = 3 � UPS'I'fiEP.M NODE 5020.Q0 ELEVATION = 35&.93 (FLOW I5 SUPERCAITICAL) CALCUI�ATE PIPE-BEidD LOSSES (OCEMA) : P�PE FLOW = 3B.10 CFS PIPE DIAt+SETER = 30.00 INCHES � CENTgAi� ANGLE = 53.5DD BEGREES MANNING'S iV = d.01300 PIPE LENGTH = 242.46 FEET NORMP.L DEPTH ( FT} - 1. 20 CRITTCAL 1]EP'I'H {FT j= 2. D9 ------------------------------------------------------------------_------------ UPSTREAM C�NTROL ASSUM�A FLOWAEPTH(FP} - 2.09 --------------------------------------------------------------___�__----------__-- GRADi7ALLY iIARIF� FLQW PROFILE COl4Pi3TED It3FORI�ATION: ----------------�------------------------------------------------------------- D�STANCE FROM FLOW DEPTH VELOCITY SPEC�F�C PRESSURE+ CONTROI, ( F'£ j ( FT ) ( F3' / SEC ) ENERGY { FT j MOMENTUP4 ( PQUNDS ) a.aaa 2.0$6 $.709 3.263 909.51 4.D46 2.050 8.84Q 3.265 909.90 0.189 2.015 8.989 3.269 90b.09 0.438 1.979 9.138 3.277 908.11 0.802 1.944 9.301 3.286 91D.98 1.295 1.906 9.474 3.303 914.75 1.930 1.673 9.657 3.322 9i9.46 2.725 1.837 9.851 3.345 925.14 3.700 1.B02 10.057 3.373 931.85 9.878 1.766 10.275 3.906 , 939.64 6.290 1.730 10.506 3.946 948.57 7.971 1.695 1D.751 3.991 95B.70 9.965 1.559 11.411 3.543 970.13 12.326 Z.524 I1.286 3.603 982.86 � 15.126 3.588 I1.578 3.671 997.Q5 � 18.453 1.553 1}..889 3.749 1012.78 r -1 � i . 22 27 33 40 49 61 77 �O1 �46 242 427 21� 033 228 317 172 939 �sa 069 460 T.517 �.482 1.446 3. . 411 3.375 2.339 1.304 Z.268 �.233 �.232 12 12 12 13 13 14 14 7. 5 15 15 219 57Q 944 343 769 224 711 234 795 616 3.837 3.937 4.049 4.177 4.320 4.483 4.657 4.$74 5.149 5.118 103Q.15 1049_26 107Q.26 1D93.29 ��a.�i 1146.09 117b.25 1249.21 1245.23 1246.55 -----------------------------------___----------------------------------------- NODE 5020.00 : HGL =< 361.016>;EGL= < 362.193>;�4WLIrlE= � 35&.930> **�*********+*****..**�*t+*��*t�****.**�***.,.*,.*,..*,.****.*...*,.*.*�****x��*,,�** FI,OW PROCE55 FROM NQDE 5Q2D_Oa TO NODE 5020.90 IS CODE = 5 UPSTREAM NQDE 5020.90 EL�I/ATIQN = 359.05 (FL,UW UNSEALS IN REACH) CA%CLTLATE JUNCTION LOSSES: PiPE FLOW DIAMETER ANGL� FLOWI�IAIE CRiTICAL VELOCI'T'Y -(CFSi iINCHE51 (DEGR�ES) ELEVATION DEPTH(FT.) {�'/SEC} UPSTREAM 26.50 30.00 0.00 359.05 1.82 5.606 DC}WNSTREAM 38.10 30.00 - 358.93 2.09 8.707 iATERAL #I 9.60 24.00 90.00 359.55 1.11 3.056 LATERAL #2 0.00 0.00 0.00 fl.00 4.00 0.000 Q5 0.00==-Q5 EQUALS SASIN INPUT=== LACFCD AND OCF.MA FLOW JUNCTION FOR3�7ULAE USED: DY=(¢2*V2-Q1*V1"COS(DEL�'A1)-43*V3*COS(DELTA3)- �4*V4*COS(DELTA4)]/1(A1+A2y"'16.1}+FRICTION LOSSES UPSTREAM: MA�FSFING'S N= 0.01300; FRICTIOI� SLOPE = D.00483 DOWNSTREAM: MIiNNING'S N= 0.01300; FRICTION SLOPE = 0.00837 AVERAGED FRICTI023 SLOPE IN J[3�iCTION ASSUMED AS 0.00564 JiJNCTION LENGTH = 4.00 FEET FRICTION E�pSSES = 0.026 E'EET Et3TRANCE L05SES = Q.D00 FEE'F JliTiCTipN LOSSES =( DY�HVI-HV2 }+( EI�TRANCE Lp55E5 } J[7PiCTION LOSSES =( 0.985)+( 0_000} � 0.485 NODE 5020.90 : HGL =< 362.155�;EGL= < 362.b78>;Fi,OWLINE= < 359.050> �k*#�k*�k #****#t *ttt1�*t**t*Y�l*#1�!**�k*Yr�k*�kY�YrYiiMyrM'i�tM'*Y�***Y�f�*�lrlrfl�tM***YciMf *Yri1r*i�**i�*i�*1�* FLOW PROCESS FROM NODE 5020.90 TO NODE 5030.40 iS CODE = 3 UPS'i'RF_AP4 3JODE 5030.00 ELEC7A'i'ION = 361.26 (HYDRAULIC JUMP OCCURS} ------------------------------------------------------------------------------ CALCULATE PIPE-BFND L05SES(OCEMAI� PIPE FLOW = 28.50 CFS P�PE DIAMETER = 30.00 ENCHES C�N'F`itAL ANGLE = 47 .7Q0 bEGREES MANNiNG' S N= 0.01300 PIPE LENG'i'H = 220.69 FEE'I' HYDRAULIC JUMP: DOWNSTREAM RUN ANA%YSIS RESULTS I30R�77�L DEPTH(�'T) = 1.53 CRITICAL DEPTH(F'i') = 1.82 UPSTREAM CONTROL ASS[JMED FLOWDEPTH{FT} = 1.82 ------------------------------------------------------------------------------ ---_____--------------------------------_---------------------------------------- GRADi3ALLY VARIED FLOW PRdFILE COMPiJTED I�3FORMATION: ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSiTRE+ CON'I'RpL ( FT } ( FT ) f FT / SEC } ENERGY ( F�` ) MONfFNTUM ( POUNDS } O.D00 1.820 7.492 2.681 604.60 0_040 1.809 7.992 2.581 604_64 �.163 1.797 7.543 2.b81 504.74 • 0.377 1.786 7.595 2.662 609.92 0.690 L 774 7.648 2.683 6fl5.17 1.113 1.753 7.702 2.58A 605.49 1.656 1.751 7.757 2.586 605.89 2.332 1.740 7.813 2.688 606.37 3.157 1.728 7.87Q 2.691 606.92 4.149 1.717 7.929 2.593 607.55 5.330 1.705 i.9$8 2.697 606.26 6.725 1.694 8.048 2.7a0 609.06 8.368 1.682 8.11b 2.704 604.93 1Q.296 1.67i 8.173 2.7Q9 610.89 12.561 1.6�9 8.237 2.713 611.94 15.228 L 648 8.302 2.719 613.08 18.380 1.636 8.369 2.724 614.30 22.134 1.625 8.436 2.731 615.61 26.650 1.613 8.506 2.737 617.a2 32.166 1.602 $.576 2.795 618.52 39.Q48 1.590 $.64$ 2.752 620.12 47.909 1.579 8.721 2.761 621.$1 59.904 1.567 8.796 2.7b9 623.61 77.619 1.556 8.872 2.779 625.51 109.361 1.549 8.950 2.789 627.51 220.690 1.544 8.954 2.79a 627.63 HYDRAULIC JUMP: LTPSTREADS RUN ANALYSIS RESUf,TS -----------------------------------------___�---------�------------------------ --___--------------------------------------------------------------------------__ ACIWNSTREAM CONTROL ASSUP9ED PRESSURE HEAi3(FT) = 3.14 PRESSURE FLOW PROFILE COMPUTED TNFORMATION: ------------------------------------------------------------------------------- . DISTANCE FROM PRESSUftE VELOCITY SPECIFIC PRESSURE+ CONTROL ( F"!' ) HEAD ( FT ) ( FT / SEC ) ENERGY (�"F 1 MQMENTUM { pOCTl�IDS } 0.000 3.105 5.8Q6 3.628 888.73 13D.713 2.500 5.BD6 3.023 703.54 ASSUMED DpWNST}2EAM PAESSURE HEAD(FT) = 2.50 GRADUALLY VARIF.D FI,OW PROFILE COMPUTED INFOR�fATI�N: ------------------------------------------------------------------------------- DISTAI3CE FROM FLOW flEPTH VF:LOCITY SPECIFIC PRESSURE+ CONTROL(FT� (F�') (FT/SEC) ENERGYfFT) MdMENTUM(PO[J3�TDS} 130.713 2.546 5.804 3.023 703.54 135.359 2.473 5.815 2.998 695.84 139.519 2.446 5.836 2.975 688.67 • 143.4�4 2.416 5.862 2.952 661.86 I47.1�0 2.391 5.894 2.931 675.38 154.641 2.364 5.930 " 2.910 669.19 �54.029 2.337 5.970 2.891 663.27 157.288 2.310 6.014 2.872 657.53 160.92b 2.282 6.061 2.853 652.25 163.450 2.255 6.113 2.836 64�.14 16b.362 2.228 b.157 2.819 642.29 169.164 2.201 6.226 2.803 637.71 171.856 � 2.174 6.287 2.768 633.39 174.434 2.1�46 b.353 2.774 529.35 175.895 2.119 6.422 2.�60 625.59 179.234 2.092 6.499 2.747 622.11 161.444 2.065 6.570 2.736 b18.92 183.514 2.038 6.65Q 2.725 516.02 185.433 2.0?D 6.734 2.715 613.43 • 187.188 1.983 6.822 2.706 61i.16 � �88.760 1.956 5.919 2.699 b09.20 190.128 1_929 �.4�2 2_693 b07.58 19I.265 1.902 7.1�1 2.687 6a6.29 192.137 1.875 7.217 2.684 605.36 192.701 1_847 7.327 2.681 609.79 192.904 1.82U 7.492 2.fi81 6a9.60 220.69Q 1.820 7.442 2.b81 6D4.64 _�----------------------END OF HYDFtALTLIC JLT�IP ANALYSIS------------------------ I PRESSURE+�pMENTUM BALANCE OCCURS AT 180.45 FEET UPSTREAM OF NODE 562d.90 � DQWNSTREAM DEPTH = 2.677 FEET, UPSTREAM CONJUGATE DEPTH = 1.589 FEET ------------------------------------------------------------------------------ NODE 5030.00 : HGL =< 363.080>;EGL= < 363.941>;FLOWLINE= < 361.260� **�**�.�***.*«.t��*�*..��*+��t�**��*++********�.�.***��**t*.*t*******��*+�** FLOW PROCESS FRQM NO�E 5D30.00 TO NODE 5Q30.90 I5 CODE = 5 UPSTREAM NODE $Q30.90 ELEVATION = 361.54 (F�,OW UNSF.ALS IN REACHj ------------------------------------------------------------------------------ CALCULATE JUNCTION LOSSES: PIPE FLOW DIAPfETER ANGLE FLOWLINE CRITICAL VELOCITY (CFS) (II�CHES} (DEGREES} ELEVATIOI3 DEP'I`H(FT. } (FT/SEC? UPS'i'REAI�! 2$ . 50 3 D. 00 90 . fl0 351 . 59 1. 92 5. BD6 DOWNSTREAM 28.50 30.00 - 3&1.26 1.82 7.4�14 LATERAL #1 0.00 0.00 0.00 O.DO O.aO D.OD4 %ATERAL #2 0.00 4.00 0.00 Q.00 �0.00 0.040 (15 0.00===45 EQUALS BASIN INPUT=== LACFCD AND OCE�SA FLOW JUNCTION FOAMULAE USED: DY=(42*V2-Q1*V1*COS(DELTAI)-Q3�V3*COS{DELTA3}- ' 44*V4"'COS(DELTA4}}/((A1+A2)*16.1)+FRTCTION I,OSSES UPSTREAM: [�4ANNI3�7G'S N= 0.013QD; FRICTTON SLOPE = 0.00483 • DOWNSTREAM: MANNING'S N= 0.01300; FRICTION SLOPE = 0.00623 AVERAGED FRICTION SLOPE �N 3UNCTION ASSiJ[�4Ed AS 0.44553 JUNCTIOAF LENG'i'H = 4. QO FEET FRICTION LOSSES = �.022 FEET EN'I'RANCE LOSSES = 0.000 FEET JUNCTIpN I,OSSBS = (DY+HV1-HV2j+(ENTRn,NCE LOSSES? • JUNCT�QN LOSSES =( 1.193}+( 0.000y = 1.193 __----------------------------------------------------------------------------- N�DE 5030.9Q : HGL =< 369.610>,EGL= < 365.134>;FLOWLINE= < 361.590> ,.***�.*.**.****+�t***+:+*,,t****+++**�**++****,.*.+...*�.+�*�*�*,��++****+++.,,w** FLOW PROCE55 FROM NODE 503p.94 TO NO�SE 5031.Q0 IS CODE = 1 UPSTREAM NODE 5Q31.D0 EI.EVAT�ON = 362.99 (FLOW IS L7NbER PRESSURE) CALCULATE FRICTIpI3 L4SSE5(LACFCD): PIPE FLOW = 28.50 CF5 PIPE DIAMETER = 30.00 INCHES PIPE LFNGTH = 90.30 FEET MANNING'S N= 0.01300 SF=iQ/KJ**2 = (( 28.50}/( 410.179f)**2 = 0.004B3 HF=L*SF = { 94.30)*(0.00483} - fl.436 ------------------------------------------------------------------------------ NODE 5031.00 : HGL =� 365.Q4b�;EGL= < 365.570>;FLOWLINE= � 362.490> ♦�**k�iF�ir�k *i#Yf Y�f4*'�**i�Yr*1r**fi * rt M f f f Yr1r }f iYr}kkkk *# #*1�*i Y 1* �l+f#�JriM+****###i�Mi** F�QW PROCESS FR02+3 NODE 5031.OD TO NQDE 5031.90 IS CQDE = 5 UPSTREAM NODE 5031.90 ELEVATION = 3b2.99 f�'LOW SEALS IN REACH) (NOTE: P05SIBLE JUMP IN OR UPSTREAM OF STRUCTUFiEI ---------------------------------_____--_--_-------------------------------------- CALCULATE JUNCTIpN LpSSES: PIPE FLOW DZAMETER ANGLE FLOWLINE CRITICAII VEI,OCITY (CFSj {�NCHES} (DEGREES) ELEVATIOI3 IJEPTH(FT.) (FT/SEC) UPSTRFAM 24.60 24.00 0.00 362.99 1.75 - 9.002 • 3�OWNSTREAM 28.50 30.Q0 - 3b2.49 ?.$2 5.806 � LATERAL #1 2.30 18.00 90.OD 363.50 0.57 1.3B8 LATERP.L #2 1.60 18.00 90.00 363.50 4.48 0.966 Q5 0.00===Q5 EQUALS BASIN INP[7T=== i�ACFCD AND OCEMA �'LOW 3UNCT�ON FORMULAE USED: By={Q2*V2-Q1*V1*C4S{aELTAl}-�3*V3*COS(DELTA3)- Q9*V4*COS(DELTA4))/((A1+A2)*16.I)+FRICTION LOSSES UPSTREAM: MANNiNG'S N= Q.01300; FRICTION SLOPE = 0.01203 DOWNSTREAM: MANNING'S N= 0.01304; Fi�IC`I'ION SLOPE = 0.00983 AVERAGED FRICTION SLOPE II3 JUNCTION ASSIJMED AS D.00643 JUNC`i'ION LENGTH = 4. 0 Q FEET FiZIC'i'FON LOSSES � 0.034 FBE2' ENTRANCE LOSSES = 0.000 PEET JUNCTION L055E5 = SDY+HV1-HV2j+(F:N'1'RANCE LOSSES) • JUNCTION LOSSES =( Q.3a3)+q p.00D} = 0.303 ------------------------------------------------------------------------------ NObE 5031.90 : HGL =< 369.614>;EGL= < 365.873>;FLOWLINE= a 362.990� ....»*,�**�*+�****.+***+*t**+�*+.f+,...�.�*..*.++.�.*��.+�.�.w.�*�w*+.�.,....*** Fi,OW PROCE55 FR4M NODE 5031.90 TO NpDE 5032.Q0 IS CODE = 1 UPSTREAM NODE 5a32.00 ELEVATION = 365.24 (FLOW IS SUPERCRITICAL) CAi�CUI.FITE FRIC�'ION i�OSSES (LACFCDj : PIPE FLOW = 24.60 CFS PIPE DIAMETER = 29.00 INCHES PIPE LFNGTH = 182.79 FEET MANNING'S 33 - 0.01300 NO�LMAI.. DEPTH{FT) = 1.62 CRITICAL DEPTH(FTi = 1.75 ------------------------------------------------------------------------------ UPSTREP.M CON'f'ROL ASSUMED FLAWDEPTH ( FT )� 1. 7 5 GRADUALLY VARIED FE,OW PROFILE COMPUTED zNFORMATION: . ------------------------------------------------------------------------------ DISTANCE FRQM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT) (FT) (FT/SECi ENERGY(FT) MOMENPiJih(POUNDSI d.00Q 1.75d 8.437 2.656 550.78 Q.047 - 1.745 8.457 2.856 55D.'79 0.159 1.739 8.478 2.8Sfi 55D.81 0.342 1.734 8.49B 2.856 55D.86 0.600 1.729 8.57.9 2.857 55D.91 0.940 1.724 8.540 2.857 � 550.99 1.370 1.719 8.562 2.858 551.�8 1.B97 1.713 8.584 2.858 551.18 2.532 1.708 8.6fl6 2.859 551.30 3.286 1.7D3 8.628 2.860 551.43 4.175 �.698 8.651 2.860 551.59 5.216 1.693 8.673 2.861 ' 551.75 5.929 1.687 8.697 2.862 551.94 7.842 1.6B2 8.720 2.864 552.13 9.488 1.677 8.744 2.865 552.35 �f.4f0 1.672 8.768 2.866 552.5B 13.665 1.665 8.792 2.866 552.83 16.330 1.66� 8.817 2.869 553.fl9 19.513 1.656 8.841 2.B71 553.37 23.374 1.651 $.867 2.872 553.67 28.]57 1.646 8.892 2.879 553.98 34.275 1.690 8.918 2.675 55h.31 42.502 1.635 8.994 2.678 554.55 54.574 1.b30 8.970 2.880 555.42 76.066 1.625 8.997 2.882 555.44 7.82.79D 1.624 9_999 2.883 555.43 • NODE 5032.00 : HGL =< 366.950>;EGL= < 358.056>;FLOWLINE= < 365.2Q0> i��t*,w.,,�.�ww��*,*,*...*.��.....*...*��}��.*.�*.,*.******�,*,**.*****�*. FLOW PRpCESS FROM I30DE 5032.00 TO NODE 5032.9Q IS CODE = 5 UPSTRF,FIM NODE 5032.90 ELEVATION = 365.53 (FL'QW UNSEALS ID} REACH) CALCiJLATE ,7UNCTIOiV LOSSES: PIPE FLOW DIAbfETER ANGLE Fi,OWLINE CRITICAL VELOCITY ICFS} (IAFCHES) (DEGREES) ELEVATIpN DEPTH(FT.j {FT/SECJ UPSTREAM 24.60 24.00' 90.00 365.53 1.75 7.834 � DOWNSTREAM 24.b4 24.00 - 365.20 1.75 8.435 LATERAL �1}. 0.00 0.00 0.00 4.00 O.OD 0.000 LATERAL �12 0.04 0.00 � 0.00 4.00 O.DQ O.00Q 45 0. D4-=�45 EQUALS BASI23 I�IPUT�== LACFCD AidD OCE2�4A FLOW JUNCTION FORMUi,AE USED: DY={Q2*V2-Q1*V1*COS(DELTAI}-Q3*V3*COS(DELTA3)- Q4*V4*COS(DELTA9J)/{(A1+A2)'15.Z)+FRICTION LOSSES UPSTRE.�M: MANNiNG'S N= 0.01304; FRICTIdN SLOPE = Q.01162 DCYWNSTREAM: MANN�NG'S N= O.fl1300; FRICTIQN SLOPE = 0.41070 AVERAGED FRICTiON SLOPE IN JUNCTION ASSUM�D A$ 0.0�126 JLTNCTION LENGTH = 9.4a FEET FRICTION LASSES = 4. Q45 FEET Ei�i'i'RA.NCE LOSSES = 0. OOD FEE`P JUNCTION LOS6ES = IBY+HV�-HV2)+(ENTRANCE LOSSES} � JUNCTION L055E5 = q 2.420}+( 0.044) = 2.02D ------------------------------------------------------------------------------ NODE 5032.9D : HGL =� 369.124>;EGL= � 370.076>;FL4WLINE= < 365.530> **r**�Ws**.+.ww+v��,r�v.**++*+*.,�r++.+t�*w+*w.*..�.*i:.�**w,r*w�*w*++,r,r,r*+****,t+wr* FLOW P3tOCESS FROM NODE 5432.9D TO NODE 5Q35.00 TS CaDE = 1 UPSTREAM NODE 5035.OD ELEVA�'ION = 366.06 {FI,DW IS iJNDER PRESSURE} � --------------------------------------------------------------------- CALCULATE FRICTION L05SES(LACFCD): PIPE FLOW = 24.60 CFS PIPE DIAMETER = 24.00 INCHES PIPE LENGTH = 35.09 FEET MP.NNING'S N= 0.01300 SF=(Q/K)**2 = {( 24.6Q1/S 226.Z28})**� = O.Q1162 HF=L*SF = I 35.09y�(Q.a1182) = 0.415 �ODE 5035.OQ : HGL =< 369.539>;EGL= � 370.991�;FLOV�Iri�= < 3b6.QbQ> .,,«********,.�****,....�...*.*.*.*.**,.�w.,�*t.�.�*+**.�.�.��„*.*...,.�«.*«x*.***��* UPSTREAM P�PE FLOW CONTROL DATA: NODE NUA4BER = 5035.00 FLOWLINE ELEVATION = 356.05 A55UMED UPSTREAM CONPROL HGL� = 367.81 FOR DOWI3STREAl�4 RUN P.PIALYSIS ------------------------------------------------------------------------------ SND OF GRADUALLY VAltIED FLOW ANALYSIS CJ r� �_J . • � � * + Y i Y � * * } i Y 4 + i � + * f * * i rt i 1 f i # * ! i f + # k � f f * # t i k t + + + * w � i i # i + f * i t * i fi � } k f * * * k * * ; rt * * * * PIPE-FLOW HYDRAULICS COMPUTER PROGKAM PACKAGE fReference: LACFCD,LACRD, At3D OCEMA HYDFAIILICS CRITERION) (c} Copyright 1982-20D2 Advanced Engineering Software (aes} Ver. 8.0 Re2ease Date: O1/01/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTANTS 7a1 'B' STREET, SUITE 800 SAF1 DIEGO, CA 92�03 - 619-235-6471 **"***"`"'*"*'"""`+*'`i*'t*** DESCRIPTIOid OF 5i'UDY **"x�*�*�t**+*ti++*�tr+**t+ * BRESSI RANCH - INTERiM MASS GRADED COidDITIONS � * SYSTEM 5000: E,ATERAL 1(AIO. 7 PER SHT_ 14 OF DWG N0. 400-8C1 * � 140-YEAR S?'QRM B'VEN'i' * +++w++v.i++*�*�*+*+***+,rf**.��*+**+++w+**��+�*.�f�r��++*+**+.*,.*+**�*�+**,r FZI..E NAME: 50Q0-lI.DAT TIME/DATE OF STETDY: 12:29 O1/17/2003 +*++**aa*aa****�*ixa*rttrr**++�**t*****x+x*a******rr*a*r�fix*t*yi*r�r**�rY*****+*• GRA�UALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NpDAL POINT STATUS TABi.E (Note: "*` indicates nodal point data used.j UPSTREAM RUN DOWiVSTAEAM RU23 NODE MODEL PRE55URE PRESSURE+ FLOW PRESSURE+ NUMBER PROCESS HEAD ( FT i M�MEN'i'UM ( POUNDS ) DEPTH ( F'i' } I�OMEi3TUM ( PO[3AFDS } • 5001.20- 5.50* 2369.29 1.29 2147.23 ) FRICTION } HyDRAiJI,IC JLJMP 5a01.34- 5.55 2383.11 1.13* 2490.81 ) MAis]IOLE 5D01.40- 5.30 23Q8.�1 1.13' 2507.44 } FRICTIpN 5001.45- 2.32 Dc 1431.33 1.33* 2076.72 } MANHOLE 5001.46- 2.32 Dc 1431.33 1.33* 2fl71.80 } FRICTION 50D1.50- 2.32*Dc 1431.33 2.32*Dc 1431.33 } CATCH BASIi�I 5041.5D- 4.55* 1011.18 2.32 Dc 329.49 ------------------------------------------------------------------------------ MAXYMLIM NUMBER OF EfdERGY BALANCES USED IN EACH PFtOFILE = 25 NQTE: STEAT7Y FLOW HY�AAULTC HE.�.D-LDSS COMPUTATIONS BASED ON THE MOST CONSERVATiVE FpRMULAE FROM THE CURREI�}'T' LACAD, LAC�'CD, AND OCEMA DESIGN MANiJALS . ****++***�*�+**��,r*.+****+.**+****x+**+++++***+*+**+***+**��+**+*.*+*�****++� DOW135TREAP4 PI PE FLOW COI3TROL DATA : I�30DE NUMBER = 5401.20 FLOWL�NE ELEVATION = 179.00 PIPE FLOW = 52.00 CFS P�PE DIAMETER = 30.00 INCHES ASS[TrSED DOWNSTREAi� CONTROL HGL = 184.5Q0 FEET NODE 50D1.24 : HGL =< �84.500�;EGL= � 166.293>;FLOWL�NE= < 179.000> ♦**i*i tt i# 1 i�kki i ii�k # Y YYc1r **t f1� **#'k**�F ***Y-l� **Y x1cYr �F *i {*YiYY++i�ki *iYtYY it+i�k�! i4�k�k*i FLOW PROCESS Ff�OM ?VODE 5001.20 TO NODE 5flQ1.30 TS CODE = 1 UPST32EAM NODE 5flD1.30 ELEVATIOI3 = 179.61 (HY�RAUL,IC JUMP OCCiJRS} • `-------------------__-__--_____--__-------rt------------------------------------ � CALCULATE FRICTION L05SES(LACFCD): PIPE FLOW 52.00 CFS PIPE DIAME�ER = 34_00 INCHES PIPE LENGTH - 40.76 FEE� 3hANNING'S N= 0.01300 ------------------------------------------------------------------------------ HYDAAULIC JUMP: DOWNSTREAM AUN ANALYSIS RESULTS I30fZMP.L DEPTH {FT} - 2. 14 & 2_ 48 CRITICAL DEFT13 (FT) = 2. 32 i�IOTE: SUGGEST CONS�DERATION OF WAVE ACTION, 1JNCERTAINTY, ETC. ------------------------------------------------------------------------------- ------------------------------------------------------------------------------- LiPSTREP.M CON'f'RO�, ASSi]i�7ED FI.,OWDEP'I'H {�`J = 1. 13 GRADUALi�Y VAAIED FLOW PFtQFILE COMPUTED II3FQRMATION: ------------------------------------------------------------------------------ ]7TS'I'ANCE FROM FLOW DEPTH VELOCITY SPECIFIC PI2ESS[TRE+ CONTR03� ( FT } ( FT } ( P'I' / S�C } ENERGY ( F'I' } MOMENTUM ( POUNDS ) O.OQO 1.�32 24.473 1D.�.36 2490.8� 10.580 1.172 23.Q01 9.392 2388.3Q 21.24b 1.213 22.018 8.745 2295.07 32.Oi� �_253 21.115 6.�80 2210.]3 40.7fi0 1.285 24.441 7.777 2147.23 HYD4ZAt]LIC JUMP: UPSTRF.AM 3tUN ANALYSIS RESULTS ------------------------------------------------------------------------------ DOWNS'I'REAM CONTROL ASSUMED PRESSi7R� HEADfFT) = 5.SQ PRESSURE FLOW PROFILE COMPUTED iNFORMATION: ------------------------------------------------------------------------------ DISTANCE FROM PRESSURE VELOCITY SPECIFIC PRE55URE+ CONTROL(FT) HEAD(FT) {FT/SEC) F�IERGY(FT} 3+10MENTUM{pOUNDS) O.Q00 5.50D �0.593 7.243 2359.29 . 40.760 5.545 10.593 7.288 -_2383^11--___ ---------END OF HYDRAULIC JiJMP A�iALYSiS-_--------- ! PRESSl3RE+MOME�3T[JM BALANCE OCCUKS A�' 29.14 FEET UPS`£R�A�7 OF NODE 5D01.20 � � DOWNSTREAM DEPTH = 5.532 FEET, IIPSTREAM CON,7UGATE DEPTH = 1.176 FEET � -----------------------------------------------------------------------------.. NODE 5001.30 : HGL =< 180.742>;EGL= < 189.746>;FLOwLINE= < 179.610> #f-}� � Y� *1 �� t Y� Y**Y! t**Y Yy� �ki 1 Y*f **4�Yi��t 1�k 1***t1� #**�r* ****tY****�!# #f Y1�1�#� Yr Y##t****ir*ir FLOW PROCESS FROM I30DE 5001.3a TQ NODE 5001.40 IS COBE = 2 UPS'3'REAM NODE 5p01.40 ELEl1ATIpN = 179.94 (FLOW IS SUPERCRITICAL) CP.�,CUI=ATE MANHOI,E LOSSES ( �CFCD j : PZPE F�,QW = 52.D0 CFS PYPE DIAhfET�R = 30.Ofl INCHES AVERAGEJ} VELOCZTY HF�D = 9. D69 FEET HPSN = .05*{AVERAGED �ELOCITY HEAD) _ .Q5*( 9.469} = 0.453 ------------------------------------------------------------------------------ NODE 5001.4D : HGL =< 181.066>;EGL= < 190.200>;FLOwLINE= � 179.44a> ♦rtt***��*tty*:*itt*rr*�rtirs*�*y**xx*f*+*�***�***rr+*t�++******ti*ay+rr*t+++*++x* FLOW PROCESS FRQM NODE 50Q�.90 TO �idDE 5001.45 IS CODE _? UPSTREAM NODE 5p01.45 ELEVATION = 192.42 (FLOW IS SUPERCRTTICAL) CAL,CULA'I'E FRICTIOAi LOSSES (LACFCi]} : PIPE FLOW = 52.00 CFS PIPE DIAMETER = 3Q.44 INCf�ES PIPE LFNGTH = 52.00 FEET I�4ANNIF3G'S N= 0.020QQ E�ORMRL DEPTH{FT} - 1.10 CRITICAL DEPTH{FT) = 2.32 I3PST�LEAM CONTROL ASSUMED FLOWDEPTH(FT) _ �.33 ------------------------------------------------------------------------- � GRADUALLY VARIED FLOW PROPILE COMPUTED INFO}2MATION: � nTSTRNCE FAOM FLOW DEPTH VELpCTTY SP�CTFIC PRESSURE+ CbNTROLfFT) (�T} (FT/SEC) FNERGY(FT} MOMEN'1'LIM(POiJNpSj O.QQO 1.325 19.678 7.393 2076.72 0.84? 1.316 19.849 7.437 2092.49 �.743 1.307 20.Q23 7.535 2108.57 2.691 1.296 20.20Z 7_638 2124.99 3.696 1.266 20_382 7.743 2141.75 4.765 1.279 20.565 7.$51 2158.85 5.905 1.270 20.753 7.962 2176.3D 7.122 1.261 20.994 8.077 2194.12 8.426 1.252 21.338 8.�95 2212.31 9.828 1.243 21.336 8.315 2230.89 11.341 1.234 2L 538 8.441 2249.85 12.980 1.225 21.744 8.571 2269.21 14.764 1.215 21.953 8.704 2288.98 16.716 1.20b 22.167 8.841 2349.17 18_667 1.197 22.385 8.983 2329.79 21.255 1.188 22.607 9.129 2350.85 23.930 1.179 22.833 9.279 2372.36 26.950 3.170 23.064 9.435 2394.34 30.991 �.i6k 23.299 9.595 2416.80 34.512 L 153 23.540 9.761 2439.74 , 39.392 �.192 23.785 9.932 2463.19 45.443 1.133 24.035 10.109 2487.16 52.4a0 1.126 24.246 10.250 2507.44 ------------------------------------------------------------------------------ NODE 500i.45 : HGL =� 193.745>;EGL= � 199.76�>;FLOWLINE= < 192.420> * * f * # * k * * * * * * + i * * * * y * * Y i f f + + } } * * f f * * # # f f * * f M 1 1 * * * k k * # * * * * Y # Y f i * 1 4 * # f # � � Y � 1 4 � 1 Y FLOW PROCESS FROM NODE 500�.45 TO NOAE 5001.46 IS CdDE = 2 • UPSTRF�IM NODE 5001.46 EL�VATIbN = 192.75 (FLOW IS SUPERCRITICAL} CALCUi�ATE MANHOLE L455ESfLACFCD}: PIPE �LOW = 52.00 CF5 PIPE DIAMETER - 30.fl0 INCHES , AVE�tAGED VELOCITY HEAD = 6.000 FEET HMN =.fl5*{AVERAGED VELOCITY HEADj =.05*( 5.OQ4) = 0.300 NODE 500�.46 : HGL =� 199.d78>;EGL= < 200.062>;FLOWLINE= < 192.75a> *i**i i i**1r * i i� kY4f4 ik}�.}****i 41r *1rYr**YrYrY�Yrk * rt k k k**Yr*Yr**# #*�k Y� t Y f Yi*+�12 ##i�kyr�kYf yr�F#ik i FLOW PROCE55 FROI�f NOAE 5001.46 TO I30DE 5001.50 IS CODE = 1 UPSTREAM NODE 5001.50 ELEVATION = 197.91 (FLOW IS St3PERCRITICAL} CAI,CiTI.ATE FRTCTION L05SE5(LACFCD� : PIPE FLOW = 52.fl0 CF5 PIPE DIAMETER = 30.d0 iNCHES PIPE LENGTH = 29.00 FEET 2+3PNNING'S N= 0.02D00 ------------------------------------------------__-_-------------------------- NORF"3AL DEPTH ( ET) = 1. 13 CRITICAL DEPTH (�'T) = 2. 32 -----------�--------------------------------------------�---__------------------- -------------------------------_____--______----_---------------------------------- IiPSTREAM CONTROL ASSt7MED FLOWDEPTH(FT} - 2.32 " GRADUALLY VARIED FLOW PROFIE,E COMPUTED iNFORMATION: ' �R` ��W_W�� -------------------------------------------------------------------------------- DISTANCE FROM FLOW DEPTH VELOC�TY SPECIFIC PRESSLFRE+ CONTROL�F'i) (FTj (FT/SEC) E�iERGY(FTJ MOMENTLFMfPOUNDS) o.oaa 2.323 10.931 9.18Q 1431.33 Q.021 2.276 1].082 4.184 1432.47 0_085 2.228 11.252 4.195 1435.89 0.193 2.184 11.443 4.215 Z441.43 • 0.348 2.133 11.659 4.243 I949.25 � 0.554 2.085 1�.884 4.28p 1459.36 0.8�9 2.037 12.136 4.326 1471.84 1.i3b 1.99D 12.409 4.362 lAB6_BO 1.528 1.942 12.706 4.450 1504.35 1.998 1.894 13.027 4.531 1524.66 2.557 1.847 13.373 4.625 1547.90 3.221 1.799 13.748 4.73b 1574.27 4.d48 1.751 14.153 4.864 1603.99 4.939 1.704 14.591 5.011 1637.35 5.043 1.656 15.069. 5.182 1674.62 7.358 1.606 15.576 5.378 1716.17 8.934 1.560 16.132 5.604 1762.38 10.839 1.513 16.739 5.B54 1813.70 13.169 1.465 17.389 6.153 1870.65 16.066 1.417 18.103 6.509 1933.85 19.752 1.370 18.88� 6.909 2003.9$ 24.00D 1.326 19.624 7.312 2�71.84 NOAE 54Q1.50 : HGL = a 200.233>;EGL= < 202.090>;FLOWL�N�= < 197.9�Q> +.:****..*.******..***.*++*++++**��**�*.�.**�*.�**�*�*t.**.**+�.�*.��.*****+�+ FLOW PROCE55 FROM NODE 5001.5D TO NODE 5D01.50 IS CODE = B UPSTRF�M NODE 5001.50 ELEVAT�ON = 197.91 (FLOW UNSEAI�S IN REACH) CALCULAi'E CATCH BASIbI EN�rRANCE LOSSESSi�ACFCDi : PTPE FL4W = 52.OD CFS PIPE DIAME'I'ER = 30.p0 INCHES �'LOW VELpCITY ��0.93 FEET/SEC. VE�OCT7'Y HEP.D = 1.856 FEET CATCH BASI�7 E2�ERGY LOSS =.2" (VEL,OCI'I'Y HEAA} _.2* { 1.856 j= 0.371 ------------------------------------------------------------------------------ NODE 5001.5� : HGL =� 202.451>;EGL= < 2�2.461>;FLOWE�INE= < 197_910> � x+ix++t**++�xx*xx�xt*yy*rt*�*y*zx***rxtw�+**ix�*ttttyrttr****�rtitf+t��rtt+*��rts* UPS�`REAM PIPE FLOW CQNfiROL 17ATA: NODE NUl+1BER = 5001.50 FLpWLINE ELEVATYpN = 197.9� ASSUMED UPSTREAM CONTROL HGL = 200.23 FOR DOWNSTREAM RCFN ANALXSIS END OF GRADUAI,LY VARIED FLOW ANALYSIS C � * * * * f w * 1 4 i # * t * k K k f Y t � � # * 4 * * Y * * * + f * t N k * * f Y W Y Y H k * * Y ! � W } 1 * * Y * # f k * * � # 1 i i ? # * * * f Y # * t PIPE-FLOW IiYDRAULICS COMPiI'I'ER PROGRA�S PACKAGE � {Keference: LACFCD,LACRD, AND OCEMA HYDRA[7L�CS CRITERTpN) - ' tc} Copyright 1982-20D1 At3vanced Engineering 5oftware (aesj Ver. B.0 Re�ease Date: OI/0�/2001 License ID 1509 Analysis prepared by: PR0.iECTDESIGN CONSUi,TANTS 7D1 'B' STREET, SUITE 800 SAN DIEGO, CA 92101 6�9-234-0349 ******�*r*�tay.xf**�**r**** DESCRIPTION OF STUDY *v*taxfv�+w**�+r,rxw**�w*,r++ * B�tESSI RANCH - iTL'F�MATE COAFDITIONS " * SYSTEM 500D: LATERAL 1(N0. 7 PER SHT. 14 OF DWG I30. 4D0-8C? "` " 1d0-YEAR STORM EVENT * Yf *4*�YYi�kik}y�#y�.k yff i iti W t f�ikf*4 f*i i*�� W t#4i Wfittt�##i�# iFYrR *Yr** rtYrYrfY�*YrYrk Yr k*Y�MYr�k *� Fzz�� rraar�: 500o-lo.pAT TiME/bATE OF STUDY: 09:27 10/23/2002 ,r**rt**t,rrr**tt**t+w*a+*++wrr***�+w**w*w�wr�►**xrxrr�+at+t+*xr*t****xx*wrt*r**+* GRADUALLY VARIED FLOW ANALYSTS FOR PIPE SYSTFM NODAL POINT STATUS TABLE {Note: '*' indicaties nadal point data used.) UPSTREP.NI RU[�I DOWN3TRF.FiM RU23 NODE i+40DEL PRESSUR� PRESSURE+ FLpW PRESSURE+ NUMSER PROCE55 HEA.D ( FT } MOrFENTiTM ( POUNDS ) DEPTH ( FT ) MOMENTUM { pOUI3D5 ) 56Q1.20- 5.50* ].305.$4 0.43 41.05 } FRICTION 5001.30- 4.89* 1�19.75 Q.59 Dc 35.76 } CA'I'CH BASIN •- . __SOD1_30----_..________4_9�*-----------1316.14--------DY59`Dc_____ _��23_ MAXIMUDS NUMHER OF ENERGY HALAAICES iiSED IN EACH PROFILE = 25 ^ ------------------------------------------------------------------------------ NO'TE: STEP.DY FI,UW HYDRAUL�C 1-IEAD-LOSS CpMPUTAT10bI$ BASED ON THE MqST CONSERVATIVE FO�MiJLAE FAdM THE C[TFtREAI'P Z.ACRD, LACFCD, P.ND OC�'MA DESIGN MR.NUA�,S. *t*+*xw*+�*,r**ww**wr*w�wr+*rt*,r*+s�*w�*w*+sx�*�,r,r*xxw+r****+**t*+**+,rx*w*�x*+** DOWNSTREA�S PIPE FLOW CON?'ROL DATA: NODE N[3I�ER = 5041.20 FLOWLINE ELEVATION = 179.D0 PIPB PI,bW = 3.20 CFS P�PE DZF.MET�R = 3D.00 INCH�S ASSUMED bOWNSTREAM CONTRQL HGL = 384.5U0 FEET ------------------------------------------------------------------------------ NODE Sa01.2D : HGL =< 164.500>;EGL= < 184.507>;FLOWLINE= < 174.00fl> •t*x*+x+x+**x+*xa**ra+t+*w+wxx*+++w+**+r+*r.*tkt*t+***r+*rs+***rw****tirt*r**rtt** FLOW PROCESS FROM I30AE SDR�.20 TO NODE 50D7..30 IS CODE = 1 UPSTREA24 ND17E 5001.30 �LEVATION = 179.61 {FLQw IS UNDEA PRESSUREi ------------------------------------------------------------------------------ CAT�CULATE �'RICTION LOSSES(LACFCD}; PTPE FLOW �= 3.2D CFS P�PE DTAMETER = 3D.00 INCHES PIPE LEIJG`iH = 9d.76 FEET MArRJING'S N = Q.013D0 5F=(Q/K}**2 - ({ 3.201/f 409.650})**z = O.00D06 HF'=L*SF = ( 40.75)*(0.000061 = O.�Q2 ------------------------------------------------------------------------------ NObE 5001.30 : HGL =< 184.502>;EGL= < 18k.5R9>;F�OWI,�NE= <].79.6�0> >Yrt*YR *YrYY kYYr YYrrt 1*! iYY*�l Y* w Y**�r i f*Yr f YrY x�rY YY *Y #!f *Yr iY.1 i+ti # �Yiyry.�kt *tt+� �F YY�Y * Yt �kY Yr* - FLOW PROCESS FROM NODE 5001.34 TO NODE 5001.30 IS CODE = B UPSTAEAM NODE 5001.30 ELEVA'F�OIV = 179.6J. SFLOW IS UNDER PRESSURE� ---------------------------------.._____-..____________..______...._-- � CALCULA'i'E CATCH BASII3 ENTP.ANCE LQSSES ILACFCD) : PIPE FLOW = 3.2� CPS PIPE D�AMETER 30_DO IIVCHES FLOW VELOCITY = 0.65 FEET/SEC. VELOCITY HEAD = D.007 FEET CA'I'CH BASIN EN£RGY LOSS =. 2" ( V�'�.,OCITY HEAD} _. Z= { D. 007) = 0. 00� ----------------------___-------------------------------------------------- --- NODE 50Qi_30 : HGL =< 164.510>;EGL= c 184.510>;FLOWLINE= < 179.610> • .*iwf+*�.*�rt*w++rrtww*r***+**�++r**raxxrxxx*+v,x*w�*r*r*+a+ww++x*x****x*xyx�*.xfi UPSTREAM PIPE FLOW CONTAOL DATA: NODE NUMBER = 50f11.30 FLOWLINE ELEVATION = 179.61 ASSUMED i7PSTREAM CONTROL HGL = �8d.20 FOR DOWNSTREP,M RiJN A23ALY5IS END OF GRADUAE�LY VARIED FLOW ANALYSTS • i • ♦* 1 rt s ti x a+ x�** y* x r*** x* r* x rt* r r* x x*�: r*: w x s* r r i��* x x r** w x* t w Y t x x i* s* f f*** y:� i i r+ PIPE-FLOW HYT7RAU�ICS COMPUTER PROG�2AM PACKAGE (Reference: LACFCD,LACi�D, AND OC�MA HXARAUI.,ICS CRITERIQN} (c) Copyzight 1982-20D1 Advanced �ngineering Software (aesl Ver. 8.0 Release DatE: O1/O1/2001 T�icense ID 15D9 Analysis prepared by: PAO�ECTDESIGN CONSULTANTS 701 ' B' S'i'REET, SU�TE 800 SAN DIEGO, CR 92101 619-234-0349 •'•"`*•*•"`**••*•••••*•*:*"�• DESCRIPTI03d OF STi.TL1Y �}*«.*.+*�***........�*�.+ * BRESS� RANCH - ULTIMATE CONDI�IONS * * SYSTEM 500D: LATERP.L 2{IVp_ 8 PER $HEE'£ �4 dF DWG 4D0-BC) * * i00-YEAR STORM E11�NT * .**..***++****.+*+*+***�+++*++*�++*.*+��++.*+�***x.*...w***.*+w++�+�+..�.�� FILE NAME: 5000-2.DA'I` TIME/DATE OF STUDY: 13:02 09l48/2002 *i**�r++�r*ry�+**s+rtx+*****�+t�+*�+t++sr++�*ita>a*t+��**a**w,rw*�,r,r�ww**,r*x,rx*w**tx GRADiiALLY VARIED FLOW ANALYSIS FOR PIPE SY5'I`EM NQDAL POINT STATUS TAHLE {Note: "*' indicates nodal point data used.j UP53`REAM RiTN bpW25ISTFtEAi�1 RUN I30DE MdD£L PRESSURE PRESSURE+ FLOW PRESSURE+ bFUMaER PROCESS HF'.AA ( FT ) MO�IENTUM { p0UND5 } I}EPTH (�'T) s10MENTiJM ( PCIUNDS } • 5001.60- 4.Q5* 391.31 0.42 124.91 . } FRTCTION • 50D1.70- 2.13* 179.32 4.86 Dc 70.41 } CATCH SASIPI 5001.70- 2.28* �168.35 4.86 Dc 24.19 ------------------------------------------------------------------------------ 2+�AXIMCR+4 Ni_TMBER 0�' ENERGY SALANCES iISED IN EACH PROFILE = 25 NQ'i'E: STEADY FLOW I-IYDRAiTLTC HEAD-LQSS Cd2+FPUTATIONS BASED ON THE MOST CONSERVATIVE FORMULAE FROM TFiE CURRENT LACRD,LACFCD, P.ND OCEMA DESIGN MANUAI,S. xkf***ir**��+►*r�.+rrrta,��r.�t*�*wtt*wy*i+rr***a.r*r.:�**�x**+**xx**+**++:r**♦ DOWI35TREAM PIPE FLOW CONTROL DA'i'A: NdDE NUMBER = SpQ�.50 FLpW1�iNE ELE[TATIOid = 180.45 PIPE FLOW = 5.40 CFS PIPE DIP.2�LETER = 18.00 INCHE$ A55ilMED AOWIdS'i'REAM CONTROL HGL = J.84.500 FEET NODE 5001.fi0 : HGL =< 184.500>;EGL= � 184.624>;FLOWLII�iE- < 180.450> ♦t t}}yr *Rfi k+Yrk ik f*ri Yr Yr�irYrikYrYrf1� Y' iFYrY�f k kYr* *f #I1 k*iF*} **Yr1rYrYrYr1 rtYr}i ****t *+iti *%***YrYr1r*ff FLOW PROCESS FRQM NODE 5a01.60 TO NODE 5D01.70 IS COAE _.] UPS'iRFT�M NODE 5001.70 ELEVATION = 182.39 (FLOW IS LFI1bER �RE5SL3RE) ------------------------------------------------------------------------------ CALCULATE FRICTIOt3 L055E5(LACFCD): PIPE �'LOW � 5.04 CFS PTPE bIAMETER � 18.D0 �NCHES PTPE LENGTH = 7. 75 FEET idANNIidG' S N = 4.0130p 5F=(Q/K}**Z - {{ S.OD}/; 105.032})*rz = 0.00227 HF=L•SF = S 7.751*{0.002271 = 0.01$ - sIODE 540�.70 : HGL =< 189.518�,EGL= < 18k.642�;FLOWi�I?dE= < 182.390> � � � 4 W 4 y # * * t f * w * f * * * + * * * t # i * * * * t f * # � * t Y f � f * � x f f t f * Y i * + * * f * t t � * * * * } Y Y � ti * * * * * } 1 k k * ► F�,OW PROCESS FROM NODE 5001.70 TO NOD£ 5001.70 iS CODE = B UPSTREAM NObE 5401.70 EL,EVATION = 182.39 ;FLOW IS LFI3DF�t PRESSUREj ------------------------------------------------------------------------------- CALCULATE CATCH BASIN ENTRANCE i3OSSES(LACFCD): PIPE FLAW = 5.40 CFS PIPE DIAMETER = 16.40 IidCHES FLOW VEiOCITY = 2.83 F�ETlSEC. VELbC�TY HEAD = 0.124 FEET CATCH BASIN ENERGY LOSS =.2"`(VELOCITY HEAD} -.2*[ 0.124j = 0.025 ----------------------..___________.._________------------___------------------- NODE 500Z.70 : HGL =� 184.667>;EGL= < 184.567>,FLOWLII�F�= < 182.390> ww**x*a**+x**rr++*****++x****rt+*rt**y*s*tttiw*+*+x**x*rw+r+t+rt*ry.►******+x**+** UPSTREANS PIPE FLOW COId'I'ROL DATA: NOBE NUMBER = 5001.7D FLDWLINE ELEVATION = 182.39 ASS[Ji+fED UPSTREP.M CONTROL I-iGL = 1$3.25 FOR DOWNSTR£AM RUN ANALX5I5 ------------------------- END OF GRP.DF7ALLY VARIEI? FLOW AI�}P,LYSIS i � � � * f * rt ? f w h * * * f * t t k k ? ? * k � * t k k * rt * � R * } � t rt * * Y * * x rt * x � + * * k x > Y Y � M Y � Y W Y * * t w * f t * x f } * * > Y * * PIPE-FLOW HYDRAiTi,ICS COMPUTER PROGR�,M PACKAG£ IReference: LACFCD,LACRA, AND OCEMA HYDRAULICS CRITERTON) (e) Copyric3ht 1482-20�1 Advanced Engineering Software (aesl Ver. B.4 Re�ease Date: O1/Ol/2D�1 License ID 15D9 Analysis prepared by: PROJECTDESIGi�I CONSUL'IA1�I'PS 701 'B' SfiR£E'F, SUITE 800 SAN DIEGO. CA 9210i 619-234-0349 i**�r*:*rit*r*+*wwwtwrt+s+ DESCRIPTION OF $T[JB�.' wxw++xww+r**ri***:wxx+i+++ * BRESSI RANCH - LFLT�MATE CONDYTIONS * * SXST£�I 5000 - �,ATERAL 3(NQ. 9 PER SHEE'i 14 OF DWG. 400-8C} * w lOD-YF�:R * *rw**wrt*wt***rt**r*x*w*rt*r*ty�*+*+�**w**��rr+r�r�w+�wx++rt**+x***�w*x**x**,r,tx* FII,E �IANSE: 5040-3.DAT TIME/DATE OF 5'Ti7DY: 13: ifi 04/O8/2002 +��*+.*+*.*x.*......,.*****.**.,�.**.*.*+x»..*.��..,..***.+***+**«...*.tf*x*++*�.+. GRADUALLY VARIED FLOW ANALYSTS FpR PIP� SYSTEM NODAL POINT STATUS TABLE iNote: '*' indicates nodal point data used.) UPSTREAM RUN DOWNSTREAAF RiJN 230DE 2�iODEL PRESSURE PRESSURE+ F'LOW PRESSURE+ I3iJMBER PROCESS HEA.D { FT ) M023ENTUM ( POLiNDS ) DEPTH { FT i i+SQMENfiUM { POT7NFJS ) � 5002.20- 2.27 DC 1255.34 1.51* 1544.77 } FRTCTION 5002.30- 2.27*Dc 1255.34 2.27*Dc 1255.34 ------------------------------------------------------------------------------ MAXIM�TM �BER OF ENEAGY BALANCES USED IN EACH PROFILE = 25 NOTE : STEI�DY FiAW HYDRA[TE�IC HEAD-LOSS COMPt7'I`ATIODIS BASED ON THE MpS'I' CQNS£RVATIVE FORMUi�AE FFt02yE TH� CURR�:NT LACRE}, LACFCD, AND OCEMA DESIGN M.�NLTAL$ . ++xfw+t+*wx**�rrr�*y,rwsws*rr�*+*�rta*�*sy**r+*�+wr+v.v.+t,t*a.*t**+*xw++*,r+*t+twf+* DOWI35'FR.EAM P�PE FLOW CONTROL DATA: NODE NL7MBER = 5042.20 FLAWLINE ELEVA'I'ION = �88.86 PIPE FLOW = 47.7U CFS PIPE DIAMETER = 30.00 INCHES - ASSiiMEJa �10WNSTREAM CONTROL HGL = 190.300 FEET •NDTE: ASSiJMED DOWNS'FREAM C4NTROL bEPTI-i( �.44 FT.) IS LESS THAN CRITICAL DEPTH{ 2.27 F'i`_} ___> CRITICA�,' DEPTH IS ASSiJI�iED AS DOWNSTREP.M COI3'I'ROL DEPTH �'pR UPSTREPIN RiJN ANAI,YSIS ATODE 5002.20 : HGL =� 390.374>;EGL= < 194.026�;FLOWT.,INE= < 1B8.660> **..�r�wt�+ti*+*++t*.+*+.*»..++*+�+Wt�v.tt+��**..***......,.�***�.**+.*.�*>.*t+*+ FLOW PROCESS FROM NODE 5002.20 'FO NQDE 5002.30 2S CODE = J. UPSTREP.M NODE 5D02.30 ELEVAfi20N = 191.41 {gLOW IS SUPERCRIfiICAL) ....---------------------------------------------------------------------------- CALCiFLATE FRICTION L055ES(LACFCDJ: PIPE FLOW = A7.74 CFS PIPE b2AMETER = 30.�0 II3CHES PIP£ LEI3GTH = 57.36 FEET MANNING'S N= O.D1300 ------------------------------------------------------------------------------ NORM..� DEPTH{FT} - 1.33 � CRITICAL DEPTH(F�) = 2.27 C� � --UPSTREAM-CON'FROL_ASST3MED-FLOWDEPTH(FT)-------2-27=====_______'___" ____-_--- GRADUALLY VARIED FLOW PROFI�E COI�PUTEiI INF�RNiAT_TON: DISTANCE FROM FL6W DEPTH VELOCI�'Y SPECIFIC PRESSURE+ CONfiROL { FT ) ( FT j ( F'I' / 5EC ) Ei1ERGY ( FT j MOiSENTUM [ POUNDS } Q.000 2.2b8 1.0.i89 3.881 1255.34 0.063 2.230 10.314 3.883 1255.93 0.255 2.193 10.Q50 3.889 1257.7i 4.563 2.155 10.598 3.9DD 1266.6$ 1.D55 2.117 10.757 3.9x5 1264.67 i.684 2.080 1D.927 3.935 1270.3� 2.483 2.042 11.�10 3.960 1277.D0 3.472 2.004 J.1.345 3.990 12B5.03 4.670 1.966 11.513 4.026 1294.43 6.1D5 1.929 11.735 4.068 13�5.27 7.610 1.891 11.97� 4.117 1317.61 . 9.82i 1.853 12.221 4.174 133�.52 " �2.19a 1.816 12.48B 4.239 1347_lU 34.975 1.77B 12.771 4.312 1364.43 �8.256 1.740 13.073 4.396 1383.62 22.133 1.702 13.393 4.490 1464.78 26.738 1.665 13.735 4.596 1428.fl4 32.252 1.627 14.Q98 4.715 1453.55 38.931 1.589 Z4.484 4.849 1481.45 47.147 1.552 34.897 5.000 15�1.93 - 57.350 1.514 15.331 5.1b6 1544.77 --------------------------------------------___-------------------------------- NODE 5002.3D : HGL =< 193.67B>;EGL= < 195.291>;FLOW�,INE= � 19�.410� **t*++*+**,rx*,r**w�**k*+*rx***x*+,r*+*w�t„ra*�+*�+*xtt*t+r****Yf�*++*rr**,�rr+ratit � UPSTREAM PiP� Fi,OW CpN"PROL DATA: NODE NUi�3BER = 5D02.30 FLOWLINE ELEVATIpN = 391.41 ASSLiMED LiPSTREPI�3 COi+PI'ROL HGL = 193.68 FOR DOWNSTREAM RUN ANAT.,YSIS END OF GRAL�iiALLY VARIED FLOW Ai+IALYSIS • � x++��x+x��r**tr*rwt�wrx�*r*rwrsrt*�..r.f.rr.ar�xf**fxw*rtxsxxx*�wx�x�x�w�x**s:wt PIPE-FLOW HYDRAUiICS COt�SPUTER PROGRAbS PACKAGE {Reference: i,ACFCD,LACRD, AND OCF.i�IA HYDRAU?�TCS CRTTERION) {c1 Copyright 1482-200i Advanced Engineering Software (aes) Ver. 8.0 Release Date: O1/41/2001 License ib 1509 Analysis prepared by: PROJECTDESIGN CONSUL�TP.NTS 7p1 'B' STREET, SUITE BDO SAN DIEGO, CA 92101 619-234-0349 x*x+***xxw*+xr*w***+***wxs D�S�RZ�'1'��V d�' S'1'�Y wr�e***r**rtr*r.*+wrw�+i*+> * BftESSI RANCH - CTT�'I'TMATE CO�iDI'iTOidS * * SYSTEM 500fl: LATER.AL 4{NO. i0 PER SHEET 14 OF DWG. N0. 400-SCj * * 1D0-YEAR w tr�*yrf*rt**++x�****+�+*xxrt*+*rt*,r*�*++s*xt�****wr*r*wx*+*t++xwr*+xt*+*+x**tx F�LE NAME: 5000-4.DAT TIME/DA'I'E bF STIJDY: 13: a9 09/48/20a2 ++**+r*t*x****t+frrt*+y*wt*r**xx*+*+rt*+***+ytti�x+*�*rr,��a*�r�.+*.v.rf�.r��++i.�*+ GRADi3ALLY VARIEi1 FLQW AI�ALYSIS FOR PIPE SYSTEM NODAI, POTNT $'I'A1'US TABLE (Note: ^*" indicates nodal point data used.} UPS'i'P,EAM Ri334 DOW2IS'i'REAM RUN NQDE MODEL PRESSURE PRESSLiRE+ FI,OW PRESSURE+ NUMBER PROC ES S HEAI) { FT } MO�IEN�`UM ( POUNDS J DEPTH {�T j MOMEiJ'I'UM ( POL7ND5 } 5403.14- 0.7}. Dc 44.24 0.58* 47.39 ) FRICTION 5003.24- 0.71*Dc • 44.24 4.71*Dc 44.24 ) CATCH BA$IN 5003.20- 1.Q5* 23.$9 0.71 bc 15.61 _--�--------------------------------------------------------------------------- MAXI[+IUM NLTMBER OF ENERGY RAT,ANCES USED TFV EACH PROFII,E = 25 -------------------------------------------------------_----___---------------_-- NOTE: STBAItY FLOW HYDRALT�,IC HEAD-LOSS COMPUTATIODiS BASED ON THE MOST CONSERVATIVE FORM[iI,A£ FAOM THE CL7FtP.ENT i,ACRii, LACFCD, A23D OCEthA DESIGN I+4P.N[7AL5. ww,r++vr**w*r*rw�x**t*+*yx:*+***+*xr*r*r*+*+xtixw*t�w�*�**�*�r+*r*ti+f.rtf.i+*rrr***r DOWi�ISTREAM PIPE FLOW CONTROi� DA'I'A: 130DE NiTMBER = 5003.10 FLOWLINE ELEVATION = 194.68 PIPE FLOW = 3.54 CFS PIPE DiAMETER = 18.00 INCHES ASS[iMED i�pWNSTREAM CONTROL HGL = 195.300 FEEi` *NOTE: ASSUMED DOW23STREAM CONTROL DEPTH( 0.62 FT.j IS LESS THAN CRITICAL DEPTH( 0.71 FT.} ___> CRT'FICAL AEPTH IS A55UMED AS DOWNST�tEAM CONTROL DEPTH FOR UPSTREAM RUN ANALYSTS -------------------------------------------------------..__....------------------ NODE 50Q3.10 : HGL =< 195.255>;EGL= < 195.744>;FLOWi�INE= <�94.580> r*r.r**�**a+.fr+i.*w*:+x*twi.*rt+.+rrr�rr+t.as+rrt*,rx****+**rx*wrr+*k****+*r+:itr FLOW PROCESS FROM NODE 5003.1D TO NODE 5003.2U IS CODE = 1 LFPSTREAM 130DE 5003.20 E��IAT�ON = 195.12 (FLOW IS SUPERCRITICAL) _------------------------------------------------------------------------------ CALCULATE FRICTIOId LOSS£SILACFCDJ: PIPE FLOW = 3.50 CFS PTPE DIAMETER = 18.OD YNCHES PIPE LEI3GTI�i = 36.75 FEET M.�biATING'S N = D.013D0 s � �TNORSSAL`AEP'I'H{FT1=--=-===��5�YL4i�y`====CRIT�CP.i�-DE�THIFTI--======0=71=====-_ __ __ _ ____ _ _ _ ____ UPSTREAM CONFROL ASSLTMED FLOY7pEPTH(FT) = 0.�1 ------------------------------------------------------------------------------ GAADi3ALLY vARIED FLDW PROPIL� COMPUTED INFORMATI�I�I: DTSTANC� FROM FLC}W bEPTH VELOCTTY SPECIPIC PRESSURE+ CONTROL { FT } ( FT f ( FT/ SEC } FNERGY ( PT � MOiSEI3TUM ( POLTND51 . fl.fl00 0.714 4.220 0.99D 44.24 D.D19 0.7D8 4.265 0.99� 44.25 4.�5$ D.702 4.311 0.991 44.26 4.�39 0.696 4.356 0.991 44.28 0.245 0.69D 4.4D6 D.992 44.32 0.396 0.685 4.454 0.993 44.36 0.590 0.679 4.504 0.994 44.42 0.832 0.673 4.555 0.995 44.48 3..Z26 0.667 4.6D6 0.997 44.55 1.489 0.661 4.661 0.999 44.65 1.9D4 0.655 4.716 1.a01 44.74 2.412 0.650 4.771 1.QD3 44.85 3.006 D.644 4.826 1.D06 44.98 3.7D4 0.638 4.887 1.009 45.11 4.525 0.632 4.947 }..Q12 45.26 5.494 D.62fi 5.006 1.016 45.42 5.541 0.620 5.D70 1.D20 45.59 8.009 0.615 5.134 1.024 45.77 9.b58 0.609 5.200 1.D29 45.97 11.fi75 0.603 5.267 1.034 46.I8 14.396 0.597 5.336 1_039 46.41 17.447 0.591 5.4�7 1.645 46.55 • 21.855 0.565 5.474 1.Q52 46.91 28.375 0.580 5.553 1.659 47.�8 36.75D 0.575 5.607 1.064 47.39 ------------------------------------------------------------------------------ NqDE 5�03.24 : HGi. _� J.95. 834>; EGL= < �96.110>; FLOWLZFdE= < 195. 120> ***r+*x***x*tr*yw*�*x*rw**��*x**:ri*+*+*+�a++*+txrt*xt+*+**�+.��,rrr*�*r+tf*+*+++ FLOW PROCESS FROM NDDE 5�D3.20 TO NOD� 5003.20 IS CODE = 8 i3P5TREAM NODE $OU3.20 ELEVATIdN = 195.i2 (FLpW IS AT CRITICAL DEPTHi ------------------------------------------------------------------------------ CALCi]i�ATE CA'TCH BASIN EA1'I'RPNCE LOSSES (LAC�'CD� : PTPE �Lpw = 3.50 CF$ �IPE DIAMETEFt = 1$.OD INCHES FLOW VELOCITY = 4.22 FEE7'/SEC. VELOCI'iY HEAD = 0.277 FEE7' CATCH SASIN ENERGY L05S =.2*(VELOCITY HEAi}) =.�2*{ 0.277} = O.Q55 NODE 5003.24 : EiGL =< 196.166>;EGL= < 196.1b6>;FLOWLINE= < 195.120> **+*v,t�*+�*+*+�+******,.*x*+�**��*,�v.«�++�++*.t�*+*++***+**�***.*«*..**„�*.*+*k� _ UPSTREAM PIP£ FLOW CON'T'ROL DATA: NODE NUNfBER = 50D3 . 20 FLOWi�IAIE ELEVATION = 395. Z2 ASSLT�A UPSTREAM CONTROL HGL = 195.83 FpR pOWAiSTREAM RUN ANALYSIS -------------------------------------------------------------------------------- ------------------------------------------------------------------------------ END OF GRADUALLY VARIED FLOW ANAi,YSIS � # *x.***,.***.,�*****.****.*******.*********�*.***.*.*�.**.�*.�.t�*��*�,**},: PIPE-FLOW HYDRALFLICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, PND OCEMA FiYDRAUF,ICS CRYTERION) (c) CopyrighC 1482-2D01 Ac3vanced Engineering 5oftware (aes) Ver. 8.D Re�ease Aa�e: �Z/O1/2001 License ID 1549 Analysis prepared by: PR0�7ECTDESIGN CpbiSULTANTS 701 'B' STREET, SUITE 800 SAN D�EGO, CA 3210i 619-234-a349 .w***�+��v.,.,r++w.�+*++��++* bESCRIPTION aF STCiI7Y •****+*•••**•••�••*•*•••*� * BRE55I RANCH - 1TL'i`Ii+1ATE COi1DITI0NS * * SYSTEM 50D0 - LATERAL 5{NO. 11 PER SHEET 14 OF DWG. 400-BC) * � 100-Y�AR * Y Yr f�k *wt *Y4t *tt�k �F* Yi Y�*►f iF4 W Y f W YrYYrM �Yr Y M* t Y* *#Yr � Y� 1E�k�k4f i�i�*# 141k}�k�i}�i� *t�i�li�! �k�f }f FTLE NAME: 50D0-S.DAT TIME/DATE OF STLiDY: 13:21 09/OB/2002 .*��*..�...**..*«..*�*....*,..+**�**..+»**+��..*�.......+*...��....**.**.,,.*.,. GRAbUALLY VARTED FLOW ANA�YSIS FOR PIPE SYSTEM NODAL POINT S'FATUS TAB�,E (Note: •*' indicates nodal point data used.) UPS'd'REAM RUN AOWNSTREP.I�F RUN idODE MObEL PRESSURE PRESSURE+ FLOW PRESSLIRE+ NUMBER PROC ES S HE.�D ( FT ) MOMENTUM { pOLFND5) DEP�'H { gT } MOMII�]'F[Tt4 I PQUNDS } • 5003.5D- a.62 22.A1 0.26* 38.b4 } FAIC'F�ON 50fl3.60- Q.53*Dc 21.55 0.53'Dc 21.55 } CATCH BASIN 5003.60- 0.77* 11.46 0.53 Dc 7.7B MAXINNM NiTMBER OF EDiERGY SALP.NCES �JSED Iid EACH PROFILE = 25 ------------------------------------------------------------------------------ NO`FE: STE.�DY FiOW HYDRAULIC HEAD-LQSS COMPLiTAT10NS BASED ON THE M�ST CONSERVATIVE FORMULAE FRQt+4 �`HE CI3RRENT LACRD,LACFCD, AND OCEMA DESIGN MANi7ALS . r�.+r.f***xxswrt*xxx�+wx*a+:r*****s+.rxwww*w*xx:**++**+**w,rxw***xx�**a+y*+.i.*i.t DOWDI5TF2EAM PIPE FLOW CONTROL DATA: NODE Ni]t3BER = 5003.50 FIAWi�INE EiEVAi20N = 194.6$ PIPE FLOW = 2.DD CFS PTPE D�AMETER =].8.00 IidCHES A5513ldED DOWNSTREAM COI3TROL HGL = 195.3D0 FEET ------------------------------------------------------------------------------ NpDE 5003.50 : HGL =< 19A.943>;EGL= < I96.377�;FLOWLINE= < 194.580> +*x++.*t*r+r+t�xt+r:*rrtr*t�i+rr+<+f++*,rr***ar**:tx+s*t+x+*y�**rtwy**�t*+t***r*rr• FLpW PROCESS FROM NODE 5003.50 T4 NODE 5D03.60 I5 CODE = 1 L3PST'REAM NODE 5DD3.6D ELEtIATI013 = 195.87 (F�,C)W IS SLiPERCRITTCAi,) CALCULA'£E FRICTION i0SSE5{LACFCD): PIPE FLOW = 2.00 CF5 PIPE D�AMETER = iB.00 INCHES PIPE LFNGTH = 4. 75 FEET N1P.NrIING' S[d - 4. D13D0 NORMAL DEPTHfFT} - 0.20 CRITICAL DEPTHiF'i) = 0.53 UPSTFtEP.M CONTROL A55UMED FLOWDEPTH(FT) = 0.53 ------------------------------------------------------------------------------ � � GAAi)L3A�,LY VARIED FLOW PROFiLE COMP[7TED INFORI�3ATIOI3: ------------------------------------------------------------------------------ D�STPNCE FROM FLOW DEPTH VELOCITY SPECIPTC PRESSU�tE+ COPITROL { FT ) � FT ) ( F'� / SEC } ENERGY ( F'T` ) MOMENTUM { POLTNDS } D.000 0.533 3.552 0.729 21.55 0.003 0.520 3.67fi 0.730 2]..57 0.�11 0.547 3.8D9 0.732 21.64 O.D27 0.493 3.951 0.736 21.77 0.05D 0.480 4.103 0.741 21.94 0.082 0.457 4.26b 0.749 22.i7 0.125 0.453 4.44� 0.760 22.47 0.38D 0.440 4.629 0.773 22.83 0.248 0.427 4.$31 0.784 23.27 0.334 0.413 5.054 O.SD4 23.78 0.439 D.4Q0 5.288 0.834 24.38 0.567 0.387 5.545 0.864 25.07 0.724 0.373 5.827 0.901 25.87 0.914 0.36D 6.134 4.944 26.78 1.147 0.347 6.47Z 0.997 27.$2 1.433 0.333 6.$42 1.061 29.01 1.785 0.320 7.251 1.�37 • 30.36 2.223 0.307 7.706 1.229 31.90 2.774 0.293 8.2�2 1.341 33.fi5 � 3.480 0.280 B.779 1.477 35.65 4.k04 0.267 9.4�7 1.544 37.95 4.75D D.263 9.508 1.597 38.64 --------------------------------------------------------_____________--------- NODE 5D03.6D : HGL =< 196.403>;EGL= � 196.599>;FLOWLINE= <�95.670> • **t*xx**rt+*rt***trt***er***�***t�*x*weyti******�w*t�+ry,*s�r+>tww+*x++x�***x*****+� • FLOW PROCESS EROi�i NODE 5003.50 TO NODE 5D43.60 IS CODE = B LTPSTAEAM NODE 50D3.b0 ELEVATION = 145.67 (FLOW IS AT CRI'FICAL DEPTH} CALCUI,A�'E CATCH BASIN ENTRANCE i�055E5 (LACFCD) : PIPE FIAW = 2.40 CFS PIPE DIAMETER = 18.Q0 INCHES FLOW VELOCITY = 3.55 PEET/$EC. VELOCITY HEP.D = 0.196 FEET CATCH BASII3 �NEFtGY LQSS = .2*{VELOCITY HEAb) _ .2*{ p.196j = �.039 -------------------------------------------------------------______------------ NpDE 50p3.60 : HGL =< 196.638>;EGL= <�96.638>;FLOwLINE= � 195.87�> *+*wkv,+rt**rt+ry+*xr**r*��rry**:***+++x++*+x�***r**��Wv.ayrfai.tw+++*+*+f+�v.��+�*♦ UPSTREP.NF- PIPE F'LOW CONTFtOL DATA: NODE NUt+fF3ER = 5003.6D FLOWLiAiE ELEVATION = 195.87 A55LFMED UPS'iREAii C�NTRO� HGL = 196.40 FOR DOWI3STREAM RUN ANALYSIS END OF GRADUALi�Y VARIED FLOW AbiALYSIS � � k * * * * * * * * � * t � t ! � Y W W # + f t 1 * # # i f f * + * # i # f * # * t + � i ! t t # t } i * * * K * i * k * k * * * * k t * t � * � * * f ti 1 i P�PE-FLOW HYDRAULICS COMPUTER PROGf2RM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRAULICS CI�tTTERiON} Ic) Capyright 19E2-2002 Advanced Engineering Software (aes} Ver. 8.0 Release Date: 01/41/2D02 License ID �509 , Analysis prepared by: ProjectDesign Cnnsultants 701 B Street, Suite B00 San Diego, CA 921p1 **+****.****�*..*.**�.�*+. DESCRIPTION OF STUDY *"'**••'�'+"�******+*..«x** * SRESSI RANCH - ULTiMATE CdNDITIONS * * SYSTEM 5400 - LATERAI� b(N0. 5 PER SI-3EET 13 OF DWG 900-SC) * * 1Q0-YEAR * i* Y t YY Y Y?!YY *Y+Y �k� tii �.� fi i*Y� 1 i� rt# t�� I�i'kf+}ii#*iii #* 1** f}*YrYrYr*****ti f%* f? 4#�! FILE NAME: 5p00-6.DAT TIMEI�A'FE OF ST[iDY: 16:49 t2/26/2002 **i� �k*YrlrYr?!Yr*tkf*tkyr� �Ir********Yr*�i �ryr �ky[ * **Y***�i * �k**tttt * * * iYr �kik�yrf �kyryryr******!r f **YrY� i� �k GRADUALLY VARIED FLOW ANALYSIS FOA PIPE SYSTEM NODAL POYNT STATUS TABLE tNote: "*" indicates nodal point data used.) U�STRF�M RUN DOWNSTREAM RUN NODE MODEL PRESSiJRE PRESSLFRE+ FLOW PRESSURE+ • Ni.TE�4BER PROCESS HF'.AD ( FT ) MOME'.N'I`UP4 ( PO[J1dD5 ) DEPTH ( FT) bfOMENTlJ?�7 ( POiTfFi?5 ) 50D5.10- 0.43 Dc �2.45 0.19' 25.91 } FRICTION 50�5.20- 0.43*Dc �2.45 0.43*37c 12.45 } CATCH BASIN 5445.20- Q.51Y 6.bfl fl.43 pc 4.54 2+3RXIMUM NLTtABER OF ENEAGY SALANCES USED TN EACH PROFZZ,E = 25 ----------------------_-----------------------__--------------------------------- NOTE: ST�ADY FLOW HYDRAUL�C HF.AD-L055 COr3PUTATI0N5 SASED ON THE MOST CONSERVATIVE FORMUI�AE FROM Ti-IE CIJRRENT LACRD, LACFCD, AND OCEMA DESIGN MAAF[TALS. *Y * �k * f ****** ***f # k k *�FYriF*�r****Yr *yr ** **�k ****Ii �M *****Y * i� Yr t *t t! fl�k�i4 i1f#��Ff y� i� ki�l#1 ♦ DOWi3STRF..AM PIPE FE,OW CONTROL DA'�'A: NQDE NUMBEi2 = 5405.10 FLOWLI�IE ELEVATION = 221.96 PIPE FLOW = 1.30 CFS PIPE DIA�+]ETER =�8.Oa INCHES ASSUMED D04�1NSTAEAi�4 CONTROL HGL = 222.210 FEET *NOTE: ASSi7MED DOWNSTRE.�.M CONTRdL DEPTH( 0.25 FT.) IS LESS THAEV CRiTTCAL D�PTH( 0.93 FT_} ___> CRFTICAL DEPTH IS ASSU2�fED AS DOWNS�`AEAM C4NTROE, DEPTH � FOR UPSTREAM RUN ANALYSIS ------------------------------------------------------------------------------ N017E 5005.10 : HGL =< 222.152>,EGL= < 223.654>;FLOWLINE= < 221.960> 1r**Yr# *Yr**Y�Y�t**i1�r* 1fYf*YffYrYrl�k * 1 Yf *i Y+#�Jr+i ��kyr#fif+i��.#** f iF* *? iFiFYr*k*k�kklrYr�lrYrfri riiF FLOW PROCESS FRQM NODE 5005.10 TO NdDE 5005.24 I5 CODE = 1 UPSTREAM NODE 5605.20 ELEVA'FIdN = 223_52 (FLOW I5 SUPERCRI'FICAL) --------------------------------------------------------------------___________ CAi,CULATE FRICTION LOSSES(LACFCDJ: PIPE FLdW = 1.3fl CFS PIPE DIAMETER = 18.00 INCHES � PIPE LENGTH 6.25 FEET MANNTNG'S N ______________0.013Da � NORMAI., DEPTH[FT} - 0.16 CRITICAL DEPTH(FT) = 0.43 UPSTREAM CONTRQL ASSiTMED FLOWDEPTH(FT1 � 0.43 GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: DFSTANCE PROM �'LOW DEPTH VELOCITY SPECIFIC PRESSE3RE+ CONTROL(FT) (FT} (FT/SECi ENERGY(FT) M0�'4ENT[}M(POUNDS) D.000 Q.427 3.138 0.586 12.45 O.Q02 0.416 3.25D 0.58Q 12.46 O.Q09 4.4D6 3.369 0.582 12.50 0.421 0.345 3.496 0.585 12.57 O.Q40 0.385 3.631 0.5$9 12.67 0.065 0.374 3.777 0.596 12.81 0.099 0.363 3.933 0.544 12.98 0.142 0.353 4.100 O.b24 13.19 0.196 0.342 4.281 O.fi27 13.44 4.264 0.332 4.476 fl.b43 13.74 Q.346 0.321 4.687 O.b62 19.06 Q.448 0.311 4.9�6 0.686 14.46 a.571 0.340 5.265 0.714 14.94 Q.721 0.289 5.437 D.749 �5.46 d.904 p.279 5.735 0.790 36.06 1.128 0.2b8 6.a62 0.839 i6.74 1.904 0.258 6.923 0.$99 17.51 1.747 0.297 6.$22 Q.970 18.39 2.17B 0.237 'I.26� �.057 19.38 2.729 0.226 7.7b4 �.163 20.52 3.444 0.216 8.322 �.292 21.$2 � 4.421 0.205 8.952 1.450 23.31 5.804 0.�.94 9.669 1.647 25.03 6.250 O.i92 9.830 1.694 25.4i ------------------------------------------------------------------------------ NODE 5005.20 : HGL =< 223.947>;EGL= � 229.100>;FLOWLINE= < 223.524> *�****..**..**«**.+��*...�**.��*.*.*+*�*+..�*�..�,�.*.�+��f.**�++*++�****#++* FLQW PROCE55 FROM NODE 5005.20 TO NDDE 5405.20 IS COD� = 8 UPSTREAM NODE 5005.2fl ELE'[IATTpN = 223.52 (FLOW IS SUBCRITICAL) CALCLTf�A'i`E CATCH BASIN ENTRANCE LOSSES(I,ACFCD) ; PIPE �'LQW = 1.34 CFS PIPE DIAMETER = 18.40 INCHES PLOW VELpCTTY � 3.14 FEET/SEC. VELOCI'I'Y HEA� = 4.153 FEET CATCH BASIN ENERGY LO85 =.2*IVELbCI'I'Y i-IEAD) =.2*{ D.153} = 0.031 ------------------------------------------------------------------------------ NODE 5005.20 : HGL =< 224.130>;EGL= < 224.130>;FLOWLI�iE= < 223.520> •�****x��**�r+a�*r+**t++***a*++rtx+++**ry�*►y*ti**�r***�*�r�r+**+**+++x**�+***++*+ UPS�'REAM PEPE FLOW CONTROL DATA: NODE NUMBE�i = 5405.20 FLOWLTNE EL�JATTpN = 223.52 ASSUMED UPSTREAM CONTRQL HGL = 223.95 FOR DOWNSTREAM RUN ANALY5I5 EI�FD OF GRAD[3A%LY VARIED FLOW ANALYSIS � J • * # } * * rt k * � W h * * * * * * * Y * Y * � M * * * * * f rt R * 1 * * M * * * � * � * # * * * * * * * * t * t Y # * Y ! Y t * Y * M W W * rt i * W µ f � ti PIPE-FLOW HYDR.AULICS COMPU'i'ER PROGAAM PACKAGE IReference: LACFCD,LACRD, ANU OCEMA HYDRAULICS CRITER�ON} (c) Copyright 1982-2041 Advanced Engineering Software {aes) Ver. 8.0 Release Date: 41/01/2�01 License ID 1509 Analysis prepared by: PROJECTDESIGN CONSULTANTS 701 'H' STREET, SUITE BOD 5AN DIEGO, CA 92101 619-234-0349 ***v....,..�.+�.++f��t�++�w�-+ 17E5CAIP'I'ION OF STCJDY ***•***•*"�**•*•••••****•** * BRESSI RANCH - ULTII+L�TE CQNDIITOI35 * * SYSTEM 5D00: iATERAI, 7(N0. 6 PER SHEET 13 OF' DWG. 40Q-BC} • * 1D0-YEAR * .***rt. �.w+�+w++v.+s.+.*�*,�.t,...*,.*.�*.*,�**..t�+,�*tt��*+*..*+*.*.,**+*�**�+* FILE NAME: 5000-7.DAT TIME/DATE pF S'I'i3DY: 13:34 D9/D8/2002 ♦Y,#*Y� �FYrY� f Yr f Yr�F*4YriYrYrklrYriFYr*Yr iFR 1rYrYr f YrYr R 1rYrY� f!r!r Yr f f Yr #*�F **ir#�F*Y� fF# ir**t tar*Yc YrYr*#**1�*tk Yrf ** • GFtADUALLY VARTED FI,OW ANAT�YSIS FOR PIPE SYSTEM NODAL POINT STATUS TABi�E tNote: '*' indicates nodal point data used.) UPSTREAM RUN DOWNSTREF�M RLR3 NODE MpbEL PRE5SUI�E PRESSURE+ FLOW PRESSiTRE+ NLR+FBER PitOCE55 H£AD ( FT} MOMEN'PUt7 ( POiJNDS ) DEPTH ( F'I`} MOMENT[JPS ( POL7N�5 } � 5Qa6.�0- 1.15* 77.77 fl.60 59.68 } FRICTION 50Q5.20- Q.B3* 57.21 0.74 Dc 55.81 } CATCH BASII3 SD06.20- �.07* 35.12 0.74 Dc 20.11 MP.XIMUi+S NUMHER OF ENERGY HALANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NQTE: STEADY Fi.�pW HYDRAUI�IC HEAD--LOSS COMPU�'ATIONS BASED OAI 'iHE MOST CONSERVATIVE PORMUI,AE FROM THE CITRRENT LACRb,�,ACFCD, AND OCEMA DESIGN t�P.NUALS. ♦+s**xws+w+**w***�**+r*x�w**�xx+rttrtxw*++wx+�wxw*w**w*x*+tir*+wwr++*ra*+**x,r�*�x DOWNSTREAM PIPE FL041 CO�1'i`FtOL DATA: NODE NLTMBER = 5006.�0 FLOWLINE Ei�EVA'iION = 246.12 PIPE FLOW = 4.40 CFS PIPE DIAMETER = 24.04 INCI-IES ASSiJM£D DOWNSTREAM CONT'RO�, HGL = 249.270 FEET ------------------------------------------------------------------------------ NODE 5D06.10 : HGL =< 249.270>;EGL= < 249.356>;FLOWLINE= < 298.320> ****k***ti*tt YYr Yi f* tY Y*i M►Yr f t�t*Yr Y***#*Y� Yr*!** *f Yi N*Y�*YW 41�y�iY�yr*�*'kW'k� *#�Fi��lrt1 Y*! i FLOW PROCE55 FROM idODE 5006.10 TO �10DE 5006.20 IS CODE = 1 UPSTREAM NOA£ 5006.20 ELEVATIO�i = 248.36 (FLOW IS SUBCRITICAL) CAi,C�iI�ATE FRIC'i'ION iOSSES (LACFCD) : PIPE FLOW = 4.40 CFS PIPE DIAMETER = 24.00 ZNCHES PIPE LENGTH = 2D.25 FEET MANNING'S N- D.01300 NORMAi� DEPTHIFTj = 0.57 CRiTTCAL AEPTH(FT} - 0.74 DOWNSTREAM CONTROL ASSLiMED FLOWDEP'I'I-t(FT� = 1.3� -________�_��_��_��,__==�_�4��=-,��_��_________________________________ � � . GRADUALLY VARIED FLOW PROFIi£ COMPiJTED I�1F'OR�TION: ------------------------------------------------------------------------------- AZSTANCE FROM FLOW AEPTH VELOCITY SPECYFIC PRESSiJREf CONTROi, { FT j ( FT ) { FT/ SEC ) ENERGY { FT ) M0S3�TUM { pOL�7DS } U.D40 1.150 2.353 �.236 ' 77.77 1.235 1.133 2.395 Z.223 76.22 2.450 1.1�7 2.438 Z.209 74.71 3.672 1.100 2.463 Z.196 73.25 4.872 1.084 2.53d �.163 71.$5 5.057 l.Ofi7 2.579 ?..171 74.49 7.22'] 1.051 2.630 7..158 69.28 8.38� 1.D34 2.683 3.14b 67.92 9.515 1.Oi8 2.738 1.134 65.72 10.630 1.Q41 2.745 Z.123 65.57 1�.723 0.985 2.85fi 1.111 64.98 . 12.791 4.968 2.918 1.1D1 63.44 13.832 a.952 2.964 1.090 62.46 14.B44 - D.935 3.052 1.D64 61.54 15.822 0.919 3.123 1.074 60.68 15.763 0.942 3.198 1.061 59.88 17.fi62 0.886 3.27b 1.052 59.�5 18.514 0.869 3.358 1.D44 58.48 19.313 0.853 3.444 1.037 57.88 24.051 0.836 3.535 1.034 57.35 20.250 0.831 3.553 1.028 57.21 ------------------------------------------------------------------------___---- NODE 5a06.20 : HGL =� 249.191>;EGL= < 249.388>;FLOWLINE= < 248.3fiD> ty*:ty**yf*r*��r*rt:�rr,rtr�**r.r*�rw***rrrwyti�*+ry.a:.+�+**++w**wx*�xww*►*�t+x�R*w FZ,C1W PROCESS FFtOM NODE 5406.24 TO D}ODE 5006.20 �S CODE = 8 � --UPSTREAM NQL1E 5�06.24 ELEVAT�ON = 248.36 (FLQW IS SiJBCRITICAL] CALCULA'i£ CATCH BASIN ENTRAidCE LQSSES(LACFCD): ' PIPE FLOW = 4.40 CF5 PIPE DIAMETER = 24.D0 TNCHES FLOW vELOCITX = 3.55 FEET/SEC. VELOCZTX HEAD = 0.19i FEET CATCH BASiN �'NERGY LOSS =.2* {�r,pCT'T`Y H�AD} �.2* ( 0. 197) = U. D39 NODE 5006.20 : HGL =< 249.426>;EGL= < 249.426>;FLOWLINE= < 248.3fi0> x�*wx+*x*r**r�++r**rrr*t+**r�y,rr*4***�r*k*er+�rwv.+++*t�***x�*w*�**+w,r+tsa*+f*a UPS'i'REAM PIPE FLOW COtI'T'R0� DATA: NODE NLTt+fBER = 5 0 0 6. 2 p FLOS�TLINE EI,£VA'i'I ON = 2 4$. 3 6 ASSUMED UPS'FREAM CONTROL HGL = 249.10 FOR DOWNSTREAM RiFN ANALXSIS END OF GRAI]UALLY VARIED FLOW ANALY5I5 � � w+***xx**x*xr+ffa+txr*+r.*rr:w*fw.rw�rrxRx*w*wx+iw*xxs*��rt*r**w*++*x*xx++***♦ PIPE-� OW HYDRAULICS COMPi3TER Pi20GRAM PAC}CAGE (Reference: LACFCD,LACRD, AND OCEMA HYbRAUI,�CS CRI'FERION} (c} Copyright 1482-2001 Advanced Engineering So£�ware {aes} Ver. B.0 Release Date: O1/D1/2DD� iicense ID 3.509 Analysis prepared by: PROJECTDESIGN CONSULTANTS 701 'B' STFtEET, SUITE 800 SAN DIEGO, CA 921p1 619-234-0349 *..+.,.+..*+�+*+++�.+**.*++ DESCR�PTION OF STUI3Y *•••*•••'�**�"'�+*++�+,�,�,.,.v.* * BRESSI RANCH - INT�R�M MASS GR�DED CONDIi'ION * ' SY5'£E2h SQOD: LATERAL 7(3d0. 6 PER SfiEET 13 pF DWG. 40p-8C) * * �DD-YEAA * *x.*.*.,*.*.*,.«.*�*****.*...+**.*++***«�.*+*.**.�**++**+�*****„**..t***:*.,� FILE I3AME: 50D0-7I.DAT `I'IME/DATE OF STi3DY: 13:38 09/p6/2D02 rt�*x******r*i��*rr�*r*r*r*t*e***t***rt****rriw*rr�tr+i.rv.�+f++**++*+�t+++*ax+t GRADUAI,LY VARIED FLOW ANALYSIS FOR P�PE SYSTEM NOI}AL POINT $TATUS TA$LE ' {13ote: "*" indicates nodal point data used.l UPSTREAi�S RUN DOWNSTREAM AUN NQAE l�EODEL, PRESSURE PRE55URE+ FLOW PRESSiJRE+ NUMBER PROCESS HEP.D ( FT j �fOMENTT3M ( POi.1NDS ) AEPTH ( FT } MOMENTUM ( PUUNDS ) � 5006.10- 1.36 Dc 254.08 0.69* 429.31 ) FRICTION 5Q06.2p- 1.36 i1c 259.08 D.61* 502.14 } JUNCTION 5006.30- 1.39 Dc 302.62 D.68* 524.16 } FRICTION 5006.40- 1.39*A� 302.62 1.39*Dc 302.fi2 } CATCH SASIi�I 5006.44- 2.59' 214.47 1.39 Dc 70.64 ------------------------------------------------------------------------------ M.a.XI�SCiM I3CTMBER QF E3�IERGY HAI,.�NCES i7SEb IN EACH PROFIi,E = 25 ------------------------------------------------------------------------------ NOTE: $TEADY FI,OW HYDRAULIC HEAp-LOSS COMPUTATIONS BP.SED ON THE t+]OST CONSERVATIVE FORMULAE Fi2pM THE CFJRRENT LACAD,LACFCD, AND OCFt�A DESIGN MANUALS. **++**+**xs*w+**w**�*+�*rw�►r**+++r+*+*wx*►*+�rww+**+a*aa*�yxr*ti+*++�**+w+*ra* DOWNSTREAM PIPE FLOW CONTROL DATA: NODE NT3MBER = 5005.10 FLOWLINE ELEVATION = 248.12 PIPE FLOW = 14.30 CFS PIPE DIAMETER = 24.4b INCHES , ASSUr�D ]]OwNSTREAi�i CON'T'ROL HG� = 249.270 �EET *NOTE: ASSiFMED �?OWNSTREAM CONTROL DEPTH( 1.15 FT.} IS LESS THAN CRITICA� DEPTI�i �.36 FT.) ___> CRITICAL DEPTH I$ ASS[.TPSED AS DOWNSTREP.M CO�TI'ROL DEPTH FOR UPSTRF.PM FtLTiV ANALYSIS NODE 5006.i0 : HGL =< 248.BZQ>;�GL= < 252.245>;FL04�TNE= < 248.12D> *x+t�*x*x+*w**w*r*w*+***w*+*rr*****r+wx*****�*r+*+++*++*�*+tweyxfiyx***i.+�**+R* FLOW PROCESS FAOM NODE 5006.1d TO NpDE 5p4&.20 IS CODE _� UPSTREA3g NODE 5006.20 ELEVATION = 248.36 (FLOW IS SUPERCRITICAL} ------------------------------------------------------------------------------- . � CALCULATE FATCT�ON ispSSES(LACFCD): PIPE FLOW 14.30 CFS PIPE DIAMETER = 24.D4 ItdCHES PIPE LENGTH = 20.25 FEET MAN23ING'S DI - 0.0�300 ------------------------------------------------------------------------------- NOFt1�iAL DEPTH{FT} - 1.09 CRIT'ICAL A�PTH{FT� = 1.3b UPSTREAM CONTRdL A55UMED FLOWDEPTHfFT} - 0.61 ---- -------- GRADUALLY VARIED FLOW PROFILE COMPU'F£D INFOAMATION: DISTANCE FRb2+� FLOW DEP'd`H VELOCITY SPECIFIC PRESSURE+ CONTROL { � ) ( � } { FT1 SEC } ��Gy { FT ) MOS�fENTi1M ( POUNDS 1 O.OaO 0.609 17.655 5.453 5D2.14 4.748 0.629 16.907 5.070 482.39 9.551 0.648 16.2Z4 4.733 464.23 14.414 0.667 15.570 4.434 447.46 19.341 0.687 14.972 4.174 431.99 24.250 0.69D 14.867 4.125 424.31 NQDE 5006_20 : HGL =< 248.469>;EGL= < 253.8J.3>;FL,OWLINE= < 24$.360> *'ttt #**!Y�* # k iFf * f* frf tk �F�Ff YrfriF Yr f k f* f Yrk* YrYr**Yr** Y� �*ir**Yc 1r*i *YYk'k �t'F �k'ktt�t �YY�#i�#tt##***f *f * Fi,OW PROCESS FROM NODE 5D06.20 Tp NODE 5006.30 �S C�DE = 5 UPSTREAM I30DE 50D6.30 ELEVATION = 248.86 {FLOW IS SUPERCRITICAL) --------------------------------------------------------�----------------------- CALCUI.,A'i'E JUNCTION LQ$SE$ : PIPE FLOW DIAMETER A?�IGLE FLOVTL�NE CRITICAL VELOCI3'Y {CFS} (INCHES) {DEGR.EES) ELEVATION DEPTH(FT.� (FT/SEC} UPST�tE.�M 14.30 18.D0 D.DO 248.86 1.39 18.416 DOWi�iSTREA3-S 14 . 30 24 . d0 -- 246 . 36 1. 35 17. 652 . LATERAL #1 0.00 0.40 O.DO 0.00 O.OQ 0.000 LATERAL #2 0.40 0.40 O.QO 0.00 0.00 0.000 Q5 0.40��=Q5 E¢URI.S BASIN INPiJ'i'=== LACFCD A�ID OCEidA FLOW JUNCTION FOR2�UL.�E USED: DY={Q2*V2-41*V1*C05(DELTAla-Q3*V3*C05(DELTA3J- Q4`V9*COS(DF.L,TA4)j/{;��+A2)*i5.1)+FRICTIDN L055E5 UPSTREA�S: MANIdTNG'S N= 0.�2040; FRIC'FION $LOPE = 0.24824 AOWNS'FREAM: 2�P.NI3ING'S N= 4.01300; FRICTION SLOPE = 0.49821 AVERAGEb FRICTIbN Si�OPE IN ,TCTNCTiON ASSUMED AS 4.17323 JUNCTION LENGTH = 4.4Q FBET FRICTIO�I %,OSSES = 0.693 FEET ENTRANCE L05SES = D.d00 FEET 3UI3CTION T,p$SES = {DY+HV7.-i-i�T2j+{�I3�'RANCE L055ES1 JUNCTION LOS5E5 ={ p,9gZ}+{ 0.0001 = 0.992 , ----------------------------------------------------------_-------------__-__--_ I30DE 5406.30 : HGL =< 249.539>;EGL= < 254.805�;FLOWLINE= < 248.860> ♦iF} Y� iF Yr friY��lrYiYr*i*t*1 Y i!i Y#t1R Y**i **YriYc f*�k *#! Y*YiYyr4W*Yi ***YriFYr** iF*YriYiF Ir*M ki fYrkYrfl** FLOW PROCESS FROM NOi3E 50D6.34 TO NODE 5�06.40 IS CODE = 1 UP5'I'REAM NODE 5dD6.40 EL�IATTON = 268.74 {FLOW I5 SUPERCRITICAL) CAF�CLTL�ATE FftiCTION LOSSES {LACFCD} ; PIPE FLOW = i4.30 CFS PIPE DiAMETER = 18.00 INCHES PIPE LFNGTH = 69.23 FEB'i MF.NI3Ii�IG'S N - 0.0200D ------------------------------------------------------------------------------- IJORM.�i DEPTH (FT) = D. 65 CR3TICAL DEPZ'H (FT} - 1_ 39 UPSTREAM CONTROL ASSLiMED FLOWDEPTHIFT) = 1.39 � �� R� �� ----_-------------------------------------------------_-------------------------__ --------------------------�__--_--___-____------------------------------------- GRADUALLY VARIED FLOW PROFI�,E CQ2+4PU�'ED INFOFtrSAT10N: • � DISiANCE F'ROM FiOW DEP'€`H VELOCITY SPECIFIC PRESSiIRE+ CONTROL{F"r} {FT) {FT/SECa ENERGY[FT] MpMENiLJM(POUNDS} q.D00 1.389 8.364 2.477 302.62 0.010 1.360 8.491 2.480 3p2.86 O.D39 1.334 8.629 2.487 303.63 0.088 1.301 8.7B3 2.499 3D4.B8 0.159 1.271 8.953 2.517 3D5.63 4.253 3..242 9.140 2.540 3d8.9D 0.373 1.2�2 9.344 2.569 311.71 0.521 �.183 9.566 2.604 315.09 0.702 1.153 9.808 2.b48 319.06 0.4i9 1.123 10.069 2.599 323.66 1.Z79 1.D94 10.353 2.759 328.9A 1.489 �.064 10.66� 2.830 334.95 1.B56 1.035 10.993 2.912 34i.73 2.292 i.005 13.353 3.008 349.37 2.8iD 0.976 13.744 3.219 357.93 3.429 0.946 12.1fi9 3.247 367.50 4.174 0.917 12.631 3.396 378.16 5.076 O.B87 13.134 3.568 39Q.08 6.3.83 Q.858 13.683 3.767 403.33 7.56g 0.828 14.283 3.998 418.09 9.327 0.799 14.942 4.268 434.55 11.652 0.769 15.666 4.583 452.90 14.880 0.7k0 1b.465 4.952 473.40 19.777 0.730 17.349 5.387 A95.3S 28.806 0.681 18.331 5.902 522.10 69.230 0.679 28.414 5.945 524.18 -----.._____,...---..________..__.._____.._________.._____..--------------------------- NODE 5006.40 : HGL =< 270.129>;EGL= � 271.217>;FLQWL�NE= < 268.74fl> . ++��*..*�***..*.....*......�.�+..*...*.*...*..�,.*.*.****�*..�.+�**�*�.*.**�.. FLOW PROCESS FROM NODE 5006.4Q TO I30DE 5005.40 zS COAE = 8 UPSTREAM NODE 5005.44 ELEVATION = 266.74 (FLOW TS AT CRITICAL DEPTH) ------------------------------------------------------------------------------ CAI,CULATE CATCH BASIN ENTRA.I�CE LOSSES {LACFCD) : PIPE FLOW = 14.30 CF5 P�PE D7AMETER = 18.00 INCHES FI,OW VEL4CITY = 8.37 FEET/SEC. VEY,OCITY HEP.D = 1.088 FEET CATCH BASIN F..NERGY i�SS =.2*(VELOCITX HEAD} -.2*( 1.088) = 0.218 NODE 5D46.44 : HGL =� 271.435>;EGL= < 271.435�;FLOSVIsIT�iE= < 268.79Q> .*�..*y.,�.**�,�....,...+.*+,+*..�*++�,.f**++..+.**..*,.***x«.........**.**...*.,.*** iJPSTREAM PIPE FLOW CONTRQi DATA: NODE I3UMBER = 5006.40 FTIOWLINE Ei,EVAT20DI = 2fi8.74 A55UMED UPSTREAM CONTROL HGL = 274.13 FOR DOWNSTREAi�I RUN ANAI,Y5I5 END OF GRAbUALLY VARIED FLOW ANAi,YSIS • � �*f�w�+t*it++*+�*�+++xx***xs*�*x*s+*�s*x*+*�tst��***a*****r+****++x�*�x*�yx*+* PI'PE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, ANU OCEMA HYDRAULTCS CRTTERION) fc) Copyzight 1982-2002 Advanced �ngzneering Software (aesl Ver. 8.4 Release Date: O1/01/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN COI3ST7LTANTS 701 'B' STRE�T, SUI7'E $00 SAN AIEGO, CA 921D1 619-235-6471 +*+*�**'*"''****'*"�*y*'`*•' DESCRIPT�ON OF STUDY 's�***�rw**+wt�*r,r*++�*�** * BRESSI RANCH - ULTIMATE CONDITIONS � * SYSi'EM 5a0a - LATERAL 8(N0. 7 PER SHEET 13 OP AWG 400-8C) * * 10a-YEAR * **+****+*++.�*+�.�.+.�+*+,,.*.*.�*.*�***�.,,***«�******.**+.*�*+***+�*****�** FILE NAi�]E: 5DD0-B.DAT TIME/DATE OF STUDY: 11:39 O1/17/2403 ttt**++t*t*+t****y*y*�tirtrtrttirts***irt**r***i�tti*rr�y.+,r****�**+�**s+wxxx**��*i.+++ GRADI,TALLY VARTED FLQW ANALYS�S FOR PIPE SYSTk�I NODAL POiNT STATETS 'i'AHLE fNate: "*" indica�es nodal poi.n� da�a used.} UPSTREAM RUN DOWNSTAEAM RUN iJODE MODEL PRE55URE PRESSURE+ FLOW PRESSURE+ NCTMBER PROC ESS HEP.D { FT J MOMENTUM ( POLTNDS ) DEPTH { F"i' } MOMEN'iUM { pOiINDS } :" 5006.5Q- 4.77* 31.93 0.53 29.30 ) FRICTION 5005.6Q- 0.68� 29.57 0.6Q Dc 26.68 ) CA3'CH BASIN 500b.6a- 0.87* 18.45 a.60 Dc 10.28 MAXXMU�7 NUM�ER 4F ENERGY BALANCES iiSED YN EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEADY FLQW HYDRAULIC HEAD-LOSS COMP[FI'ATIONS BASED ON THE MOST CONSERVATIVE FdRMULI�E FROM TI3E CURRENT LACRD,LACFCD, AND OCEMA DESIGIV MANTJAi�S . **+**t�+***t***+**r+*tii*+iyy*w*�****��****��**rt�r*r+*r�r+i�*+t+t�i.+*+ti++*ra♦ DOWNSTRF�it4 PIPE FLOW COAi'I'R0� DATA: NODE NUMBER = 5006.50 FLOWLIfTE ELEVATIpN = 2A8_50 PIPE FLOW = 2.50 CFS PIPE DTAMETEFt = 1B.00 INCHES A55UMED DOWNSTREAM CON'I'ROL HGL = 249.270 FEET ------------------------------------------------------------------------------ NQDE 5d06.50 : HGL =� 249.270>;EGL= < 249.3B6>;F'LOWLINE= < 248.5D0> k iF *?#}yr�r }*�. }# y' � yr y� � y k**�k#�Jr*4 *# � �r * �r****** *Yr ** **#t�riY Y �c # Yr * Y i YY�i�YYrYf Y! Y i*Yr*Yi t** ir • FLOW PROCESS FROM NODE 5006.50 TO NODE 50�6_60 IS CQDE = 1 UPSTREAM NODE 5006.60 ELEVATION = 248.56 fFLOW IS SUBCRIT�CALj CAI,CiJLATE FRICTTON LOSSESiI1ACFCD} : PIPE �'LOW = 2.50 CFS PIPE DIAMETER = 18.00 INCHES PIFE LENGTH = 6.25 FEET i+fANNING'S N= 0.01300 NQRMAL DEPTH ( FT} - 0. 50 CFtI`F�CAL DEPTH ( F'I'} - 0_ 60 ---------------------------------------------------------------------------__-- DOWNSTREAM CON'!'ROL ASSUMED FLOWDEPTH(FT) = 0.77 • ------ —_________________________________________________________ � -_GRADUALLY VARIED FLOW PROFILE CbMPUTED INFORMATXpN: DISTANCE FROM FLOW �EPTH VELOCITY SPECIFIC PRESSUREt CONTROL ( F'I' } ( FT i { FT / SEC ) ENERGY ( FT ) M4MEN'PUM ( POUNDS ) 0.000 0.770 2.736 0.886 31.93 D.559 0.763 2.767 0.882 3i.69 1.111 0.756 2.799 0.878 31.46 1.654 0.749 2.831 Q.874 3Z.24 2.189 0.793 2.865 0.8'70 3i.03 2.714 0.736 2.899 O.BfiS 3fl.82 3.230 0.729 2.934 O.Bfi3 30.62 3.735 0.722 2.969 4.B59 34.44 4.229 0.715 3.046 0.856 34.2b 4.711 0.708 3.044 0.852 3fl.0$ 5.184 0.707. 3.082 a.849 29.92 5.635 0.695 3.122 0.846 29.77 6.075 0.688 3.162 0.843 29.63 6.250 0.685 3.179 0.842 29.57 ------------------------------------------------------------------------------ NODE 5006.50 :�fGL =� 299.245>;EG�.= < 249.9Q2>;FLOWLINE= � 248.560> ++f*w�t,r,��*+fv.wxr�wv.rv.rv.+***+++�*��r++t+**+��*x�r****�rs***r+*��++***si.�*i*,re* FLOW PROCESS FROM NODE 5046_64 'PQ NODE 5006.6a I$ CODE = S UPSTREA� i30DE 5006.60 EI..EVATZON = 248.56 (FLOW IS SiJBCRITICAL) ----------------------------------------------------------___------------------- CALCULATE CA�'CH BASIN ENTRRNCE LOSSES(LACFCD}: PIPE FLOW = 2.50 CFS PIPE DIAMETER = 18.00 INCHES FisOW VELOCITY = 3.1$ FEET/SEC. VELOCITY HEAD = 0.157 FEET CATCH BASIN ENERGY L055 =.2*qVEI.,OCITY HEAD} _.2*( 0.157) = 0.03� ------------------------------------------------------------------------------ � NpBE 5006.6Q : HGL =< 249.433>;EGL= < 249.433>;FLOWLINE= < 248.560> ***.�*+*,r+++��**�+**+**++t..+****++r*f+�++��#*+�..+*+t*��.+.**��+�+***�***t+*+ UPS�'R.F..AM PIPE FI�OW CON'PROL DATA: NODE NUMBER = 5006.60 FiAWLINE ELEVATION = 248.56 ASSUMED UPSTRFAi�f CONTROL HGi, = 249.16 FdR DOWNSTFZEAM RUN ANALYSIS ----------------------------------------------------------------------------_-- ------------------------------------------------------------------------------ EI3D OF GRADl3ALLY VARIED FLpW AbiALY5I5 *## # Y �.#*f i++* �} �i f Y! * * �#####**Yi il Yrfi i # *i Yt# i ti ****+**rt f 1f*�kr * �kt}}}i#f# * *Yr***Mi�*'1"t PIPE-FLOW HXDRAULICS COMPUP�R PROGAAM PACKAGE (Ref�rence: LACFCD,I.,ACRD, ANB OCF�N3A HYI7AAULTCS CRITER�Ofij (c} Copyright 1982-20Q2 Advanced Engineering So£tware {aes) Ver. 8.0 Release Date: 0}./O1/2002 License ID 1509 Analysis prepared by: PROJECi` DESFGN CONSUI,'i'AN'I'S 703 '�' S'FREET, SUETE $DO SAN DT�GO, CA 92101 619-235-6471 ***+*****'`****'`*********** DESCRIPTION OF STUDY **+*++��++r:r*:r**r�rrt*ff*� * BRESSI Rz1NCH - ULTIMA'T'E CONDITIONS * * SYSTEM 50DD - LA�'EItAL 8(hIO. 7 PER SHBE`F 13 OF DWG 40Q-8C) * * 100-YEAR * ***��*�*...+t,,..,*�**�....t***r,.��*.*�**.*.**....>,.,,...*«..�.*.w.*****��+ � FILE NAME: 5D04-8.DAT ti � '��w+xw*��rrr*�:+xrt*wfrt+rxi.wwxrrrrrr*+r*��yrr*+W*v.��f*+s**w***xxx+�krt�r*r*+**rx+ PTPE-FLOW HYDRAULICS COMPUTER PROGRAN4 PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRA[.TLICS CRZTERIOPIj (c1 Copyright 1962-2001 Advanced Engineering Softwara (aes] Ver. 8.4 Release Date: Q1/O1/2001 License �D 1509 Ana�ysis prepared by: PROJECTDESIGN CONSULTA�]'I'S 7Q1 'B' STREET, SUITE BDO SAN DiEGQ, CA 92101 6Z9-234-0349 *.«�.�**�..:..+**«.++..+*+* DESCRIPTION DF STUDY ++.*..*..*...�..f.+.**�**. " BRESSI �NCH - ULT�MA'i`E COi3D�TI0NS * ' SYSTEM 5000 - LATERAL 9(NO. 8 PER SHEET 13 OF bWG 40a-SC) * * i00-YEAR * x*,rx+x**�++**+�**��*w�+a**x�*w*�x*ex**+x*xxw�*w*****+xi.w**++*xt*+*++*,rx+** FI�E NAME: 5000-9.DAT 'FII�/DATE OF S�'LTDY: 13:44 09/08/2002 ♦�k*i YY 1�1! }+*Yrf #*i�#Y** W 4*�FY*Y�Y f Y Yf ** i# i�f # t�k f t Y f Y� i4Y* iFikty.� f+#{}itW�t+i* **1 �Y�*t � Y GRADiJALLY VARIED FLOW ANALY5I5 FOR PIPE SYST�hI NODAL POTNT STA'I'CTS TRBLE {Note: ""'• indicates nodal point data used.J UPSTREAM RUN DOWNSTREAr3 RUN NODE MODEL PRESSLTRE PRESSi3RE+ FLOW PRESSURE+ NUMBER PROCESS H�AD (�I' } MpMEN'PCJM ( POUNDS ) DEPTH ( FT i I�iOMENTI3M ( POCTNDS ) � 5007.50- 1.38 Dc 268.86 0.87* 349.12 } FRICTION 5007.60- 1.36*Dc 268.86 1.38*Dc 268.66 MA.XIMUM NLJMBEI2 OF ENERGY HALANCES USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEADY FT�UW �IYDRALTLIC HEAD-LOSS COMPUTATIONS BASED ON THE M05T CONSERVATTVE FORMLTL�AE FROM THE CURRENT LACRD,LAC�'CD, AND OCEMA DESIGN MAidI1AL5. **.****.*...�.+**�**.�,-...**.*.«.x..�**.....*««..****�***+****�*+++*.�**.**.** bOW�IS'i`FtEAM PIPE FLOW CONTROL DATA: NODE NUMBER = 5007.5U FLOWLINE £E�EVATION = 261_15 PIPE Fi,OW = 14.74 CFS PZPE pIAME'I'ER = 24.00 �I3CHES ASSUMEb DOwNSTAEAM CONTROL HGL = 261.740 FEE'F *NOTE: A55UMED DOWNSTR£.AM CONTROE� DEPTH{ Q.58 FT.} IS LESS THAN CRIT�CAL AEPTHI 1.38 FT.} ___> CRiTTCAL DEPTH IS ASSiIMED AS DOWNS'I'REAM CdNTROi DEPTH FOR UPSTRF.AM FtUEd ANAI,YSIS ------------------------------------------------------------------------------ NQDE 5047.54 : HG� = a 262.D30>;EGL= < 263.980>;FLOWLINE= � 261.160> :x**xww+*r***+*rx*f*w***r*te**tt+**+t+*+*xxt***wti**t*rrr�r+art*.ir*+►txx*x+*�+r♦ F�.OW PROCESS FROM I30DE 5047.5� TQ NODE 5007.60 IS CODE = 1 UPSTREAM I30i?E 50D7.60 ELEVATIOI+t = 262.fi8 {FLOW I5 SUPERCRITICAL) CPZCUL�ATE F'RICTION LOSSES (LACFCDI : . - PIPE FLOW = ]4.70 CFS PIPE DI�NiETER = 24.00 INCHES PIPE LENGTH = 36.48 FEET i+iPNNING'S N= D.01300 ?�TORMAL DEPTH(FT) = 0.76 CRTTICAL �EPTH(FT) = 1.38 ....---------------------------------------------------------------------------- ------------------------------------------------------------------------------ � � � UPSTREAbi CO3Q'i'ROL ASSUMED FLOWDEPTH(FT) _ �.36 GRADUALLY VARIED FiOW PROFILE CdiIPUTED INFORMATIDN: __----------------------------------------------------------------------------- DISTANCE FROM P7�OW DEPTH VELOCIiY SPECIFIC PRESSURE+ CON'T'ROL ( FT } ( FT ) ( FT/ 5EC ) EiJERGY ( F'i' j MO�ITUM ( POLTNDS ) O.DDO 1.382 6.348 2.048 268.$6 0.024 1.357 6.474 2.009 26B.99 Q.101 1.333 6.606 2.011 269.36 0.235 1.3�9 6.746 2.016 27D.00 D.434 1.285 6.892 2.023 270.9J. a.�aa 1.26D 7.D46 2.032 272.11 �.055 1.236 7.249 2.044 273.62 1.497 1.212 7.3&0 2.056 275.45 2.043 1.168 7.5b0 2.076 277.61 2.707 1.163 7.750 2.097 280.13 3.506 J..134 7.951 2.121 283.a2 4.4fi2 1.115 8.163 2.150 286.31 5.601 1.091 8.38$ 2.184 290.Q3 fi.957 1.066 8.626 2.223 . 294.20 8.570 1.042 8.878 2.267 298.85 10.445 1.016 9.346 2.3i6 304.41 �2.604 D.994 9.431 2.376 309.72 15.592 4.969 9.734 2.442 316.a3 i8.996 0.945 1D.056 2.516 322.98 23.215 0.921 10.404 2.602 330.61 28.552 0.897 10.768 2.698 339.40 35.555 D.873 11.i62 2.808 348.19 35.480 0.870 11.201 2.820 349.12 ------------------------------------------------------------------------------ �iODE 5407.60 : HGI� _< 264.062>;EGL= < 264.688�;FiOWLINE= < 262.5$0> ♦*t*wt**xt***xyrtrt�*+�*�rk****xrr++tr+t*:+ta*rtr*xrt*�*wr�#��w+*+***+�*****�tw�k�+ UP5'i'REAM PfPE FLOW CONTROL DATA: NODE NiTMBER = 5407.6p FL,OwLiI3E ELEVATION = 262.68 A55UMED i3P57'REAM CON'PROL HGL = 264.05 FOR DOWNSTREAM RUN ANALYSIS EN9 OF Gi2Ab1,3ALLY VARIED FLOW ANAi,YSIS � L_J I� t*w**x***xx*r*wx*�x+*w*s*r�tiwrr*x*x*tx*rrt��r+rw+**�*��x�*x**+w**+w**++******ax PTPE-FLOW HYDRAi7LIC5 COMPUTER PROGRAA? PACKAGE [Reference: L7aCFC�?,LACAD, AND OCEMA HYDRAIFLICS CRITER�ON) (c] Copyright 1982-2001 Advanced Engineering Software ;aes1 Ver. 8.0 Release Date: O1/41/2D01 License ID 1509 Analysis prepared by: �ROJECTDESIGN CQNSULTANTS 7p% 'B' STREET, SUITE 804 SAS+1 DIEGO, CA 921D1 619-234-4349 *rt,�.*.....****.*�..�.�.,**x DBSCRIPTION OF STUDY *..k*......**�v.+*#��,.+.�r++ � BRESSI RANCH - ULTTMATE CONDTTTONS * * SYSTEM 5000 - LATER.AL 10 {NO. 5 O?�I SHEET 12 OF 37wG ADO-8C) * * 100-YEAR + w,.,�**+x+.,***.***«..***..,*x.**+**�**+�.***.*.�.***.***+xt*.*****t+*«***+.** FILE 3dAME: 500tl-�O.DAT T'TME/bATE OF STUDY: 14:03 09/08/2002 �**.k*.,..:.«**..�*t.**.*+.*.**+*+*„**+�..:+:**:.*t..*,�r,.�*,.f,.++.t�+,��..+Y.>..�� GRAili3ALLY VARIED �'LOW ANA�XSIS FOR PIPE SYSTEM NpDAL PpTNT STATUS TABLE (Note: "'" indicates nodal point data usec3.} [3PSTREA�i Ri}N DOWNSTREAM RUI3 NODE MQD�L, PRESSURE PRE$SURE+ FLOW PRESS[JRE+ � NUMBER PROCESS HEAD ( FT? MODfEN�UM ( POU21D5} DEPTH ( FT ) MOMENT[7t+� { POUNDS} : 54Q9.14- 0.5fi 20.38 0.42* 21.58 } FRICTION 5409_20- 0.52*Dc 20.18 0.52*Dc 20.�8 } CA'�`CH BASIN 5409.20- 0.75* 10.74 0.52 Dc 7.30 MP.XIMUM NUMBER OF ENERGY HAL.�NCES USED I?d EACH PRqFILE = 25 NpTE: STEAAX FLOW HYDRAULIC HEAD-LOSS COMP[7TATIONS SASED ON THE MQST COAISERVA'i`TSIE FORMC3I,AE FROM THE CURR�T LACRb, i�ACFCD, AND OCEMA DESIGN MA,NUALS. �,r****x******x�***r*+*:+*+******++**ax*x+rx*rx***t�+**r*xsw*xx��r*y**t***twx:+:** DOWNS'PREAI�4 PTPE FLQW CONTROL DATA: NODE N�3MBER = 5009.1D FLOWf,INE ELEVATION = 297.04 PIPE FLpW = 1.90 CFS PIPE pIAt�SETER = 16.00 TNCHES ASSUMED DOWNS'iREAi�i CON'I`ROL HGL = 297.600 FEET ------------------------------------------------------------------------------ SdODE 5009.7.� : HGL =< 297_462>;EGL= < 297.799>;F'LOWLINE= < 297.044> +trxx**+r+*wrttyr*r****rWaw**rr*t+rtsxr**s+t*s+*rr�ti�W+*++��x,rw+,r*w�+tat+�++:f+r FLOW PROCE55 FROM NODE 5009.10 TO �IODE 5009.2b I5 CODE = 1 UPSTREAM NODE 5009.20 FGEVATION = 297,28 {FLOW IS Si3PERCR2T1CALf CAiCUI�ATE FftICTION LQSSES {�,pCFCD} : PIPE FiOW = 1.90 CF5 PIPE DIANfETER = 18.00 �NCHES PIPE LENG�'}i = 2�.25 FEET MANNING'S N= 0.01300 I30RMF.i DEPTH(FT} = 4.41 CRI'PICAL �EPTH(FT) = 0.52 --_....___----------------------------------------------------------------------- ------------------------------------------------------------------------------- UPSTREAM CONTROL ASSUMEi1 FLOWDEPTH(�'T} = 0.52 � . _-GR�LsUALLY VARIED FLOW PROFILE COMPiT'i'EB INFORMATION: --------------------------------------------------------------------------- DI5'FANCE FROi+F �LClW DEPTH VELOCI'I`Y SPECIF�C PRESSURE+ CONTROL [ FT ) { FT } ( FT / SEC ) ENERGY ( FT } MOM£i�!'UM I POLRQDS ) 'D.000 4.519 3.499 0.7D9 20.18 D.D10 4.515 3.538 0.709 2fl.19 D.041 4.511 3.578 0.710 20.19 D.094 0.507 .3.619 0.710 20.20 �.173 D.502 3.6fi1 0.71D 20.22 Q.279 0.448 3.703 0.711 20.24 Q.416 4.494 3.747 0.712 2p.27 0.587 D.490 3.791 0.713 20.30 D..795 0.465 3.837 0.7i4 20.33 1.046 �.461 3.883 0.715 20.3B 1.346 Q.477 3.931 D.717 20.42 1.7QD 0.473 3.979 D.7i9 20.47 2.118 �.468 4.029 0.721 20.53 2.610 0.464 4.080 0.723 2D.6D 3.188 fl.460 4.132 0.725 20.67 • 3.659 0.456 4.185 D.728 20.74 9.676 0.k52 4.239 0.737. 20.82 5.638 0.447 4.295 "0.734 20.91 6.798 , fl.443 4.352 0.737 21.00 6.2�6 4.439 4.410 0.741 21.10 9.987 0.435 4.470 D.745 21.21 12.271 0.430 4.531 0.749 21.33 15.356 0.426 4.594 0.754 21.45 19.942 �.422 4.658 0.759 21.56 20.250 0.422 4.650 D.759 21.56 ------------------------------------------------------------------------------ . NODE 50D9.20 : HGL =< 297.799>:EGL= < 247.989�:FLUWL�NE= < 297.280> :****rw*f*trrtrv.+*�+�*+rrwrttt*+�***itt****twtr�r*****�rrfr�r*r�*r�ti�r�t*+r*�*y*+rt FLOW PROCESS FROM NODE 5Q09.20 TO NODE 50D9.20 IS CODE = 8� LiPSTREA�i NODE 5009.20 ELEVATION = 297.28 (FI�OW IS AT CRITICAI, DEP'FH} CAL�CUIjATE CATCH BASIN ENTRANCE LOSSES (L�ICFCD) : PIPE F�,OW = 1.9� CFS P�PE i3IP.METE�t = 16.OD INCHES FLOW VELOCITX = 3.50 FE�I'/SEC. vELOCITY HEAD = O.J.90 FEET CA'i'CH BASIN �NEFtGY L05S =.2* (VEi.,OCITY HEAI)} -.2* ( 0. 190) = 0.038 ------------------------------------------------------------------------------ idODE 5ao9.zo : xc� _� z9s.o2�>:�G�= � 29s.o27>;FLowz,z�= < 297.zso> .**�*****�**.*.**�*****..�***..**�,.,.*..*«...�.**..*****+****�.t*+t�.��.*,.**...� UPSTREAM P�PE FLOW CONi'ROi� DATA: NQDE NLFMBER = 5009.24 FLOWL�DiE EF�EVATION = 297.28 A5ST3MED UPSTkEP.M CONTROi� HGL = 297.80 FOR DOWNSTREAP'F RLTN ANALYSIS ------------------------------------------------------------------------------ ------------------------------------------------------------------------------- END OF GRADUALLY VARIED FLOW ANALYSIS C J � ♦ * < * x * � } # * rt f * � * k w f w * * f * � * * M Y * ► } * i * R f * k * � * k � k * * 1 f k � * * rt k � k # * * k k * * � * * t k * w Y * * � W 4 k t PIPE-FL6W HYDRAULTCS COMPU'iER PROGRAM PACKAGE (Reference: LACFCD,LACAD, A1VA OCEMA HYDRAULICS CRFTERION} (c1 Copyrigizt 3982-2001 Advancec� Engineezing Software faes} Ver. B.0 Release Date: O1/01/2a01 License ID 1509 Analysis preparEd by:. PROJECTDESIGN CONSULTAI3T5 70� 'S' STREET, SUITE 804 SAN �IEGO, CA 92301 519-234-0344 +i*+*t+r*r+i+*rr+w*r*�+:w• DESCRIPTION �F S'��Y °*****++w,rx++**ws,r:****r+x * SRESSI RAI3CH - LFLTIMATE CdNDIT�ONS * * SYSTEM 540D -- I.ATERAi, 11 {N0. fi ON SHEET 12 OF DWG. 444-BC) * ` 100-YEAR * rx**a��r�,ryrtsxrt*stix*wx+sw*+wwr��ar:x*yxtt*yws**yx**rr��rr*ti.r.�fr.*t�:rrrr FiLE NAME: SDOd-11.DAT TIME/DATE OF STUDY: 14:01 09/08/2042 �*++�t*�kw+�k**+*wxx*f+++*��v.+�+t++*w+��rr�y��++*t++*+*xewxx*,r**+r*+**,r**x**xi�*� GRADUALLY VARIED F�,OW ADiALYSIS FOR PIPE SY$TEM AiODAL POINT STATUS 'iABLE {I3ote: '*" indicates nodal ppint data used.i UPSTREAi�S RUN DOWNSTREAM RUN NODE i�10DEL PRESSURE PRESSUAE+ FLOW P�iE55iJRE+ N[7MBER PROCESS HEAD { FT } MOMF.NTUM I POU23DS ) DEPTH ( F'I') MOMENTUM ( POUNDS } 5009.50- 0.56 13.39 0.18* 23.15 � } FRICTION 5409.60- 0.41*Dc 11.25 0.4i'Dc 11.25 } CATCH BASIN 5009_60- - U.59* 5.96 0.43. Ac 4.11 ------------------------------------------------------------------------------ MA.XIMUM NUMBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 NOTE: STEADY FLOW HYDRALFLIC HEAD-LOSS COMPUTATTONS HP.SED ON 'I`HE MOSi' CONSERVA?'IVE FORi�IULAE FROM THE CURRENT LACAD,LACFCD, AND OCEMA b� S I GN S�SP.DiLTAI,S . Y�l�YrYfti nY*+�tf�Fi*t t+�t vt1 i� f tti� �/it��t ik *i*ik! 1*t �4Y*� Wwi f�Ftif Y�1 i�*Yr iF�Yrk Y� iF iFYrk iFYriYk kY�Rf* i#i4 1�OWNS'I'REAM PIPE FLOW CONTROL DATA: NODE NT3MBER = 5D49.50 FLOwLINE ELEVATION = 297.04 PIPE FLOW = 1.2D CFS PIPE DFAME7'EI2 = i8.04 INCH�S ASSUM.��'.A DOWNS'FREAM CONTROi� HGE� = 297.60D FEET NODE 5bD9.50 : HGL =� 297.223>;EGL= � 29&.689>;FLOWi�I�IE= < 297.040� Yr}y ##*�Fi�# *k �r**RlYrYr fYriFYr*tkY� klryr� 1rf*fY� iF*iF%� *Yr**YrirYr*k**Yr*yrt t* 1 f**t # fYrtf�k*Y * tttk** ***♦ FLOW PRDCESS FROM NQDE 5049.50 TO NObE 5009.60 IS CODE = 1 UPSTREF�F NODE 5009.60 ELEVATION = 296.60 IFF,Ow IS SUPERCRITICAi,} ----------------------------------------------------------------_-------------- CP.�,CLTL,.�TE FR�CT�ON LOSSES (LACFCD) : PIPE FLpW = 1.20 CFS PIP£ DIAMETER = 18.40 INCH�S PiPE LENGTN = 6. 25 FEET t�3ADTNTNG' S N = 0.0130D NORMAL DEPTH(FT) = 0.16 CRITICAL DEPTH(FT} = 0.41 _w-�« =r=====__�==_��________________________________________________________ UPSTREAid CONTRQL ASSUMED Fi�OWDEPTH { FT} = 0. 4J. ------------------------------------------------------------------------------ ------------------------------------------- -----_____--_-__..____-_____..___--- . . __GRADUALLX VARIED FLdW PROFILE COMPU'FED INFORMATION: DISTA�ICE FROM FLOW DEPTH VELOCITY SPECIFTC PR�SSURE+ CONTROL(FT) {FT) (FT/SEC} ENERGY(FT) MOMENTiT2+f(POUNDSJ 0.000 4.4�0 3.068 0.556 11.25 O.DQ2 0.399 3.178 0.556 1�.2b O.OQ9 Q.389 3.294 0.558 11.29 0.020 4.379 3.419 0.5b1 11.36 D.038 4.359 3.551 D.5b5 11.45 0.052 4.359 3_b94 0.571 1Z.57 0.095 �.349 3.846 0.579 11.73 0.136 0.339 4.010 D.589 11.9i �.188 4.329 4.187 0.6Q1 12.1C 0.2�2 0.3i8 4.378 0.616 12.41 0.331 0.308 4.584 �.635 12.72 0.428 Q.298 4.808 0.657 13.06 0.546 0.288 5.452 0.685 13.49 0.689 0.278 5.317 0.717 13.96 0.655 D_268 5.fi08 0.757 14.5D 1.079 0.258 5.928 0.804 15.11 , 1.342 0.248 6.281 0.861 15.81 1.670 D.238 6.fi7J, 0.929 16.60 2.081 0.227 �7.i05 1.012 17.50 2.607 0.217 7.590 1.112 18.52 3.294 0.2�7 8.134 1.235 19.64 4.222 0.197 8.749 1.385 21.03 5.541 0.187 9.447 1.574 22.56 6.250 0.183 9.712 1.649 23.16 ------------------------------------------------------------------------------- IdODE 50D9.64 : HGL =< 299.010>;EGL= < 299.156>;�'LOwI,INE= < 298.600> •• +**+*wy+rs�**�a*�*rsti*r**x**++x*ttt++nrx**a++*+�t*+xt**tit+*a*t*f**tt**++t+*+**+ FLOW PROCESS FROM 230DE 50D9.60 TO NODE 5009.60 i5 CODE = 8 iJPSTREAM I30DE 5009.b0 ELEVATION = 298.60 (�'LOW IS AT CR�TiCAL DEPTH). ------------------------------------------------------------------------------ CALCULATE CATCH BAS�N ENTRP.NCE LOSSES(LACFCD): P�PE PLOW = 1.20 CFS PIPE DIAMETER = 18.Op INCHES PL4W VE�,CICT�'Y = 3.07 FEE'i'/SEC. VELOCITY HEAD = 0.146 FEET CATCH BASIN ENERGY LO55 =.2*(VELOCZTY HEAD) _.2*( 0.146) = O.D29 NODE 5009.b0 : HGL =� 299.i85>;EGi= � 299.185>;FLOwLINE= < 248.6d0> tlrtkYrlr Yr Y� Y�1r* YrYrY� ***YrYr** *i �Jr*YrYr�lr*k*iFYr1r *i�Yr iFY **�k * 1r iFY� Yr f Yr *�RiFR R Yr YrYrYr *k �k*Yrk f*� 1rYYr f YrYr �YY�*Y�lr *k UPSTREAt+i P�PE FLOW CQNTROL DATA: IdODE NUMBER = 5009.50 FIAWL�NE E�,EVATIOI3 = 296.60 ASSUMED UPSTREAM CONTRO�, HGL = 299.fl1 FOR DQWNSTRF..AM RUN ANALYSIS END dF GRADUALLY VARIED FLOW ANAI�Y5I5 . ***tff*tt#*#*i#**f1w*#***f**tt#�#*f#t#*ttttt*titk**t***fti****t*t##i4tYf#W*##* PTPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYI}RAL7LICS CRITERIONj � (ci Copyright 1982-2D01 Advanced Engineering 5oftware (aesj Ver. 8.0 Release Date: O1/O1/2QQ� License ID 1509 Analysis prepared by: PROJECTDESIGN CONSUL`i'AN�'S 701 'B' STREET, SUI'I'E SDO SAN DIEGO, CA 92i01 519-234-0349 . • v�*y�W>***r�y.,r�*****www*�r,r* DESCREPTIQN QF STLTDY ***++*t*+*fx*�,r******,�,�a,r* * BRESSI RANCH - TNTERTM CONDZTIONS '" * SYS�`E�7 5000 - LATERAL 12A (NO. 7& 8 OF SHEET 12 DWG. 400-SC) * * �04-YEAR * t**�**++*+*++**+++*++*++f*++t*+t***+*****+«****t*****«**+*++*t**+***+***+* FYLE NAME: 50Q-12AI.DAT �'IME/DATE pF STUDX: 16:05 11/07/2002 *,.*�*******,r***+******+***.,*,,,.,.«*�***�**********+****+****,r***********�****�r** GRADUAE�LY VARIED FL�OW ANALYSIS FOR PIPE SYSTEM NQDAL POIN''i' STATUS TABLE (Note: "*" indicates nodal paint data used.) UPSTREAM RUN DOWI3STRE.n.M RUN NODE N30DEE� PR�SSi7RE PRESSURE+ FLOW PRESSURE+ NUMBER PRpCESS H�P.D { FT } MOMENTUM { POLJAFDS i DEPTH ( FT } MOMEN'I'UM ( PpUNDS j 501Q.50- 5.Q5* 803.B1 0_55 54.12 } 5a10.60- } 501a.70- } 5aio.so- } 5010.80- FRICTION JL3�7CT I ON FRICTION CA'I'CH BASIN 4.23* 643.43 0.70 Dc 3.93* 583.48 } HYDRATJLIC JUMP 0.70*Dc 49.41 1.01* 0.40 0.70*Dc 49.41 '74.49 49.41 26.31 0.70 Dc 17.65 ------------------------------------------------------------------------------ M71XIM[FM �1[FMSER OF ENERGY BAL.n.t3CES USED FN EACH PROFi�,E = 25 ------------------------------------------------------------------------------ NOTE: STE.�FJY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ONI THE MOST CONSERVATIVE FpRMULAE FROM THE CURREN'i` LACRD,LACFCD, AND OCF�+1A pESIGN MANiJALS . *****+****+v�*«**w*****�**�,r****************,r**,.w+**�+******�«************v��**+ DOWI�STREAM PIPE FLOW CONTROL DATA: r�onE rr�rrxaER = 5010 . 5o F�aw�rrrE ELEVATION � 310 .75 PIPE FLOW = 4.00 CFS PiPE AIAMETER = 24.00 IiJCHES ASSIJMED DOWNSTREAM COid'I'ROL HGL = 315.800 FEET ------------------------------------------------------------------------------ NODE 501Q.50 : HGL =< 315.SD0>;EGL= < 315.825>;FLOWLINE= < 310.750� ***,�*r**w*,rW*wx*wvrxv�**w,tvc,r,r***+,��t**ww*ww*+****w******a*r,rxw+�w*,twwwvr,r**y,******* FI,OW PROC�SS FROM NODE 5010.SD TO NODE 5010.6Q IS CODE = 1 UPSTREAM NODE 5010.60 ELEVATION = 313.59 {FLOW IS UNDER PRESSUR�} ------------------------------------------------------------------------------ CALCULATE FRICT�pN LOSSESILACFCD}; ' PIPE FLOW = 4.00 CFS PIPE DIAMETER = 24.00 I[dCHES PIpE LENGTH = 69 . 95 FEET N7AN'NING' S N = 0. 07.3 00 SF=(Q/K)**2 = ({ 4.00)/{ 226.320}}**2 - p.a0031 HF=L*SF = ( 59.951*f0.00a31) = 0.422 ------------------------------------------------------------------------------ NODE 5010.60 : HGL =< 315.822>;EGL= < 315.$47�;FLOWLIDTE= < 311.590> *****+**+******�**************�**,r�**+**r*,t***w�++t*�*+******��,r*******++++,r+f* FLOW PROCESS FROM NOD� 5D10.60 TO NODE 501Q.70 IS COD� = 5 i3PSTREAM NODE 501Q.74 EL�VATZON = 311.92 [�'LOW IS CTIJDER PRESSURE) ------------------------------------------------------------------------------ CALCi3L.�TE JUNCTIQN LpSSES : PIPE FLOW D�AME'I'ER ANGi.� Fi�OWLINE CRITICAL VELOCITY SCFS) (iNCHES) (DEGREES) ELEVATION DEPTH(FT.f (FT/SEC) � UPSTREAM 4.00 24.00 55`00 3�1.92 0.70 1.273 DOWNSTREAM 4.00 24.00 311.59 0.74 1.273 LATERAL �� D.04 0.00 O.QO 4.00 0.00 O.Ofl4 LATERAL #2 O.OQ 0.00 o.aa O.DD O.D4 O.ODO 45 0.04=-=Q5 EQUALS BASZN IAIPLI�'=== I�ACFCD AND QCEMA FLpW JUNCTIpN FORMUi�AE USED: DY= {Q2"��72-Q�. �Vl *C05 (DE.LTA�) -43 *V3 *COS (DELTA3) -- Q4*V4*COS(DEL'i'A4}J/({A1+A2j*1&.�)+FRICTION L055E5 UPSTREAM: MANNING'S N= 0.02400; FRICTIDN S�,OPE = O.QD107 17�WNSTRE.a,M: MANNZNG'S N= 0.01300; FRICTION SLOPE = 0.40031 AVERAGED FRICTTON SLOPE IN 3UI3CTION ASSUMED A5 a.aaa69 JUNCTION LENGTH = 4.00 FEET FRICTION LQSSES = 0.403 FEET EN'I'RANCE LQSSES = D.000 �'EET ,TUNCTIQN LOSSES = ( DY+HVl-HV2 ) + ( EN�fFi.FiNCE LOSSES ) JUNCT�ON LOSSES ={ 0.024?+( 0.000} = O.D24 NODE 5410.70 : HGI.� _< 315.$4b>,EGL= < 315.871>;FLOWLIN�= < 311.920� th Yrrt �lr �k Y� Yrf k* i* rt f Y� k 1rYrYrYrfrYrYrYr tM YrY� ltktk Yr YrYrYrk * k 17r#'k **yr ** **� *Yr**MYr YrtYrlrYrYr t 1rk *�ktkYrYrYrYr **** *** FLOW PROCESS FROM NODE 5410.70 TO NQDE 5014.80 IS CODE = 1 UPSTREAM NODE 5010.80 ELEVATION = 318.00 {FiyDRP,UI,IC JUMP OCCURS) ------------------------------------------------------------------------------ CALCULATE FRIC3'�ON LQSSES{LACFCD}; PIPE FLOW = 4.00 CPS PIPE DIAMETER = 24.00 INCHES PIPE i,ENGTH = 38.D4 FE�S' MANNING'S N= 0.0240fl IiYDRAUL�C JUMP: DOWNSTREAM RUN ANALYSIS RESULTS ------------------------------------------------------------------------------ • --NQFtMAL-DEP'I`H {g'�') -_------0�39-----------CAITICAL-DEP'I`H (FT} -=-A'---6'7D------- UPSTREAM CON`i'RpL ASSUMED FLOWDEPTH(FT) = 0.7Q ------------------------------------------------------------------------------ GRADUALLY VARIED FL�OW PROFILE COMPLTFED iNFOgMA'iION: ------------------------------------------------------------------------------ DISTANCE FRQM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTRO�, { FT ) { FT } ( F�' / SEC ? ENERGY { FT ) MOMF'N'€`UM ( POLTNDS ) O.DDd Q.701 4.a70 0.959 49.41 Q.003 0.689 4.172 0.959 49.44 a.013 0.676 4.279 p.967. 49.52 0.03D 0.664 4.390 0.963 49.66 0.056 0.651 4.507 0.967 49.86 0.091 4.638 4.630 0.971 5D.13 0.136 0.626 4.76a 0.978 5Q.46 0.194 0.613 4.695 0.9B5 50.86 0.265 0.601 5.038 0.995 51.34 0.351 0.588 5.189 1.006 51.89 fl.455 0.575 5.348 1.020 52.52 0.580 0.563 5.515 1.035 53.24 0.729 0.554 5.693 1.054 54.06 0.907 0.538 5.B81 1.075 54.97 Z.Z18 0.525 6.060 1.099 55.99 1.371 0.512 6.291 1.127 57.12 1.675 0.500 6.516 1.159 58.37 2.D42 0.487 6.755 1.196 59.75 2.490 0.475 7.�10 1.238 61.27 3.447 0.462 7.282 1.2$6 62.94 3.753 0.449 7.574 1.341 64.7B ,• 4.676 0.437 7.$86 1.403 66.80 � 5.9A8 0.424 8.222 1.475 69.01 7.857 0.412 8.584 1.556 71.44 11.339 4.399 8.974 1.550 74.11 38.00a 4.397 9.429 1.664 74.49 ------------------------------------------------------------------------------ HYDRAITL�C JC7MP: UPSTREIiM RUiQ ANALYSIS RESLTL�'S ------------------------------------------------------------------------------ ---------------------------------------------------------------------------__--_ DOWNSTREAM CONTROL ASSi]MED PRESSURE HEP.D(F'�') = 3.93 � `^PRESSUi�ETFLOWTPROFILE�COMPiTPED�INFORMATION-f_Y�_____________________________ DISTANCE FROI�i PRESSi3RE VELOCITY SPECIFIC PRESSURE+ CONTROL { FT ) HEAD ( FT } ( F'i`/ SEC 1 ENERGY { FT ] MOMENTUNi { pOCJNDS } 4.a00 3.926 1.273 3.951 583.46 �2.119 2.OD0 1.273 2.425 � 2a5.90 • ------------------------------------------------------------------------------ ----------------------------------------------------------------�..__W__--------- ASSUMED DpWNSTREAkI PRESS(7RE HEP.D {F'x'} = 2. DO -----------------------------------------,------------------------------------- GRADUALLY VARIED FLOW PROFILE COMPiPPED INFORMATION: DISTANCE F130M FLOW DEPTH VEI,OCITX SPECIFIC PRESSURE+ C ONTROL ( FT ] ( FT } { FT / SEC ) ENERGY ( F�' ) MOMENPUM ( POU�3TJ5 ) 12.119 2.000 1.273 2.025 205.90 �2.443 1.948 � 1.282 1.9'74 195.62 12.766 1.696 1.299 1.922 1&5.90 13.086 1.844 1.32d , 1.871 �.76.17 13.406 7..792 1.3A7 1.82� i66.65 �3�.724 1.740 1.378 ]..770 �57.3B 14.642 1.66B 1.413 1.7Z9 �48.36 14.357 1.636 1.453 1.659 �39.62 14.671 1.5B4 1.498 1.619 131.19 14.983 1.532 1.598 1.570 123.D6 15.293 1.481 1.604 1.521 Z15.26 15.601 1.429 1.665 1.472 3.p7.81 15.906 1.377 1.73� 1.A23 104.71 16.207 1.325 1.81}. 7..376 93.99 16.5D5 1.273 1.896 1.329 87.65 16.798 1.221 1.991 1.282 81.71 • 17.084 1.169 2.097 1.237 76.19 17.364 1.117 2.216 1.193 71.10 17.634 1.065 2.351 1.151 66.46 17.893 1.013 2.504 1.110 62.30 18.136 0.961 2.678 1.073 58.65 18..361 0.909 2.878 1.03$ 55.53 16.559 O.B57 3.309 1.007 52.98 16.723 O.B05 3.378 0.983 51.D6 16.838 0.753 3.G94 0.955 49.84 16.8$3 0.701 4.07a fl.959 A9.41 38.OD0 D.741 4.Q70 0.959 49.A1 -----_______..__�--------�N�D OF HYDFtAULTC JL7MP ANALYSIS------------------------- I PRESSURE+MOMENTUM BAI,ANCE OCCURS AT 17.J.9 FEET UPSTREAM OF NODE 5010.70 DOWi�iSTREP.M DEP`�'H = 1.149 FEE�', UPSTREAM CON,NGATE DEPTH = 0.398 FEET --------_....------------------------------------------------------------------- NODE 5010.8� : HGL =< 318.701>;EGL= � 318.959>;FLOWLINE= � 318.000> �+*+*************+***+�**�+*�ttt+****�t+++�+****+****f�f**t+..**�.*t+��++*�++* FLOW PROCESS FROM NODE 5430.80 TO NODE 501D.80 IS CpQE = 8 UPSTREAM NODE 5010.80 ELEVATIpN = 318.00 {FLpW IS Ai` CRT'T`ICAL DEPTH) CAI.�CULA'i'E CATCH BASIN ENTRANCE LOSSES (LACFCD) : PI�E FE,OW = 4.00 CFS PIPE DIAMETER = 24.OQ INCHES FLOW VELOCI'I'Y = 4.07 FEET/SEC. VELOCITY HEAD = 0.257 FEET GATCH BASIN ENERGY LpSS =.2"(VELpCITY HEAD) _.2*{ 0.257) = 4.051. NOAE 5a10.80 : HGL =< 319.D30>;EGL= < 319.D34>;FLOWL�NE= � 318.000> *f***************t+t+*++++**+++*+*+*�+++**+++*+*+:*+**++**�r�y.**w+�ww,r***�tt+�f UPSTRF�IM PIPE FLOW CONTRpL DATA: � NODE id[IMBER = 5010.80 FLOWLINE ELEVATION = 318.00 ASSUMED LIPSTRE.�M CONTROL HGL = 318.70 FOR DOWNS'I'R.EAM RUN ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS � * r t Y 4 R * rt i } ? } * � k k * * � k � # * f * * * k f M * * k * x � w * * * � * f * � * t * * * * x Y R � � * W f f i # * k k f � t x * k ? * t t * * Y PIPE-FLOW HYDRAULICS COMPUTEA PROGRAM PACKAGE (Reference: LACPCD,LACRD, AND OCEMA HYDRAiTLICS CRITERION} (cj Copyright 1982-2001 Advanced Engineering 5oftwaxe {aes) Ver. 8.0 Release Date: D1141/2001 License ID 1509 Analysis prepared by: Project�eszgn Consu}.tants 7D1 B StrEet, Suite 800 San Diego, CA 92101 (619) 23�-6473 +*.*.w*.*f:.Ww�*.*w+w.+++* DESCRTPTION QF S'i'UDY ••«+r*+*+xw**t*r..*.*r«xv.. * BRESSI RP.NCH - ULTIMA'FE CdNDITI0N5 * * SYSTEM 5400 - LATERAL 12A 1130. 7 OF SHEET �2 DWG. 400-8C} + " 1D0-YEAR * *a*,t***wx*+**f*rtti****x*e*t**�**��xre*rt�rrwyt-r�+�rw+**y,�+xw�x�x***�*r*wwr*t*+ FILE NAME: C:\2244\50Q-12AU.DAT TIME/DATE �F STUDY: 34:4D 10/22/20D2 **r��rt�Y*��**++�y.+*+*��x*ww�**xxrtsw***x*+.w*+ww�wr+r**++wtyti**+er+rtt**r*:r�*ti GRADUALLY VAATED �'LOW ANALYSIS FOR P�PE SYSi'EM NODAL POINT STATLTS TABLE (Nate: "*' indzcates noda]. point data used.} UPSTREAM RUAI DOWNST3Z£P.M RUN � NQDE MODEL PRESSiFRE PRESSURE+ FLOW PRESSURE+ NUMBER PROCESS HEAD { FT J MOMENTUM { PDUNDS } DEP'I'H { FT } MOMEN'i'UM ( POUNDS } 5010.50- 5.05* 798.11 0.44 31.33 ) FRICTION 5010.60- 4.22* 635.25 0.56 Dc 28.55 } CATCH BASIN 5010.6Q- 4.23* 633.59 0.56 Dc 10.42 MAXIMUM ATCTMBER OF ENERGY SAI�ANCES USED IN EACfi PROFILE = 50 ------------------------------------------------------------------------------ NOTE: STEADY FLOW �3YDFtAULIC H�i}-L05S COMPUTA'FION$ SASED ON THE M05T COIdSERVATIVE FORMCTLAE FAOM �'HE CT3RRENT LACRD,LACFCD, ANb OCEMA DESIGN MANiTAI,S . �..�***«...*+*+.*t�.*.�..,,...*.....:*.*.*�.��ti��+**»***.....�**++*�+.*+**** bpWN$TREP.M PIPE FLOW CONTRQL DATA: NODE NUMBER = 541D.S0 FLOW�IDIE EL�.i1ATION = 310.75 PIPE FLOW = 2.6fl CFS PIPE DTAMETER = 24.OD INCHES ASSUMED DOWNSTREP.M CONTRDL HGL = 3�5.$00 FEET ---------___------------------------------------------------------------------- NODE 5010.50 : HGL =� 315.800>;�GL- � 315.811�;FLOWLItdE= < 314.754> +:.w*w*+**r*�++*+s*tx**�*+****r**�*y*+rw**ti*r**rrrw+a*+rtr*�+�ii.+++*k*s:+t+++wr FiOW PRpCESS FROi�S NODE 5010.50 TO NODE 5010.50 �S CODE = 1 UPSTREAM NO➢E 5014.60 ELEVATION = 311.59 (Fi�OW IS UNDER PRE55[T�t£) CALCU3�ATE FRICTION L055ESfLACFCD�: PIPE FLOW = 2.60 CFS PiPE BIAMETER = 24.00 zNCHES PIPE LENG'I'N = 69. 95 FEET MANl�IING' S N = 0. 01300 5F=;4/K}**2 - ({ 2.601/I 226.137]}**2 = p.000�3 C � � --H�=L*5F-= ( 64.95}�(0.000�3) --T_ " O.D09----_ ------------------------ -------------------------- NODE 5a1D.60 : HGL =< 315.809�;EGL= < 315.820>,FLdWLINE= < 31�.590> rt * } * k k � k * * � * t t i * * Y Y R Y * M w w Y * 1 * # * W µ µ * * W # i # * * 1 rt 4 * * * * * * * * * t Y * t � R f * * * # * Y 4 * * * * # k * * * * FLOW PROCESS FROM NODE 501D.60 TO NpDE 5�1p.60 I5 CODE = B �PSTREP,M NODE 5010.60 ELEVATION = 311.59 (FLOW IS UNDER PR�SSURE} CALCULATE CATCH BASIN EN'I'R�ICE LOSSESfLACFCDi: P�PE FLOW = 2.64 CFS PIPE DIA�fETER = 24.04 INCHES FLOW VELOCTTY = 0.83 FEET/SEC. VELOCITY HEAi) = 0.01� FEET CATCH SASIN ENERGY LQ55 =.2*(VELOCI�'Y HEAi)) =.2*I 0.01I) = 0.002 NODE 5010.60 : HGL =< 315.$22>;EGL= < 315.822>;FLOWLINE= < 311.59D> wwx:+w+*r:*��x++**sw*�sf.*wx+*x++x�xrt**+rxxw*xxrx*y*r�i+*++F*+*x*+*w*++r***rw UPSTREP.2�I PIPE FLOW CONTROL DATA: NObE NiTMB�R = 5010.50 FLOWLINE ELEVATION = 311.59 A55iJMED UPSTREAM CONTROL HGI.� = 312.15 FOR DOWAiSTREAM Ri723 ANALYSzS II3D OF GR�UAi�LY VARISD FLOW ANALXSIS . • � * k * # * * * w * w * w w * * * * * * * * * w * * * * * * * k R 4 * * � � k * * * * W k k � * * * * * t * * * * * * * * * * * * * * w * * * * * * * * * * k PIPE-FLOW FiYDRAULICS COMPUTER PROGR�M PACKAGE (Reference: LACFCD,LACRD, AN�D OCEMA HYDRAULICS CRZTERIONj (c) Copyright 1982-2001 Rdvanced Engineering Software (aes} Ver. B.Q Release Bate: O1/O1/2041 License ID 1509 Analysis prepared by: PRQJECTDESIGN CONSUL�ANTS 7D1 'B' STREE7', SUrTE 8DD SAN DIEGO, CA 9210� b19-234-0349 • .• ************************** DESCRIPTION OF STUDY *+******+*+**+++++++*++*** * BRESSI RANCH - INTERIM CONDTIONS * * SYSTEM 5D00 - LATERAi. 12 {NO 9, Z0, 11, 14 PER SHEET 12 OF DWG 400-BC) "` * Z00-YEAR * ****w**,r,r+,r*�,r*�*�*+*�*************************++**,.****.,,,.*********+*+**.. FILE NAME: 5000-12I.DAT �'IME/DATE OF STiTDY: 16:13 11/07/2002 *f***++*+t++++++**+*x**+++***rff*yr**y.+*++++***ttitrrw**�w*w+v.*www,rW,r*,rwwwww*+w,r GRADUALLY VARIED FLQW ANALYSIS FOR PIP� SYS'I'h� i10DAL PO�NT S'T'AT�]S TA$LE (Note: `*" indicates nodal. point data used.l UPSTREAM RUN DOWNSTREF1i+] RUN NODE MODEL PRESSiJRE PRESSURE+ FLdW PRESSURE+ NUMBER PROCE55 HEAD(FT} MOMENTUMIPOUNDS) DEPTH{FT) �70MENTUM{pp�DS) 5430.10- 5.38* 2039.79 Z.80 1194.62 } 5010.11- } 50�0.22- } 50�0.30- } 5d10.40- } 5014.50- } 5010.50- FRICTION 5.37* FRzcrrorr+�Erm 5.06* FRICTION 5.06* JCINC T I ON FRIC'I'i0N CATCH BASIN 2035.81 1942.20 1941.73 7.31* 2629.70 } �rD�uL�C �trMP 2.21*Dc 1124.7i 1.69 2.12 2.21 Dc 3..39 2.21*Dc 1240.24 1127.93 1124.71 1456.93 1124.71 3.94* 825.23 2.21 Dc 297.31 ------------------------------------------------------------------------------ t+lAXIMUM NUMBER OF ENERGY SALANCES USED IN EACH PROFILE = 25 NOTE: S�'EADY FLOW HYDRAULIC HEA17-LOSS CpMPUTATIONS SAS�b OI3 THE MOST CONSERVATIVE FORMULAE FROM TH� CL7RitEN'i' LAC12D, I�ACFCD, AND OCF:�IA DESTGI3 MANiJALS . ****v.**+w*��,��,***+********+**+**********+***************«**,,.*********�*��** DOWNSTFtF.I�,,M PIPE FLOW CONTROL DATA: I30DE I�iTMBER = 5010.10 FIAWLENE ELEVATION = 310.42 PIPE FLQW = 44.30 CF5 PIPE DIAMETER = 30.00 INCHES ASSUMED DOWNSTREA.id CONTROL HGL = 315.$QO FEET NODE 5D10.10 : HGL =< 315.800>;EGL= < 317.065>;FLOWLINE= < 310.420> Yrtktk'k k 1rYr* ** iF Yr�k * *YrYr f Ir*Y� * Yr***# t****t***f ** #* *** *'k *Yrt**#ti# #t*ttt*ti # # # # # ttttt�k# f * FLdW PROCESS FROM NODE 5010.10 TO NODE 5010.11 �S CODE = 1 UPSTREAM NODE 5010.�1 ELEVA'PION = 310.92 {F�,OW XS UNDER PRESSURE) CALCULA'PE PRICTION LOSSES(LACFCDJ: PIPE FLOW = 44.30 CFS PIPE DIAi�SETER = 30.�0 INCHES PI PE iENGTH = 41 . 7 5 FEET MAi3idI33G ' S N = 4. 013 0 0 5F={�/KJ**2 = (( 44.30}/{ 410.174j1'*2 = 4.d1166 � HF=L*SF = i 41.75)*(0.0116b) = 0.467 NODE 5010.1� : HGL =< 316.287>;EGL= < 317.552>;FLOWL�NE= < 3J.0.92�� +r****w**«****tt*t*+***r***��t*+r*s*****wt*++++*t+**wr**�********w+***�w***+* FLOW PROCESS FROM NODE 5010.11 TO NODE 5010.22 T5 CODE = 3 UPSTREAM NODE 5014.22 ELEVATION = 311.46 (FLdW IS UNDER PRESSURE) � --------------------------------------------------------------------------- CAL�ULATE PIPE-BEidD LQSSES(OCEMA}: PIPE F�OW = 44.3D CFS PIPE DIAMETER = 30.QQ INCHES CEi�PI'RAL ANGLE = 28.50D DEGREES MANNING'S N= Q.01300 PIPE LENGTH = 4.84 FEET BEND COEFFICIENT(KB) = 0.14068 FLOW V�LOCITY = 9.D2 FEET/SEC. VELOCITY HEAD = �.265 FEE'Z' HB=KB*(VELOCITY HEAD) = f 0.141j*( 1.265) = D.178 SF=(Q/K)**2 = {( 44.30}/{ 410.1761)*"`2 = D.41166 HP=L*SP = L 4.84)*(0.01165j = Q.Q56 TOTAL HEA3] LdSSES = HB + HF =( 0.178)+( 0.056) = 0.234 t�ODE 5�10.22 : HGL =< 316.521>;EGL= < 317.786>;F'LOWL,INE= < 311.46Q> ..,...*****,.,.****�*�**�**�*�t+*tt***t*****,.****+*t**ttt�.*.��,�.****�********�*w** FLOW PROCESS FROM NQDE 5010.22 TO NODE 5�10.30 IS CODE = 1 UPSTREP.M NOi3E 5010.30 ELEITATIpN = 311.60 {FLpW IS UNDER PRESSURE) ----------------------..__---____---________________.._------------------------- CALCULATE FRICTION L4SSE5(IJACFCDj: PIAE FLOW � 94.30 CFS PIPE DIAMETER = 30.00 INCHES PIPE L�NGi'H = ��.87 FEET MANI3ING'S N- 0.0130Q SF=f41K)**2 = ({ 44.30)/( 410.1751)**2 = 0.0}�166 HF=L*SF = { ��.87)*(0.011661 = 0.136 ------------------------------------------------------�_--_-____--___--------__ NODE 5D10.30 : HGL =< 3�b.660>;EGL= < 31�.924>;FI,OWLIIdE= < 31i.60�> ***r�xwwwww,rW,r�r�*,�******,r,r******,r**�*****�,***ww*,r******+****+*************s**a* FLOW PROCESS FROM NdDE 50id.30 TO NODE 5010.40 IS CODE = S Ul?STREAi�S NODE 5 4� Q. 4 0 E�,EVATION = 311 . 9 3 ( Fi�OW I S UNDER PRESSURE J ------------------------------------------------------------------------------- CALCULATE JUNC`i'ION LOSSES: � PIPE FLOW DTAME"I'ER ANGLE FLpWLINE CR�i'iCAi VELOCITX (CFS) (TNCHESa (DEGREES) ELEVATION DEP'i`H(FT.) {FT/SEC1 UPSTFtEAr7 44.30 30.DD 90.00 311.93 2.21 9.Q25 DOWNSTRFAM 44.30 30.00 - 311.54 2.21 9.Q25 i�ATERAL #1 0.00 0.00 0.00 0.00 0.00 O.QOD 31ATERAL #2 O.DO 0.00 O.DD 0.40 a.ao 0.440 Q5 O.DO===QS EQUALS BASIN INPiJT=== LACFCD Ai�TD OCEMA FLOW JUNCTION FORI�fidLA� OSED: DY=((�2"V2-Q1"V1*COS(AEL'I'A1)-43*V3*COS(AELTA3}-, Q4'�V4*COS(DEL'I'A4))/(fA1+A2)*16.1)kFRICTI023 LOSSES UPSTREAM: MP.�7DTING'S N= 0.01300; FRICTION SLOPE = O.O1Z66 DOWNSTREAI�: MANNII3G'S N= 0.01300; FRICTION SLOPE = O.D1166 AVERAGEI� FRICTION SLOPE IN JLii3CTION ASSUMED AS O.D1166 Ji3NCTI0N LENGTH = 4.40 FEET � FRICTION LOSSES = 0.047 FEET ENTRANCE LOSSES = O.pQO F�ET JUNCTION LOSSES = f DY-rHVl-HV2 }+{��'Rp,�CE LOSSES ) JLTNCTION LQSSES =[ 2.57b)+( O.OQO} = 2.57b NODE 5010.4p : HGL =< 319.236�;EGL= < 320.50�>;FLOWLYNE= < 311.930> ********,,*************************t*�******+*****�*+�#**,�*�ww***��**w*t**�t� Fi,OW PROCESS FROM NODE 5010.40 Tp NODE 5b10.50 IS CODE = 1. UPS�'REAM NODE 5d10.50 �LEi7A�`�ON = 32a.33 (HY�RAULIC �7L}MP OCCi3R5) _______________--_______------------------------------------------------------- CALCULATE FRICi'ION LOS5E5(LACFCDj: PIPE FLOW = 44.30 CFS PIPE DIAMETER = 30.d0 223CH�S PIPE LENGTH = 70.00 FEET MPNNING'S N= 0.02400 ------------------------------------....______-__-______------------------------ • `-HYDRALTi,TC JCFMP: DpWNSTRE.a.M RUN ANALXSIS R�SULTS NORMAL DEPTH ( FT )= 1. 3 6 CRITICAL DEPTI-I (�'T )= 2. 21 UPSTREAM CON�'ROL A55�3MED F'i�OWDEPTH(FT) = 2.21 GRADUALLY VARIED FLOW PROFIF�E COMPU'PED INFORMATIQN: DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ � CONTROL ( �"I' } ( FT ) { FT/ SEC ) ENERGY ( FT ) MOMENTiJM ( POLTNDS f D.ODfl 2.213 9.b35 3.656 1124.71 0.018 2.179 9.753 3.657 1125.14 O.D73 2.145 9.9$0 3.662 1126.43 0.16$ 2.111 �0.016 3.670 1128.60 0.305 2.a77 �4.160 3.681 1131.67 0.488 2.D43 10.314 3.696 1135.66 0.723 2.009 �0.477 3.714 1140.61 1.014 1.974 14.650 3.737 1146.54 1.367 1.94D 1Q.834 3.764 1153.49 1.791 1.906 1�.027 3.796 1161.51 2.295 1.872 11.232 3.632 1170.65 2.891 1.636 1�.449 3.875 11.60.94 3.593 1.604 11.678 3.923 1192.46 4.418 1.770 11.92D 3.977 1205.26 5.391 1.736 12.176 4.039 1219.41 6.539 1.701 12.A47 4.109 1234.99 7.9Q2 1.667 12.733 4.1B6 1252.08 9.533 1.633 13.036 4.274 1270.76 11.507 1.599 13.356 4.371 1291.15 13.931 1.565 13.696 4.4B0 1313.34 16.976 1.531 14.056 4.601 1337.47 20.925 1.497 14.43B 4.736 J.363.66 26.311 1.463 14.844 4.8$6 1392.�b 34.332 1.429 15.275 5.054 1422.83 48.632 1.394 15.734 5.241 1456.1b 70.000 1.394 15.745 5.245 1456.93 I-IYDRAUL�C J[1MP: UPSTAEAM RUN ANALYSIS RESUL?`S .: -------------------------------------------------------------- - --------------- �_ ------------------------------------------------------------------------------ � -_DOWNSTREAM_CON'PROL'A55UMED PRESSCFRE-I-IE.�D(FT)„=_`y--7-31--------------------- ___ __ __ __ _ _ __ ___ _ _ _ PR£SSLTRE FLOW PRpFX�,E COMPLTPED I�FFORMAT�ON: DTS'I'ANCE FROM PRESSURE VELOCITY SPECIFIC PRESS[JRE+ CONTROL ( FT } HEP.D { F�' } ( FT / 5EC } ENERGY { FT ) MOMENTiJkf ( POUNAS ) 0.000 7.306 9.025 . 8.�71 2629.70 59.$93 2.540 9.025 3.765 1157.54 AS5i3�7ED DOWNSTREA2+1 PRESSUR.� HEP,D ( FT) = 2. 50 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------- GR�.Ili3ALLY VARIED FI,OW PROFILE COMPLPPED INFORMATION: AiSTANCE FROM FLOW BEPTH VELOCITY SPECIFIC PR�SSURE+ CONTROL(F'I') (FT) (F3'/5EC) ENERGY{FT) MpMENTUM(POUNDS) 59.891 2.500 9.022 3.765 1157.64 b4.D16 2.489 9.027 3.755 11�4.54 60.125 2.477 9.035 3.7g6 ZZ5�.77 b0.224 2.466 9.047 3.737 1Z49.23 60.316 2.454 9.06D 3.729 1�4b.$B 60.402 2.443 9.075 3.722 1i44.68 60.481 2.431 9.092 3.716 1142.63 60.55� 2.4Z0 9.11D 3.709 1146.71 60.625 2.408 9.130 3.703 1138.92 60.69a 2.397 9.151 3.696 1137.25 6D.750 2.385 9.173 3.593 1135.70 60.8Q6 2.374 9.196 3.686 1134.26 b0.858 2.362 9.221 3.6$3 1132.92 , 60.906 2.351 9.296 3.579 1131.69 • 54.950 2.339 9.273 3.676 113D.57 60.990 2.328 9.341 3.672 1129.55 61.026 2.316 9.330 3.669 1126.62 61.059 2.305 9.360 3.665 1127.80 61.088 2.294 9.391 3.664 1127.D7 61.�13 2.282 9.423 3.662 �126.45 61.�34 2.271 9.456 3.660 1125.92 61.151 2,259 9.490 3.658 1125.48 61.165 2.248 9.524 3.657 1125.15 • 61.175 2.23fi 9.560 3.656 1124.91 61.181 2.225 9.597 3.65b 1124.76 61.183 2.2�3 9.635 3.656 1124.71 70.Q00 2.2i3 9.635 3.656 1124.71 ------------------------END OF HYDRAULIC ,NMP ANALYSIS------------------------ I PRESSURE+MOMENTUM BP.LANCE OCCURS AT 52.41 FEET UPSTREAM QF NODE 5��4.40 � � DOWNSTREAM DEP�'H = 3.10Q FEET, UPSTREAM CO�JUGATE DEPTH = 1.525 FE�P ------------------------------------------------------------------------------ NODE 5014.50 : HGL =< 322.543>;EGL= < 323.9B6>;FLOWLINE= < 320.334> w+*�***�xxtt*++*+ww+��*t+t+*++******tt�**�w�w�+************w*a**********t****t FLOW PROCESS FROM NODE 50�4.5a TO NODE 501Q.50 IS CODE = 8 UPSTREAM NODE 50I0.54 ELEVATION = 320.33 IFLOW IS AT CRITTCAL DEPTH) ------------------------------------------------------------------------------ CALCULA�`E CATCH BASIN EN�`RANCE LOSSES(LACFCD}: PIPE FLOW = 94.30 CFS P�PE DIAMETER � 30.00 INCHES FLpW VELOCITY = 9.54 FEE'I'/SEC. VELOCITY I-IEAI) = 1.442 FEEF' CA'I'CH BASIN FNEFtGX LOSS =.2*(VELOCITY HEAD) _.2*{ 1.442} - 0,2gg __----------------------------------------------------------------------------- NODE 5610.50 : HGL =< 324.274>;EGL= < 324.274>;FLOWLINE= < 320.33d> tk4Yr*t1� YrYr7r**i'tkt t�k**�k #*i*t#t*y��l Y41 Y#t # i t*t *'tt#yrtf #t#*Y*yry yryryrNtkyrkyr*1� **** *** ***�** UPS'i'REAM PIPE FLOW CONTRQL DATA: NQDE NUMBER = 50�Q.50 FLOWLTNE ELEVATxON = 320.33 ASSUMED UP$TREAM CQNTKOL HGL = 322.54 POR AOWNS`i'REAM RUN PNALYSIS ------------------------------------__---_____...�___-------------------------------- END OF GRADUALLY VARIED FLOW ANALY5I5 • `� � 'w+***w*.s�x*wr**+w:Y+*+x**�+*�*+*t��x.r�rrx*t��+**�:wr+w*r*wfr��y�*�**t�rti**« PI�E-FLOW HYDRAULICS CaMPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRD, PND OCEMA HYDRAULICS CRITERION) (c) Capyright 1982-2DD1 Advanced Engineering Software {aes} Ver. 8.0 Release Aate: O1/03/200� License ID 1509 Analysis prepared by: Pro�ectDesign Consultants 70� B 5treet, Suite BD� San Diego, CA 92101 f619) 235-6971 '•«•*•*'••'•�***•*•*•••w•' DESCRIP'iI023 OF STUDY *+**•+.+*+*.**+*.+«..+.... * BitE$SI RANCH - tJLTIMA'FE CO�ITI03�iS * " SY5'FEM 500D - LA`i`ERAI� 12 (AIp. 9, 10, 1�, & 12 PER SFiEET �2 OF * * DWG 4QD-8C} - 10D-YEAR * *#*# *'i* Yrk+***i�*1F# k t* *Y' *'� Y f Yr **+F *k yriFYrYrY� * Yrir * KiF Yr# ** Yr **#* iF YrYr*Yr**Yr**#*#�1'Y W i! # tf i� FILE NAME: C:\2244\50D0-12U.�AT i`YME/bATE OF S'PUDY: 15:20 10/22/2002 *t+*********+**a*+�**x**wwxrt+**+w***3****tx**w*+**ww*ti**x**+*a*+aw*x*xxi.+w+x*� GRADUALLY �IARTED FLOW A�+IALYSIS FOR PIPE SYSTEM NODAL POINT STAT[1S TABL� (D?ote: '*' indicates nodal point data used.l UPSTREAM RL7?�i DOWi�TSTREAM RUN • NObE MODEL PRE55URE �RESSURE+ FLOW PRBSSURE+ NLT2+IBER PROCE55 HEAD ( FT j MdrFEN'I'UM ( POUNDS ) i7�PTH ( FT} MOMENTUM { POUNDS y 5410.1Q- 5.38* 1991.60 1.9B 10E8.74 } FRICT1423 5010.1�- 5.34* ].978.34 2.02 1483.61 } FRICTIOI�+BEND 5�10.24- 5.45* 2013.3Q 2.19 Dc 1073.01 } Ju�vcTzaN 50�0.2i- 6.27* 2011.32 1.59 847.37 ) FRICTZON�BEND 5010.22- 6.28' 20J.3.02 1.58 648.91 _ } FRICTION 5Q10.34- 6.22* 1496.01 1.57 ' 853.23 } MANHOLE 5010.31- 5.93* 1406.75 1.84 797.70 } FRICTION 5Q10.32-- 5.89* 1893.55 2.04 Dc 789.70 MP.XIMUM i1UMBER OF EfVERGY SALPNCES USED II3 EACIi PROFFLE = 50 NdTE: STEAirY FLOW HYBF2AULIC HEP.D-LOSS COMPUTATIOt3S BASEb ON T'HE MOST COI3SERVAT�VE FOAhSiFLAE FROM THE CURRENT LACRD, LACFCD, AND OCEM.A DESIGN MANUALS. ***�**w***y+w*rx****x��+s�rs+r�v.**r*****w*t++r.*x**+*�x*+**+*+.*+�+.xr*++++i.+*�*** AOWNSTREAM PIFE FLOW CONTROL DIaTA: NODE N[.TMBER = 5 O 10 . i 4 FLOWL�NB ELEVATIQN = 31 D.a42 PIPE Fi�OW = 42.9D CF5 PTPE DTArSE2'ER = 30.0{} TNCHES ASSUMED DOWNSTR.F.A2+� CONTROL HGL = 315.80D FEET ___------------------------------------------------------------______----------- C � • NODE 5Q10.10 : HGL =< 315.800>;EGL= < 316.986>;FLOWLINE= < 3iD.420> x..w,+��*��++***+*.***��..t*r*...****..�*�**��*.�****.�*******«***+**.+****+* FLOW PROCESS FROM NpDE 5010.Z0 TO NODE 50i0.11 IS CODE = 1 UPS�RE.�M NODE 5D10.11 ELEVATION = 3�0.42 (FLOW I5 UNDER PRESSURE) �-------------------�--------------------------------------------------------- CALCUL.�TE FRTCTIQN LOSSESILACFCDa: PIPE FLOW = 42.94 CFS PIPE AIAMETER = 30.40 INCHES PIPE LENGTH = 41.75 FEET l�AATNTNG'S N= 0.0�300 5�=(Q/K}**2 - {( 42.90}/( 410.178j)**2 = 0.01094 HF=L*SF = ( 41.75j*l0•p1094) = Q.457 NODE 5010.11 : HGL =< 316.257>;EGL= < 317.443>;FLOWLINE= < 310.920> *yxrx*x***r+w+*r*e******w***rw**+a+*x*+rt+�**�*+sw*rt*+xxx**w**+w++***+�*x*��wa• FLOW PROCESS FROM NODE 5Q10.11 TO NODE 5010.20 IS CODE = 3 UPSTREA.PS NObE 5010_24 E�EVATIDN = 311.35 {FLOW IS LFNDER PRESSUREj CALCUI�ATE PIPE-BENii LOSSESlOCEMA): PZPE FLpW = 42.90 CF5 PIPE DIA24ETER = 30.00 INCHES CENTRAL Al+IGLE = 23.fl04 DEGR�ES MANNING'S N= 0.01300 PIPE LENGTH = 35.04 FEE'i' BEND CQEFFICI£idT(iCB) = 0.12638 FLOW VELOCITY = B.74 FEET/SEC. VELOCITY HEP.D = 1.185 FEET HB=KB*{VELOCITY H£AD} _( p.326f*( 1.165j =- 0.150 5F=(4/Kj+i2 = ({ 42.9�j/{ 41D.1541)*t2 = 0.01094 HF=L*SF = ( 36.p41*{0.010941 = 0.394 TOTAL HEAD LOSSES = HB + HF = S 0.150j+( 0.394) = a.544 N�DE 5010.20 : HGL =� 315.801>;EGL= < 3�7.987>;FLOWLINE= < 311.354> yr�r �kyr#yr tiy� yryr �Ir y.yry.�Yyr yr� � yr yr�y� f YY Yi Y i*i Y****k! ik'M yrM ri k'*YrY� YrYrYrtR iA'Y�' **Y� YrtkiM tk*irYrYrYrlrf *** Y� * i� *tt4i FLOW PROCESS FROM NODE 5010.20 TO idODE 5fl10.21 TS CObE = 5 iJPSTREAM I30DE 5410_21 ELEVATIOid = 31i.37 (�'LOW i5 iTNDER PRESSURE} __------__----_......------------------------------------------------------------- CALCUL.�TE JUI�CTION LOSSES: P�PE FLOW DIAI�ETER ANGLE FLOWLINE CRTTiCAL VELOCITY (CFS} (TNCHESj (DEGREES} ELEVA'�'ION DEPTH;FT.f (FT/SEC)� [iP5'FREAM 34.6D 30.Q0 0.00 31i.37 2.OD 7.�49 DOWt�ISTREAM 42.90 30.D0 - 31�.35 2.19 8.739 i,ATERP.i, #� 8. 30 18. QO 94. D4 311 . 85 1.�2 4. 647 �.ATERP.i� �2 0.00 Q.�O 0.04 0.4a O.DO D.00Q Q5 0. oa=-=4� ES?UALS BASIN I?dPUT=== LACFCD P.ND OCEMA FLOW JUNCTION FORMiJI�AE USED: DY=IQ2*V2-Q1*V1*C05(DEi,TAIj-Q3*V3*COS(DELTA3)- Q4*V4*CbS(DELTA4))/([A1+A2]*1fi.Z1+FAICTION L05SE5 UPSTREAM: MANNING'S N= 0.013D0; FR�CT�QN SI,OPE = 0.007�2 DOW3d5�`R£AM: MANNING'S N= 0.013Q0; FFtTCTION SLpPE = O.O1D94 AVERAGEJ7 FRICTION SLOPE IN JUNCTIObi ASSUMED AS O.d0903 JUNC'I`I023 LENGTH = 1.5D FEE'I' FRICTIQI3 LQSSES = 0.014 FEET FNTRPNCE LOSSES = O.ODO FEET Jl3i�IC'i'IObi LOS5E5 = (DY+HV1-HV2j+(ENTRANCE LC?SSES) 3iiNCTI0i3 L055ES ={ Q.428)+( 0.040i = 0.428 NODE 5D1D.21 : HGL =< 317.643>;EGL= � 31$.915>;FLOWL�13E= < 3�1.370> .x.�.**++��+�.�..�..*�*w...�.�w...+.r.�f..s*.t.+.i+**.+:..*.*.*..f.++:ff�t.*++* i � FLOW PROCESS FROM NQDE 5010.21 TO NODE 5010.22 �S CODE = 3 UPSTREAM NDDE SO�D.22 ELEVATION = 311.46 (PLOW IS UNDER PRESSUREj ------------------------------------------------------------------------------ CAI,CULATE PIPE-BEND L05SE5 (OCE�SA) : PiPE F�,OW = 34. 50 CFS PTPE DIAT�fE'I`ER = 30 . flD INCHES CENTRAL ANGLE = 4.500 DEGREES M.�NNING'S N= 0.01300 PIPE LEt3GTH = 7.30 FEET BENb CpEFFICIENT(KB) = 0.05652 FLOW VELOCITY = 7.05 FEET/SEC. VELOCiTY HEAi) = 0.77� FEET HB=FSB*{VELOCITY HEAD} _( O.D57)*( 0.771) = Q.044 SF=IQ/K)**2 = ;( 34.60)/( 410.16511*`2 = 0.00712 HF=L`SF = ( 7.3D)'�(0.00712i = 0.052 TQTAL HE.AD L055E5 = HB + HF =( 0.044}+{ D.052} - 0.09b ------------------------------------------------------------------------------ I30AE 5010.22 : HGL =< 3�7.739>;EGL- < 318.530>;FLOWLI�= < 31J..460> **wt***x*�ry*r*+�rr*.*r***r*y*x:+xr**+*y*w**�,w+*rtrw+ry***�rt*tx*�**tixti*x+w+*+�+ �'LOW PROCESS FROM NOAE 5010.22 TO NODE 5030.3� IS COAE = 1 i3PSTREAM DFODE 5010.30 ELEt7ATION = 31�_60 {FLQW IS UNDER PRESSURE) ------------------------------------------------------------------------------- CALCT3LA�'E FRICTIQN LOSSES(LACFCDj: . PIPE FL(7W = 34 . 54 CF$ PIPE DIP.3+IE7�R = 30. a0 INCHES PIPE LENGTH = 11.87 FEET MAN�IING'S N- 0.01300 SF=iQIK)**2 = (( 34.60}/( 410.225})**2 = 0.4071� HF=i*SF = ( 31.87)*i0•04713) = O.OB4 NonE 5�1D.30 : HGL =< 317.823>;EGL= < 318.595>;FLOWI�INE= < 311.600> ri YrYr* Yr *ri * Yr kYrYrlr Y�*iFY� Yr Yr�**M'yr'k1' iF1*k fY�* f'hi# i�*1�'t*�'h�Y# k*�** i�.y.* 1 i•*RY•**Yr*k **# }#�I.�yrY 1� i4t � FLOW PROCESS FROM NObE 5010.3D TO DIO�E 501D.31 IS CODE = 2 UPSTREAM NODE SQla.31 ELEVATION = 311.93 {FLOW I5 UNDER PRESSLFRE} CAT,CT3LA'FE i�IAN}�OL$ LpSSES (LACFCI31 : PIPE FLOW = 34.60 CF5 PIPE DIAMETER = 30.00 INCHES FLOW VELOCI'I'Y = 7.05 FEET/SEC. VELOCITY HEP«D = 0.771 �'�ET FiMN =. 0 5*( VELOC I'FY H EAI] j=. 0 5*( 0. 7 71 }= D. 0 3 9 NODE 5410.31 : HGL =< 317.Bfi2>;EGL= � 318.633>;FLOW�INE= < 311.930> #*} f Yrs �� F# tf i� i## i�#Y� Yr##? i�Y��R 4Y�1�! �F4 **YYY YrY! 1rlY Yrt * Y Yc* Y f k Y 1� f� 1 W 4* W iF 1 M**f f*Y t�!* *YrYrYri� FLOW PROCESS FROM NODE 5014.31 TO NODE 5010.32 I5 CODE = i � UPSTREAM NODE 5410.32 ELEVATION = 312.43 (FLOw IS US�iDER PRESSURE} --------------------------_---------------------------------------------------- CALCUL�ATE FRICTION LOSSES(LACFCDi: PIPE FLOW = 34.60 CFS PTPE DIAMETER = 30.04 INCHES PIPE LENGTH = 8. 00 FEET MADF�iING' S N = 0. fl1300 SF=IQ/K)**2 = {; 34.60}/( 410.140)1**2 = O.D4712 HF=L*SF = � 8.00)*(0.407�2j = Q.D57 NODE 501D.32 : HGL =< 3�7.919�;EGL= c 318.690>;FLOWi�IN£= < 312.030> +.*.�+*:+*+****+**********�***.�.+�+�x.*******.*.,.*.****.***...*****.*******�+ UPSTREAM PIPE FiOW CONTROL DATA: NODE NUMSER = 5010.32 FLOWL�NE ELEVA3'IpI3 = 312.D3 ASSUMED UPSTREP.I+f COiQ'I'ROL HGL = 314.03 FOR DOWNST32EAM RUN ANALYSIS -----_--_------__--------------------------------------------------------------- -----------------------------------..____________------------____..____..____---- ENb 0� GAADiJALLY VAATED FLOW Ab7ALY5ES �� , . •�t " . L flw . .- � -• . . . - ;�.r� :�, r " _ .. , , � � .} . �+- � ��.r 4�. . _ � , r .. ... �. __ a .,n . ..a ,... r... . M ,. � �� ,..r'r . .; � � . .i � - , ,� � - - � ' , ' P . ' ' t 1 � � ' � ., ' T r.` ' • ' 1 * � � + I' x• -- • t , � �� '�- ' , - .�� ': ..�.. . _ . _ ` . �� __._ � , � w . y r •` . .i _• _ •_ _ • . . �� J **...**„***�*.***�*��+��,t***,.,..**..�.**�..,.*.�.,�.��.�*x*.*.**��* PIPE-FLOW FiYDRAULICS COMPUTEA PRQGRAM PAC}CAGE (Reference: LACFCD,LACRD, AND OCEMA HYDRA[Ti,IC5 CRITERIONj Ic1 Cogyright 1982-2002 Advanced Engineering Software (aes) Ver. 8.0 Release Date: 01/41/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTANi`S 7�1 'B' STREET, SUITE 800 SAIV DIEGO, CA 92101 6i9-235-6471 C� ��r*v.w�v�+r�**�*+****��**** DESCR�PTION OF STUDY *+****++�*+**+�s**t�*��**� " BRESSI RANCH - ULTIMATE CdNDT�ONS * '` SYSTFM 50a0 - LATERAL 13 {NO. 1.3 PER SHEET 12 OF DWG. 400-8C} * "' 1fl0-YEAA * k�F*�*k**i**t#it�ifi�k�i*#�**** f *fi*?1r�lrtY�Yrtk* *�kiF f kiFk*Yr�lr******tYcY*�Jr�Jr�L*yry' *�k*iFlrYrik�k* FILE NAME: SQOp-13U.DAT TIME/DATE OF STUDX: �3:29 41/17/2Q43 #'k'k#'k1r #*#***�k *Y� * iF1riF�M � �Ir #i*t* **�IYY*YY�tYriYi! Y iYiF*ik4�ktt i # y.** �F �k�*iF*t*** i f �r Yt�ti 1� Y �i*ti GRADUALLY VARIED FLQW ANALYSIS FpR PIPE SYSTF�i NODAL POINT S'I'ATUS TABLE fNote: •*• indicates nodal poant data used.) UPSTRF.AM RUN DOWNSTREAL� RUN NODE MODEL PRESSiJRE PRE55iFRE+ FLOW PRESSiJRE+ I3LFMBER PROCESS HF.A17 ( FT� MOMEI�ITUM ( POUNDS } DEPTH ( FT j MOMENTUM ( POi]ATDS ) 5010.23- 5.76* 541.b1 4.67 21B.21 ) FRICTION 501fl.29- 4.59* ) CATCH SASI�I 5o�o.z4- s.a�* 512.30 47b.77 1.16 Dc 1.16 Dc 154_86 47.87 MAXIMUM Ni7MBER pF EIVERGX BALANCES USEB 3�i EACH PROFILE = 25 ------------------------------------------------------------------------------ NOTE: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASEF? ON 'I'HE N30ST CONSERVATIVE �'ORMUI.AE FROM THE CiFRRENT LACRD, E,ACFCD, AND OCEi�1A . DESIQ3 MANUAi�S . yr1y� i i 4yr�} # i i�#*#*Y�*�k * f*Yr** i*YrYrt1� Ye i Yr �k �k Y� *tf i 1 Yr#t �! Y144+i}i** TYrYr*iFrti� �ki *** Y*tf *tY*t ** 170WNSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = 5010.23 FLOWLIl3E EL�.vATTON = 313.8$ PZPE FLpW = 9.00 CF5 PIPE DIAMETEA � i8.00 INCHES ASSUMED DOWNSTREAM CONTRpL HGL = 317.643 FEET NODE 5010.23 : HGL =� 317.643>;�GL= < 318.D46>;FLOWLINE= < 311.880> ��*****f*�.�*��..��*�*..*..*��*.�,.*�.*.*�*��..*�.****�.�.x�*��*******,.*..*.** FLOW PROCESS FROM NODE 5010.23 TO NODE 5010.24 IS COI?E = 1 UPSTREAM NODE 5010.24 ELEVATIOi3 = 313.04 (FLOW IS UNDER PRESSI3RE) CALCULATE FRICTION LOSSES�LACFCDJ: PIPE Fi,OW = 9.OD CFS PIPE DIAME�'ER = 1$.00 TNCHES PIPE LENGTH - 5.49 FEET MANIVYNG'S N= �.41300 sF=cgix�**z = c� 9.00)/� 105.060})�*Z - O.Oa734 HF-L*SF = { 5.09)*f0.00�34} - 0.037 NODE 503Q.24 : HGL =� 317.680�;EGL= < 318.083>;FLOWLINE= � 3�.3.090> � * f * * * * * * * # # * � * t Y � 1 * Y # # * t � * * } } * * * k f * * * * * * * * # * * * � f * * f W � M i W f Y i } i * � * } * y * * * * # # t i t w 1 � FLOW PROCESS FROM NODE 5010.24 TO NODE 5010.24 IS CODE = B UPSTREAM NOBE 5010.24 ELEVATION = 313.09 (FLOW �S UNDER PRESSURE} CAi,CULATE CATCH BASIN ENTRANCE LOSSES[LACFCD}: PxPE FLOW = 9.00 CFS PIPE DIAMETER = 18.00 I�CHES FLOW VELOCITY = 5.09 FEET/SEC. �IE�OCZTY HEAD = 0.4D3 FEET CATCH BASIN ENERGY LOSS =.2'(VELOCITY HEAD) =.2*( 0.403) = 0.081 3+i0DE 503d.24 : HGL =< 318.164>;EGL= < 318.164>;FLOWLINE= � 313.094� "' �k i Y#* i t i f Y Y 4*4*Y�'t#i*# **#i1 YrY� iF *Yr*Yr *YrYrik * Yr *�F k 1� �M tk** ***tt �iyi i�kiFi# #** fr fi tk }1� �/r*#****#*i UPSTREAM PZPE FLOW C�NTROL DATA: NODE NUMBER = 5010.24 FLQWLINE ELEVATiON = 313.09 ASSUMED UPSTREAM CONTROL HGF. = 3�4.25 FpR AOWNSTREAM RUN AAIALYSIS _------------------- END OF GRADUALLY VARIED FLOW ANALYSIS . . . -..- - - � � , .� aa. , �VaY. � a } , . � t._.�. ., . '�� 4 � _�. '.s .. ,. .. R M . . _ 1 . _ . _� ._ J .e- . '. { h .1., • /r�- . .1. v .. Y 1 r . , l� • � r . r. � r . , e: - . ' . i , -.S ' . � ' ,. - ' �* , ' . , '� , . r . • 1 i� � � _ � � � . � � 4 , �L.V �!UR ��r , � � �'..'. . . .. �. A. ._ • . • � • • r.. . w i- 'v 0 � **ik #'+t Y�# Y� f**Yi 1r Yr f*1 t*#t! t%t t Y?* **ir* iF�F1i i� t x**Yr! *Yi! yryrrt+yr�4}klYrk YrlriFk tk�F*tY k* M Y�k k4w �1 f ti Analysis prepared by: Prajec�Design Consultants 701 B Street, Suite 80Q San Diega, CA 9210]. I619} 235-6471 i ...ti�.....x*�*,,..*.***.�... FESCRIPTION OF STUDY *�..*++*.:*,..+*..�*...**.� * BRESSi R�3dCH -- ULTIMA'T'E CONDTIONS * * SYSTEM $p00 - LATERAi 13 (NO. Z3 PER SHEE'i 12 OF bWG. 404-BC) * ' 100-YEAFt * .w.f�x*w*t.�.a...*+�k.*..{.��r*.i++,�..�r*:++*t.x*+*�i*.+.s..rt.w*..*.*.ti.** FILE NAME: C:\2244\500D-13U_DAT TIME/DATE OF STUDY: 14:09 10/22/20D2 �*+,r*+w******....+*+*+**+++**+**********+**.**�**�*+*.W�«*v.*+***x*�.**+..******,. NQDE NUMBER 50i4.23- } 5010.24- ? 5010.24- PIPE-FLOW HYDAAiTLYCS COMPUTER PROGRAIrS PACICAGE IReference: LACFCD,LACRD, A�TD OCEMA HYDRAfJ�,TCS CRITERI�FV} {c) Copyright 1982-2Q01 Advanced Engineering Safeware (aes) Ver. 8.0 Release Date: O1/D1/2001 iicense ID 15Q9 GRADUALLY VARIED FLOW ANRLY5I5 FOA PIPE SYST�1 NODAL POINT STATUS TABLE (Note: "*" ind�cates nodal point data used.l 13P5TREA�4 RiTt3 DOWAISTRE.�M RUN MQDEL PAE$SURE PRESSURE+ FLpW � PRESSURE+ PROCESS HEAD {�'T} MOMF�ITUM ( POUNbS } pEPTH { FT) MOD4F.i�ITUM ( POUNDS) 5.78* 643.82 0.66 221.04 FiZICTI0I3 4.55* CATCH BASIN 5.03* 507.89 472.35 �.16 DC 1.16 Dc 154.66 A7.67 ------------------------------------------------------------------------------ MP.XI2�IUM NL7I+FBER OF ENERGY HP.LANCES USED IN EACH PROFILE = 50 NOTE: STEADY FLOW HYDRAL}I,IC HEP.D-LOSS CdMPU'TAT�O�IS BASED ON THE MOST CO23SERV7ITIVE FORMUi�AE F'ROM 'i'HE CURRENT T�ACRD, LACFCD, ANE1 OCFMA bESICN 2+SPNiJAI,S. x+xw**+w***titi*�rw++ws+***w*+s*****t:w+*xx+x*�*w+**+++*tirt�frir**rr�+****�*�*+ti�* DOWNSTREAM PIPE FiOW CON'f`ROL DATA: AiODE NL7S�fBER = 5010.23 FLOWLI33E ELEVATION = 311 . B6 PIPE FLOW = 9.D0 CF5 PIPE DIAMETER =�8.00 INCHES ASSLTI�fED DOWNSTREA2+3 CONTFtOL HGL = 317.643 FEET NODE 5010.23 : HGL = c 317.fi43>;EGL= < 318.046>;FLOWLINE= < 311.860> r,�+r*++*+**t*wY�rfrrr+�*++s�+��rt+v.rrwy�*r*+**r*+*�r*****+*+**�*fxrw*r�+�+*�**w♦ F�OW PROCESS FROM NODE 5410.23 TO NODE 5010.24 IS CODE = 1 UPSTREAti NODE 5D10.24 ELEVATION = 313.13 fFLOW TS UI3pER PRESSL�RE) --------------------------------------------------- - ---------------__-------- CALCUi1.�TE FFtICTION LOSSES (LACFCD] : PIPE FLOW = 9.OD CrS PiPE DIANIETER = 18.00 INCi�iES PIPE LENGTH = 5.09 FEET MANNTNG'S N= D,p1300 SF=(Q/K}��z - (; 9.p0}/{ 105.D641}"*2 = O.00i34 �� HF=L*5F = ( 5.091*{0.a0734) = O.D37 ------------------------------------------------------------------------------ NO�E 5D�0.24 : HGL =< 3]7.680>;EGL= < 3�8.083>;FLOWLINE= � 313.130> ��w�*xt�tx+**yx*srt*r*t+++++�x*x*x+x+�*+t*t*+**rt+wr*ei+*++r��t+rrt+r�****+**x* FLOW PROCESS FROM NODE 5D1�.2� TQ NODE 5010.24 I5 CODE = 8 UPSTRSAbS NODE 5010.24 EL�l7ATI0N = 313.13 (FLOW IS UNDER PRESSiTftEj ------------------------------------------------------------------------------ CALCUZ,ATE CATCH BASIN F�i'i'RANCE L05SES S�CFCD) : PIPE F�ow = 9.oa CFS PIPE DIASiETER =�8.00 INCHES FLOW VELOCT'i'Y = 5.09 FEET/SEC. VEI�OCITX HEAD = 0.4D3 FEET CATCH BASTN EI3EFtGY L055 =.2";VELOCITY HEADj =.2*f 0.403} - 4.0$1 ------------------------------------------------------------------------------ NODE 5010.24 : HGL =< 318.164>;EGL= < 318.164>,FLOWLINE= < 313.�30> *�w+w+**r+*w.*f.r*+sr*yrryx*�rsr�xxxxxx++i.wr�rt+t:+�*rr.v.w++xw+sxr��+**x*xt*+*r UPSTREAM PIPE FL'dW CONTROL DATA: NODE NUMBER = 5a1Q.24 � FLOWLINE ELEVATI03�1 = 313.13 ASSUMED UPSTR�AM CONTROL HGL = 314.29 FOA DOWNS'I'REAsf RUN ANALYSIS _ __________________________________________��4=====___�-��_�_�« ________== END OF GAP.DUALLY VARIED FLOW ANALYSIS i • � ��z - - .,, � . „ } , � �"� „ � � , . _ V . . � . . , . � �_. . . . - , _ .�,. �.� ,�w ��.�.a,, . .. . . N,� . _ . , .� .. . . _ . � . �. _ . , , , _ _ r,,2 S � x • • x ,� , � • � . �'�y � . . . •,, . - , . „ . ' , Y ' _ T� . .f « � , � � . 1" -�• . . . � _ _ ,w" a • ;1q, , . ' . _ . . . .+. . .t- ' � ' ' , .,,1, - _ , a .., _ . ' _��.� " � � . - � > � `* �� . - . _ � �' . e ` � • . -r S . i , * . � � � - a � _ . -.. '�A. .,i#�i' a t.�t,'h_ t,' .a:.�., . ,,.. . _ .� s��'-` ":�' , r., w.it:' �r � � . . .� ��{ ' .J. '��._ _ ., r d. CJ :a>xtw.*x<�*wxrxx.r***�x++rr+r�w****yrtxta***x**s+x*+�*w*>.*x�+*+*.��.r*rr�*xw* Analysis prepared by: ProjectDesign ConsulCants 701 B SCreet, Suite 80D San Diego, CA 92141 (fi14} 235-6471 . �..+*v.x>,+.=.+*.,.�..+�.._.* DESCRIPT�ON OF STLiDY "•••*•*•"`""•*•*+..�«+:�..t * BAESSI RANCH - iJ�i�TIMATE COidDITIpNS * * SXSTEM SDDfl - LAT�RAI� 14A (N0. 5 PER SHEET 11 OF DWG 4D0-8C) * * 100-YEAR * �**is**r*y�*�rti*w**a+r*�****�*xw*+w+**+r�wrrtr�tr��rr�r�i**ry*r+t+*�ia*n.**wwx FTLE NAME: C:\2244\500�-14A.DAT TIME/DATE OF 5TT3DY: 17:33 10/22/2002 wx.rwyr�w**wxw+*rtrrteryr*+ir#i.rrr*yr*tit*t*w++yrftrw*wr*fr*yr**ryrwkyr�*w*xxtr*xa.rt*##tt.**x*ir I30DE NCTMBER 5Q11.50- } 5011.50- } 507.1.64- PIPE-FLOW HYbRAULICS COi+FPUTER PROGRAM PACKAGE iReference: LACFCD,LACRD, AND OCEMA HYDRAULICS CRITERION} fc} Copyright 1982-2D01 Advanced Engineering Software Iaes1 Ver. 6.0 Release Date: 0�/O1/2001 �icense ID 1509 GRADUALi�Y VARIED FLdW ANALYSIS FOR PIPE SYSTEM NODAL POINT S`FATUS TABLE {Note: '*" indicates nodal point data used.j UPSTR£AM RT3N DOWI3S'I'REAPS RLTN MODEL PAESSURE PAESSURE+ FLOW PRESSUREt PROCESS HEAn ( FT} MQI+IE�ITUM I POUNDS} DEPTH {�'T} MOMENTUM ( POUNDS ) 4.71 Dc � 44.24 0.33" 89.44 FRIC`I'ION 4.71*Dc CATCH SASIN 1.05� 44.24 23.89 D.71"Dc a.7a. �C 44.24 15.61 MA?i2l�iLiM NL7MSER OF Eid.ERGX BALANCES [TSED II3 EACH PROFILE = 50 NOTE: ST�Y FLOW HYDRAT3LIC HEAi)-LQSS C42+SPUTATiONS BASED ON THE MOST COI3SERVATIVE FORMULAE FROM THE Ci3RRENT LACRD,LACFCD, AND OCEMA DESZGN MANUALS. • *W*wr*.***..r*.**tw*+**+*+.*+***.s+*++*frWr+v��r�.+*rat:>+r�.rrwr�rrt*s.w+***+*.**�+ DOWNSTREAM PIPE FLOW CONTRQL DA'i'A: NODE NUMBER = 5411.54 FLOWLII3E �I.EVATION = 330.33 PIPE FLOW = 3.54 CF5 PIPE DTAMETEA =�8_fl4 INCHES ASSUMED DOWI35TREAM CONTROL HGL = 330.320 F£E'F *NOTE: ASSUNIBD DOWIdSTAEAsf C4NTROL DEPTH �-0 • D1 FT. } IS LESS THAN CRITICAL DEPTH{ D.71 F'I'.} ___> CfZITICAL DEPTH IS ASSUMED AS bOWNSTREAM CONTROL DEPTH FOR UPSTAEAM RUN ANALYSIS -------------------------__-_-_---------------------------------------_-------- NOAE 50J.3.50 :�3GL =< 330.651>;EGL= < 332_930>;FLOWLINE= < 33�.330> rre*yrtrxwwrr*��t*+**+k+t++x**x*xw*i�*+�rwx�+:v,x�tts**�*,ryr��r**++�ts**�r*r,rai.�+* FLOW PROCESS FR�M NODE 501]..50 'I'O NODE 5011.b0 IS CODE = 1 UPSTREAM DiODE 5411.6Q ELEVATION = 332.39 (FLOW �S SUPERCRITICAL) � • CALCL7TIATE FRICTION LOSSESfLACFCD�: PIPE FLOW 3.50 CFS PIPE DIAhIETER = 18.00 IbiCH�.S PIPE LENGTH � 8. 25 FEE�' MANIdI13G' S I3 = 0. 01300 NORMAL DEPTH{FT) = 0.26 CRITICAL DEPTH(FT] = D.71 ------------------------------------------------------------------------------ ------------------------------------------------------------------------------ UPSTREArS CO�+T'I'ROi ASSi]2+fED FLOWDEP'�`H (FT} - 0.71 GRADUALLY VARIED FLdW PROFILE COMPUTED INFdgN3ATI0N: ------------------------------------------------------------------------------ DISTA3dCE FROM fiI�OW DEPTH VE�OCITY SPECIFIC PRE55[JRE+ CONTROL I�'T j ( F'T J ( FT / SEC 1 FNERGY ( FT ) 2+40MFS1'T'LiM ( POUNDS 1 D.000 0.714 4.22D 0.99a 49.24 D.001 0.745 4.290 Q.991 49.25 0.004 0.596 4.362 0.991 49.29 O.OD9 0.687 4.437 0.992 44.35 0.016 D.678 4.514 0.994 44.43 0.025 0.659 4.594 0.996 44.5A D.037 D.6fi0 4.676 0.999 44.67 0.051 0.651 4.762 1.003 44.84 0.066 0.641 4.650 1.ao� 45.03 0.089 0.632 4.942 1.012 45.25 0.113 0.623 5.037 1.Q18 45.50 0.140 0.614 5.136 1.424 45.78 0.171 0.60� 5.238 1.432 46.09 0.2p6 0.59b 5.344 1.d40 46.44 0.245 0.587 5.454 1.Q50 46.82 0.29fl 0.578 5.559 1.060 47.24 • 0.339 0.569 5.688 1.072 47.70 0.395 0.560 5.812 1.085 48.20 0.456 D.551 5.991 1.340 48.74, 0.524 0.542 5.075 1.�16 49.32 0.600 0.533 6.2ib 1.�33 49.95 D.683 0.524 ' b.362 1.153 50.fi3 D.775 0.515 5.534 1.375 5 L 36 0.877 D.5D6 5.674 1.Z98 52.14 0.990 0.497 fi.641 1.224 52.98 1.114 0.488 7.0�5 1.253 53.88 1.252 D.479 7.198 ]..2&4 54.84 1.404 0.470 7.389 1.318 55.87 1.572 0.4b1 7.59D 1.356 55.97 1.758 0.452 7.801 1.397 58.14 1.965 0.443 8.022 1.443 59.40 2.144 0.434 8.255 1.493 60.74 2.449 0.425 8.501 ]..548 fi2.�7 2.734 0.4J.b 8.759 1.5d8 63.69 3.053 0.407 9.D33 1.574 55.33 3.411 0.39$ 9.321 1_748 67.07 3.614 �.389 9.627 1.829 fi8.93 4.270 p.384 9.950 1.918 70.93 4.790 D.371 1D.293 2.Oi7 73.U6 5.384 0.362 10.658 2.�27 75.35 fi.059 0.353 11.046 2.249 77.80 6.Bb7 0.344 11.4b0 2.384 80.43 7.805 p.335 11.901 2.535 83.26 8.25D D.331 12.085 2.500 84.44 • � NODE 50�1.50 : HGL =< 333.104>;EGL= < 333.380>;FLOWLiNE= < 332.390> *x*+**x*rx�w�*r*ry*x++*+x***+r*+x�*x****x*.�**x*wxw*�t*w**+ra**�*r*�*x*r�***�x FLOW PROCESS FROM NODE 5011.fi0 TO NODE 501�.60 IS CODE = 8 UPSTREA�S NODE 5011.60 ELEVATION = 332.39 {FLOW I5 AT CRITICAL DEPTH} CAI�CULATE CATCH BASIN ENTW�t3CE LOS5E5(LACFCD} : PIPE FLOW = 3.50 CFS PIPE DTAME'i'ER = 18.Q0 INCHES FLOW VELOCITX = 4.22 FEET/SEC. VELOCITY HEAD = 4.277 FEET CATCH �ASIN ET3ERGY LQSS =.2*IVELGCITY HEAD} _.2t( 0.277) = Q.055 -------------------____-------------------------------------------------------- NODE 5011.60 : HGL =< 333.436>;EGL= � 333.436>;FLOWi�I4�TE= < 332.390> ♦r***x<rx�xx*xw+*r*w�,r**rt**xrt+sa+*t++ts*v.+*+t++��k�k+t+*�ii�++i.*rw++*++++*rt++�r+�rrr UPSTREP.M PIPE FLOW CONTROL DATA: NODE NC7I�BER = 5011.64 FLOWLINE ELEVATION = 332.39 ASSUMED UPSTREAM CONTftOT� HGL = 333.10 FO%2 DOWNSTREAM RUN ANALYSTS --------------------------------------�..____�_�-__----------------___------------ ------------------------------------------------------------------------------ EI3D OF GRADUALLY VARIED �LOW A�FALXSIS • rl �' u �'`�{ � " . . • k . + � . ,� . . , . : • ,� � '1r S ,. , r ' ' � . y ;+ . -' aai. w��R a l. ' w � � ��n ♦ w - �� a � . � . . � . � . �a � . . `+ �L/� � � e • tii^—� 1v t �. 4ti ._ ' • , � � F.w , r \ - . . . • . � . • A ' r � u } . _ . � i - , .a � ' • . �' � r r. t � _'.� � �? r r • � � ' � , ., • .� . , 7 ti . . { � , F , . y � , . , . , '_ _ � ;' • , . � .' .• , .. ,� { � • r "L 0 � 1 i . • ' , . ' _ ,hi � "' �+ - . �.Y. 'r�errr �u� . . 1 r s � , wi,l'Fi�, , � . �L ,. ,. , . , ..r _ . � . __. ' �. .. � S'-`'�� t. _ ' �. . _ .. . r � *wxxxt�x*.rtr*�+s**wx*>*xri*rrr*.Y.t++tarr�*wr*.Rr�r*x+xs++x*xk:�*x*x*xx+xxw+xx PZPE-FLOW 3-IYDRAULiCS CO2+FPUTER PROGRAM PACKAGE {Reference: LACFCD,LACRD, AND OCEMA HYDRAUi,�CS CRTTERION) (c} Copyxight 1982-20D1 Advanc2d Engineering Software (aes) Ver. B.0 Release Date: O1/O1/2QD1 License Tp 1509 AnaZysis prepared by: ProjeCtDesign Consu�tants 701 B Street, Suite 640 San Diego, CA 421p1 (b191 235-647� .++.x�*xxx**fx.xxyx:.x+t** DESCAiPT�ON OF S'i`UDY ****"**'****�*"**w*°�***'* * BRESSI AP.h7CH - UI�TIMATE CONnIT�ONS * * SYSTEM 5000 - LATERAL 14 (NO. 4 PER SHEET �1 OF DWG 4D0-SC1 ` * 100-YEAR * �ti Yr *Yc�kik ir YrMf Yrf R Yrfrk *iM f YrY� * 4 iFY� Yr *YrY� Y� f* Yrtk�F#Yr iYY�Yr# iF1i� Yr*i� f Yr f k YrYr *MllrYrk�F*Yr�FY� Yr* }YrYrYrf ♦ FILE A3AME: C:\2244\5000-14.DAT TIi+fE/DATE OF STUDX: 15:D6 10/22/2002 +***++t**+*R+*fr*wry.,rrw�rf*rtx***rtx*+*****+***a*++*tfw+*rr*tir*++*+*y.t�**�**twt* GRADUALLY VARIED FLOW ANALYSIS FdR PIPE SYSTEM IdOI}AL POII3'T' Si'A�'FJS 'i`fiBLE iNate: "*" indicates nodal point data used.l UPSTREA2+3 RUN DOWNSTREAM RUN : NODE MODEL PRESSURE PRESSURE+ FLOW PRESSL3RE+ 13I3NffiER PROC ESS HEJi?] ( FT } MQMI;NTUM { pOUNDS } DEPTH ( F'T ) MOMENTUM ( POT3NDS ) 5011.20- 0.78 Dc 54.33 0.64' S7.21 } FRICTION 5011.20- 4.76*i1c 54.33 D.78*Dc 54.33 } CA'1'CH SASIN 501�.2Q- 31.14' 3351.55 0.78 Dc 18.96 ----------------------------------------___------------------------------------ NF.�XIMUM Ni3MBER pF ENEFtGY SALANCES USED IN EACH PROFTLE = SO ------------------------------------------------------------------------------ sIQTE: ST�.�.E}Y FLdW HXDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE I�iOST CONSERVA'I`IVE FORMU�AE FROM THE CL7RRENT LACRI�, T.,ACFCb, AND OCEMA DESIGN MANTJALS . *.+t..*++w**.***�..,..«..*.w.>�*.�*.,,*�+++�+�+*+**.x*.**..*.,..*�..�.*..*.....**„*+* DOWNSTREAM PIPE FLOW CONi'ROL DATA: NODE NUMBER = 5021.�0 FLOWLINE ELEVATION = 330.D0 PiPE FLOW = 4_3D CFS PIPE i}IAMETER = 18.00 iNCHES • ASSLiMED DOWNSTREA2�S CON'T'ROL HGL = 330.32Q FEET *NOTE: ASSUi�SED DOW135'TREAM CONTROL DEPTH{ 0.32 FT.} I5 LESS THAI3 CRITICAL DEPTH( p.78 FT.j -__> CRT�'TCAI, DEPTH IS ASSiJMED AS DQWNSTREASS CONTROL DEPTI-i FOR UPS7'REAM RiTI� ANALYSTS NODE 5011.�0 : HGL =< 330.643>;EGL= < 331.142>;FLOWt�II�= < 330.000> Y-1k 1k ** ifrt# hi�** ****> / k YrY�# iYlY�k Yr Yr>Yi �#*#} f i� 1r }lY�Y�Y�* Y��kiFYr *Yck frYriFri Yr �r*Yrf *�k*YriFk k kM i f i�ir t1� �Ff FLOW PROCESS FRQNF NODE 5a11.10 TO NODE 5011.20 IS CODE � 1 UPSTREAM NODE 5D1�.2b ELEVATION = 33D.26 iF�ow iS SUPERCRI'iICA%} ------------------------------------------------------------------------------ � � CALCULATE FRICTION L�SS�S{LACFCD}: PIPE FLOW 4.10 CF5 PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 22.25 FEET �I.�NNTNG'S N= 0.01300 NORMAL DEPTH[FTj = 0.62 CRITTCAL DEPTHIFT) = D.76 UPSTREAM CONTROL A55UMED FLOWDEPTH(FT) = 0.78 GRP.DUALLY VARIED FLOW PROFILE COMPUTED INFORidA�'Ipi�I: ------------------------------------------------------------------------------ pISTANCE FFtOM FLOW DEPTH VELOCITY SPECIFIC PRESS[JF�+ CON'I`ROL ( FT ) ( FT ) ( FT/ SEC ) ENEgGY {� � MOMEN7'CJM { ppiJAIDS ] 0.600 0.775 A.448 1.083 54.33 0.004 D.772 4.470 1.083 54.33 a.Q15 0.769 4.492 1.D63 54.33 0.034 D.766 4.5k5 1.063 54.34 0.062 0.763 4.538 1.083 54.35 0.496 0.75D 4.551 1.063 54.36 0.144 0.757 4.584 1.064 54.37 0.199 0.754 4.6a7 1.084 54.39 D.264 0.751 4.631 1.D84 5k.41 0.339 0.748 4.655 1.465 54.43 0.426 0.745� 4.679 1.D85 54.46 0.524 0.742 4.704 1.086 54.49 a.634 0.739 4.729 1.086 54.52 0.758 0.735 4.754 1.087 54.56 4.845 0.733 4.779 1.088 54.59 �.046 Q.730 4.805 1.D88 54.63 : i.213 0.727 4.83D Z.089 54.58 1.396 0.724 4.856 1.090 54.73 1.595 0.721 4.883 1.091 54.77 1.B15 U.71$ 4.910 1.092 54.83 2.053 0.714 4.936 �.093 54.88 • 2.312 0.711 4.964 }..094 54.94 2.594 0.706 4.991 1.095 •55.41 2.900 0.705 5.419 i.097 55.07 3.231 0.702 5.047 1.096 55.14 3.541 0.699 5.076 3.100 55.21 3.981 0.696 5.105 1.101 55.29 4.405 Q.693 5.13� 1.103 55.37 4.854 0.644 5.163 1.1�4 55.45 - 5.362 0.687 5.193 1.106 55.54 5.9D4 0.684 5.223 1.108 55.63 6.494 0.681 5.253 1.110 55.72 7.136 0.57$ 5.284 1.112 55.82 7.836 O.b75 5.3k5 l.iZ4 55.92 8.605 Q.672 5.347 1.�3b 56.02 9.44$ 0.669 5.379 1.i38 56.13 J.4.376 D.666 5.411 1.3.21 56.24 11.4R2 D.663 5.443 1.123 56.35 12.591 0.66D 5.476 1.126 56.48 13.8i5 Q.657 5.510 1.128 56.60 15.24? 0.65Q 5.543 1.131 56.73 16.872 0.65I 5.576 1.134 55.85 16.736 0.648 5.612 1.137 56.99 20.903 D.644 5.647 1.14p 57.I3 �' 22.250 0.643 5.666 1.142 57.21 . � ��---------------------------------------------------------------------------- NODE 5011.20 : HGL =< 331.435>;EGL= < 331.343>,FiOWLINE= < 33d.260> �ty+x+tx**t*ai+x+*�*wr+x+�++*art+w+xx*xt*+�*+�+*+**+*t*x*tr**t*�w*f****x+x****a FLOW PRpCESS FRQM NODE 5D11.20 TO NODE 5011.20 IS CODE = B UPSTRE.�M NODE 5011.2D ELEVATION = 300.2b {FLOW IS AT CRITICA.L DEPTH} CAL�CiJL.�TE CA'�'CH $ASIAI EI3TRA23C� LOSSES(LACFCD} : PIPE FLOW = 4.10 CFS PIPE DIAMETER = 16.00 INCI-IES FLOW VEIACITY = 4.45 F'EET/SEC. 1IELOCITY HEAD = 0.307 FEET CATCH BASIN ENERGY LOSS =.2"{�LOCITY HEAD} -.z*( 0.3D7) = 0.061 ------------------------------------------------------------------------------ NODE 5011.20 : HGL =< 331.404>;EGL= � 331.404�;FLOWLINE= < 300.260> YrYrM ti i� �kYr} Yr f YYrt***t+*Y�f YrtiliiF�k *i*t 1t1xW ttf4 fiFf *t}r Y�1k Yr iriFY�lrYrY� YrYr*#Yrt �R fYrYY! Y f YYrY M e1 Y i3PSTRE.�Ni PIPE FLOW CON�'ROL DATA: ?,FODE NUMBER = 5011.20 Fi.OWLINE ELEVATiON = 300.2fi ASSUMED UP5'F�tEAM CQNTAOL HGL = 301.04 FOI2 DOWNSTFt.F.7�M RUN ANALYSIS -------------------�_------------------------�_-------------------------------- Ei�iD OF GRADUAE,LY VARTEI7 FLOW RNALYSIS i- • �� " - i- ' - .. .. .. � .. . ,. . ' L , .•�a . _ - + � T. `r� � i,' - - �. �.r � .yr " Yk � 1. • +IM� .... .�. . . � . � , . . n w.... -. � , - * � •s� � ' .. � � � -` � ',i � - .s , '9 y�:, . . � ' . z' .'x �... • � � . � �.,� . � • � 0 ,. . , . � . .,.r +.+ -• �r . 0 v � "i�+: h u.. ��.. _ - . .� _ _ . _. ' .,`� - 4 .. . � , . . � , . . . _ � s'. � ...� • �*�x�*rxxe*sw+*rr**xa++r+w*rw*yx**+*x*x***++��x*+�r�rr�>wrr*++x*+s*�+*t+x�*�w PIPE-FLOW HYDR.AUL�CS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, PND OCEMA HYDRAULICS CRITERIpI3i (C) Co�ayright 1982-2041 Advaneed Engineering 5oftware (aes} Ver. 8.4 Re].ease Date: O1/O1/2001 iicense ID 3509 Analysis prepared by: PROJECTDESIGN CONSULTANiS 7Q1 'B' STREET, SUITE B00 5AN DIEGO, CA 92101 619-234-0349 *�*+*.*+..*.+*�t...*....:. DESCRIPTIO�I OF STUDY **•«*.*+.+.:+:**.*****.+*+. * BRESSI RANCH - T3L'£IMATE CONf?ITiONS * * SYSTEM $040 - F�ATERAL 7.5 (GREEiJH_AVEN STA 5+92 RT} * * 100-YEAR * *w*t,*a*t+xxsxtw*+x*t++x+x**tt*,r+w*+x*xxwrtrkr*rxW+++i.xxxwx*�w+a*xw,rx*x�+w�* FILE NA2+IE: 5000-15.DAT TIihE/DATE OF STiiDY: �4:29 D9/0$/2402 .**.....++,r+..**t*.,,*f...i.+..**.«.�f..*+w.�*....*.**+......*.f*x.++.�x*+*.*.. GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTFM . NODAi POINT STATUS TABLE (�Iate: '"' indicates noda.� point data used.} UPS'I'REANS RUN AOWNSTREAM RUI3 NODE MODEi PRESSURE PRESST7RE+ FT,OW PRESSURE+ NUMBER PROCES S HEAD ( FT ) 2+IOMFT]'I'iiM { p0[JNDS � DEPTH { gT ) MOMEN'T'UNi ( PdUNDS ) • 5011.50- 0.71 Dc 44.24 0.33* 84.32 } FRICiI�N 5011.60- 0.71*Dc 44.24 0.71*17c 44.24 } CATCK SASIN 5011.60- 1.05* 23.89 4.71 Dc 15.61 -------------------------------------------------------------------------------- S�iAX�MU�'i NUMBER OF ENERGY BAiANCES USED IN EACH PROFILE = 25 ---------__......----------------------------.._---------------------------------- � NOTE: STEADY FLOW HYb1�AiJLTC HEAD-L055 CQMPUTATiONS SASED ON THE MOST CQNSERVATI�7E FORMULAE FROi+1 THE CURRENT LAC]ZD, L�ACFCD, P.ND OCErSA DESIGN MAI3UAL5. w**s:wr*t+****,.rrt*+**�r�+w�r+t+w*Wr*r*rr�r�+rr.ia+y.rwswt*e�*rt*xwr�*�**,r*�*r+t++# DC}WNSTREAM PIPE FLC7W COI3TROL i7ATA: NODE NiThffiER = 5 O 1 Z. 5 a FLqWLINE ELEVA'I`I ON = 3 3 0. 33 PIPE FLAW = 3.50 CFS PIPE DIAi+fE'IER = 18.OQ INCHES ASS{7MEL} ApWNSTREAi�I CONTROL HGL = 330.320 FEET 'NOTE: ASSUNSED DOWNSTAEAM CONTROL DEPTH( -0.01 FT.i IS L£55 THAN CRTTTCAL ]7EPTH; 0.71 FT.] _�_> CRITICAL DEPTH IS ASSLTMED AS DOWNSTREAM CONTROL DEPTH FOR UPSTREAI� i2UN ANALYSIS NODE 5D31.50 : HGL =< 330.661>;EGL= � 332.924>;FLpWLINE= < 330.330> x+,r>*+a*+xx**x*rw**s*�*+++wrxs+.**r*x�***+*ri,rrw+rxrx*wxx:+rx*x*rttxw****:xt+*w FLOW PROCESS FROM NODE 5011.54 TO N4DE 507.1.60 IS CODE = I UPSTREAM NODE 5a11.fi0 ELEIIATIOPI = 332.39 (FLOW IS SUPERCRITICALI CALCi3LATE FRICTION L05SES (i�ACFCD) : PIPE FLOW = 3.50 CFS PIPE D�AMETER = 1B.Q0 II3Ci�3ES PIPE LENGTH = 8.25 FEET MP.NNING'S N= 0.01300 • • --NORMP.L_DEPTH(FT}-=--___-0�26--`- "`�--�CRITICAi-DEPT'H(FTj-=__-___0�71------- ______ _� _ _ ____ _____ UPSTREAM CONTROL ASSUMED �LQWDEPTH(FTj = 0.71 GRADUALLY VARYED FLOW PROF'ILE COMPUTED INFOFti�ATION: ------------------------------------------------------------------------------ DIS'I`ANCE FROM k'LOW DEPTH VELOCITY SPECI�'IC PRESSURE+ CONTROI.� ( FT1 { FT } ( FT/ 5EC ) ENEFtGY ( FT ) MOMEN'FL7i�5 ( POLTNDS } 0.000 0.714 4.22� 4.990 44.24 0.60q fl.646 4.352 Q.991 44.29 O.Q16 �.676 4.514 4.994 49.43 O.D37 0.660 4.676 4.999 44.67 O.D68 a.641 4.&5D �.007 45.03 0.�13 D.623 5.037 1.018 45.50 O.I71 a.605 5.238 1.032 46.09 0_245 b.5B� 5.454 �.050 46.82 0.339 D.569 5.688 1.D72 47.70 0.455 D.551 5.941 1.1Q0 46.74 4.600 0.533 5.216 Z.133 49.95 0.775 D.515 b.5Z4 1.175 51.36 0..994 0.497 5.641 1.224 52.98 �.252 0.479 7.19$ 1.284 54.$4 1.572 D.461 7.590 ]..356 �6.97 1.9fi5 0.943 S.D22 1.443 54.40 2.449 0.425 8.5D1 1.548 62.17 3.053 D.407 9.033 1.674 65.33 3.614 0.389 9.627 1.829 68.93 4.790 0.371 14.293 2.017 73.06 6.D69 D.353 11.046 2.249 77.80 7.605 0.335 1J..,9D1 2.535 83.26 __84250________�_R_331-----12_067----------2_594------------84�32----- • 4TNODE' S01i.60 : HGL =� 333.104>;EGL= < 333.38�>;FLOWLINE= � 332.390> ***�***�**�**.«„�*«**„x�,.****�**+�w�t�r*�r,.�w,�f*+*rs,r��f+w*�+t+,r*t**,�,�Yw.*�**�r:* FLOW PROCESS FAOM NODE 5411.66 TO NODE 501i.60 IS CODE = 6 T3P5T�tEAM NODE 5011.60 ELEVATIQN = 332.34 (Fi,OW IS AT CFt�TICAL DEPTH] CALCIILATE CATCii BASIN FNTRANCE L055E5(LACFCD}: PIPE FLOW = 3.50 CFS P�PE DIAMETER =�8.�0 INCHES FLOW VELOCfTY = 4.22 FEET/SEC. VELOCITY HEAD = 0.277 FEE'i CATCH BASIN FNERGY Lp$$ _.2*{�LOCITY HEAD} _,2*{ 0.277} = 0.055 ------------------------------------------------------------------------------ PIODE 5011.60 : HGL =< 333.436>;EGL= < 333.436>;FLpwLINE� < 332.390� ,�+x+**+rt+t**+xt*r*rrt*y,wrwtxtt*f*+�**ra**r*r�**r*r*w****�r*t*+*r**r*r*w***i.x*+ UPSTREPI�1 PIP,E FLOW CONTROL AATA: NODE i�IUMBER = 5011.fi0 FLOWLINE ELEVATION = 332.39 ASSiJidEB UPSTREAM CON'iROL HGL = 333.1D FOR DOWNSTREP.M RUN ANAI,YSIS ------------------------------------------------------------------------------ END OF GRADUAI,LY VARIED FLOW AAFALYSIS r � �J • > x w w++* x*** x r** f M*� w� r� r: k w f* s w* x x t* s x* y w k x** r f r r k�# x+�+ M* x f * x** r x** r*�� r w x k�* PIPE-FLOW HYDRAULICS COMPUTER PROGR.�M PACKAGE {Reference: LACFCD,LACFtD, AND OCEMA HYDRAULICS CRITERI�N) {c} Copyright 1982-2001 Advanced Engineering Software (aesl Ver. B.Q Re�ease Date: 41/O1/2001 License iD 15fl9 Ana�ysis prepared by: PRO.TECTDESIGN CONSCTI,TANTS 741 ' S' STREET, SLiITE 804 SAN DIEGO, CA 92101 619-234-0349 w++*+**++*�+x,r*****++++*++ A$SCRIPTIflN OF $`j'iJQY **trr+t***w+*****ri***+rrts ' BRE55I RA�ICH - UL7'IMA'TE CON7J�TTONS * * 5Y5TEM 500Q - LATERAL 16 ('GG' STREET CO23NECTION) * * 100-XEAR * .�..+*tt«*tx».«*.*x+.*.*..*�.+*.�,.,.+.+,..++.*�....*****.w.*�.**�..*�**.**.w F�LE NAME: 5011-16.DAT TIME/DATE O�' ST[3DY: 14:25 09/48/2002 ♦Y�1r YriF**YrYr*tF�FtYrYr t#YYr iIc * f*#t* i+Yr�r fF***yr ** Y Yi k*kfiM' kk # tt1Y #YY Y Yt t 1T�t* t! *! f**Y!i Y f*YYrt GRAAUALI.,Y VARIED FLOW ANAi,YSIS FOR PIPE 5YS'i`Er3 NODAL POINT STATiJS TABLB ' (Note: "*' indicates nodal point data used.) i7PSTREP.M RUN DOWNSTREAih ALTAI NODE MODEL PRESSURE PRES$UR�+ FLOW PRESS[TFt�+ NUMBER PROC E55 HEAD ( F'i' ) MOMENTi7I+S ( POUNDS } DEPTH ( FT } �IOMEiJ'F`iJ3+4 { pOLRdDS ) 5D12.50- 1.37 Dc 261.51 0.96* 306.34 . } FRiCTIDN . 5012.60- 1.37*Dc 261.51 1.37*pc 261.51 ------------------------------------------------------------------------------ MAXIMUM NL3MBER OF ENERGY BAL�P.NCES USED IN EACH PROFILE = 25 NOTE: STEADY FLOW HYDRAULIC H�P.D-L05S COMPUTATTQNS SASED pN THE MOST CONSERVATNE FORMZJLAE FR�M THE CURRENT LACi�D, I,ACFCD, P.DiD OCEMA DESTGN MA.23i7ALS. *....�+tit:+w+.+.**..r*.*.**..+�.,.*,�ti*W,.,..*..,.tw.�*+**.*..*.**..**+****t**�.» � DOWNSTREJ�M PIPE FLOW CON�'ROL DATA: NpDE NUMBER = 5��2.50 FLOWLZNE ELE�7ATION = 338.45 PIPE FLOW = i4�.40 CFS PIPE D�AME'i'ER = 24.00 INCHES ASSUMED DOWI3STRF�M CONiROL HGL = 339.52D FE£T "I30TE: ASSUMEA DOWNSTREAN3 COI�ITRQ� DEP'i'H ( 1. 07 FT. } I5 LE5S THAN CAITTCAF, DEPTH( 1.37 FT.) ___> CRITICAL DEPTH IS A55UMED AS DOWNSTk.EAM CdNTROL DEP'TH FOR UPSTR.£AM RT3DI ANALYSIS NODE 50�2.50 : HGL =� 339.4i4>;EGL= < 340.846>;FLOWLTNE= < 338.45D> +�++i.+t**++*x*�+*rww�*�w**x*r�r*+*+**�*wx+x>xx*x+r*x*k�r+*w*r*kr***+*xxx++***+ FLOW PROCESS FRONf NOD� 5012.50 TO NpDE 5012.60 IS COI3E = 1 UPSTR£A�f NODE 5012.60 ELEVATION = 339.36 {gl,pW IS 5�1PERCRITICALi ------------------------------------------------------------------------------ CALC[TL.ATE FRICTION L05SE5{�CFCD} : PIPE FLOW = 14.40 CFS PIPE pIAMETER = 24.OQ II3CHES PIPE LENGTH = 35.03 FEET 2+fPNN2NG'S N= 0.013flD ------------------------------------------------------------------------------ I30RMAL AEPTH(FTi = 0.87 CRITICAL DEPTH{FT) = 1.37 ` � � ==UPSTRE.�M-CONTROL`A55UMED-FLOWD£P'i'H(FT1===-=-=1=37===-==yy-`-==-------------- GRADUALLY VAitTEL1 FLOW PROPIL� COMPiJ'FED iI3FORMAT�ON: DISTANCE FROM FLOW DEP'FH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT) (FT} {FT/SEC) ENERGY{FT) MOMENTUM{pOi.J�+IDS} 0.000 1.367 6.291 1.982 251.51 4.024 1.347 5.394 1.983 251.59 0.120 1.328 5.502 1.984 261.84 0.279 1.308 fi.619 �.9$7 262.26 0.513 1.2$8 6.73fl 1.992 262.85 0.832 1.268 5.652 1.998 263.63 1.243 1.249 b.979 2.OQ5 264.61 1.759 1.229 7.111 2.D14 265.78 2.392 1.209 7.249 2.026 267.Z5 3.J.b0 �.189 7.393 2.039 268.75 4.079 �.170 7.544 2.054 270.58 5.174 1.15D 7.7d1 2.071 272_fi5 6.473 • 1.130 7.Bb6 2.p91 274.95 $.014 L 110 $.�38 2,114 277.54 9.829 �.091 8.218 2.140 280.39 13.987 �.071 8.447 2.169 283.53 14.5b4 1.057. 8.605 2.202 28b.98 17.649 1.031 8.813 2.238 290.75 21.397 1.012 9.432 2.279 294.85 25.0�4 D.992 9.261 2.324 299.32 31.825 0.972 9.503 2.3']5 304.17 35.Oi0 D.964 4.608 2.396 306.34 NODE 5412.bD : HGL =< 344.727>;EGi,= � 341.342>;FLOWLTNE= < 339.36D> . ***i� ***�kiM kYr�MYr**Yc *Yi *#i 1 YY1 Y f k Y**YY#Y1� *ikYYr4fltti� #lrYriYrYrYriF* tk*Yr�** i*i**! t�k # t*Y *�Y* f# i7P5�'REAM P�PE FIAW CONTROL DATA: 3dODE NLJMBER = 50i2.60 FLOWLINE ELEVATION = 339.36 ASSUi�SED UPSTREP.2+� CON'T'ROL HGL = 340.73 FOR DOWNSTREA..t�4 RLiN ANALY5I5 END OF GRADUALLY VARTED FLOW ANALXSIS '^'f T~y~�Y_4�LL�LLYYyy� • � *+**rx*xr*****+*r+�tvw*�**�+z*+�**+�+x*x+*�tw+tx*r��rWx�w*x*�+xew*w****v+�+*++ PIPE-FLOW HYDRAi3LIC5 COMPU�'ER PROGRAM PACKAGE (Reference: LACFCD,LACAD, AND OCEMA HYDR.AU�,ICS CRITERION) ;c} Copyright 3982-2001 Advanced Engineering Software (aes} Ver. 8.0 Aelease Date: OZ/Ol/2001 License ID k509 Analysis prepared by: PROJECTDESIGN CONSULTP.NTS 7D1 'B'� STREET, SUITE 800 SAN DIEGO, CA 92101 519-239-0349 ++**Wi*+s*++x**x�+*+*.*+++ DESCFLIPT'ION OF ST[TDY *wr***+*+i*+****x*:**r+**+ ' HAESSI RANCH - LILTIMA'i'E CO[QDITIONS * * SYSTEM 5004 - LATERF�I1 17 ('I' STREET/GREEI37iAVE CIRCLE) w * 100-YEAR * t#�t*1 f*Wit*�k �.;yr*iy �.yryr*'� *'+t��i** *tt#'Y'� 1t4+�k *4*y�s**fi}x ** �k ir** iFYrY� rtYrY� Yr*Yrk **YrY� Yrik* Yr kri f FILE S�7AME: 5000-17.AA'i' TIME/DATE pF STUDY: 14:34 D9/08/2002 +Y�yrf * Y�1r�F Y� f ir Yr� ***Yr*t4* fi�kYrY*R *yr* **Yr* YriF * ri* iF* ri Yr* * Y� tYrY�* #Yc!? f i*ti YYY t4 *f f x Yr Y Y* f*x tt *Y GRP.DUALLY VARFED FLOW ANALYSIS FQR PIPE SYSTEM NODAi� �OINT STATUS TABLE (Note: "*' indicates nodal point data�used.} UPSTREAM Rt3N DOWNS�'REA2+I AUN I30DE MODEL PRESSURE PRE55URE+ FLOW PRESStJRE+ NIJMSER PFtOCE55 HE.�D ( FT ] M�MENTUM { POUI3D5 J DEPTH { FT J NSOMENTi7M ( POTJNDS ] � 5013.14- 2.66x 252.D2 D.64 59.83 } F}�ICTION 5013.24- 2.44' 205.23 0.79 Ac 56.06 -----------------------------------------------------------_-_____�_----------- MAX�NSiTM NUMBER Q�' FNERGY BAi�AAICES iFS�A IN EACH PAOFILE = 25 NOTE: STEADY FLOW HYDR.Ai.Ti�IC HEAD-i�055 COMPU'FATIOiVS SASED ON THE �SOST CONSERVATIVE FORMULAE FROM THE C[JRRF.NT LACRD,LACFCD, AND OCEMA DESIGN MANI3ALS . � Yct* **�kY�Y * t Yr W#*�Y� �ki i� � �k *4+�k}�*1tM #� *t Y f! Y�k * f W 44*tfi'k# *�r'ki�*** # iF Yr�k�FYr iFik k Yr Yi Yc�R*#i�#}!��• DbWAIS'FREP.M PI PE FLOW CONTRQL DATA : Y30DE NL7MBER = 5013.10 FLpWLINE EI,�VA'd'ION = 345.03 P�PE FLOW = 4.20 CFS P�PE DIAMETER = 18.Q4 INCHES ASSUMEp pOWidS`i'REAM CONTROL HGL = 347.890 FEET __________________..__________....___.._____.._____-------------------------------- NODE 5013.14 : HGL =< 347.890>;EGL= < 347.978�;Fi,OW�INE- < 3�5.03D> iY� �ik*4iYi yr*i�#* f*##YCYr ***i� * fM* *iF* * *iY*i* *#** **ri *#Yr* kY� YriFfYrMMM **#*Yr** **** * titk **# *Yr* k FLOW PROCESS FROM NODE 5013_10 TO NODE 5013.24 IS CODE = 1 UPSTRERM NODE 5413.20 ELEVAT�ON = 345.52 (FLOW IS UD?1�ER PRESSUREJ ------------------------------------------------------------------------------ CAL,CLFLATE FRTCTION LpSSESSLACFCDI: PIPE FLOW = 9.20 CFS PIPE DIAt+�ETER = 38.00 INCHES PIPE LENG?`H = 43..00 FEET M.�I3idING'S N = 0.01340 SF=(Q/K}**z - (( 4.2�}/( �p5.039}]+*2 - O.Q0160 HF=L`5F = ( 41.00)*(0.�0164} � p.Qfi6 NODE 5013.2fl : HGL =< 347.956>;EGL= � 348.043>;FLOWt,INE= < 345.520> fr�r.ftt�+:*rt*x+*+x+*k.**++i*++*►r*+*x*+*+s*+*r+**r�twr+ty+**tirt+*r*r++x+ix*w+w� UPSTR£AM PIPE FLOW CON'T'RpL DA'I`A: C J � � NODE �3L7M�� = 5pZ3.20 FLUWLII�' ELEVATiON = 345.52 A55UMED UPSTitEF�M CONTROL HGL = 346.31 FOR DOWI3STREAl�1 RU23 A�1AI,YSIS END OF GR�UUUAI,LY VAR�ED FiOW ANALY$IS • � *+r**.+r*xx*r*�+w*w***t+x+rt*x++x****r�*s**x**r**rrrw+x+s*+*�***+x+x+�**�tfwx*. PIQE-^LOW HYDRAULICS CO3�iPUTER PROGAAM PACKAGE (Reference: L.ACFCD,LACRD, AND OCEMA �TYFJRAUL�CS CRITERION} (cj Capyright 1962-2001 Advanced Engineering Software (aes} Ver. 8.0 Release Da�e: O1/41/200� License Tp 1509 Anaiysis prepazed by: PROJECTDESIGN COAISUL'£ANTS 7Q1 'B' STREET, SUITE B00 5AN DIEGO, CA 921�1 619-234-0349 .�....*..Y�{�,.+..+.��,t,�x� DESCRTPTION pF STUDY .*,.***.*..�.,.�.t.+....�..* ' Bi�SSI RANCH - ULTIMATE CONi]ITIONS * * SYSTEM 50D0 - LATERAi �8 (GftEENHAVEN CIRCi,E 5'FA 3+14.85 R'Fj * * 100-YEAR * ♦,o-�+�*+**rtw+*rxrr*wtr*rrrw�ex�*��**+r++w�r+t�t+*xRr�**r�r*+*w+xr**wk�w*�rt* FILE NA�SE: 5000-18.F}AT TIt3E/BATE OF STUDY: 14:40 49/08/2002 ♦rrwr�v.*+�x�e**x,r+i**+xk*xw*,r*+**x,r*x*x+r**�****rt+*e**wrttt�*rw+�*�i.�f�+�+��+** GRAbUALLY VARiED FLOW ANALYSIS FOR PIPE SYS`I'EM NODAi POiNT STATiJS 'i'ABLE INote: '*" inc3icates nodal point data used.) UPSTREPM R[JN DOWNSTREAM R13N NODE MdDEL PRE55URE PRE55URE+ FLOW PRESSURE+ NUMBER PROCESS HEAD { FT } MOMENTL7M { POC7I3DS ) DEPTH { pT � MOMEN'i'UM ( POUNDS ) � 5015.50- D.86 Dc 70.41 0.71� 74.Od } FRTC'i'IOAI 50�.5.60- 0.86*Dc 7Q.41 0.86*Dc 7D.4� } CATCH BASIN 5D15.60- L 2E"� 38.89 0.86 Dc 24.19 ----------------------------------------------...._----------------------------- . MP.XIMU�i 23UM$ER OF ENEAGY HT�L�A�TCES l3SED iN EACH PitOFTLE = 25 NOTE : 5'iEADY FLOW HYDRAULIC HEAD-LpSS CDI�'SPUTATIOAiS BASED ON THE MOS'F COI3SERVATIVE F4Rl�SUi�AE FRdM THE CLfRRENT LAC?�D, LACFCD, P.EV77 OCEMA DESIGN MPI�JALS. *t:**x*kyr.��*,�+ay.*�aw+***+*++xx**�t*+*+rtxw*xx+x*�x**+t>x***�**r��t***�ix*wx+* DOWidSTREAM PIPE FLOW CO�I'F'ROL DATA: I30DE N[.]rFBER = 5D15.50 FLOWLINE ELEVIaTION = 350.23 PIPE FLOW = 5.00 CFS PTPE DIAMETER = 1$.40 INCHES ASSUMED DOWtdSTREAM COI3'PROL HGL = 350.460 FEET *NQTE: ASSUMED DOWNSTRFAI�! CONTROL DEPTHI 0.23 FT.) IS LESS THAi�1 CRITICAL DEPTH( 4.86 Fi'. ) __-> CRITICAL DEPTH IS A55i7MED A5 DOWNSTftF.AM CONTROL DEPTH F4R UPSTREP,NF RUI3 AAIALYS25 NQDE 5015.5D : HGL =< 350.444>;EGL= < 351.508>;FLOWLINE= < 350.23D> ,r�,.*tv.+++..,.*...***.*..*.fx*+��++*++**..:+*�*i*.....W+��t�**+****��**.*i+ww,.. FLOW PRpCESS FRpi�i NOA� 5Q15.50 TO NODE 5015.6b IS CODE = 1 U�STREA2� NOI�E 5D15.60 ELEVATION = 35D.53 {FLOW IS SUPERCRITICALI CAI�CULATE FAICTION LOS5E5(LACFCD}: PTPE FLOW = 5.0{} CFS PFPE DIAMETER = 16.OD INCHES PIPE LENG'I'H = 25 . 2b FEET P3ANIdING' S N = 0. 013 DO ------------------------------------------------___---------------------------- � � --NORNL�L-DEPTH(FT1--=-----�=69=====_-==--CRITICAL-DEPTH{FTjTyA4`-`=0�$6-====__ i3PSTREAM CONTRQL ASSUMED FLOWDEPTHIFT} - Q,S6 ---------------- GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATIO�i: DISTANCE FROM FiAW DEPTH VELpCITX SPECIFIC PRESSURE+ CONTROL{gT) (PT} (�'T/5EC) F.N�RGY(FT) MOMENTUM{POUN�S1 O.Q00 0.860 4.768 1.2�3 70.41 O.b17 D_B54 4.814 1.2I4 70.42 • O.Q69 D.847 4.$60 1.214 70.44 0.�59 0.840 4.9D7 1.214 70.47 0.292 0_834 4.956 1.215 70.52 0.472 0.827 5.Oa5 1.2�6 70.58 0.703 0.820 5.055 1.217 7�.65 0.992 D.814 5.1D7 1.2�9 70.74 i.344 D.807 5.160 1.220 70.84 1.769 0.800 5.2z3 �.222 70.9fi 2.276 0.794 5.268 I.225 71_10 2.875 0.787 5.324 1.227 71.25 3.581 0.78d 5.382 �.23D 71.42 4.413 0.773 5.44a 1.233 71.50 5.39D 0.767 5.504 1.237 71.80 6.543 0.760 5_56i �.241 72.02 7.9D8 0.753 5.624 1.245 72.25 9.535 0.']47 5.688 �.249 72.50 11.497 0.740 5.753 1.254 72.77 13.895 0.733 5.620 1.250 73.06 16.893 0.727 5.689 1.266 73.37 2D.759 D.720 5.959 1.272 73.70 � ---------25-264----------0_714------&-Q21------____1`27$-- -74_00----- NOAE 5015.60 : HGL =< 35�.390>;EGL= < 3�1.743>;F�OwLINE= � 350.530> +***+*�*,.w��*+****+********+**+**�*******.+*.*,.***�***+*+****�*+*+*+***�*** FL,OW PROCE55 FRO�I NODE 5015.60 TO NOD� 5Q15.60 IS CODE _& UPSTREAM NODE 5015.5� ELEVATION = 350.53 {FLOW IS AT CRITICAL DEPTH) ------------------------------------------------------------------------------ CALCULATE CATCH BASIN ENTRANCE LOS5E5(LACFCDj: PIPE F'I.,OW = 5.00 CFS PIPE DIAI�E�'ER = 18.00 INCHES FLOW 17ELpCITY = 4.77 FEE7'/SEC. V�LOCITY HEAD = 0.353 FEET CATCH BASIN Ei�IERGY L05S =.2*iV�LOCTTY HEA�i) _.2*( 0.353) = D.07� --------------------------------------------------------------------------__--- NODE 5a15.b0 : HGL =< 357..614>;EGL= < 351.814>;FLOWI.INE= < 350.530> *.**********�,*.t+�***+*+�.,�*******+**t+***t+**x*+.rw�.�+t**k�,r**+�***+.+*****+ UPST2:F.AM PIPE FLOW CONTROL DATA: NODE �]�[7MBER = 5015.60 FLOWLTNE ELEVATIpI3 = 350.53 ASSU�fED UPSTREAM CONTROL HGL = 351.39 FOR DOWNSTREAM RT,Ti�I ANALYSIS END OF GRAD[TALLY VA3�IED FLOW ANALYSIS � • .w...*�*.x,.,.,�,*.�,.��*�***....,..��.***t*.,��..,..***.�.*�.*x.�*,.�...�w PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AND OCEMA HYBRAULICS CRIT�RION) {c} Copyright 1982-2Q02 Advanced Engineering So�tware faes} Ver. B.a Release T}ate: Q1/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN COi+fS[TI,TANTS 701 'B' STREET, 5i3I'PE $04 SAN DIEGO, CA 921Q1 619-235-6471 • � **�r**,r*w*+rr*�+t+t+{w**** DESCRIP'!'IOI3 OF S�`LTDY *++�**t*ti*:+�a+t*********� ' BRESSI RANCH - UI,TIMATE CONDITIONS * * SYSTEM 5000 - T,ATERAL 19 (NO. 6 ON SHET 9 OF DWG 400-8C, VILLAGE GREEN * � 100-YEAR + +**�v�+*+***��+r*++ai.*+*t+t+rt*ati��rtr*�r�:s**+**�*+*a�rw�w*�*+**+*t**�*xy FII�E NAME: 5000-19. DAT 'i'IME/DA'3'E OF STUDY: 10:29 01/17/2003 Y***t*** f i f Yi �k Y y Y�Jri}#y� *Y•f *YCYc�k Y* iF Y��k f f YrYrk Yr f f k***�ktkt �Jr ** fYYy ti*1Y4 if�.##{t**# iF# iYA k ir ir GRAAUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM fFODAL POINT 5i`ATUS TABLE (13ote: '*" indi.cates nodal point data used.l UPSTREAM RLTN DOWNSTREAM RiiN NODE MbDEL PFZESSURE PRESSURE+ PLOW PRESSURE+ NL7t+�BER PROCESS HEAD ( F'i') MpMEN'I'UM ( PpUNDS } pEpTH { FT ) M04�SENTUM { pOUNDS ) 5031.10- 1.56* 100.55 fl.5$ 90.97 } FRICTION 5031.20- 1.35* } CATCH BASIN 5031.20- }..42* 76.59 �i.sa 0.66 Dc a.6s Dc 39.A0 i3.97 ----------__�------------------------------------------------------------------ MP.XIMUM NUMBER OF ENEf2GY BALANCES USED IN EACH PROFIE,E = 25 NOTE: STEADY FLOW HYDRAi3LIC H�P,TT�-LOSS COMPUTATIONS SASED OA} THE MOST CONSERVATIVE FOR?+]ULAE FROM THE CLTRRFNT LACRD,LACFCD, AND OCEMA DE5IGI3 MANUALS. **..*�*****+++�***.ww+t�f*��*�*******xx�.�*.**,.****.�**�*++.*.+�*#*+�,r.+�+wv.++.� DUWA}STREI�M PIPE FLQW CONTROL DATA: NODE NUMBER = 5031.1p FLOWI,INE ELEVATIOI3 = 363.49 P�PE FLOW = 3.20 CFS PIPE DIAME'i`E32 = 18. a0 INCHES ASSUMED DOWI3STREAM CON'£RQL HGL = 365.050 FEET ------------------------------------------------------------------------------ NOTI� 5031.10 : HGL =< 365.050�;EGL= � 365.101>;FI.�OWLINE= < 363.990> +}#; �****Yr? *YrYr ****1i tif 1*Y�k�k k2Yk�Y*+#�##** i�****Yr* **�FY iF*Yr*!�***t*#�**fY**Y tt Y ilYf FLOW PROCESS FROM NODE 5032.10 TO NODE 5Q31.20 �5 CODE = 1 UPSTRF�FIM NQDE $031.20 ELEVATION = 363.71 {FLOW SEALS EN REACH) ------------------------------------------------------------------------------- CALCULATE FRICTION LOSSES(LACFCDJ: PZPE FLOW - 3.20 CFS PIPE DTAMETEA = 18.0p INCHES PIPE �ENGTH = 22.25 FEET MANNING'S N- 0.033D0 DOWNSTREA3�7 CQNi'ROL ASSUl�3ED PRESSURE HEAD(F`F'] = 1.56 PRESSURE FLOW PROFILE COMPUTED INFORMA'i'ION: -------------------------------------------------------------------------------- � DISTANCE FROM PRESSiJRE VELOCITY SPEC�FIC PRESSURE+ CONTROL{FT} HEAII(FT) {FT/SEC] ENERGY(FT} MOMENTLTM(POUNDS) a.000 i.sbo �.s�� _sii loo.s5 6.696 1.506 1.811 1.551 93.93 -------------------------------------------____------------------------------ N�ftMAL I7EPTH{F'i') = 0.57 CRITICAL DEPTH{FT) = 0.68 _----------------------- ASSl7I�4ED DOWNS`FREAM PRESSURE HEI�D(FT} = 1.50 -------�--------------- GRADUALLY VARIED FLOW PROFILE COMPU'FED I13FORMATION_ DI5TAI3CE FROM FLOW DEPTH VELOCITY S1'ECIFIC PRESSURE+T 'Yy CONTROL{FT) (FT} (FT/SECf ENERGY(FTj MpMENTUM(POCTNDS} b.696 1.500 1.$10 1.551 93.93 �.4.266 1.457 1.820 1.519 90.39 Z3.763 1.439 1.838 1.487 86.93 Z7.218 1.442 1.862 1.456 83.59 24.641 1.369 1.89i 7..425 80.23 22.250 1.353 1.906 1..410 78.69 ------------------------------------------------------------------------------- NpDE 5031.20 : HGL =� 365.063>;EGL= < 365_120>;FLC}WE,INE= < 353.71D> .,+**+**�*.********„�*...,�+**++�**+***.*�,.,...***�+*+++�.�.ti+�+x��**.***.+*+*++* �'LOW PROCESS FROM NODE 5Q31.20 i`0 NODE 5431.20 IS CQDE = 8 UPSTREAM NODE 5031.20 ELEVATION = 363.7I fFLpW IS SUBCRITICAL} ---------------------__--------------------------------------------------------- CALCULATE CATCH BASZN E�I'I'RANCE F�055£S ( LACFCDI : PIPE FLOW = 3.20 CF5 PIPE DIAMETER = 16.00 INCHES FLOW LTELOCI7'Y = �.91 FEET/SEC. VELOCTTY HEAD = 0.056 FEET CR'f'CH BASIN ENERGY i�OSS =.2* {VELOCI�'Y HEAD} _.2* { 0. Q56) = 0.011 • ------------_------------------_------------------------------------------------ NODE 5D31.24 : HGL =< 365.131>;EGL= < 365.131>;FLOWLT�TE= � 363.710� * ***ri # �k **}Yc Yr****t#1�f�4}}}*Yr*?f f Yr�M �k f �F �k * �k***tt* * t Yr �R *�+Y#iF# **iYY� * Yr ***Y� t t* i Y#i Y1*f �Y�k UPSTftEAM PIPE FLOW COddTROL DATA: I30DE NUMSER = 5031.20 �'LOWLINE ELEVATION = 353.71 ASSiIMED LTPSTREAM CbNTROL HGL = 364.39 FOA pCK�NSTREAM RUN ANALYSZS ------------------------ END O�' GRADUALLY VARFED FLQW ANALYSIS • • ** r r w r r a� r rt++> �* r t* r M � r�* r x i� w r� r t r� r r+ x r��*+* r x x* x� x� x x i�* i r y: r�� x y f r* w r+ x+�♦ P�PE-Fi,OW HYDRA[.TE,ICS COMPiITER PROGRAt4 PACKAGE (Reference: �,ACFCD,LACRD, AND OCEMA HYpRAUi,ICS CRITERION} (c) Copyright 1982-2D03 Advanced Engkneering 5oftware (aes) Ver. 8.0 Release Date: OZ/O1/2001 License ID 1509 Analysis prepared by: PROJECTDESiGN CONSLTLTAN'i`S 701 'B' STR�ET, SLTITE 800 SAN DI�GO, CA 42141 619-234-0349 **t�r*++*�****�*w**w*r++++ DESCRIPTION OF STUDY *w***�*"'r**r+*rra++*r++w+r * BRESSI R.ANCH -- ULTINSATE CONpITIONS * * SYSTEM 500� - LATEitAL 20 [N0. 7 023 SHT. 9 OF DWG 40b-8C, VILI,AGE GREEN * * 100-YEAR * f* Y f*f �*�t4�i1 fY'Y�FYr* M�YriFYrY� Yr kiFY� �klrikYrY� Y� ik IrYrYr**k Ir#*k fit Y*1*tti� # Mri Y�lY�Y� Yr rtYrYrYr rtYrR*M'YrYrYc* FILE NAME: 5000-24.DAT TIME/DATE QF STUDY: ]4:51 49lOB/2002 +y.+.xx***w+w�*++r�t**+*y**�+*t+**rt***rr***r*+++i.rt*+**we*xxx*tx***y**ix*ti*wxrxx GiL�DUALLY VAAIED FLOW ANALYSIS FOR PIPE SYSTFM NODAL POINT STA�`US '�'ABLE {�}ote: "'�' andicates nodal point data used.) UPSTREAM RUN DOWD}S'E`REAM RtJN NODE MODEL PRESSURE PRE55URE+ FLOW PRESSURE+ NUMBER PROCESS HEP.D ( F'T? MOMENTUi+4 ( POUI3DS � DE PTH ( FT ) MOMENT47M [ POi}NDS ? 5031.50- 1.55* 93.05 D.23 49.84 ) FRIC'i'ION ) HY�sRAULIC JUMP 5031.60- � 0.55*Dc 22_94 0.55*Dc 22.44 } CATCH HASTN 5033.60- 0_79* 12.23 0.55 Dc $.2i ------------------------------------------------------------------------------- 3�FP.}CFMUM I3EJMBER OF ENERGY BA,LANCES USED IN EACH PROFILE = 25 idOTE: STEAL)Y �'LOW HYDRAULIC HEA.D-L055 CDMPUTATIONS BASED ON THE i+I05T CONSERVATIVE �'ORMULAE FftOM THE CURREI�I'i' I.ACRD, i�ACFCD, ANb OCEi+iA DESIGN MANCIALS. �ti�+�+rtwrx*wr***x*+xs****rw*******+s**:+xr**��v.wt++x+t***�rrrwwx**+**r*�w,r*,kx �aw�s�R� PIPE Fz�ow corr�rRa� pA�ra: NODE NLT�IBER = 5031.50 FLOWLTNE ELEVAT�ON = 363.50 PIPE FLQW = 2.10 CFS PIPE DIAMET'ER = 1$.00 INCHES ASSUMED DOWNSTP.EAM CONTROL HGL = 365.050 FEET NODE 5D3]..50 : HGL =< 3b5.Q50�;EGL= < 365.Q72�;k'I,pWLINE= < 353.5�Q> rt*,r*+*rtxx***y*srri+ti*i,ki�**+s:**{��y.+++*t*+****r*+txr*+�*w*trs*�**rxky*++tx+ FLOW PROCESS FROM ?dODE 5031.50 TO NODE 5031.60 ZS CODE = 1 UPSTREAt+f NODE 5031.60 ELEVATION = 3fi6.07 (HYDRAULIC JUMP OCCURS) ------------------------------------------------------------------------------ CA�,CULATE FR�CTION LOSSES(LACFCD): PIPE FLOW = 2.1a CF5 PIPE bTAMETER =�8.00 INCH£S PTPE LFNGTH = 10.28 FEET MAI�1D}ING'S N= 0.0�300 HYDRAT3L�C J[JihP: DOWI3S�'REAM RUN A.NAi.,YSIS RESUiTS NORMAL DEP'I`HIFT} = 0.20 CRTTICAL DEPTH{FT} - 0.55 C � � i3PSTREP.M CO�1'I'ROL �SSUME� FLOWDE�TH(FT) = 0.55 - ---------------------- GRP,DUALLY VARIET] FLOW PROFILE C0�IPUTED INFORMATION: DISTANCE FROM FLOW DEPTH VEI,OCITY SPECIFIC PRESSCTR£+ CON'i'ROL ( FT } ( FT J ( FT / SEC j ENERGY ( FT } 2+�OMFN'I`iJ�I ( POUNDS i D.000 0.547 3.603 0.749 22.94 O.Ofl3 0.533 3.730 0.'i44 22.96 D.0�2 � 0.519 3.864 0.751 23.04 O.D28 0.506 4.006 0.755 23.17 D.052 0.492 4.161 �.761 23.35 0.085 D.478 4.326 0.769 23.6D 0.129 0.465 4.503 0.780 23.9� 0.}.85 0.451 4.693 0.793 24.30 0.256 0.437 4.896 0.81a 24.7b 0.343 0.424 5.120 0.831 25.3� 0.451 O.Q].0 5.36� 0.85fi 25.94 0.583 0.396 5.622 0.867 26.68 0_744 0.383 5.9D7 0.925 27.53 0.941 0.369 6.218 0.974 28.50 1.181 0.355 5.559 1.024 29.6f 1.475 0.342 5.935 1.089 30.87 1.837 0.328 7.350 1.167 32.31 2.288 0.314 7.81Q 1.262 33.94 2.$55 0.301 8.323 J..377 35.81 3.582 4.267 8.698 1.5z7 37.94 4.533 0.273 9.545 1.689 40.38 5.821 0.259 10.278 1.901 43.18 7.65b Q.�45 31.114 2.7,65 46.42 14.260 Q.233 �1.99D 2.4b7 49.84 • -------------------------_______----__-_---------------------------------------- __HYDftAULIC JUMP: i1P5TREAM RUN AI3AT,Y5I5 RESULTS ---- ----- DOWNSTREAt+� CbN'PRO� ASSLTMED PRESS[JRE HEAD{gT) = 1.55 , PRESSURE FLOW PROFILE COMPUTED �NFORMA`PION: • ------------------------------------------------------------------------------ DISTA%ICE �'ROM PRESSURE VELOCITX SPECIF�C PRESSUAE+ CDNTRQL I FT J H�AII ( F'T ) {�T / SEC } ENERGY ( FT } MOMFNTLJM [ POLTNDS } D.a00 1.550 1.186 1.572 93.05 0.200 1.5D0 i.188 1.522 87.54 -- ---------�---------- ASSUMED DOWNSTREAM PAESSURE HEAD(FT) = 1.5D GRADUALLY VARIED Fi�OW PROfILE CO�fPUTED II3F'ORMATIO�I: ^'�T"'__.._____.._ _..-----------------------------------------------------__---------------------- DISTANCE FROM FLOW LIEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL{�f {FT) (FT/SEC1 ENERGY(FT) MOMEN'i'UM{POUNDS) 0.200 1.500 1.388 1.522 87.54 0.352 1.462 1.196 1.484 83.38 D.502 1.424 1.2].1 1.447 79.29 0.652 1.386 1.231 1.409 75.28 0.801 1.347 1.255 1..372 71.36 D.949 1.309 1.283 1.335 67.53 2.097 1.271 1.315 1.29B 63.82 1.244 1.233 1.35� 1.26Z 6D.21 1.394 �.195 �.391 1.225 56.73 1.535 i.157 1.435 1.169 53.38 1.678 1.119 1.485 1.153 50.16 1.621 1.081 1.540 1.117 47_OB 1.962 1_042 1.6a1 1.D62 44.15 • . 2.101 1.D04 3.669 ?.048 41.37 2.238 0.966 �.745 1.D�4 38.75 2.372 0.928 3.828 0.984 36.29 2.503 D.89D 1.922 0.947 34.Oi 2.530 0.852 2.D27 0.9I5 31.9U 2.753 0.814 2.144 0.885 29.98 2.869 0.776 2.277 0.855 28.25 2.979 0.737 2.428 0.829 26.75 3.076 0.699 2.599 0.804 25.4fi 3.165 0.661 2.796 0.783 24.41 3.236 0.523 3.024 0.7fi5 23.52 3.285 D.585 3.290 0.753 23.�1 3.304 0.547 3.603 0.749 22.94 14.28D 0.547 3.503 0.749 22.94 ------------------------�ND OF HYDR.ALFLIC JL}MP ANALYSIS--_____----____________� � PRE55URE+MOMEI�T`UM BAL,P.NCE OCCUFtS AT 1.80 FEE�' T3PST32F�M OF NODE 5D31.50 I � DOWNSTREP.M DEPTH = 3.086 FEET, IIPSTREAM C�NJTJGAT£ DEPTH = D.242 FEET --------------------------------------------------------------------------------- NODE 503�.6D : HGL =< 366.617>;EGi�- < 366.819>;FLOWLINE= < 366.Q70� x*wrt*x**++*�+*atxt***++�r�a*r*+***+*r�rfitk+**x****rr*if**+*f++w<***fisy*w**+x+ FLOW PROCE$$ FROM I301?� 5431.b0 TO NODE SD32.60 IS CODE = 8 LiPSTREAM NODE 5fl31.50 ELEVA'I`ION = 366.07 (FI,OW IS AT CRITICAL DEPTHj --------------------------------------------------------------------------------- CAi�Ci7LATE CA'�`CH BASZN EN'£�tANCE I.�OSSES (LACFCA) : P�PE FLOW = 2.10 CFS PTPE DIAMETER = 16.00 INCHES FLOW VELOCITY = 3.60 FEET/5£C. VEiOCITY HEAD = 0.202 F£E�' CATCH BASIN ENEftGY L05S =.2*(VELOCITY HEAD) _.2�( 0.202} = O.Q40 ------------------____-------__--_--------___------------------------------------- NODE 5031.6a : HGL =< 36b.859>;EGL= < 356.859�;PL04�TLII3E= < 365.470> � *a�r+�+*t�x+wxx**,w+****r�***+***,r**r*r�w+�+**ax+�x*+y***+**�r�*�+i.+�+��rr**+t*� UPSTREAM PIPB FLpw CON'T'�70L DATA: NODE NC7MBER = 5031.60 FIAWLINE ELEVATIpN = 366.47 ASSUMEA UP5'f'REAM CONTROi� HG� = 365.62 FOR DOWi3S'i`REAM RLTN ANALYSTS __-------------------------------------------------------.._--___--_____�_________ ----------------------------------------------....-------------------------------- EI3A OF GRADUALLY VARIED FLOW ANI�LYSIS . � APPENDIX 4.L11. SYSTEM 5�25 (` C' STREET) � � � *****x***}*}***�*******�#*#�*+##�xr�***w*�wx:*+*t**a+*++x*t+�r*+�r**+�*++rt�*r� PIPE-Fi,OW HYDRAULZCS COMPUTER PRpGR�M PACKAGE {Reference: LACFCD,LACRD, AND OCEMA HYDRALTL�CS CRITERION) (c} Copyright 1982-2002 Advanced Engineering Software (aesi Ver. 8.0 Release Date: 01/O1/2002 License ID 1509 Analysis prepared by: PROJECT DES�GN CONSULTANTS 7Q1 'B' STREET, SUITE 800 $AN DIEGO, CA 92101 619-235-6471 .*�t��*��*+��+��t*�+.+**�* DESCRIPTION OF STi3DY *•*�'��*++.w*�„f„****..*��+ * BRESSI RP.NCH - INTER�M CONDITIONS * �' SYS'd'EM 502 5( GARDENGA'PE ROAD ) * * ZDO-YEAA * x*wxx******+f++*+*t*+�+r++#r*+*�yy�rt*t*+*+*+,r*r*,rr+*t*w**wr*******s*�,rxr++ FILE NAME: L5025I.DAT 3'I2+FE/DATE OF STLTDY: 13:37 Q1/17/2003 tw..�++t**f***++*+++**�+**.+****�*.��****++,,*�**�+�*+w++**��*,�,�.**+..*.*tt+*+ GRADUALLY VAAIED FLOW ANALYSIS FOA PIPE SYSTEM iQODAL POINT S�`ATUS TABLE (I3ote: "�" indicates nodal point data used.) UPS'I'REAM RUN DOWNSTREAM RUN NODE MODEL PRESSURE PRESSURE+ FLOW PRE55URS+ NUMSER PROCESS HE.� ( FT} �1pt+7Et�'1'[3M { pOUNDS ) DEPTli i Fi'} MOMENTUM ( POiiNDS? . 5025.OQ- 2.90"� 1136.77 1.49 1063.19 } FRICTION 5025.10- 2.48* 976.70 1.92 Dc 955.13 ) JIJNCTION 5Q25.20- 5.42* Z630.61 1.29 1199.87 } FRICTIqN 5425.27.- 3.97* 1346.30 1.65 994.63 } MA�FHOLE 5Q25.22- 3.74"� �300.72 1.92 Dc 955.13 } FRICTION 5025.23- 9.33* 1416.28 1.92 Dc 955.13 } CATCH BASIN 5025.23- 6.67* 1110.55 1.92 Dc 180.80 �7AXIMlR+] I313MBER OF ENE3tGY BAi�AiJCES EJSEB IN EACH PROFIF�E = 25 ------------------------------------------------------------------------------- NOT�: STEADY FLOW HYDRAULIC HEI�I]-LOSS COMPUTATIONS BASED ON THE MOST CONSER�IATIVE FpRMULAE FAOM THE CURRENT LACRD,LACFCD, AND OCEMA DESIGN MANUALS. +w�w,ri.***++w*t*+*******+****+wi�*+*��*.�r.+.i�**+tttf*++******a+.+*r**�w��*e+i DOWNSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = 5025 . QO F7AWLTNE EL�7ATI01�i = 359 . 2b PIPE FLOW = 35.20 CFS PIPE DZAME�'ER = 24.Q0 INCHES ASSUMED DpWNSTREAM CpNTROL HGL = 362.160 FEET NODE 5025.OD : HGL =� 362.�60>;�GL= < 364.109>;FLOwLINE= < 359.260> *.��.,***�**++�+�...�*��***�*.**�*+�.***.*+„�*s��*+++**+��+.�**��**��ti��*�+*+ FLOW PROCESS FR�M NODE 5025.Q4 TO NODE 5425.10 I5 CODE - 1 UPSTREAM NODE 5025.14 ELEVATION = 352.27 {FLOW IS UNDE� PR£SSi3RE) • ----------------------------------------------------------------------------- � CALCULATE FRICTION LOSSES(LACFCDf: PIPE FLOW 35.2� CFS PIPE DIAMETER = 24.00 INCHES PIPE LENGTH = 94.60 FEET MANNTNG'S �� 0.0130D SF=(Q/K)**2 = ft 35.201/I 226.223)}**z = D.Q2421 HF=L*SF = I 90.50)*(0.024211 = 2.194 ------------------------------------------------------------------------------ NODE 5Q25.10 : HGL =< 364.353>;EGL= < 3b6_303>;F�OWLxNE= < 3b2.27Q> t**tt+***+**.**��**.***3+***�++*��w�*..��.*+�t�***�*�******��*****�**t**�**+� FLQW PROCESS FROM NODE 5025.10 TO NODE 5025.20 IS C4DE = 5 UPSTREI�M NQDE 5025.20 ELEVATIQN = 362.93 {��,pW I� �p� pRE554JRE) -----------------------____---------------------------------------------------- CALCULATE JUNCTION T�OSSES: PIPE FLOW DIAME`I'ER ANGLE FLOWI�YNE CRITICAL VELOCITY iCFS} (INCHES) {DEGREES} ELEVA�'�ON pEPTH{F'I'. } {F"I'/SEC) UPS'I`REAM 35.20 24.00 90.00 3fi2.93 1.92 1�.244 DOWNS`F'REAM 35.2Q 24.�0 - 362.27 1.92 11.205 LATEFtAL #1 O.QD O.OD 0.00 0.40 0.00 0.040 LATERAI� �k2 0. 4a 0. 00 0. 00 d. Q� 0. 00 0. 000 �s o.oa===4s �4u�s BaszN INPUT=== LACFCD AND OCEPiA FLOW JUNCTIOA3 FORMUi�AE USE17: DY=(Q2*V2-Q1*V1*COS{DELTAI)-Q3*V3"COS(AELTA3j� (�4*V9*COS(DELTA4}j/,({A1+A2j*�6.1)+FRICTION I,OSSES UPSTRL�AM: NSANNING'S N= Q.D1300; FRICTYOI�I SLOP� = 0.02421 DOWNSTKEAM: NiANNING'S N= 4.01304; FRICTION SLOPE = 0.02421 AVER.RGED FRTCTTON SLOPE �N JLTNCTION ASSUMED AS 0.42421 Ji7i�7C'FION LEI+3GTH = 9. pp FE�T FRICTIQN LOSSES = 0.097 FEET ENTRANCE LOSSES = 0.000 FEET JUNCTION LOSSES = (DY+HVl-IiV2)+(ENTRANCE LOSSES? J[]�7C'FION L05SE5 =-( 3�996)+(-0-000}`=_-�3`996^__«'TT______..___.. � ------------------- - _ ____--------- NODE 5025.2� : HGL =< 368.349>;EGL- < 370.29$>;FLOWt,zl�iE- < 362.930> ri Y� f**i##*##+w***'t� L t i f�kik+iFii 1Y*Y�Y Y� Y Y� * Y***#Yrir***Y� �k f 1c k Yi Yrk ikYrYrfikYr}�F*�F ri Y� iF�h *##i# #*�Y FLOW PROCESS FRQM NODE 5025.20 TO NODE 5425.2� 35 CODE = 1 UPSTREAM NODE 5Q25.21 EL�VATION = 364.56 (FLOW IS UNDER PRESSUREJ -----------------------------------___----------------------------------------- CIiLCULATE FRICTYON L055ES(i�ACFCD}: PIPE FLOW - 35.20 CFS PIP� DIAMETER = 24.00 INCHES PIPE LEIdGTH = $.25 FEET NSANNII3G'S N = 0.01300 SF=iQ/K?*'2 = {{ 35.2Q)/( 22b.225}1**2 = Q.42421 HF=L'SF = ( 8.25)*(0.02421) = 0.2D0 NQDE 5025.21 : HGL =< 368.549>;EGL= < 370.998>;FLOW.GIAiE= < 364.580> �*.**t*v��*�.++.r+.w+�+�.�+�w.�.****++*��+*+.*..*****..**�****,.*�*,.****+**++�. FLOW PROCESS FROM NpDE 5025.21 TO NODE 5025.22 IS CODE = 2 iJPSTREAM NODE 5025.22 ELEVATIQN = 364.9I (FLUW IS [INDER PRESSURE) ------------------------------------------------------------------------------ CALCULA'PE MANHOLE L05SES(LACFCD): PIPE FLOW = 35.20 CF5 P�PE DiAMETEFt = 24.00 INCHES FLOW VELOCITY = 11.20 FEE'P/SEC. VELOCI�'Y HEA17 =�.949 FEHT HL�] _ .0$*(VELOCITY HEAD} _ .05*( 1.949) = 0.097 ------------------------------------------------------------------------------ NODE 5025.22 : HGL =� 368.6A6�;EGL= � 370_596>;FiOWLINE= � 369.910> 3*f 2ik#Y11 �kYri Y i i it��r ik Yr* *i 1 Y**** ****# *#*** ilr k+Y� i?}y.* �r *####**#i�t �*f iiii+ii# t*i�+f FLOW PROCESS FROM NODE 5025.22 TO NODE 5425.23 TS CODE _� UPSTREAM 230DE 5Q25.23 ELEVATION = 3b5.41 (FLOW IS [JNDER PRESSURE) i-------------------___------------_____--------------------------------------- � CALC%FL�ATE FRICTIpN LQSSES(LACFCD}: PIPE FLpW 35.20 CFS PIPB DIAMETER = 24.00 INCHES PIPE LET}GTH = 45.04 FEET MANNING'S N= 0.013dQ S�=fQ/K1**2 = (f 35_20i/f 226.225))**2 = 0.02421 HF=L*SF = ( 45.40)*(0.02421} - 1.089 --------------------------------------��-------------------------------------- NODE 5025.23 : HGL =< 369.736>;EGL= < 371.6B5>;FLOWialNE= � 365.�10> t+*************+************�t*+#**wwtrr+t�++**�*+++*+tt+*+t*�**:ff�*f*******t FLOW PROCESS FROM NODE 5025.23 TO NOD� 5025.23 IS C�DE = 8 UPSTREP.�f NODE 5025.23 ELEVATION = 365.41 (FLOW IS LTNDER PRESSUR�) CALCULATE CATCH BASIN ENTAANCE LOSSES{�ACFCD): PIPE FLOW = 35.24 CFS PZPE DIAMETER = 29.Q0 INCHES FLOW VELOCITY = 11.24 FEET/SEC. VELOCITY HEAD = 1.949 PEET CATCH BASIN �1ERGY LOSS =.2*(VELOCITY HEP.D) _.2*( 1.949j = 0.390 ------------------------------------------------------------------------------ NODE 5025.23 : HGL =< 372.D75>;EGL= < 372.475>;FLOWLINE= < 365.4�Q> *�*****�*�*******+*+�**+�******+++**w��:t�+t*********t�*�**++++**�+**+**��*** UPSTREAM PIPE FLOW CONTROL DATA: NODE NUMBER = 5025.23 FLOWLINE ELEVATION = 365.41 A55L7P7ED UPSTRF.AM CONTAOL HG�, = 367.33 FOA DCw�iNSTi2EAM RUN ANALYSIS --------------------------------------___-------------------------------------- END OF GRADUAi�LY VARIED FI,OW ANALYSIS � . • x*x*wx*wx+**w**x**y*++**w��x***+y+*+**w�x**�*sy**rt**rx�rxw*sw*rxr�x*+*rt*ww**r� PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,i.ACRD, AND OCEMA HYDRAULICS CRITERIONJ (c) CopyrighC. 1982-2001 Advanced Engineering Software (aes) Ver. 8.0 Release Date: O1/41/2003 License In 1509 Analysis pzapared by: PRQJECTDESIGN CONST_TI,TANPS 701 `B' STREET, SUIT$ 604 SAN DIEGO, CA 9210i 619-234-D349 *t*++�r:xr*r*+*+**s*+++*+w �ESCAIP'I'ION OF ST[TDY w**»+*wf+*�v,��,r�.+t+*t**+ " BRESSI Ra.I+1CH - ULTIMATE CONDITIObiS * * SYSTEM 5025 {GARd3E23GATE ROAD1 * ' 1 D 0 -YEAFt * t*w**y*rr*+r��t�rr+rrrr*r+r+**rfr*r*r*�*x++++*w*x*x*w**wrata+w*t*t*+rr*rrtr FII,E NA�+IE: L5025.DAT TIME/DATE OF STUDY: 15:09 09/08/20Q2 .r*r**t�k*.w��+«.**+,r****...**.,rw.*****,r**w.*w.+f++*rtt.t.+w.wti.,r+.t**�.++w*w�.*� GRADL3ALLY VARIED FLOW ANAi,YSI$ FOR PIPE SYSTEM NODAL POI?d'i' STATUS TABLE (Note: '*' indicates nodal point data used.j UPSTREAM R[3N DOWNS'F`REAM RI3�1 FIODE 2+30DEL PRESSURE PRESSiJ3�+ FLOW PRESSURE+ NCFMBER PROCESS HEAD ( FT i MQMENTtJsf { p0UND5 ) bEPTH { p�' ) MOM�]TiJ�i { pOiFNDS } : 5025.p0- • 2.90* 462.7$ 0.76 279.71 } �'RICTION } HYDitA[JI,IC JL7i4P 502�.10- 1.25"�Dc 2D7.35 1.25*Dc 207.35 } JITNCTIdN 502�.20- 1.56 163.72 4.54* 177.61 ) FFt�CTIQN 5Q25.30- 1.01 Dc 122.51 4.60� 172.7.J. ) MANFiOLE SU25.40- � 1.D1 DC 122.51 Q.65' 158.67 ) FRICTION 5025.50- 1.01*Dc 122.51 1.01*Dc 122.5� ) JUNCTION 5025.60- 1.29 84.93 0.39* . 113.03 } FRICT�OPI 5025.70- O.BZ*Dc 51.34 0.81*Dc 6i.34 } CATCH BASIN 5D25.7p- 1.2i* 33.57 0.83 Dc 2i.27 MAXIMUM NU2+4BEf2 OF ENERGY SAi�ANCES USED IN EACH PROFILE = 25 NO'i'E : STEA.pY FLOW HYDRA[JZ,IC I-IEAD-LOSS COMPU'I'ATIONS BASED ON TH� MOST CONSERVA'�'I�IE FORMUi�AE FROM THE CIFRFtEN'i' LACR1}, LACFCD, AND OCEM.� DESIGN MP.N4JALS. «.+****,,.**+.**+**.��*...*.��.*..*.*�.v��.�,+++�.�+�w+***.*****�«..**.**«*.*.+*v. DOWNSTREAl�f PIPE FLOW COi3TROL DATA: NODE NLTMBEFt = 5025 . DO �'L,OWLINE ELEVAT�ON = 359.26 PIPE FLOW = 12.10 CFS PIPE DIAMETER = 29.00 INCHES ASSUMED DOWI35TREAM CONTFtOi� HGL = 362 .�60 F�ET HODE 5025.Op : HGE� = � 362.160>;EGL= � 362.39�>;FLOWL213E= < 359.2b0� • � *t*Wi**k**1fk******************f*fk*****t*YfY****t*t�!*y**�*fkk**f**�k*�MM***# FLOW PROCESS FROM NODE 5D25.D0 TD NODE 5025.10 IS CODE = 1 UPSTREAM NODE 5Q25.1D ELEVATION = 362.27 (HYDRAF3L�C �P OCCURS} ------------------------------------------------------------------------------ CALCULATE FRICTION LOSSES(TaACFCD]: PIPE FLOW = 12.�0 CFS PIPE DIAME'�ER = 24.00 INCHES PIPE LEI3GTH = 90. 60 FEET i4P.AiNING' S N = 0. Q1300 ' ---------------_-__--____------------------------------------------_--_---_______ HYDRAU�IC JUMP: DOWNS'iREAM RUI3 ANALYSIS RESULi'S ------------------------------------------------------------------------------ NORM.�I, DEPTH(FT) = ' 0.74 � CRITICAL I?EPTFi(FT) = 1.25 ------------------------ UPSTREA!-S CONTROL ASSLJMED FLOWDEPT`H(FP) = �.25 GRADUALLY VARiED FLOW PROFILE COMPUTED INF'ORMATIdN: �"��^ "" ------------------------------------------------------------------------------ DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONT�tOL ( FT i ( FT ] { FT/ gEC ) ENERGY ( FT ) MOMENTUM ( POLFi�iDS j D.D00 1.249 5.Bb2 1.793 207.35 0.026 1.229 5.976 1.784 2D7.43 0.102 - 1.208 6.095 1.786 207.69 0.234 1.188 6.220 1.789 208.13 D.429 1.168 fi.350 1.794 208.75 0.694 1.148 6.48b 1.8D1 209.56 1.D37 1.127 6.fi29 1.810 21U.58 1.467 1.107 5.778 1.821 2J.�.BQ 1.997 1.087 5.935 1.$34 213.25 2.640 1.067 7.�00 ]..85p 214.93 3.413 1.646 7.273 1.868 216.85 4.33b 1.026 7.454 1.889 219.p3 � 5.a33 1.aD6 7.645 1.914 2z1.4a 6.735 0.985 7.846 1.942 224.22 6.2$1 0.965 8.058 1.974 227.27 10.121 fl.945 8.281 2.010 230.63 12.321 Q.925 8.517 2..452 234.39 14.971 0.904 8.766 2.098 238.42 18.39$ Q.884 9.030 2.151 242.89 22.186 0.864 9.314 2.210 247.77 27.223 Q.644 9.606 2.277 253.31 33.790 Q.623 9.921 2.353 258.93 42.792 D.B03 10.255 2.437 265.27 56.26D 0.783 10.6�3 2.533 272.17 B0.716 D.752 10.994 2.64D 279.59 90.600 - 0.752 10.995 2.64}� 279.71 -------------------_----------------------------------------------------------- HYLiRALFLIC �Ti7MP: UPSTftF_AM RUN ANA�YSIS RESULTS DOWNSTREAM CONTi�OL A$SUMED PRE$$URE HEAD(FT) = 2.90 ^^^'^^^^^T' ^ _____________________________________________��cc�T�c_��a====��=_==_===�=_____ PFt�SSUR£ k'LOW PROFIL£ .COMPUTED I23FORMATION: DISTANCE FROM . PRESSURE VELQCITY SPECIFIC PRESSURE+ _ CbNTROL { �� ) }i�� { � } ( FT / SEC } ENERGY ( FT f MOMEI3TCTM I POUN�DS ) 4.000 2.900 3.852 3.�3D A62.78 29.642 2.OD4 3.852 2.23D 286.35 ___�_______��_��R�==�=--��z��=4 « ��_��________________________________ ASSUMED DOWNST'REAM PRESSURE HEAb(FT] = 2.OD ----------------------�______________�-_=====T « _,-�____--_-==�_==___==_-_=___ GRP.DUALLX VARIED FLOW PROFF�,E CaMPUTED INFORi2ATION: DISTANCE FROM FLqW DEPTH �IELpCTTX SPECiFIC PRESSURE+ i • CON'I'ROL { � ) ( FT ) { gT/ SEC J ENERGY ( FT } MOMENTL7M ( POUNDS ] 29.642 2.000 3.850 2.23� 266.35 30.58D 1.970 3.Bb2 2.202 280.75 31.472 1.94D 3.884 2.174 275.42 32.336 1.91D 3.913 2.148 270.28 33.177 1.86D 3.947 2.122 265.32 33.996 1.850 3.986 2.097 260.52 34.794 ]..820 k.�30 2.072 255.90 35.573 1.790 9.078 2.046 25�..45 36.332 1.760 4.131 2.D25 247.17 37.070 1.73D 4.189 2.D02 243.06 37.76'7 1.700 4.250 1.961 239.14 38.482 1.670 4.317 1.959 235.4� 39.153 J..540 4.388 1.939 231.87 39.749 1.610 4.464 1.919 228.53 40.417 1.580 4.544 J..901 225.44 41.005 1.550 4.631 1.8B3 222.48 41.563 1.520 4.722 1.$66 219.79 42.065 1.490 4.820 1.851 2�7.33 42.569 1.460 4.923 1.836 215.11 43.Op9 J..430 5.434 1.823 213.14 43.4D2 1.40D 5.151 J..812 2i1.43 43.741 1.370 5.275 1.802 2�0.01 A4.p21 1.340 5.4D7 1.'794 248.87 44.233 1.31� 5.548 1.7B6 208.03 44.369 1.280 5.698 1.784 247.52 49.437 �.25D 5.858 1.783 207.35 90.600 1.25Q 5.858 1.']83 207.35 -----------------------END OF HYDR.AULTC JUMP ANA.LYSiS------------------------ PRESSUAE+MOM£N`I'UM BALANC£ OCCUFLS AT 31.89 FEET UPSTR�AM OF NODE 5025.aD � DOWI35TREAM DEPT4-I = 1.925 FEET, LFPSTREAM CONJUGA'i'E DEPTH = 0.781 FEET NODE 5025.10 : HGL =< 353.519>;EGL= � 364.p53>;FLOWLINE= < 362.270> +fi***+*ww�,rw*r**w**t+++f++r*+r*+a**+.+*******+**t+itrr�*��r�+r+x+++tiw+f++++Yt Fi.OW PROCESS FRpM NOA� 5025.1D �'0 AIOAE 5025.20 ZS CODE = 5 UPSTREAM NODE 5025.2Q ELEVATION = 362.6D {FLOW IS AT CRIfiICAL DEPTH} (I30TE: POSSIBLE JUMP IN OR UPSTREAid OF STRUCTURE} CALCLTL.��'E 3Lii�TC'I'ION T.,OSS�S: PIPE FLOW DIAMETER AI3GLE FLdWLINE CRITICAi, VELOCITY {CFS) (INCHES) (DEGREES) ELEVATION DEPTHfFT.) {g'p/5EC} UPSTR£Ah4 B.�D 24.D0 . D.00 _ 362.60 1.D1 �0.581 DOWNSTREAM . 12.i0 24.00 - 352.27 1.25 5.669 LATERfiI. �1 4.40 24.00 9U.OD 362.93 0.70 4.D71 LATERAL #2 D.00 0.00 Q.00 O.DO 0.44 0.404 4� 0.00===Q5 EQUALS BASIN INP1J'I'=== LACFCD AND OCF� FT,(?W JUNCTION FORMCII�AE USEA: pY=f4z"Vz-Q1*V3*COS(DELTAII-Q3'V3*COS(DEL'�A3j- Q4*V4*C05(DELTA4)}/{(A1+A2)*Z6.1J+FRICTION LOSSES UPSTREAM: MANNING'S N= 0.0].3D0; �'R�CTION SLOPE = D.03685 DOWNSTREAM: MANNING'S N= D.01300; FR�Ci`ION SLOPE = 4.00562 AVERAGED FRIC�'ION SLOPE IN ,TUNCT�ON ASSUMED AS 0.02123 NNCTION LENGTH = 4.a0 FEET FRICTION LOSSES = D.485 FEET ENTRAiQC£ L05SES = 0.000 FEET JUNCTTON I,OSSES = (DY+HV1-HV2j+{��E �,OSSES) JLTNCTIOI3 LOSSES =( 0.871}+i 0•OOOj = 0.871 _ NODE 5D25.20 : HGL =< 363.185>;EGL= � 3fi4.924�;F'LpwLINE= � 362.600> � � r*****r**t***�******+�*+w��+axf��e**w+*ww***w**��****«*****r*t*+***t��+*wr�* FLOW PROCE55 FROM NODE 5025.20 TO NODE 5025.30 IS CODE = 1 'UPSTREP.M NODE 5025.30 ELEVATION = 372.66 {FL4W i5 SUPERCRITiCAL} -------------------------------------------------______---------------------- CALCULATE FRICTION LOSSES(LACFCDJ: PIPE FLOW = B.1D CFS PIPE DIAMETER = 2A.00 INCHES PIPE LENGTii = 272.00 FEET MANNING'S N= 0.0130Q --------------------------------------------------------------_---------------- NORMAL DEPTH{FT) = 0.58 CRITICAL DEPTH(FT) = 1.�1 UPSTREAM CON'i`ROL ASSUMED FLOWDEPTH(FT) = 0.60 -________ „�4��======��RT_«« __��_��r====T« _��___________________________ GRP.DLiALLY VAATEI} FLOW PROFILE COMPUTED INFORMAT'TON: � ----------------------------------------------------------------=------------- DISTANCE FROM �'LOW DEP'I'H VELOCZ'PY SPECIFIC PRESSL3RE+ CONTRdL{FT) (FT} {FT/SEC) ENERGY(FT) MOMFNTL7I�(POUNDS} O.00a 0.602 10.176 2.211 172.1Z 1.146 D.60I 10.�92 2.2�5 172.33 2.344 0.60� 10.209 2.220 172.55 3.598 D.6DQ 10.225 2.224 172.77 4.9i3 0.599 10.241 2.228 172.99 6.295 0.598 10.257 2.233 173.21 7.753 •0.598 10_273 2.237 173.43 9.292 0.597 1D.29a 2.242 J.73.66 10.923 D.596 10.345 2.24'7 173.BB 12.655 0.59b 1D.323 2.2�1 174.1D 14.50b D.595 10.339 2.256 174.33 16.488 fl.594 1b.355 2.250 174.56 1B.621 0.593 10.372 2.265 174.78 20.931 � 0.593 10.389 2.27p 175.01 � 23.447 0.592 10.4D5 2.274 175.24 26.210 D.591 1b.422 2.279 175.47 29.270 4.591 10.439 2.284 175.70 32.599 0.594 10.456 2.289 _ 175.93 36.595 0.589 10.473 2.293 176.16 41.�04 0.5$9 10.490 2.298 176.39 45.448 0.588 J.0.507 2.303 176.63 53.4d3 4.587 10.524 2.348 176.$6 61.473 0.587 10.541 2.313 177.10 73.440 0.586 10.558 2.3�8 � 177.33 - 93.977 4.585 10.575 2.323 177.57 272.000 a.585 10.578 2.324 177.61 ------------------------------------------------------------------------------ NODE 5025_30 : HGL =< 373.262>;EGL= < 374_871>;F'I,OY7�IN�= < 372.560> **.««**,.«.««**„+t++*+t*..**t*�.**�**..*++***«*«***+++**+**t**„**+*.«*.*+�*t**++*. Fi�OW PROCESS FROM NOAE 5D25.3Q TO NODE 5Q25.4D I5 CODE = 2 UPSTREAM NODE 5425.40 ELE`IATION = 372.99 (FLOW TS SUPERCRITICAL) ------------------------------------------------------------------------------ CAr,CL3L�ATE MANHOLE LOSSES[LACk'CDj : PIPE FLOW = B.1Q CFS PIPE DTAMETER = 24.00 INCHES I+�VERAGED VELOCITY HEAD = 1.457 FEET HMiQ =.D5*(AVERAGED VELOCITY HEAD) _.05*{ 1.457) = O.D73 ------------------------------------------------------------------------------ NODE 5025.40 : HGL =< 373.639>;�GL= < 374.943>;FLOWLINE= < 372.990> **t* *******Yr i?YYr4 Y*-! 1�#kYfrt f*ik f4f1 � f Y*Yi 4 f*Y�W yryry� y�1 yr�k�W4*�Y*} *1�t+�irtt�4*1F�r tk'tY��* W t tt�k FLOW PROCESS FROM NODE 5025.40 TO NODE 5025.50 IS CQDE = 1 UPSTAE.�M NO1]E �5D25.50 EL�TATION = 38D.81 [FLOW I5 SUPERCR�TICAL) CAi�CULA,TE �'RICTION LQ5SE5 (LACFCD) : L � � PIPE FLOW - 8.10 CF5 PIPE DIAMETER = 24-p0 INCHES PIPE LENGTH = 295.19 FEET M.�AiNING'S N 0.013�D N4RMAF, DEPTH(FT) = 4.64 CRITICAL DEPTH(F'�'} - 1.01 "` ------------------------- UPSTREAM CONTROL ASSUMED FLOWDEPTH(FTj = 1.03 -- --------------------------------- GRADUALLY VARIED FLOW PRQFILE COMPUTEA INFQRMATIQN: --------------------------------------W..----------------------__--------------- DISTANCE FROM FLOW DEP'7'H VELOC�TY SPECIFIC PRESSURE+ COI�Ti'ROL {� J { FT } ( F'i'/ 5EC ) ENERGY � Ft j NIOMENT[JI+� ( POCJNL)S ] 4,000 1.012 5.D79 1.413 122.51 O.D24 4.997 5.�76 1.413 122.56 0.092 4.982 5.277 1.415 122.70 0.206 0.967 5.392 1.417 122.93 0.377 4.952 5.492 1.420 123.25 0.605 0.937 5.605 1.425 123.67 0.900 D.922 5.724 1.431 124.20 ' 1.269 0.907 5.847 1.43$ 124.82 1.722 0.892 5.976 1.447 125.56 2. 271 0. 877 6. ].10 1.457 ].26. 42 2.926 •D.862 6.250 1.469 127.39 3.711 0.847 6.396 1.483 128.49 4.639 0.832 6.549 1.498 129.72 5.737 O.Bi7 6.709 1.516 131.10 7.�38 D.602 6.877 1.537 132.61 8.583 0.787 7.052 1.56D 134.2B 10.424 0.772 7.236 1.586 136.11 12.636 0.757 7.430 �.615 i38.12 15.322 0.742 7.633 �.647 340.30 . 18.63� 0.727 7.847 1.684 �42.68 22.746 0.712 8.071 1.724 �45.2fi '28.21i fl.697 8.308 2.77� �46.Db 35.6D9 O.fi62 8.559 k.82U 151.08 46.640 0.667 8.623 1.877 154.35 65.600 d.652 9.142 1.944 157.90 295.190 0.649 9.�b2 1.953 156.67 -------_-------------------------------------------------------------------------- NODE 5425.5D : HGL =< 38i.822y;EGL= < 382.223>;FLOWLINE= < 380.Bi0> +++***+�+x*****rt**�*ts**f**yKrtswt*►*rr*��*rs*w�*+***x*�*w*w+*+++rt*tw++tetr+r FLOW PROCESS FROM NODE 5025.5D 'I'O ?�iODE 5425.6Q I5 CODE = 5 i3PSTREAP3 NODE 5025.6Q EL�IATTON = 381.31 (FIAW IS AT CRITICAL DEPTHi (NQTE: POSSISLE JLTMP IN OR UPSTREAi�i OF STRUCTUR�) CAi,CULATE 3iJNCTION T USSES : PIP£ Fi,OW DIAN4ETER ANGL£ FLpWLINE CRIT�CAL VELOCITY {CFS) {fNCHES) (DEGREES) ELEVATION bEPTH{FT.) {�"�/SEC} UPSTREAM 4.50 18.00 BS.OQ 381.31 0.81 12.313 DOWNSTREP.M $.10 24.OD - 380.8J. 1.61 5.08D LATERAL �}. 3.60 � 16.OQ 85.00 381.31 0.72 4.260 LATERAL #2 4.Op �.00 0.00 O.OQ 0.00 O.D00 Q5 0.00=-=Q5 EQiTALS BASZN INPiJ'P=== LACFCD Ai�iD OCEMA FLOW JUNCTION FO�fiJLAE t75ED: DY=fQ2*V2-Q1*V1"COS(DEi,TAl]-Q3*V3*COS�DE�TA3)- Q4*V4"COS{DELTA4J)/((A1+A2�*16.�)+FRICTION L055ES UPSTftEAi+i: MP.�TNIDiG'S N= 0.01300; FRICTION SLOPE = 0.48352 �DOWNSTREAM: MANNING'S N= 0.013D0; FRIC'i'ION SLbPE = 0.40493 AVERAGED FRICTION SLOPE IN JiTDiCTION A55iJ3�D AS 0. D4Q23 NNCTION LENGTH = 4.00 FEET L � � PKECTION LQSSES = 0.177 FEET ENTRANCE LOSSES = D.000 FEET J[7NCTI�N L05SE5 = (DYtHV2-HV2)+(ENTRANCE LOSSES� JUNCTION LQSSES =( 1.8321+( O.D00} = 1.E32 ------------------------------------------------------------------------------ NODE 5025.6D : HGL =< 381.70D>;£GL= < 384.055>;FLOWLINE= < 361.310> +*x*x+**x**ww�***+**tx****t*tr*t*rt+t****r*yr��*+**�*w**t�r++ti+rr��+****+w+**+� FLpW PROCESS FROM NODE 5025.60 TO NODE 5025.70 zS CODE = 1 UPSTREAM NODE 5D25.74 ELEVATION = 385.90 (FLOW I5 SUPERCRITICAL) CAE,CUI.ATE FRIC�2�N LDSSES(LACFCD): PIPE FLOW = 4.5D CFS PIPE AIAMETER = 18.00 �NCHES PIPE LENGTH = 45.87 FEET MAN�ING'S N- 0.0130Q ------------------------------------------------------------------------------ NOF�AL DEPTHIFTi = 0.37 CRITFCAL DEP'I'H{FT) = 0.81 _--_________�____________________��_��_-_-_-___________________�=_==___=___=_= UPSTREAM CONTROL ASSUMED FL4WDEPTH(F"i`) = D.81 �T «__�______________________________________�_--_______=__======___�____�_____ GRADUAL�,Y VARIED FLOW PROFILE COMPUTED INFQP,rSAT�ON: ..__ ________ ________________..----------------------__.._----_-- DISTANCE FROM FI�OW DEPTH V£LOCITY SPECIFIC PRE55URE+ CONFFtpL ( FT j q FT ) {�T / 5EC ) ENERGY ( F"T' j MpIIF..NTUM ( PCiUNDS j 0.000 4.6�4 4.593 �.142 61.34 D.008 0.796 4.720 L 143 b1.38 4.033 4.779 4.854 i.145 61.52 0.07$ 0.761 4.997 3..149 61.76 4.145 0.743 5.149 1.155 52.10 4.237 0.726 5.309 1.164 62.56 0.358 0.7D6 5.480 1.175 63.�3 0.511 O.b91 5.663 1.�89 63_83 � 4.702 O.b73 5.857 1..206 64.67 0.936 0.555 5.065 1.227 65.65 1.221 0.638 6.287 1.252 66.78 1.5b6 O.b20 6.525 1.281 68.a9 1.981 0.602 6.78i 1.317 69.57 2.480 0.585 7.055 1.358 73.26 3.082 0.567 7.353 1.407 73.16 3.80B D.549 7.674 1.464 75.30 4.690 0.532 8.022 1.532 77.71 5.768 D.514 B.444 . 1.610 84.40 7.103 0.495 8.8�2 1.703 83.41 6.781 a.479 9.262 1.811 86.79 � 1D.937 U.461 9.755 1.94Q 90.57 13.�99 0.443 10.297 2.09� 94.B1 17.795 0.426 10.896 2.271 99.57 23.887 0.4D8 11.560 2.485 344.92 35.170 0.390 i2.300 2.741 2i0.45 45.670 0.390 12.309 2.745 �i1.03 NODE 5025.7D : HGL =< 386.714>;EGL= < 387.042>;FLOWLINE= � 385.9Q0> �*w��ww***r**r+t*+t**+t++t�+t*ts*t+rw*+�rr�fy.�ax+***x+***+***w+***+*****�*�*x♦ FLOW Pi�OCESS FROM NODE 5025.70 '�'0 NODE 5025.70 IS CODE = 8 i3P5TREAt+I NODE 5025.70 Ei£VATION = 365.90 (F�OW IS AT CRITTCAL DEP'I'H) ------------------------------------------------------------------------------ CALCULATE CATCH BASIN ENTRANCE LOSSES(LACFCDj: PIPE F'LOW = 4.50 CF5 PIPE D�AMET'ER = 18,OD INCHES FLpW VELOCITY = 4.59 FEET/SEC. V�LOCITY HEAD = 4.328 FEET CATCH BASIN �NERGY LOSS =.2"IVEI+OCITY HEAi1) =.2*( 0.3281 = Q.065 ------------------------------------------------------------------------------ NQDE 5425.70 : HGL =< 387.107>;EGL= < 387.107>;FLOWLINE= < 385.90D> i � *k4*******kk4**************k****i**rt�WM*#f*�#t******kk1********M*t**f*w***1**f UPSTREP.M PIPE FL4W COidTROL DATA: NODE NUMBER = 5425.7D FE�OWLINE EL�ilATION = 385.90 ASSUMED UPSTREAM CO�I'I'ROL HGL = 386.71 FOA bC7WN5'i'REAM RUN ANALYSIS - - ------------------------------------_-____ END OF GRADUALLY VARIEl7 FLOW AI3ALYSIS _ �� * Yt*�1� *iic Yc * iiY'iF** iriY��t**��kic�**yr **iFk'M'k*iF****'k##ff �#i� Y��tt*?*k Y� #+kyr+YyrifN�Li#Yf+kjr PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE fRe€erence: LACFCD,LACRD, AND OCEMA HYDRAUL�CS CAITERION) Ic) Copyright 1962-2402 Advanced EnginEering Software (aes) Ver. 8.0 Release Date: O1/01/2002 License ID 1509 Analysis prepared by: PR0�7ECT DESIGN CONSULTANTS 70� 'B' STREET, SUITE 800 SAN DIEG4, CA 9210� 619-235-647� �� J � *w,r*�+v�++*rt*+►>�***s+w+++* DESCRIPTiON OF STU�Y ww****x��+w+xx***k�*�****� * SRESSI RANCH - LiLTIMATE CON7�TTIONS "' * SYSTEM 5025 - LATERAL 1(GARDFNGATE RD 1+50 L'f`} * * 100-YEAR * *�*.+*****+**..***�***�***..�****..*�**#*.�++*,�+��+.��+*..�...*..�tt+*+*+� FILE NAME: 5025-1.�AT Tz�1E/]3ATE OF STUDY: 13:33 O1/17/20fl3 * Y� Yr Yr}Yr*Yi Yr*Y�?i *#*#*+*1 #i#yryr�F#1*yr1�kY�*1Y Y*t tti! �*t! k1r1r****Y� f�F ***YrYrY� k Yr k YrYri�lrYriF**Y� *i� _ GAADiJAI.�Y VARZED FLpW ANALYSIS FOR PIPE SYSTEM NODAL POTNT STATUS TABL£ (NoCe: '*" indicates nodal point data used.) UPSTREA2+3 RUN DOWNS`f`REAM RUN ?�IODE t40DEL PRESSURE PRESSLTRE+ �'LAW PRESSURE+ �I�IMBER PROCESS HEAD ( FT ) i+]OI+7ENTUM ( POLTIJDS ) DEPTH ( FT ) MOMENTUM ( POUNDS } 5025.20- 0.90 57.35 0.34* 100.32 } FRIC'�'IQN 5025.21- Q.72*Dc } CATCH sASIN 5D25.21- 1.04* 52.59 28.02 0.72*Dc 0.72 Dc 52.59 16.97 ------------------------------------------------------------------------------- MAXIMUE] NUMBER QF ENERGY BALAD3CE5 USED T13 EACii PitpFILE = 25 NpTE: STEADY FLOW HYDRAULIC HEAD-L055 COI�PUTATTONS gASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CURREN'P LACRD,LACFCA, AND OCF.MA pESIGN MAAi[JALS. ***+.�+*��....�.+�.*.�,�+.*+*�**t+.+**.**,.**..�***....,+.*�.*...,�*�«.,,..�**++++�� AOWNSTREAM P�P� FLOW CON'PROL DATA: NO3�E NUI+SBER = 5025.20 FLOWLINE ELEVATIOI3 = 362.60 PIPE FLAW � 9.20 CFS PIPE DIAMETER = 24.4Q INCHES ASSUMED AC?WNSTREAM CONTROL iiGL = 363.500 FEET -------------------------------------------------------------------------------- NODE 5fl25.2a : HGL =� 362.93B�;EGL= < 365.158>;FLOWLINE= < 362.600> {��r*+r+f�+***t***+�++�+xrt*iti*+x�aw+.******+wi.**t�+�+++++�++�+�,+*+++++*t+*++++t*� FLpW PiZOCE55 FROM NODE 5025.20 TO NODE 5025.21 IS COD� _% L3PSTREAM NODE 5D25.21 ELEVATION = 364.58 (FLOW I5 SUPERCRITZCALf CRLCULA'FE FRICTI�N LOSSESfLACFC�i}: PIPE FLOW = 4.20 CFS PIPE DIAMETER = 24.D0 INCHES PIPE LENG'iH = 6.25 FEET MANNTNG'S N= 0.01340 NORMAL DEPTHIFT} - Q.27 CRITICAL DEPTH(FTj = 4.72 UPSTREAM CONTROL ASSUMEIJ �'LOWDEP`i'H IFT) = 0. ]2 � __GRAAUALLY VARIED FLOW PROFILE C�MPUTED INFORMATION: DISTANCE FROM FLOW DEPTH VELOCITX SPECIFTC PRESSUFtE+ � CONTAOL(FT) (FT} {g�/SEC) ENERGY(FT} MOMENTCTM(POUNDS) 0.000 0.719 4.129 0_9$4 52.59 0.004 0.701 4.275 p.985 52.b5 0.016 D_683 4.430 0.988 52.82 0.038 4.655 4.597 0.993 53.12 0.072 0.697 4.775 1_OD1 53.5b 0.118 0.629 4.956 1.012 54.13 0.�.79 0.6Z1 5.171 1.02b 54.87 0.257 0.592 5.391 1.044 55.75 D.356 0.574 5.63D 1.067 56.84 0.478 0.55fi 5_888 1.095 56.12 0.629 0.53$ 6.167 1.129 59.54 0.814 0_520 6.471 1.171 61.33 1.039 4.502 6.803 1.221 63.3i 1.314 4.484 7.166 1.281 65.58 1.650 0.455 '1.564 1.354 66.18 2.062 Q.497 S.D03 1.442 71.14 2.571 0.429 8.488 1.549 74.52 3.205 0.411 9.027 1.677 76.36 4.003 d.393 9.629 1.$34 82.75 5.027 0.375 10.304 2.024 87.77 6.368 0.357 11.065 2.259 93.53 8.167 Q.339 11.929 2.554 lOD.15 8.250 0.338 11.952 2.557 100.32 ------------------------------------------------------------------------------ NODE 5D25.21 : HGL =� 365.299>;EGL= < 365.564�;FLOWLINE= < 369.580> � �x*��+��Wwt�**frr*r*++++****tk*�+a*wrr*a��+w��fr**�+�****�*+,r*****++*+t*+*+* FiAW PROCESS FROi� NODE 5Q25.21 TO NODE 5025.21 IS CODE = 8 UPSTREAM 13QDE 5025.21 ELEVATION = 364.58 {�'�,QW IS SUBCRITICALf ------------------------------------------------------------------------------ CALCULATE CA'i`CH SASII3 ENTRANCE LOSSESILACFCD}: PIPE FI�OW = 4.20 CF5 PIPE DIA�SETER = 24.00 INCHES FLOW VELOCITY = 4.13 FEET/SEC. VELOCITY HEAD = 0.265 FEE�' CATCH BIaSIN ENERGY LOSS =.2*(VELDCITY HEADj =.2*{ 0.265) = 0.053 NODE 5025.21 : HGL =� 365.617>,EGL= < 365.617>;FLOWLINE= < 369.580> *'k**�! 1k# tt14'4i��lr# #'1.'k#'1.* * # * * �k �k Yc*Y� *ir * ** i� * *i�iri** #*i� *1ti #ti } ##*}yr** ***Yc�k *** * * ** **i� *i� *#i� UPSTA�AM PIPE FLOW CONTROL 17ATA: NQDE Ni��IBER = 5Q25.21 F�.OWi,INE ELEVATION = 364.58 ASSUMED UPSTFt.F.AI� CON'I'ROL HGL = 3b5_3� FOR 7JClWt�iSTRE:AM RUN ANALYSIS END OF GRAD[JALLY VARIED FLOW I�NALYSIS � � *�f****M#*1**Y*i**�*�*Y*rt*�***t�*t14W*k**�fif*rt#*�*****tkwY*w*+**M*w#�**f*4**** PIPE-FLOW HYDRA[TLICS COMPUTER PROGRAM PACKAGE (Reference: LACFCD,LACRD, AN�I OCEMA HXDRACJ�,ICS CRITER�ON} Sc) Copyright 1982-2001 Ad�anced Engineering Software {aes) Ver. B.0 Release Date: 01/O1/2D01 License ID 1509 Analysis prepared by: PROJECTDESIGN CO235ULTANTS 701 'B' STi�EET, SUITE B00 sArr Dr�co, ca gziai 619-234-0349 *�***.*+v.+�++..*.,.....*�*** AESCRIPTIQN O�' STUDY ***•*'**••*"•**+*.++*+*+** * BAESSf RANCH - ULTIMATE CONi7ITIQNS * * SYSTEM 5025 - LATERP.L 2 iGARDENGATE ROAD STA 7+35 LT) * ' 100-YEAR * **+**��www.�t+**xx�*+*+w*+xy+wws�s*wxw�***x�r+*w**rrr�..y.y.w**xR*t+x,r►w*a*♦ FTLE NAME: 'S025-2.DAT TIt+3ElDA'i'E OF STUAY: 15:29 09/OB/2p02 i.,�*t�,rv.+***w*r*t*++t*+++***+++s*+rt****+*rt*y+*ti>*+►x*a.w*www**r**t**t*+*ttt**wxrt GRADUALLY VAR�ED FLOW ANALYSIS FQR PI�E SYSTEM NQi}AL PQ�NT STATUS TASLE �Note: "*" inc�icates nodal point data used.} UPSTREAM RUN DOW[dSTRE.�M RUN NODE MODEL PRESSURE PRE55URE+ FLOW ' PAESSURE+ NUMBER PROCES 5 HEAI) ( FT ) [�pMEN'T'UM ( POUNDS ) DEPTFi ( FT ) MOY+IENTUM ( PdUNDS } • 5D25.80- 0.73 Dc 47.54 a.34* 91.48 } FRICTION 5025.90- 0.73'Dc 47.54 0.73*Dc A7.54 } CATCH BASIN � 5025.90- 1.06* 25.73 D.73 Dc 16.72 MAXIMi7M NUMBEA OF ENERGY HALANCES USEi] IN FACH PROFiLE = 25 ----------------------------------------------__--__---------------------------- NQ'!'E: STEADY FLOW HYDRAULIC 4-IEAD-LOSS COhFPUTA�`IdI3S BASED ON THE MOST CONSERVAT2ITE FORMT3LAE FROM THE CURREN'E` L+AC�tD, LACFCD, AND OCEMA DESIGN MAidLTALS. ,.***�*�.**.**..*,.******�t*:.,t***+t+*.*+.+***..�.�,.�+v,*,...�..«.*.,+�,.�**.+..*... DOWNSTREAM PIPE FLOW CONTROL I}ATA: NOAE NUt+fBER = 5025.80 FLOWLINE ELEVATION = 381.30 PTPE FLOW = 3.74 CFS PIPE DIAMETER = 18.00 INCHES ASSUM£D DOWNSTR�AM CONTRpL FiGL = 387..8D4 FEET *N07'E: A55iJMED DOWNSTREA3�1 CONTRQL ]7EPTH{ 0.50 �'T.) IS LESS THP.N CRITICAL DEPTH ( 0.'13 FT. ) ___> CRI'I'TCAL DEPTH IS ASSiJAFEA A5 DOWNSTREAM CONTROL DEP'�`H F�R LiPSTREAM RUN AiJAT,YSIS ____--__------------------------------------------------------------------------ NODE 5Q25.80 : HGL =< 381.639>;EGL= < 384.OD4>;FLQYTL��NE= < 38J..300> Y!* * M t*!** y W Yr y.ik W yr�Y*tEi� t��h # Y�# * Yr* Y**�h## R Yr *YrYrYri�YrYriF* tF1r*M**�k i* i*Y *4yrf �#+* W W f Y+y.y� f yri�F* FLOW PROCESS FROM •NODE 5025. SO 'i'p �TpDE 5425.90 IS CODE _ � UPSTREP� NODE 5025.90 ELEVATIOi�I = 385.21 (FLOW IS SUPERCRITICAL) CALCULATE FRiCTION LDSSESILACFCDj: . PIPE FLOW = 3.70 CFS PIP� AIAMETER = 18.Oa INCHES PIPE LFNGTH = 32.49 FE�'I' MRNNING'S N- 0.01300 ------------------------------------------------------------------------------ r � LJ � --NORMAL_DEP'T'H(FT)_=+ " `==Q=32==--=_---=-CRITICAL-DEP'I'H(FT1=Y==-=--0-73=====__ UPSTREAM CONTRO� ASSUMEb FLOWAEPTH(FTj = D.73 -------------------- GR�DUALLY VARIED FLOW PRQFILE COPfPUTED xNFpftMA'I'IOI3: ---------------------------------------------__-_------------------------------ DISTANCE FROt+S FLOW bEPTI-� VELpCITY SPECIFIC PRESSURE+ CONTROL(FT) (FT} {gT/SEC1 ENERGY(FT} MOMENTUM(POLRJDS) 0.400 Q.735 4.296 1.022 47.54 O.OD6 0.718 4.425 1.�22 47.58 0.027 0.702 4.559 1.D25 47.70 0.062 0.685 4.702 1.029 47.90 0.116 0.669 4.854 1.035 48.20 fl.189 0.652 5.015 1.043 48.58 0.286 0.63b 5.187 1.054 49.07 0.409 0.6I9 5.371 1.d68 49.fi7 0.562 0.6D3 5.567 1.085 50.38 0.751 0.586 5.778 1.105 51.22 0.9B1 4.570 6.003 1.�30 52.19 1.260 4.553 6.245 1.160 53.31 1.597 U.537 6.507 1.195 54.59 2.004 D.521 6.764 1_237 56.04 • 2.A94 0.504 7.044 1.286 57.66 3.OB9 0.4&8 7.425 1.344 59.53 3.612 0.471 7.78b 1.413 61.61 4.700 0.455 8.179 1.444 63.96 5.BD3 0.438 8.609 1.540 6fi.59 7.193 0.922 9.081 1.703 69.55 8.985 0.405 9.642 1.838 72.87 11.375 0.389 10.178 1.998 76.62 � 34.722 0.372 10.819 2.191 8Q.85 39.845 0.356 11.533 2.423 85.64 29.359 D.339 12.336 2.7U4 91.D7 32.490 0.339 12.336 2.7fl4 9]..08 I30DE 5025.9D : HGL =< 385.945>,EGL= < 386.232>;FLOWLINE= � 385.210> +*.t.s.r*�**#v.*w+**w***.*w*w«*r*w..«.**w****t*+*t*w++*..r�r.r+****�+*.*�*�..�* FLOW PAOCE55 FROM NOD� 5025.90 'T'O i�IQDE 5425.9D IS CODE = B UPSTRE,P.I� NODE 5025.90 ELEVATIOid = 385.21 (FLOW zS AT CRITICAL DEPTH) GALCLiLATE CATCH BASIN ENTRPNCE LOSSES(LACPCD}: PTPE FTAW r 3.70 CFS PIPE DIAMET'ER = 18.00 INCHES �FiOW VELOCITY = 4.30 FEET/SEC. VEi�OCYTY H£AD = 0.287 FEET CATCii SASIt�i EN£RGY LOSS =.2*(V�LOCITY HEAD} z,2*( 0.267) = O.D57 ------------------------------------------------------------------------------ NODE 5025.94 : HGL =< 386.289>;EGL= < 36b.2$9>;FLOWiINE= < 385.210> xx,r*+*w�x*rrr*ri**t+*t:r**r*rr**trr+**�r**r+�+►r+:x*w*wx**rr****srr*i*+*rt*+tr• UPS'�'REAM PIPE FLOW CONTROL DATA: NODE NCTMBER = 5025.90 FL�WLINE ELEVATIOI3 = 365.21 ASSUMED iJPSTREAM CONTROL HGL = 385.94 FOR DOWNSTREAD4 RiT3d ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS � ***t*++*t+**�*�f�*+**+***>+t:++*r**�*�ra�*f**:aw�*t+awtiti�*�++++*+s***+f�**++� PIPE-FLOW HYDRAL]LICS COMPUTER PROGRAI+7 PACKAGE {Reference: LACFCD,LACRD, A13D OCEMA HYDRAULICS CRITER�ONj � (c1 Copyright 1982-20Q2 Advanced Engineering 5oftware {aes� Ver. 8.6 Release Date: 01la1/2002 License 3D 1549 Analysis prepared by: ProjectDesign ConsulCants 701 B 5treet, Suite B00 San Diego, CA 921Q1 *tii+***�***t*+a**++++iit*r E3E�CRIP'I'IDi� �F STI.7DY +y��:wr*f�*+��t*t*****+*** w BRESSI RANC4-I - INTERIM CONDITSOA3S * * SYSTEM 5a00 - SD FOR TEMP. DESILT. BASIN AT PP STREET KNUCKLE * * 100-YFAFt ' +ti***,rww+.x*��+***�*�*�+ar+i*ytxrtiiity**+*r*r*+t+iyy****�*�rtt�r�f*i**irf*�+ FILE iVAME: 5400-DB.DAT 7'xME/DATE pF STUDY: 13:16 01/02/2003 fY��FY�Y�ilYri**iri *1r�*i**i��hY�?Y��kiFf1 **Yr*�kYr�MiMi�*'k'k**YrYr*'M*Yrik'M1�Y�i�ir#***i�** t*!t*Y*! YYYttY* GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NODAL POINT STATi3S TABLE {Note: '*' indicates nodal point data used.} UPS�'F�EA?9 RUN DOWNSTREAM AUN NODE MQDEL PRESSUR� PRESSURE+ FLOW PKES5URE+ NUMBER PRpCESS HEAD;FT) MOMF.NTUMIPOUNDS} DEPTEi(FT) MOMEPITCJM{POUNDS} 5p14.b1- 1.33*Dc 241.40 1.33*Dc 241.4fl ) Fxzc�rzaN 5Q1Q.62- 3.D8* 422.39. 1.02 265.23 • ) MANHOLE 5a10.63- 2.78* 390.15 1.33 Dc 24�.40 ] FRICTION 5010_64- 3.52* 971.15 1.33 Dc 241.94 ] CATCH BASIN 507.0.64- 4.Q2* 4D9.79 1.33 Dc 64.QZ ------------------------------------------------------------------------------ ?�SAXIMi]M NLTMBER OF F�7ERGY BALANCES USED IN EACH PROFILE = 50 ----------------------------------------------------------------------------.._ NOTE: STEP.DY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE I�OST CONSERVATIVE FORMULAE FROM THE CUftRE�IT LACR17, LACFCD, AND OCEMA DESIGN M.a.iJ[JALS. �t+Yf***��rt**rts*+++��***�r��rt+:x*+++**w*++a.t+**a*ti�**+++**+i�w+x***,r**+**+a*�♦ DOWNS3'REAM PIPE FLOW CONTROL AATA: NQDE NLTMBER = 5d10. bl FLOWLITFE ELEVATION = 338. 40 PIPE FLOW = 12.30 CFS PIPE DIAME�'ER = 18.00 INCHES ASSUMED DOWNSTREAM CONTROL HGL = 339.330 FEET ---------------------------------------------------------------------___----____ NODE 5014.61 : HGL =< 339.330>;EGi�= < 340.�86>;FLOWLINE= < 33$.p00> t*f �k * #! �F*t1'*t t # f * t �k tY i i i 1 Y �k * yr y� *}**i�*****Yr * * *# i�*i * **#i�*i� # * * * *f?*}iFYr*�* �kf Yr** * �k *'kk FLpW PROCESS FROM [+IODE 5014.61 TO NODE 5010.52 IS CODE = 1 UPSTREAM NODE 5010.62 ELEVATIOAI = 338.45 (FLOW UNSEALS IN REACH) ------------------------------------------------------------------_---------___ CALCULATE FRICTIQN LOSSES(LACFCD}: PIPE FLOW = 12.30 CFS PIPE DIAMETER = 1$.40 II3CHE5 PIPE LENGTH = 45.a0 FEET t4ANNiNG'S N- 0.02900 _�-> NORMAL PIPEFLOW I5 PRESSURE FLOW ------------------------------------------------------------------------------- , NORMAL DEPTH(FT} = 1.50 CRITICAL DEPTH(FTj = 1.33 DOWNSTREAM CONTROL ASSiFMEb PLOWDEPTH{F'F) = 1_33 - - ---- - ____--- _______________________________ ----------- GAAIJUALLX VARIEB FI.,OW PRbFILE COMPUTED INFORMATZON: ------------------------------------------------------------------------------ DISTANCE FROM FLOW �EPTH VBLpCTTY SPECIFIC PRE5Si7RE+ COAITROL ( FT } { FT ) ( FT! SEC } EN£RGY ( F'I' } N30MEi3TLTM { POUNDS ) r1 � l� o.oao 1.330 O.Da3 1.333 0.407 1.337 0.012 1.34Q 0.02a 1.344 0.029 1.347 0.039 �.350 0.05� 1.354 0.069 1.357 0.079 1.361 0.096 1.369 0.119 1.367 0.139 1.371 0.155 1.374 0.178 1.378 0.203 1.381 0.229 1.389 0.256 1.388 0.286 1.391 0.316 1.395 0.349 1.398 0.383 1.401 0.418 1.405 0.455 1.40$ 0.494 1.412 0.534 1.415 0.576 1.418 0.620 1.422 0.665 1.425 0.712 1.429 0.760 1.432 4.810 1.435 O.B62 1.439 4.915 1.442 0.970 1.446 1.026 1.449 1.085 1.452 1.144 1.�l56 1.206 1.459 1.269 1.4b3 1.334 1.966 1.401 1.469 1.470 1.473 1.540 1.976 1.6i3 1.480 1.687 1.483 1.763 i.486 1.842 �.490 1.923 1.493 2.007 � 1.497 2.095 1.500 ___> FLOW IS UNDER PRESSURE 45.00D 3.075 �.azz 7.408 7.394 7.38Q 7.365 7.352 7_339 7.325 7.312 7.299 7.287 7.274 7.262 7.254 7.238 7.226 7.219 7.2D3 7.19i 7.1$0 7.170 7.159 7_149 7.138 7.128 7.118 7.109 7.099 7.D9Q 7.081 7.073 7.064 7.056 7.048 7.044 7.032 7.D25 7.018 7.011 7.D05 6.996 6.993 6.967 6.982 6.977 6_972 6_96B 5_9fi5 5.9b2 5.959 6.958 z 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 ia� 18b 18b 18b 187 187 187 188 188 188 189 19fl 190 191 191 192 193 199 195 196 197 198 199 24D 201 zoz 2q9 2fl5 206 208 209 211 212 219 21fi 2i7 219 221 223 22$ 227 229 231 234 236 238 241 244 246 299 252 24i.40 241.41 241.42 241.44 241.47 241.50 24Z.53 24Z.57 24�.61 24�.66 241.72 241.77 241.84 241.91 241.98 242.06 242.15 292.24 292.33 292.43 292.54 242.65 292.76 292.88 293.01 243.14 243.28 243.42 293.57 243.73 243.89 244.d5 294.22 244.44 294.59 294.78 294.97 295.18 245.39 295.6D 295.83 296.06 246.30 246_55 246_61 247.08 247.35 247.64 247.95 248.27 248.61 6.96Q 3.82$ 422.39 N0�7E 5010.62 : HGL =< 391..525>;EGL= < 342.278>;FLOWL3NB= < 338.95Q> **�«***+**.**.�****�**..****+***�*��*******,.*..*.,�**+**..*******.*.*+*.***t*t FFAW PROCESS FROM NODE 5410.62 TO NODE 5010.63 IS CODE = 2 UPSTREAM NODE 5010.63 ELEl7ATIaid - 338.78 {FLOW IS UNDER PRESSi7AE} CALCUE,A`i'E MANHOLE I,OSSES {�CFCD) : PIPE FLOW = 12.30 CFS PIPE DIAME`f'ER = 18.00 INCHES FLOW VE�OCITY = 6.96 FEET/SEC. VELOCITY HEAD = 0.752 FEET •Ht�d = .QS�(VELOCITY HEAD) _ .05*[ fl.752} = 0.038 "NODE 501D^63 � HGL =�< 341 564>;EGL= a`+392+3�5>;FLOwLT13E= � y338 780> � # * # y[ 1r * k * t * f i Y i * * * 'k * * iF M 'k iF # f� * * � # # 1r Y� # * ! Y fF iF Yr Yr Yr ir ir Yr i� Yr * * * * ri * * Y } Yr * * I� 'k # � i 'F * * Yr * M ♦ Yi > * * �r it f FLOW PROCE55 FROM NdDE 5014.b3 TO NQdE SQIQ.b4 IS CODE = 1 UP5'I'R�AM NODE 5010.64 ELEVA`I'ION = 338.98 IFLOW IS LTNDER PRESSURE] CALCULATE FRTCTION L05SES[LACFCD}: PIPE FLOW - 12.30 CFS PIPE QIANiETER = 18.00 INCHES PiPE LENGTH = 20.00 FEET MANNING'S N= 0.02400 �SF=�¢/K?*�2 = (I 12.30j/{ 55.898))"*2 = 0.04673 HF=L*5F = � 20.00}*ffl.04673} = 0.935 NODE 5010.69 : HGL =� 342.498>;EGL= < 343.250>;FLOWLINE= < 338.98p� +*�*+iW��s�wr�*�rw++�*+**+*****a*t*++t+**+t�***x+*++*+*�**+�***+xt*****�y*w*�� FLOW PROCESS FROM NODE 5014.64 TO NODE 5010.64 IS CODE = 8 UPSTREP.M NODE 5010.64 ELEVATION = 338.98 iFLQW IS UNAER PRE55URE) ___________�------------------------------------------------------------------ CALCULATE CATCIi BASIN ENTi2P.NCE LOSSES (LACFCD) : PIPE FLOW = 12.30 CFS PIPE DIAMETER = 18.00 INCHES FLOW VELOCITY = 5.96 FEET/SEC. VELOCITY 3iEAD = 0.752 FEET CATCH BASII3 ENERGY LOSS =.2"(VELOCITY H�AD) _•2*( D.752) = 4.150 NODE 5D10.64 : HGL =< 343.401>;EGL= � 343.401>;FLONTL,INE= � 338.96p> tf i t�k##*i*** �k t**#!* Y 1111�*fY�YYY#i 1 y y�4**f f**i! Y� Y! y Y Yf � i 1 f t yr�k* #****k�* *YrYrYr�k�M Y� #�F** UPSTREAM PIPE FLOW CpN'I`ROL DATA: fIODE 3�TLTMBER = 5020.64 FLOWLINE EL�IA7`ION = 338.98 ASSIiI�EED UPSTREAM CON'f`ROL HGL = 340.31 FOR DpWNSi'KEAM RLTN ANALYSIS END OF GRADUALLY VARIED FLOW ANALYSIS • • r1 L_J • . *+**f*x+<+�****+�a�***�*�t+��rrt+�a++�xt�+.ia***r*t+*++***+wx++*+*+++++*****�ww PIPE-FLOW HYDRAULICS CO2+IPUTER PROGR�M PACKAGE (Refexence: LACFCD,LACRD, AND OCEMA HYDR.AULICS CRITERIDN) � (c1 Copyright 1982-2002 Advanced Engineering Software (aes) Ver. 8.fl Release Date: O1/O1/2fl02 License ID 1509 Analysis prepared by: ProjectDesign Consu�tants 741 B Street, Suite 800 San Diego, CA 92I0�. i+i*.+*r****++**t**�r+.w**v. bESCKIPTXON OF S'£LTDY t*****+**�*w.w**+,r+*+***** ` BRESSI RANCH - EI, FUERTE ROADWAY * t SYSTEN7 600D: OS-3, PA-13 MASS GRADE DESiLT SASIN RISER * '� 10 0-XEAR STO}u5 EVEN'i` : CLEARED PND GR�ED ' C' VAi�UE * ��*****.**+**++++***f++*t+*+w+++v..w*i+«��.��fr��**��****,r�*�+**,.**.**+* FILE D3AME: P6000.DAZ` TIME/DATE OF STUDY: 12:48 12/30/2002 i� * Y� k * �k Y �1k *Yr# * # * YrYrYriFYriF** f * � Yr�k! w * #�r#t k k t *t*i**Yr#**tiii #YrY YY*Y144! *� # * Y� * Y� r f # ** i� Yr GRADi]ALLY VARIED FLOW ANALYSIS FQR PIPE SYST�I NODAL POINT 5�'ATUS TABLE (Note: "*" indicatEs nodal point data used.j UPS�'REAM R[i�I AOWNSTREAM RUN NODE MODEL PRESSURE PRESSiJRE+ FLOW PRESSURE+ NUMBER PRpCESS HEP.D(FT) MOMEN�UM(POUNDS) DEPTH(FT} MOMENTUM(POUNDS? 6Daa.90- 2.40 1054.26 0.71' 30p0.31 ) FRICT�ON 600i.aa- z.i� D� • } ,7[iAiCTIdN 6001.90- 2.17 Dc } FRICTION 6002.00- 2.17*Dc } CATCH BASYN 1036.09 1D36.09 1�36.49 1.65� 1.78* 2.17'Dc Z140.62 �492.38 1036.09 6Dfl2.00-- 3.77* 770.77 2.17 Dc 284.36 ..----------------------------------------------------------------------------- MAXIMLTM NUMBER OF ENERGY BALANCES USED IN EACH PROFILE = 25 NOTE: STEADY FLOW f-IYDRAULIC HEAb-LOSS COMPUTATIONS BASEp ON THE M05T CONSERVATIVE FORMULAE FROM THE CiTRRENT i�ACRD,LACFCD, ANI) OCEMA DESIGN MAI3iJAL5. JUNCTION Ai�IALYSIS USTNG FULL IN'I'EGRATION FO}u+FfJLATION +t*.*ti+��+*:v.**.+��*t++�++***...**�..**«.**,..*.**�*��*****.tt*++*..��..�v.w**.. DCIWNSTREAM PIPE FLOW CONTROi, DA�'A: NODE �TUrSB�R = 600Q.90 FE�OWLINE ELEVATION = 199.6Q PIPE FLOW = 41.88 CFS PIPE DIAMETER = 30_OD INCI�iES ASSLT�IED DOWNSTREAM CQNTROL HGL = 202.000 FEE'�' NODE 6400.94 : HGL =� 2D0.3�7�;EGL= < 22�.236>;FLOW�,INE= < 199.6Q0> *+�+�+t��..++�+��+t�*t+�**�„+.***��+..***.�*****.�+*****.�++++��.+�+�.�,�..+ti� FLOW PROCESS FROM NODE 64D0.90 TO NODE 6001_00 IS CODE = 1 UPSTREA3+3 NODE 6001.00 ELEVAfiION = 243.64 (FLOW IS S4JPERCRITICAL) ------------------------------------------------------------------------------ CALCULATE FRICTION LQSSES(LAC�'CD): PEPE FLOW = 41.88 CF5 PIPE DIAMETER = 30.00 INCHES PIPE LF,NGT}i = 103 . 00 FEET MP.IdNING' S N = 0. 0�340 NORMAL DEPTH ( FT} - 0. 67 CRIi'iCAL I3EPTH { F'f') = 2. l� ___________________________��_______===____====_=__========__________________ --- __[JPSTRF..AM CONTROL ASSUhI�D FLOWDEPTH (FT} - 1 .66 ----------------------------------------------------------------------- GR.ADUALLY VARIED FLOW PRO�'ILE COMPUTED INFORMATION: DISTANCE FROM FLOW DEPT1-Y VELOCITY SPECIFIC PRESS�JRE+ CONTROL ( F'T' ) ( FT J { FT / S EC j Ei3ERGY ( FT j MOMEIJ'PUM I P011NDS } 0.000 1.657 12.129 3.991 114Q.b2 0.220 1.617 12.963 4.031 �159.76 4.472 1.578 Z2.826 4.134 1182.03 a.�61 1.538 33.214 4.25i 1204.59 • 1.D90 1.499 23.629 4.385 1230.62 1.468 �.459 14.075 4.537 1259.32 1.899 1.920 14.553 4.7�p 1290.93 � 2.394 1.380 15.067 4.9D7 1325.70 2.960 1.340 15.621 5_132 1363.92 3.612 1.301 16.219 5.3B8 1405.94 9.364 1.261 16.865 5.6B0 1452.12 5.234 1.222 17.564 5.015 1502.92 5.245 1.182 1B.3Z4 6.349 1558.84 7.427 1.143 19.151 5.841 1620.45 8.8�8 1.103 20.453 7.351 lb$8.44 10.466 1.D63 21.041 7.943 1763.61 12.439 1.024 22.32b 8.530 1845.88 14.827 0.964 23.321 9.935 1939.35 17.760 0.945 29.643 ZQ.380 2092.33 21.430 0.905 26.110 11.498 2157.9i 26.137 O.Bb6 27.747 12,828 2286.97 32.389 Q.826 29.582 14.423 2432.82 41.141 �.787 31.650 16.351 2596.3a 54.547 Q.747 33.994 18.7p2 2783.43 79.534 0.707 36.668 21.599 2997.63 103.000 0.707 36.7D2 21.636 3000.31 ------------------------------------------------------------------------------ � NODE 5�02.00 : HGL =< 295.297>;EGL= < 247.581>;FLOWLINE= < 243.640> w****�s*f**t**y+rf�Wwt*�*�+wrtaw**+*�a++**r*t+�+itiya*W��*�f******fa�*iyyrt��x FLQW PROCESS FROM NOAE 6001.00 TO NODE 6001.9Q FS COpE = 5 UPSTREAM NpDE 6001.90 ELEVAT30N = 243.97 (F�OW IS SUPERCRiTICAL} • CALCULATE JUNCTIbN L05SES: . PIP� FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCITY iCFS} {�NCHES) (DEGREESi ELEVATION DEP'I'H{FT.j (FT/SEC} UPSTREAM 4i.88 30.00 0.00 293.97 2.�7 11.186 DOWNST]2EAM 9Z.$$ 30.Ofl - 243.59 2_17 12.126 LA3'ERAL #1 d.00 0.00 0.00 0.00 D.04 0.000 LATERAL #2 0.04 0.00 O.OQ p.Ofl O.DQ p.000 Q5 0.04===Q5 E(?UAI,S BASIN FNPUT=== �CiIJCTION ANALYSIS USING FULL INTEGRATION FORMULATIdN UPSTREAM: MANNING'S N= O.Q1300; FRICTION SLOPE = O.D1418 DOWNSTFZEAM: MF.NNING'S N= 0.013DQ; FRICTION SLOPE = 0.01725 AVERAGED FRICTION SLpPE IN JUI3CTION ASSi7MED AS Q_01572 JUNCTION LENGTH = 9.00 FEET FRICTION i.OSSES = 0.053 FEET EN'd'RP.NCE LOSSES = D. Q00 FEET .TUNCTION LOSSES = ( TftANSITION LOSS } + ( FRTC'I'ION LOSS } �+ ( �Z'Rp,NCE LOSSES j ,7UNCTTpN LOSSES � f 0.�52}+( 0.063}+� 0.04Dj = Q.115 NQDE 6��.90 : HGL =< 245.752>;EGi,= < 247.595>;FLOWLINE= <�F243.974> �*+***+++*+r********f*.v��w***++*****+..rr*tt*+*f****rwrf+++**+x�++*****+r*w+�� FLOW PROCESS FROM NObE 6aa�.9a TO NODE 6002.00 TS COi�E = 1 EIPSTREA�7 NODE 6002.d0 ELEVATION = 249.57 (FLOW IS SUPERCRT'I'TCAL) CALCULATE FRICTION LOSSES(LACFCD): PIPE FLOW - 41.88 CFS PIPE DIAMETER = 30.D0 INCHES PIPE LENGTH = 30.OD FEET N3ANNING'S N= 0.0130D NOFtN1AL DEPTH(FT) = 1_57 CRITICAL DEPTH{FT} = 2.17 __ �----------------- UPSTREAt+3 CONTROL-ASSLTMED FLOWDEPTH ( FT }= 2. 17 -------------- _____---------------------------------------------__..__-- GRADiJALLY VARIED FLOW PROFILE COMPUTED INFORMATION: DTSTANCE PROM FLOW BEPTH VELOCITY SPECIFIC PAE55URE+ CONTROL(FTj (FT) (FT/SEC) ENEFtGY(FT} MOMENTUMfP0UND5] 0.000 2.16$ 9.259 3.500 2035.09 0.066 2.144 9.344 3.501 1036.28 0.274 2.120 9_933 3.5D3 1p36.86 0.622 2.497 9.525 3.5�6 1037_84 1.132 2.p73 9.622 3.511 1039.21 � �.614 2.049 9.723 3.5�8 1D40.99 2.685 2.025 9.828 3.526 1043.19 3•759 2.001 9.938 3.535 1�45.62 5.a72 1.978 �0.052 3.548 1d48.69 6.637 1.954 10.171 3.561 1052.41 8.492 L 934 10.295 3.577 1056.39 10.67b 1.946 10.429 3.595 1060.84 33•238 1.883 10.558 3.615 1065.79 15.239 1.859 10.697 3.637 1071.24 19.756 1.835 10.841 3.661 1077,21 23.887 1.811 10.992 3.b89 1083.73 26.7b5 1.788 11.148 3.719 109fl.BD 30.00D 1.762 �1.182 3.725 �492.38 NODE 6002.Q0 : HGL =� 245.738>;EGL=`<� 248 D70>;FLOWLINE= � 244.570> ******��***.�ww�*�*****�***>»*****�***�*�*�*t**w��***�**�tt**�f*+******�**+*w FLOW PRpCESS FROM NODE 60Q2.00 TO NODE 6D02_00 IS CODE = B UPSTREAhf NODE 6002.00 EL�VATION = 244.57 (FLOW LTNSF.ALS IN REACH} ----------------------------- CALCUI�A'Z'E CATCH BASTN FNTRANCE LOSSES(LACFCD): PIPE FLOW = 41.88 CFS PIPE DIAMETER = 3p,p0 INCHES FLOW VELOCITY = 9,26 FEET/SEC. VELOCITY HEAD = 1.332 FEET CATCH HASIN ENERGY LOSS =.2'�{��,pCi7*y HEAD) -.2*( 1.332? = 0.266 -------------------------------� NODE 6Q42_OD : HGL =< 2A8.336>;EGL= � 246.336>;FLOWLINE= < 244.570> �**��,r+**�**�*��**.��w*,r***�,.*,«*t*�+v�ww�***+*,,*,.*��*f�*****�,...*��+x�*r+****** UPSTREAM PIPE FLOW CO[dTROL DATA: �NOpE NUMBER = 6dQ2.OQ FI,OWLIAIE ELEVAT�pN = 244.57 ASSUME�} UPSTREAM CON'I'ROL HGL = 246.74 FOR DOWNSTR�'.AM RUN ANALYSzS ----------------------------------------- END OF GRADUALLY VARIEI7 FLOW ANALYSIS r� L_J � * * ? fi * * ? * * k * # 1 i � * * * * f Y k t Y Y 1 t # t * k * f t * * * ? * * � * * � f f * f k * * * * * * * * * * # # * * * rt * * * * * � i 1 # # * * * PIPE-FLOW HYDR.AULTCS COMP4T'PER PROGRAM PACKAGE (Reference: LACFCD,LACAD, AND OCEMA HYDRAULICS CRTTERZON) (c) Copyright 1962-2002 Advanced Eng�neering Software (aes) Ver. 8.0 Release �ate: O1/O1/2042 License ID �509 Analysis prepared by: PR0.7EC'F D�SIGN CONSUL�'ANTS 701 'B' STREET, Si7ITE 8Q0 SAN DIEGO, CA 92101 619-235-647� +**+++�+ait+++******.+*++* DE5CKIPTIOi3 OF' STUDY �v.��rt>�+++*>��*�*+*+,r,r*� ' BRESSI RANCH - EL FUERTE ROADWAY * * SYSTEM 6000: OS-3, PA-13 TO EL FUERTE SYS�'EM * * 140-YEAR STORr7 EVENT - ULTIMATE CONDITIONS * *�!t**t�kt **t*i *i i tti! �k! t Y i Y! rt Y rt 1#Yf YrYrtt * Y� Y� * irlr yr�k **�lr*!�k** #**� � t+** tttt*�rttt** FILE NAME: P6000E7.DAT TIME/DA'I'E OF ST�7DY: 73:24 Q1/21/2003 .**+*+*�*.***+��******...**+*.....,*�+**<*+*fi*�*�****i�t**+**.+�+*+*�*,r+,r�*�** GRADUALLY VARiED FE,OW ANALYSIS FflK PIPE SYSTEM NODAL POINT STATUS TABLE (Note: "*" indicates nodal point data used.} UPSTREAM RUN DOWNSTRE7IM RUN NODE MODEL PRESSURE PRESSURE+ FLC3W PRESSURE+ Ni3[�EBER PR�CESS HEAD ( F'i' } M0�7E33'I'1FM { POUNDS ) DEPTH ( FT j MOMENTi3M ( POUNDS i � 6000.9Q- 2.4D 1fi98.53 0.84* 4538.10 ] FRICT�ON 6001.00- 2.38 Dc 1b98.22 2.03* 1773..93 ) 3LTNCTION 5D01.94- 2.38 Dc 1b98.22 2.20� 1718.89 } FRICTION 6002.oa- z.3s�D� I698.22 2.3s*�� i�sa.22 } CA'i'CH BASIN 6002.a0- 5.08* 1171.81 � 2.38 Dc 346.10 MAXXMUM NUMBER OF ENERGY HALANCES USED IN EACH PRpFTLE = 25 NOTE : STEADY F%OW HYDRAUE�IC HEAD-LOSS COI+SP[)'I'ATZOPIS BASED QN THE MOST CONSERVATEVE FQR23ULAE FROM THE CURRENT LACRD, I..ACFCD, P,�iD OCEMA DESIGN MP.NL7ALS . JUNCTIDN ANALYSIS USIAiG FULL INTEGAATION FORMULATION t**++*+*�***+*.**�tt��,�..�.��.:**t**+��t*«+�*�+**�*��*+�+.,+.f+:�**++�**** DOW�75TREAM PIPE FLOW COI�3'T'ROL DATA: NODE N[JMBER =�6000.9Q FLOWLINE ELEVATION = 199.5Q PTPE FL�W = 58.00 CFS PIPE DIAMETER = 30.00 INCH�S ASSUMED DQWNSTREAM CbNTROL HGL = 2fl2.fl0a FEET ------------------------------------------------------------------------------ NODE 6000.90 : HGL =< 240.439>;EGL= < 225.404>;FLL3WLI33E= < 199.600> k�k*4 fy�i+�FiFi*�l Y*!� i�#f �F#***** * *###*i� **#'k �'t'k###�tE*y'��*'kY�YiFiFi***# *�M i�#** * **#+#+* # *#Yr FLOW PROCESS FROM NODE 600D.90 TO N4DE 6D01.Op IS CODE _� UPSTREAM NODE 60a1.00 ELEVATIOId = 243.64 (FLOW I5 SUPERCRITICAL} ------------------------------------------------------------------------------ CALCIFLATE FRICTION LOSSES(LACFCDJ: � PIPE FLpW = 58.00 CFS P�PE DIAMETER = 30`00 TNCH�S PIPE LENGTH � 103.00 FEET MANNING'S N 0.033pD � ------------------------------------------------------------------------------ NORMAL DEPTH(FT} = 0.79 CRITICAL DEPTHfFT} = 2.38 -----------------------_-------------------------------------------------------- ________-_--__------------------------------------------------------------------- UPSTREAM CONTROL ASSUMED FLOWDEPTH(FT} = 2.03 ------------------------------------------------------------------------------ ------------------ --__-___----_-__--------------------------__--____---------- GRA1]UALLY VARI�IJ FLOW PROFILE COI�fPUTED INF'ORMATION: ------------------------------------------------------------------------------ DI5TP33CE FROM FLQW DEP'i'H VELQCIT7C SPECIFIC PRESSDRE+ CONTROLfFTj (FT) (FT/S�C} ENERGYGFT} M4MENTUM(POLFNi}S) 4.000 2.039 13.558 4_89D 1771.93 0.214 1.989 13.879 4.977 1794.87 0.467 1.939 14.228 5.OB0 1821.28 0.763 1.8$5 14.645 5.199 1851.3$ �.109 1.835 15.0�7 5.339 1865.42 �.511 1.785 15.463 5.500 1923.68 I.976 1.']35 15.945 5.6$b 1966.52 2.515 �.685 16.470 5.900 2014.31 3.134 1.63b 17.Q39 6_145 2067.50 3.863 1.585 17.657 6.430 2126.6� 4.703 L 53b �8.329 6.7Sfi 2192.22 5.683 3.485 19.062 7.132 2265.0� 5.828 Z.437 19.863 . 7.567 2345.79 8.174 �.387 2D.740 8.D70 2435.4b 9.765 1.337 21.741 8.655 2535.12 11.661 1.28� 22.760 9.336 2646.03 13.941 1.238 23.929 10.139 2769.69 16.719 1.188 25.223 i�.073 2907.90 20.13b 1.138 26.663 Z2.189 3062.84 24.439 1.D68 28.270 �3.50b 3236.99 29.985 1.Q36 30.074 15.a91 3433.63 . 37.38b 0.969 32.109 1.7.007 3656.58 47.801 0.939 34.417 19.343 3910.68 63.891 0.889 37.052 22.220 4201.96 93.902 0.639 40.084 25.$04 9538.09 103.QQ0 0.639 4D.084 25.804 9538.10 NODE 6001.00 : HGL =< 245.674>;EGL= < 248.530>;FLOWI.INE= < 243.640> *+***+t{**++�++++,.��*...*...*.***...***�*.***�+...+++**+***.*��*+***.*�**.*t*+�* F7AW PROCESS FROI� NODE 6001.00 TO NODE 6001.90 I5 CODE = 5 UPSTREP,M NODE 60fl1.90 ELEVATIOTF = 243.97 (FF�OW IS SETPERCRYTICAL) ------------------------------------------------------------------------------ CALCULATE Ji3NCTI0N LOSSES: PIPE � FLOW DiAMETER ANGLE FLOWLINE CRITICAL VELOCT'T'Y {CFSj {INCHES) {DEGREES} ELEVATION DEPTH{FT.) (FT/SEC) UPSTREAM 58.D0 30.QQ a.ao 243.97 2.38 12.687 DOWNSTREAM 58.D0 30.Q0 - 243.64 2.38 13.562 L�ATERAL 111 0.00 O.pa 0.00 0.00 O.QO 4.OD0 LATERAL #2 0.00 0.00 0.00 Q.00 O.aO 0.000 45 O.Ofl===QS EQUALS BASIAi iNPl1'I'=== JUNCTION ANALY5I5 iJSING FULL II3'I'EGRATION FORMULATION UPSTREAM: i+3F.i�iNIi�iG'S N= 0.013�0; FRICTION SLOPE = 0.0].SO1 DOWNSTREAM: MANNING'S N= D.01300; �'RICTTON SLpPE = 0.02027 AVERAGED FRTCTION SLQPE IN JUNCTIO�F ASSUMED AS D.01914 Ji3PTCTION �,EI�iGTH = 4.00 FEET FRICTION LOSSES = 0.077 FEET ENTRa,NCE L05SE5 = O.QpO FEET JUNCTION LOSSES ={TiZANSITTON L05S}+(FF2�CTION E,O55)+(ENTRANCE LOSSES) - ,7[TNC`I'TpN LOSSES = { 0 . 061) + ( 0 . 077 ? } i 4 . a09) = 0 . 137 ------------------------------------___...._------__-__-------------------------- • NODE 600L 94 : HGL =< 246.168>;EGL= < 248.667>;FLOWLINE= < 243_970> � r++�*x***�ir+*+�*t�tir��*irr�t�+w+t�*+++++t*rr*tft+**�f*+*++s>w*�x++�**+*�+*+ FLQW PROCES$ FRO� NODE 60Q1.90 TQ NODE 6002.00 IS CODE = I UPSTRF�iM NODE 6002.D0 ELEVATION = 294.57 (FLOW IS SUPERCRITICAI,) ------------------------------------------------�_-__-_-_--_-__--------------- CALCULATE FRICTION L05SES(i�ACFCD): PIPE FLOW = 58.00 CFS PIPE DIAMETER = 3fl.00 INCHES PIPE LENGTH = 30.OD FEET MANNENG'S N= 0.41300 NORMAL DEPTH(FT} - 2.05 CRI`iICAL DEPTH(FT} - 2.38 UPSTREAM CONTR�L A55LJ�IED FLOWDEPTH(FT} = 2.38 ------------------------------------------------------------------------------ -------------------------__-_�-_--_--__---------_----_-_-___----------------------- GRADUALLY VARXED FI.,OW PROFILE CO[�3PUTED II+iFORMATION: _-____------------------------------------------------------------------------- DISTANCE FRONI FLOW DEPTH VELOCITY SPECIFFC PRESSURE+ CONTROLSFT} �FT) (FT/SEC} ENERGY{�j MOMENTUM(POSJNDS) 0.000 2.379 12.026 4.626 1698.22 0.14'7 2.366 12_�62 4.527 1698.34 0.562 2.353 12_101 A.526 1698.69 1.296 2.339 J.2.141 4.630 1699.27 2.290 2_326 12.163 9.632 1700.07 3.567 2.313 12.227 9.636 1701.09 5.Z39 2.300 12.273 9.640 1702.33 7.019 2.287 12.320 9.645 1703.78 9.227 2.273 12.359 9.651 1705.43 11.789 2.260 12.920 4.657 1707.30 Z9.'�4Q 2.247 i2.973 4.664 1709.37 Z8.12D 2.23q i2.527 4.672 1711.66 2�.983 2_221 12.583 4.681 1719.�9 � 26.397 2.2Q7 12.641 4.690 1716.84 30.000 2.198 12.683 4.697 1718.89 ------------------------------------------------------------------------------ NODE 6002.00 : HGL =� 246.949>;EGE,= < 249_196>;FLpWLINE= � 299.570> ! 1tt i YYi t iti Yr Y 1 i Y Y 1�kYiFfit W+}*i}�.#�.�k#�Jr*�#it�ktffi�Jr#* #*# t**YrYr�F �r f*** t*��F+***** **** FLOW PROCESS FRQM NpDE 6002.00 TO NpDE b002.00 IS CODE = 8 UPS'I'REAM NODE 5Q02.00 ELEVATION = 249.57 (FLOW UNSEALS iN ftEACH} CALCULA'TE CATCH BASIN ENTRANCE LOSSESILACFCD): QIPE FLOW = 58.00 CFS PIPE DIAi+�ETER = 30.00 INCHES FLOW VELOCITY = 12.03 FEET/SEC. VELDCITY HF,I1�J = 2.297 FEET CATCH BASIN ENERGY L05S =.2*(VELOCITY HEAD) _•2*I Z-247) � 0.449 ------------------------------------------------------------------------------ NODE 60a2.00 : HGL =< 249.646>;EGL= � 244.646>;FLOWi,INE= < 244.570> ��.***++**+�+++�+**�,,�w+.w��+****��,��.�w�*��t�*w***t**.��**��t.****��** UPSTREA3�1 PIPE FLOW CONTRpL DATA: NpDE NUMBER = 6d02.00 FLOWi�INE F�,EVATIbN = 249.57 ASSUMED UPSTREAM CONTROL HGL = 246.95 FOR DOWNSTREAM RUN AAIALYSTS _-__---_____..------------------------------------------------------------------ --------------------------------------------------------------___-------------- Ei3D OF GRADUALLY VARIED FLOW ANALYSIS • !� APPENDIX 4.LI2 SYSTEM 7000 � � • W } i i * * # * * f # * N * * ! * * k * w * * * * # i * * � * * } t t 1 t � * 1 � * t * * f + * � * � 1 � � + # f � * * * 1 * f * * * * * * * * * * w � � * PIPE-FLOW HYDKRULICS C4MPUTEA PROGRAM PACKAGE {Reference: �,ACFCi?,i�ACRD, AND OCEMA HYflRAULiCS CRITERIpN) (c) Copyright 1982-2002 Advanced Engineering Software {aes) Ver. 8.0 Release Date: Q1/O1/24Q2 License ID 1509 Analysis prepared by: PR0�7ECT DESTGN CONS[TLTT�NTS 7Q1 'B' STREET, SUITE 80D 5AN DIEGO, CA 92101 6I9-235-6471 ******ftt+�*tti*r+wf*v��*y.* ��S�R�PTI�I3 �F S'PLTI}Y *!rk**YrkYr*it*�k#ttifYfi�kYY## � BRESS� RANCH-IN'I'/ULT CQNfYi'IONS-Si'ARTIFFG W5=140.40 PER SIiT 9. DWG 397-2J " * SYST�M 70DD: SD LOCATED AT SOLTTHWEST CORNER OF PA-12 {N0. 1, 2, 3 PER " * SIi�' 20 OF DWG. 400-BC? - 100-YEAA STORM EVEI3'I' * *i.******�*+,tx+**�****+*++++t*++*at:yi*rtx*t+r*+**r�*+�+*,�ar+a++*�i��wxx+x+++ FILE NAME: 7400-1I.DAT TIME/DATE OF STUDY: 14:19 01/17/2003 * r + * + + * t + y i t * r s * * + y.f * t � * a + ,t,t * * * a * � + x x + x ,t r + * * ,t * x # iF * * } *�k Y��k * * * # Y * i Y ! t Y t Y ? Y Y i * * y i * GRADUALLY VARIED FLOW ANRLYSIS FOR PIPE SYSTEM NODAL POINT STATUS TASLE (NoCe: '*" indicates nvdal point data used.l UPSTRF.AM Ri]iV DOWNSTREAM RUN NODE MODEL PRESSURE PRESSUR£+ FLpW PRESSURE+ N[JMBER PROCESS HEAD(FT} MOMENTUM(POUNDS) DEp'I'H{��j MOMENTUM(POLTNDS) • 7000.40- 2.50� 598_Ofi L 48 4B5.67 ) Ji7t3CTION 704�.QQ- 2.A4* 587.02 1.31 516.71 ] FRICT14N 70a2.OQ- 1.92* 488.61 1.68 Dc 479.95 ) �UNCTION • 7D03.D0- 3.21 736.98 0.59* 1243.11 } FRECTION 70D4.00- �.66 Dc 974_95 1.39* 498.76 } ,TUNCTION 70D5.D0- 1.68*Dc 474.95 1.66*Dc 974.95 } FRICTION 7006.00- 1.78* 477.4� 1.68 Dc 474.45 } CATCH BASIN 70Q6.00- 2.83* 359.32 1.b8 Dc 136.18 MAXIMU�I N13MBER OP EPiiERGY SALA33CES USED IN EACH PAOFFLE = 25 NOTE: STF�pY FLOW HYDRAULIC HE.�D-LOSS COMPUTATIONS BASED ON THE MbST CONSERVATIVE FORNf[7LAE FROM THE CURREAIT LACRD, LACFCD, AND OCF.MA DESIGN MANUALS. **�kYrkikk*�*ii!*#141l�i*1r**# ri�k*fi* * i� *it*#*#ii�i}*Y�k# i�i*i� ii iFri fiF****Y��1�t tYritf Y�Y�k ti*tt DOWNSTREAM PIPE FLOW CONTROL DATA: NQDE NUMBER = 7Q4d.OD FLOWLINE ELEVATION = 137.50 PIPE FLOW = 22.20 CFS PIPE DIAMETER = 24.00 INCHES ASSUMED DOWNSTREAM CONT'RQL HGL = 140.00D FEE1' NODE 7000.dd : HGU =< 140.000>;EGL= � 140.775>;FLOWLINE= < 137.5D0> �t+++#�*.+.�***�...**�*.f***.*.+�.+*.�..�*�*�+++****+�*:�*+..�++.�»�*+*�..�.** • FLOW PROCESS F'ROM �IODE 7000.00 TO NODE 7001.00 IS CdDE � S • UPSTRE.�M NODE 700�.00 ELEVATION = ?37.83 IFLOW IS LTNDER PRESSUREa ----------- CALCULATE JUNCTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLINE CRITICAL VELOCITY (CFS} (INCHES) (DEGREESj ELEVATEON DEQTH(FT_) (FT/SEC) EiPSTREAM 22.24 29.40 33.04 I37.83 1.68 7.066 DpW�TSTREAM 22.20 29.00 - 137,50 1.b8 7.466 LA`rERAL #1 O.flO a.ao O.OD 0.00 D.00 �.400 LATERAL �a o.00 a.aa a.aa o.00 o.oa o.aao Q5 0.4D===QS EQUAi�S BASIN INPUT=== LACFCI7 AND OCEMA FLOW Jf7NCTI0N PORMi]I�AE USED: DY=(Q2*V2-Q1*V1*COS{DEL'I'A1)-Q3*V3*COS(DELTA3)- Q4*V4*COSfDEE,TA4)}/IjA1+A2)*16.1}+FRICi'ION i3OSSES [iPSTREAM: MANNXNG'S N= 0.01300; FRICTIpN SLOPE = 0.44963 DOWNSTREAM: MP,t3NING'S N= 0.01300; FRIC7'TON SLOPE = a.00963 AVERAGED FRICT�ON SLOPE II3 JLTI3CTION ASSl7�iED AS D. 04953 JUNC'FZON LEidGTH = 2.99 FEET FRICTIdN LOSSES = 0.023 FEET Ei�TI'RA3�ICE LOSSES = 0.000 FEET JUNCTION LOSSES = (DY+HV1-HV2y+(ENTRANCE LOSSESi JUNCTION LOSSES =( 0.274}+( 0.404} - 0.279 ----------------------------------------------------------------------------__ NQDE 7001.Qa : HGL =< 190.279>;EGL= < 141.049>;FL,OWLINE= < 137.630> wwv.��x*�**�+»**��*�**..*+�*.**.,��.,.w..s,***++.*+*�**�+.*+*�*+..***+*++�*.**�*,�.. FLOW PROCESS FROM NdDE �aai.oa TO N�DE 7042.D4 IS CODE = 1 iJPSTREAM NODE 7002.40 EiEl7ATI0N = 138.79 (FLOW SEALS IN REACH} ------------------------------------------------------------------------------ CALCUi�TE FRIC'FION LOSSES(LACFCD�: PIPE FLQW = 22.20 CFS PIPE DIAMETER = 24.q4 INCHES • _-PIPE-LENGTH+"^`===48�40-FEET=====_====�9ANNING-S�N`=-==0�413D0===^�=�`-`YyW= M3WNS7'REAM CQNTROL ASSUMED PRE55URE HEAD(FT) = 2.44 -----------_-------------- PRESSURE FLOW PROFILE COMPU'T'ED INFORMATION: -------------------------_-_---------------------------------�----------------- DI6TANCE FROt�f PRESSURE VELOCITY SPECIFIC PRESSURE+ CON'FROL { F'�' ) HF,p,p { FT ) ( FT / SEC ) ENERGY ( FT } MOMEEIdITUM ( PdUNDS } Q.000 2.444 7.066 3.219 587.02 42.785 2.4D0 '].066 2.775 500.04 NORMAL DEP'FH{FTj = 1.23 CR�TTCAL DEP�'H(FT) = 1^68 � _-__------------------------------- ASSUMED 170WNSTREAM PRESSURE HE.�{FT} � 2.04 -------------------------- GRADUALLY VARIED FLOW PROFILE COMPUTEB INFORMATIdN: DISTANCE FROM FLOW DEPTH VF..L,OCITY SPECIFIC PRESSURE+ COIVTROE, ( FT j {�'T ) ( FT / 5EC 1 ENERGY ( FT ) MOMEN'PUM I POUNDS ) 42.786 2.000 7.fl64 2.775 500.04 43.851 1.9$7 7.070 2.764 497.81 44.778 1.9'75 7.062 2.754 495.79 45.626 1.962 7.096 2.744 493.92 96.412 1.9k9 7.133 2.735 492.18 47.145 1.936 7.132 2.727 490.53 47.633 1.924 7.154 2.719 488.99 48.OD0 1.920 7.160 2.717 A8B_b1 NOpE 7002.Oa : HGL =< 140.71fl>;EGL= < 141.507>;FLOWL�NE= <}38.794> . *+*++*++*�r+r*+�*w+rf*+�i.+�*+��**w+*r�*******r+�+**txt*w�*�ki.****txy*t�rr*�r�*+i� FLOW PROCESS FROM NODE 7d02.Q4 TO NODE 7003.00 IS CODE = 5 � UPSTRF�M NpDE 7043.00 ELEVATTON = 139.12 ;�LOW TJNSEAI,S IN RFACH) (NOTE: PpSSIBLE JUMP IN OR UPSTREAM OF S�RUCTURE) -------------------------- CALCULATE JUI3CTION LOSSES: PIPE FLOW DIAMETER ANGLE FLOWLSi�E CRITICAL VELOCITY (CFS) IINCHES} {DEGREES} ��,�]ATION DEPTH(FT.} (FT/SEC} UPSTREAt� 22.2Q 24.OD 90.00 139.12 1.68 28.621 DOWNS'�R£AM 22.20 29.00 - 138.79 1.6$ 7.162 LATEI�AL �1 4.00 4.00 0.00 0.04 0.00 0.000 F�ATERAL �2 Q.00 a.QQ O.QD 0.40 0.00 O.00a Q5 0.00===Q5 EQUAE�S SASIN INPUT=== LACFCD AND OCEMA FLOW Ji3NCTI0N FOR3�7ULAE USED: DY-(Q2*V2-Q1*V1*COSfDEL'TA1,)-Q3*V3*COS{DELTA3)- ¢4*V4*COS(DELTA4j}/((A1+A2)i16.1}tF1'�ICTTON L05SES UPSTREAM: MANI3ING'S N= 0.01300; FAICTION SLOPE = Q.26683 D(}WNSTRF�M: MANNING'S N= 0.01300; FRICTIOAi SLOPE = p.00B39 AVERAGED FRICTION SLOPE IN JUNCTION ABSUMED AS 0.13761 JUNCT�ON LENGTH = 4.OQ FEET FRICTEON LOSSES = 0.550 FEET ENTTFtANCE LQSSES = 0.400 FEET 3Ul3CTION L{}SSES = (DY+HV1-HV2)+(ENTRANCE LOSSESj JUNCTION I,OSSES = {10.924}+( 0.000) = 1Q.929 -------------------------- NOAE 7003.00 : HGL =< 139.711>;EGL= < 152.431>,FLOWL�IN�= < 139.120> •�/!r ***Yr� t t i#t t y� i*ii� ir 1 f iF** *�c �ttY Yt iy� M##** **f iFYr f Yr�k*i �Ic t�k!! �# *1rYrYr*Yr##i! fi+*f *#**iYr# FLOW PROCESS PROM NQDE 7003.00 TD NODE 7004.00 IS CODE = 1 UPSTREAM NQI3E 7D04.00 EL�/ATION = 164.17 {�Z,,pW IS SUPEACRTTICAL) -------------------------------------------------�_------------------------------ : CALCUE�ATE FRICTiON LQSSES (J�ACFCD) : PIPE FLpW 22.20 CF5 PIPE DIA2hETER = 24.00 INCHES PIPE T,ENGTH =. 75.�0 FEET MANNTNG'S n� = o.a�3oa __----------------------------------------------------------------------------- NORMAI, DEPTH { FT }� 0. 5 6 CRIT'ICAL DEPTH { F'�' )= 1. 6 B _ _--------------------------------------------_ iJPSTREAM CON'PRpI, ASSUMED FLOWDEPTH(�'T) = 1.39 �-------------------------------------_____-------- GRADUALLY VARIED FLOW PRpFILE COMPUTED INFORMATION: ------_----------------------------------------------_-------------------------- DISTANCE FROM FLQW DEP'I'H VELOCI'i'Y SPECIFIC PRESSURE+ COI3TROL(FT) fFT� (FT/SECj �I3ERGYIFT} MOMENTUM(POUNDS} 0.040 �.391 9.512 2.797 498.7b O.Z38 1.358 9.771 2.842 505.i1 0.3D2 1.325 1d.049 2.894 512.39 0.494 1.291 10.3A5 2.954 520.65 4.717 1_258 10.665 3.025 529.97 0.978 1_225 11.fl07 3.107 590.44 1.28p }..191 �1.375 3.2p2 552.15 1.631 1.35& i1.772 3.311 565.22 2.038 1.125 12.199 3.437 579.75 2.511 1.a91 12.660 3.562 595.89 3.060 1.058 13.160 3_�49 613.80 3.702 3_025 13.741 3.947. 633.66 4.953 a_991 14.289 4.169 655.67 5.335 0.958 �4.930 9.921 680.10 6.380 D_924 15.630 4.720 707.2a 7.624 0.891 16.347 5.069 737.32 9.119 0.658 17.240 5.476 770.85 ' 10.93fi O.B24 18.176 5.954 Bp8.24 • 13.176 D_791 19.199 6.51$ $50.04 15.9$8 0.75$ 20.342 7.187 896.91 • ' 19.605 4.729 21.619 7.9B6 949.64 24.421 4.691 23.fl51 8.947 1009.21 3i.180 0.658 24.667 34.111 �076.60 41.55b Q.624 25.500 �1.536 ��53.90 60.935 D.591 28.595 13.295 1242.37 75.00a 0.591 28_613 13.311 1243.�� NODE 7009.00 : HGL =< 165.561>;EGL= < 166.967>;FLOWLINE= < 164 �7Q> ` # * * * f * * * * # * * t f k Y W * * * * * * t * * t Y � 4 * W * * f # # k f k 1 f * � k t * 4 f � * � * * 1 * f * * # f * W * * * * * � * * * * * � * * M FLOW PROCESS FRQM NODE 7004.40 TO NOQE 7005.Dp ES CODE = S UPSTR��M NODE 70QS.Oa ELEVATION = 1b9.50 ��LOW TS AT CRITICAL AEPTH) ----------------------------- CALCULATE JIINCTION LOSSES: PIPE FT,OW DIAh3ETEA ANGLE FLAWLTNE CRITICRL VELOCYTY (CFS} (INCHES) (DEGREES) ELEVATION DEPTH{FT.) (FT/SEC1 UPSTREAM 22.2D 24.00 17.40 164.50 1.68 7.875 DOWD}STREAD7 22.20 24.Q0 - 164.17 1.68 7.875 LATEFtAL #1 Q.00 0.04 O.dO 0.00 O.DO O.00D LATERAL #2 a.oa 4.06 a.ao O.QO 4.00 O.00U 4S a.aa===�5 EQUALS SASIN INPUT=== F�P.CFCD AND OCEMA FLOW �3UNCTION FOftMULAE USED: DY=(Q2*V2-(�1`V1*COS(DELTAI)-Q3*V3*Cb5(DELTA3j- Q4*V4*COSIDELTA4)}/((A1+A2}*7.6.1J+FRICTION LQSSES UPSTRF�M: MANNING'S N= Q,QZ300; FRICTION SLQPE = 0.00923 DOWNSTREAM: MANNING'S N= 0.01300; FRICTION SLOPE = 0.04923 AVERAGED F'RICTION SLQPE IN JUNCTION ASSLT2+FBD AS 4.00923 JUNCTIDN LENGTI-3 = 4.00 FEET . FRICTION LOSSES = D.p37 FEET ENTRANCE LOSSES = 0.000 FEET JiJNC'I'TON LASSES = (AX�HV1-HV2f+{ENTRA1�iCE i,05SESj �c�zorr r�ossEs = � 0. 330 )+( 0. UOa) = 0. 330 ---�---------------------------------------------------------------------------- NODE 7405.00 : HGL =� 165.181>;EGL= < 167_144>;FLpWLINE= < 164.500� ***r**i+*tyr++*x*,t*a*+*w,�t****y,w*t****t:*rrts**y,x***r+xxrtt+t*�,rwa**�ttt+**v.+** FLOW PFOCESS FR0�7 NODE 7005.00 TO NODE 70p6.00 IS CpDE = 1 UPSTREAM NO]�E 7006.00 ELEVATIQN = J.65.04 (FLi?W IS Si.JBCRI'iFCAL} ------------------------------- CALCULATE FRICTION LOSSES(LACFCD): PIPE FLOW = 22.20 CFS PIPE D�AMETER = 24.p0 IAICHES PIPE L�NGTH = 25.Q0 FEEi MANNING'S N= 0.026D0 ------------------------------------- 230RMAL DEPTH(FT} = 1.81 & 1.93 CRITICAi� DEPTH{FT) = J.68 NOT�: SUGGEST CONSIDERATION OF WAVE ACTION, UNCERTAINTY, ETC. ___-----------------------------------------===------- DOWNSTREAM CQNiRQL ASSUMED FLOWDEPTH(FT) = 1.6$ __��--------------------------------_-----=_=__________ GRADUALLY VARIED FLOW PROFILE COMPCT'I'ED TNFORMA�'ION: --------------------------------- DISTANCE FROM FI_,OW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT} (FT} {FT/5EC} ENERGX{FT) MQMENTUM(POUNDS) 0.004 1.68Z 7.872 2.644 474.95 O.Q20 1.fi86 7.852 2.644 479_96 0.084 1.691 7.832 2.699 474.98 ' 4.197 1.697 7.811 2.645 475.01 0.369 1.702 7_792 2_645 475.06 0.593 1.707 7.772 2.645 475.11 0.894 3.712 7.753 2.646 475.18 � 1.266 1.737 7.734 2.646 475.2b � 1.730 1.722 7.715 2.647 975_35 2.298 3.727 7.696 2.647 475.46 2.983 1.732 7.b78 2.64$ �75.58 3.805 1.737 7.fi5a 2.648 475.71 4.789 I.792 7.b92 2.649 475.65 5.964 1.747 7.524 2.650 476.OQ 7.367 1.752 7.6d7 2.65� 476.17 9.449 1.757 7.589 2.652 476.35 11.074 1.762 7.572 2.653 476.54 13.532 1.767 7.556 2.554 476.74 16.549 1.772 7.539 2.655 476.96 20.310 1.777 7.523 2.557 477.18 25.OD0 1.782 7.507 2.658 477.41 ------------------------------------------------------------------------------ NODE 7005.00 : HGL =� 166.782>;EGL= � 1b7.658>;FLOWLTNE= < 165.000> .+�+��..*�...��+��*++�+**************.**+*�w.+*�t**�t*****w*****++�++:�*+�.�.* FLOW PROCESS FROM NODE 7pD6.d0 TO NODE 7p06.00 IS CODE = 8 UPSTREAM NODE 7406.00 ELEITATION = 165.00 (FLQW UNSEALS IN REACH} ------------------------------------------------------------------------------ CALCULATE CATCH BASIN EN'fRANCE L4SSE5(LACFCD): PIPE FLOW = 22.20 CFS PIPE DEAD3ETER = 24 . DO I?�ICHES FLOW VEL�C)CITY = 7.51 FEET/SEC. VELOCITY HEAD = 0.876 FEET CA'i'CH BASIt3 FNERGY LOSS =. 2*( VELOCITY HEAD) _. 2�{ p_ g'7 O - 0, 175 NpDE 7006.d0 : HGL =< 167.633>;EGL= < 167.$33>;FLOWLINE= < Z65.000> f 1�** ** i�# ***# i� *#**�k #� iF * f f f k k k iA'YrY�'k'kiFYr**f Yi 1 k* *ri f f ri Y� Y� fYr�lriFiFiFk 1� Yrtk*** ***i i f fY Yl�i�Y1 Y� if UPSTREAM PIPE FLOW CONTROL DATA: � NdDE NUMBER = 70Q6.Da FLOWLI�IE ELEVATION = 1b5.04 . A6SUMED UPSTREAM CONTFtOL HGL = 16b.6$ FOR DOWI+iSTREAM RUN ANALYSIS --__--------------------------------------------------------------------------- ------------------------------------------------------------_--------------____ END OF GR�UUALLY VARIED FLpW ANALYSTS • � APPENDIX 4. L 13 SYSTEM 5000 � C� � � f 4 # * * � f * * * # * Y ! 1 * M � # i # Y Y Y Y # # i � * } � Y * i # i } W � 1 � * * * � i W W + f * # * � i # * * # * � * * Y Y k * k * # * * * i k ♦ PiPE-FLAW HYDRAULiCS COMPUTER PROGRAM PACKAGE iRe€erence: L1ICFCD,LACRD, AND OCEMA HYDRAULICS CRITERION} {c1 Copyright 1982-2002 Advanced Engineering Software faes) Ver. 8.� Release Date: 01/01/20D2 License ID 15D9 Analysis prepared by: PROJECT DESIGN CONSULTAI3TS 701 'B' STREET, SUITE 600 SAN DIEGO, CA 92101 619-235-6471 "*********""'************** DESCRIPTIOid �F 5TUI7Y *********t#Y�liYt*i*YY#ftii * BRESSI RANCH - INTERIM CdNDITIONS * * SYSTEM 8000: SD NO. 4& 5 PER SHT 20 OF DWG_ 400-8C * * 1D0-YEAR STOR?�7 EVENf ' �*.��*.*.*�*�v.ww*�s..�+#**++w+W+t�W.�*«+w.�x***++*+**+**+��****.+*.,..��,.�+ FILE NAME: 80DD-J.�.DAT TIME/AAT� OF STUDY: 13:5� O1/2Z/2003 r�*r*,r*+*+,r**�,ir*,r******r+r**+*t*+s*+*t*++�*t�****at+*+*t**fyyttirts+f****++yrts*s GRI�DUALLY VARIED FLOW ANALYSIS FOR PIPE SYSTEM NdDAL PUINT STATUS TABLE (Note: "*" indicates nodal point data used.} UPSTREAI� RiJPT DOWNSTRE.AM RUN NQDE MQDEL PR�SSl7RE PRESSURE+ FLOW PRESSURE+ . NCIMBER PROC�SS HEAAIFT) MOMENTUM(POUNAS) AEPTH(FT) MOMENTUM(POUNDS) � 8�00.00- 1.52 Dc 35i.42 0.79* 562.22 } FRYC'i'ION 8000.50- 1.72 359.06 0.73* 622.14 ) FRICTION 8441.00- 1.52 Dc 351.42 1.16� 387.59 ) MANI-30LE 8D02.D0- Z.52*Dc 351.42 1_52*Dc 351.42 ) FRICTiON 8003.00- 1.69* 356.77 1.52 �c 351.42 } CATCH BASIN 8003.00- 2.43* 281.48 1.52 Dc 109.'70 ------------------------------------------------------------------------------ MAXIMUM NCTMBER OF ENEFtGY HI�LAt3CE5 USED IN EACH PROFILE = 25 ------------------------------------------------------------------------------ NO'i'E: STEADY FLOW HYDR.AULIC HEAD-LOSS COMPUTATIONS BASED ObI THE MOST CONSEAVAT'�VE FORMULAE FRpM THE CURREN'P I.ACRD,I�ACFCD, AND pCEMA �ESIGN MANUA�,S . ♦+i.�+s****a�ress**�r*++i.+*+t**+**a+*+,t+��s��i.i.ti�tsx**��*ti�t�*x***+�k��w***xx*s DOWNSTREAM PI PE FLOW CONTROT� I}ATA : NODE NUMBER = 5000.00 FLC3WLINE ELEVATION = 219.Da PIPE FLOW = 17.94 CFS PFPE DIAMETER = 24.00 INCHES AS SZ7hlED DOWI�STREAM CON'£ROL HGL = 2 2 0. 5 2 0 FEET *NOTE: ASSiTMED DOWNS`i'REAM CONTROL DEPTH( 1.52 FT.} IS LE55 THAN Cf�TTTCAL D�PTH{ 1.52 FT.} ___> CRITTCAL DEPTH IS ASSUMED AS 1Xl4V�ISTREAM CONTROL DEPTH FOR UPSTREFi2+] RUN ANAi�YSIS ------------------------------------------------------------------------------- NODE 8d00.4Q : HGL =< 219.740>;EGL= < 223.532>;FLOWLTNE= < 219.000> *** *}}}�r ii#�Jr+�li # yr y� ik+Y*Yf f�r yryfy� t*k 1* i}yr* i� * f i i�*}}}*i *##* i1r #* iF *# i� * k i k*********ii f* t •. Fi,OW PROCESS FROM NODE B000.00 TO NODE 800D.5a IS CODE = 1 •`� UPSTREAM NODE BOOa.5D ELEVATTON = 219.04 {��OW IS SUPERCRITICAi�) ti CALCLTLATE FRICTION LOSSES{�,pCFCD): PIPE FLOW = 17.90 CFS PTPE DIAMETER = 24.00 I�CHES PIPE LENGTH = 4.00 FEET MANNING'S N- 0.02904 -__� NORM.�i, PIPEFLOW IS PRE55URE FLOW NORMAL 13EPTH ( F'T f= 2. D 0 CRITICAi� DEPTH ( FT )= �. 52 ----------------�_-------------------------_____------------------------------- -----------------------------------------------------------------------..__-___ UPSTREAM CONTROL A55U[�4ED FLOWDEPTH{FT) = 0.73 ----------------------------------------------------------�_..__.._----__..___T__ GRADUALLY VARxED FLOW PROFILE COMPLT'I'ED INFORMATIOI3: DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROi,(FTj (FT) (FT/SEC} ENERGYlFm} MOMENi'UM{pQ�D5) 0.000 0.726 17.370 5.914 522.14 2.026 0.758 16.369 4.932 590.21 4.000 0.790 15.519 4.532 562.22 __--__�_�---------------------------------------------------------------------- N017E BODD.50 : HGL = � 219.766>;EGL= < 224.454>;FLOWLINE= < 2�9.040� ****.*******t.**�*�*++t.��*�*+***..��f��.��++t*+.*.�**ti�..*,�,�t++++++�*��.�* FLOW PROCESS FROM NODE 8000.50 TO NODE 8D01.00 IS CODE = 1 UPSTRE.�,M NODE Sa01.00 ELEVATION = 251.48 (FLOW IS SUPERCRITICAL) CALCULATE FRICTION LOSSES(LACFCD}: PTPE �'LOW = J.7.90 CFS PIPE DIAbfETER = 29.40 INCHES P�PE LEt�iGTH = 112.00 FEET MANNING'S N- 0.02400 ------------------------------------------------------------------------------ 130RMA�, DEP'I'H ( FT) = 4. 7i CRI'i'ICAL DEP'i'H { FT} = 1. 52 --=====-=--=--==-------------------------------------------------------------- . -----------------__--------------- i7PSTREAM CONTROL ASSUMED F'LOWllEPTH{F'F) = i.16 ------------------------------------------------------------------------------ ------------------------------__-__--_____--------------__---_-_----------------- GRADUAF�LY VARIED FT,QW PROFILE COMPLTFED TNFORM71'T'TpN: ___________________----------------------------------------------------------- DISTANCE FROt+1 Fi�OW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL S FT ] ( F'I`) ( FT/ SEC } ENERGY ( F'I' � N30t�3E[3TUM ( POUNDS ) 0.000 1.16b 9.475 2.554 367.59 0.152 1_142 9.656 2.590 391.78 0.321 1.124 9.844 2.630 396.27 0.507 1.106 10.041 2.672 401.08 0.713 1.068 10.245 2.719 406.22 0.94D 1.070 30.459 2.77D 411.71 1.193 1.052 �4.583 2.825 417.56 1.973 1.034 1�.9Z6 2.886 • 423.80 1.78A 1.016 11.I60 2.951 930.45 2.�3a 0.998 1�.435 3.023 437.52 2.517 0.981 11.681 3.3a1 445.05 2.951 0.963 11.961 3.186 453.06 3.440 0.945 12.254 3.278 451.57 3.992 0.927 12.561 3.378 470.63 4.62D 0.909 12.884 3.488 480.26 5.339 0.691 13.224 3.60B 490.50 6.170 0.673 13.581 3.739 501.44 7.190 0.855 13_95b 3.B82 512.98 8.288 0.837 }.4.353 9.038 525.32 9.671 0.8Z9 14.77� 4.2D9 538.45 11.377 4.801 15.2�2 4.397 552.94 13.554 0.7$9 15.679 9.b03 567.35 16.481 4_765 16_174 4.834 583.25 • 20.781 0.748 16.698 5.080 600_23 � 28.957 0_730 17.255 5.356 618.36 112.4Q0 0.72b 17.370 5.414 622.14 ------------------------------------------------------------------------------ NObE 8001_Qp : HGL =< 252_640>;EGL= � 254.034>;FLOWLINE= < 251.48D> �*�+�+*+*��**��+*+�+t**�x****�*************.*�*****��****+*+++***+�*�xw�*�� FLOW PROCESS FROM NODE saai.00 TO NODE 6002.04 I5 CODE = 2 UPSTREP.M NODE 8002.OD ELEVATION = 251.$1 (FLOW IS AT CRITICAL DEPTH) ------------------------------------------------------------------------------ CALCtTLATE MANHOLE LQSSES(LACFCD): PIPE FLOW = 17.90 CFS PIPE DIAMETER = 24.00 ��ICHES AVERAGED VELOCITY HEAD = Q.754 FEE'I' HMN =_05�(AVERAGED VELOCITY HF.Ap) _.05*f D.754) _ �.03B NO`�'E: F1�IERGY GRAD� LINE HA5 BEEN ADJUSTED DUE TO CHANGING IN FLOW L�NE ELEVATIONS ------------------------------------------------------------------------------ NODE 8002.00 : HGL =� 253.334>;EGL= < 254.088>;FLOwLTNE= < 251.810> **t**t*«*+*.*„**t+..,*w�+v�*�*+++*+***********�*****++**��,.,�***********�*****+* FLOW PROCESS F12pM NODE 8402.00 TO NODE 8D03.4Q IS CODE = 1 UPS7'REAM NODE $Oa3.Op ELEVATION = 252.41 (FLOW IS SUBCRITICAL) ____________-------------------------------------------------------------------- CALCiJL�ATE FRZCTION LOSSES(LACFCD): PIPE FLOW = 17.94 CFS PIPE D�AMETEFt = 24.00 INCHES PIPE LENGTH = 30.04 FEET MANNING'S i�i = 0.024fl0 � --------------------------------------------------------------_---------------- NORMAL DEPTH(FT1 = 1.71 � 1.99 CRI'PICAL DEPTH{FT} - 1.52 NOTE: SUGGEST CONSIDEI2ATTpN OF WAVE ACTION, UNCERTAIN'I'Y, ETC. ------------------------------------------------------------------------------- ------------------------------------------------------------------------------- IJOWN5TI�EAM CQN!'RpL ASSUMEI? FLOWDEPTH(FT} - 1.52 � �---------------- GRADC7ALLY VAAI�D FLOW PROFILE COMP[3TED INFORMATION: ------------------------------------------------------------------_------------ DISTANCE FROM FLOW DEP'i'H VELOCITY SPECIFIC PR�SSLIRE+ CONTROL ( FT ) i FT 1 ( F7' / SEC ) ENEi�GY { FT j MOMEIVTUM ( POUNDS ) a.000 1.524 6.966 2.278 351.42 0.016 1.531 6.933 2.278 351.43 0.064 1.539 6.9D0 2.278 351.47 0.149 1.546 6.858 2.279 351.52 0.274 1.553 6.83b 2.279 351.60 0.444 1.560 6.805 2.28D 351.70 0.5f4 1.568 6.�74 2.281 351.83 0.939 1.575 6.743 2.281 351.97 1.277 1_562 6_713 2.262 352.13 1.6$6 1.5B4 6.684 2.284 352.32 2.175 1.597 6.655 2.285 352.53 2.75$ 1.609 6.626 2.28fi 352.76 3_449 1�.6�1 6.598 2.288 353.00 4.266 1.618 b.570 2.289 353.27 5.233 1.626 5.543 2.291 353.56 6.380 1.633 5.516 2.293 353.87 7.747 1.b40 6.490 2.295 354.20 9.387 1.647 6.4b4 2.297 354.�5 11.377 1.655 6.438 2_299 354.9I 13.828 1.662 6.413 2.301 355.30 16.913 1.664 6.388 2.303 355.70 20.922 1.676 6.364 2.306 355.13 26.399 1.684 6.340 2.3DB 356.57 30.OD0 1.587 6.329 2.304 356.77 ---------------------------------------------- ---______----_ • NODEF 8003.OD : HGL =< 254.Q97>;EGL= < 254.7�9>;F'LOWLINE= � 252.410> � � i i# rt Y i i* i f t i Y 1* Y� 4! i i Y# i t*�+� f i Y W# i* rt Y* f f* i 4 i!* k f Y i* i** 1� i 1 1 Y 1*** W*# 1#*� f i*? f FLQW �ROCESS FROM NODE 8003.OQ TQ NODE 8003.04 IS C6D� = B UPSTREAM NODE $Q43.00 ELEVATION = 252.41 (FLOW UNSEAI�S IN AEACHi -----------------------------------------------------------------------___—___ CALCULATE CATCH BASIN EN'FRANCE I.ASSES (IaACFCD} :' PIPE FLOW = 17.90 CFS PIPE DIAME'PER = 24.00 INCHES FLOW VELOCITY = 6.33 FEET/SEC. VELOCITY fiEAD = 4.622 FEET CATCH BASIN �A7ERGY i3OSS =.2*{V�LOCITY HEAD} _.2*( a.622) _ �.129 ------------------------------------------------------------------------------ NODE 8D03.DD : HGL =� 254.$99>;EGL= � 254.$44>;FLOWLINE= < 252.410> *�*+�+�+**++***++.,�ftt+*+,�*++��+tst+�,�****....+w,.,�*�...�f+�wt+***+**+**�*+**+ UPSTREAM PIPE FLOW CON'I'ROL BATA: NOflE NUMSER = 84D3.00 FLOWLINE ELEVATION = 252.41 ASSUMED UPSTREAM CONTROL HGL = 253.93 FOR DOWNSTREAM RUN �]ALYSIS ------------------------------------------------------------------------------ END 0�' GRAI)UALLY �ARI�D FLpW ANAI,YSIS . � r � LJ � APPENDIX 4.1.14 SYSTEM S� 00 � n LJ � � i� 1��**� k t�+ 4� i�* f i# f#}* W Y W f+ W f�++# i* 1# W*** t!# i Y 4 k k Y Y* Y k k k f*� 1 1� 1 f! 1� ti f W M PIPE-FLOW HYDRAULICS COI�4PUTER PROGRAM PACKAGE (Reference: �,ACFCD,LACRD, AND OCEMA HYDRAULICS CRITERIONJ {c1 Copyright 1982-2002 Advanced Engineering 5oftware taes} Ver. B.Q Release Date: 01/D1/2002 Lzcense zD 15�9 Analysis prepared by: PR03ECT BESIG23 CONSULTANTS 701 'B' STREET, SUITE 804 5AN DIEGO, CA 92101 619-235-6471 �*"`"'***'`'`"''"""'s***"`*'**"''* DESCRIPTIO23 OF STUDY *s*+**+rw+.++xr**+�*******�,r ; BRESSI RRNCH - IId'PERIM CONDITIONS * ` SYSTEM $lOD: SD i�10. �& 2 PER SHT 21 OF DWG. 400-8C * � 100-YEAR STO�2.M �,'V�]''P * *+.+�++*t++w+t**�***�*t��++++�*�*��...*+�+,.*..��.��ti��,.*�**{+*v�***+.*.� FILE NAME: $�00-lI.DAT TIME/DATE OF STL7DY: 14:Q4 O1/21/2003 ***t+*t*:***�++*t:+�******.*..+***:�*+�....��*�*«..*�*+**��.�.�+*++***+*.*,.,.*.,, GRADUALLY VARIEI7 FLOW AtdALYSIS FOA PIPE SYSTEM NpDAL POINT STATUS TABLE {Note: "*" indicates nodal point data vsed.} v�sT� Runr nowrrsTR�r�s Rurr NOA� M4DEL PR8S5URE PRESSURE+ FLOW PRESSURE+ NUMSER PROCESS HEAD ( FT ) MOMENTi7M ( POL]2SDS } DEPTH ( FT } PSOMEN'I'UM ( POUNDS a • B�OO.OD- 1.62 Dc 418.51 0.$2* 683.31 } FRICTION . B10Q.50- 1.64 429.28 0.76* 753.69 } FRICTION 6101.00- 1.62 Dc 438.51 i.25� 456.88 } MA.NHpLE B102.00- 1_62"Dc 4�8.51 i_62*Dc 41$.51 } FitICTION 8103.00- 1.89* 434.51 1.52 Dc 418.51 } CATCH BASIN 8103.00- 2.70• 333.83 1.62 Dc 125.02 ------------------------------------------------------------------------------ M.�XIM[TM NUN3BER OF ENERGY BALANCES USED IN EACH PROFILE = 25 ------------------------------__------------------------------------------------ NQ'i'E: S'E`EADY FIAW HYDRAULIC HEAL7-LOSS CON3PUTATIONS BASED ON 'iHE MQST CQNSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, ANL7 pCEMA DES�GN M.ANUALS. +.�******�*+*+*++*+***�*******«**�+,r+*�**�,r+f��+++++f+f+tf*�x*t.x+*********#+� DOWNSTR.BAM PIPE FLOW CONTRQL DATA: T70DE NiTMBER = B10D.Q0 FLOWLINE ELEVAT�bN = 209.50 PIPE FLOW = 2D.30 CF5 PIPE DIAMETER = 24.00 INCHES ASSUMED DOWNSTRE.�M CpN'Ti20L HGL = 211.120 FEET NODE 810D.00 : HGL = � 210.321>;EGI_,= < 219.656>;FLOWLINE= � 209_500> **+��t++w**�****++t***wwtii+tti��rti�r*yr��+++*t�at**+++*+*+++tx*Y�****y*t+t*yit+• FLOW PROCESS FROM NODE $10fl.00 TO NODE 8100.50 IS CODE = 1 UPSTREP�1 NODE 8100.50 ELEVATTON = 243.54 (FLQW �S SUPERCRITICAI.f --------------------------------------------------_..___------------------------ CALCULATE FRICiI0I3 LOSSESILACFCD�: . PIPE FLOW - 20.30 CF5 PIPE DIAME'I'ER = 24.Od INCHES � PIPE LENGTH = 9.00 FEET �SANNING'S N= Q.02904 =_> NORMnL PIPEFLOW IS PRESSURE FI�OW NORMAL DEPTH{FT) = 2.00 CR�TICAL AEPTH(FT} � 1.62 UPSTREAM CON'I'ROL ASSUt�1ED FS.�OWIJEP'I'H(FT) = 0.76 ------------------------------__--_----------------------------------------------- ------------------------------------------------�___--------------______--_-___ GRADUALLY VARIED FLOW PROFILE COMPUTED INFORMATION: DISTANCE FR4M FLOW DEPTH VELOCT'T'Y SPECIFIC PRESSCTRE+ CdN�'ROL ( FT j { FT ) ( FT / SEC 1 ENERGY ( F'T ) MOMENTUM ( PO[FidDS ) O.D06 4.758 38.507 6.137 753.69 2.173 4.792 17.530 5.567 713.74 4_04Q 0.821 16.7p2 5.156 b83.31 NODE 8100.5a : HGL =< 210.298>;EGL= < 215.677>;FLOWLINE= < 2fl9.590> �k*1� Y! 1 Y!i #t#* Yt�1fi YYY1 i!!! � i�! 41 ii t Y Yti f Y*** tt******YrYryryr***# ****YriM �*�***i� YrYriF** FL4W PROCE55 FROM NODE $100.50 TO NOflE $�Q1.OQ IS CODE = 1 UPS'1'REAM NO�E 8101.00 ELEVATION = 249.18 (FLOW I5 Sl3PERCRITICAL) CALCULAT� FRICTION LOSSES(LACFCD): PIPE Fi,OW = 20.30 CFS PIPE DIAMETER = 2A.00 INCHES PIPE LENGTH = 129.00 FEET MANNING'S N= 0.02400 ------------------------------------------------------------------------------ f70RMAL DEPTHSFT) = 0.74 CRITICAL DEPTH(FT) = 1.52 -----------------------------------------------..______----___.._____----__-------- ------------------------------------------------------------------------------ UPSTf�AM CONTROL ASSUMED FLOWDEPTHfFT1 = 1.25 ------------------------------------------------------------------------------ ----�-------------___��_--_____--------------------------------------------------- GRADiJALF.Y VARIID FI,OW PROFILE COMPUTED TNF'QRMATIOI3: • ---------------------------------------------__-------__-_--_-------------------- DISTANCE FROM FLAW DEPTH VEIACITY SPECIPTC PRESSURE+ CONTROL ( FT ) { �' } { �/ SEC ) FNERGY ( FT ) i+fOMEI3Tl�iI� I POUNDS } O.Q60 1.249 9.836 2.752 456.68 0.147 1.229 10.027 2.791 461.B3 0.31D 1.208 10.227 2.633 467.17 0.491 1.18$ 10.436 2.880 472.91 0.693 �..158 10_fi55 2.932 479_08 0.917 i.147 i�a.884 2.986 465.71 1.16b 1.127 11.I24 3.050 442.81 1.443 1.107 1i.375 3.117 500.41 1.753 1.087 11.639 3.19]. 508.55 2.099 1.066 11.915 3.272 517.25 2.487 1.046 12.206 3.361 526.54 2.923 1.D26 12.511 3.458 536.47 3.415 1.DQ5 12.832 3.564 597.fl7 3.974 0.985 13.170 3.680 558.39 4.6�2 0.965 13.526 3.807 570.47 5.344 D.945 13.901 3.997 583.38 6.193 0.924 14.24$ 9.100 597.1b 7.�87 D.904 14.717 4.2b9 bf1.88 6.367 0.884 15.164 9.455 527.52 9.792 0.663 15.630 4.559 644.49 11.557 0.$43 16.129 4.885 662.45 13.815 0.823 16.b59 5.135 • 681.72 16.860 0.$02 Z7.222 5.411 70Z.38 21.347 Q.782 I7.822 5.718 724.54 29.382 0.752 �8.463 6.058 74$.33 124.000 d.758 18.607 6.137 753.69 � -----------------------------------------------------...._____-----______�______ � NODE 8]41.00 : HGL =< 254.429>;EGL= < 251.432>;FLOWI.,TNE= < 249_180� • * * * * * * # k * f * * * * � � Y + * � * * i * i f # f } * * * 1 � * k * * * * * * } f ? * } * # * 1 * � � * * � * * * * * ? i k Y f * t i � � t i i * � * FLpW PROCESS FROM NODE 8101.00 �O NODE $1d2.00 IS CODE = 2 UPSTREAM NODE 8102.OQ ELEVATION = 249.51 (FLOW IS AT CRITICAi, DEPTH} -----------------------�_----------------------------------------------�______ CALCULA7'E MANHOLE LOSSES(LACFCD}; PIPE FLOW = 20.30 CFS PIPE DIAMETER = 24.00 INCHES AVERAGED VELOCITY HEAD = 0.8fi4 FEET HMN =.05�(AVERAGE�s VELOCITY HEAB) =.05*; 4.864} - Q.Q43 d+70TE: ENERGY GRADE LENE HAS BEEN ADJUSTED DUE TO CHANGING IN FLOW LINE ELEVA'I'TONS --------------------------------------------------------------------------__--- NODE 8102.OD : HGI, = a 251.i27>;EGL= < 251.991>;Fi�OWLINE= r 299.51p> i�wx+**+**wx,rra+r+�****t++�+irttti�*�rr**erittit***t*r,��,w��rf�rf+f,�,rxx�***,o-++****+t FLOW PROCESS FROM NODE 8102.00 Tp NODE 8103.00 IS CQDE = 1 UPSTAEAM NODE 8103.D0 ELEVATION = 249.91 (FLOW IS SUBCRITICALf ------------------------------------------------------------------------------- CALCUE,ATE FAICTXON LOSSES ( I�P.CFCD j: PFPE FLOW = 20.30 CFS PIPE DFAMETER = 29.00 INCHES PIPE LENGTH = 2a.OD FEE�' MP.NNING'S N= O.D2400 ___> NORMAL PIPEFLOW IS PRE55URE FLOW ------------------------------------------------------------------------------- NORMAL DEPTH(FTy = 2.Od CRITICAL DEPTH(FT) = 1.62 ___---_ _------------------------------------------------------_-_---_------------ --------------------------------------�__________----------------------------- DOWNSTREI�M CONTROL ASSUMED FLOWAEPTH{FT) _ �.62 ------------------------------------------------------------------------------- ------------- ---------------------------------------------------------------- GRADUALLY VARIED PLOW PROFILE COMPUTED INFORMATION: DTSTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSiiRE+ • CONTAOL S�"I'? ( FT } { Fi`/ SEC j ENERGY ( F'I' � MOMENTtTA4 I POUNDS j Q.0�0 1.617 7.458 2.4$1 418.5i O.fl91 1.632 7.393 2.481 418.56 0.167 1.6A7 7.330 2.482 418_72 0.387 1.663 7.269 2.489 418.99 0.709 1.678 7.211 2.486 419.36 1.142 1.693 7.154 2.489 419.83 1.694 1.709 7.099 2.492 420.40 2.376 1.729 7.047 2.496 421.07 3.J.98 1.739 6.996 2.504 421.64 9.166 1_755 6.947 2.505 422.70 5.295 1.770 6.9d0 2.510 423.66 6.58$ 1.785 6.855 2.516 424.71 6.051 1.801 6.812 2.522 425.86 9.b40 1.816 6.771 2.528 427.31 11.509 1.831 6.732 2.536 428.45 13.488 1.847 6.695 2.543 429.8$ 15.63A 1.862 6.,660 2.551 431..41 17.927 1.877 6.527 2.560 433.09 2Q.000 1.89i 6.501 2.558 439.51 ------------------------------------------------------------------------------ NODE 8103.00 : HGL =< 251.8D1>;EGL= < 252.478>;FLOWL�NE= < 299.910> ..�+..w��+++��+++**�*.*****t*.�.**...��***..+.�***ttt**.*��+++�*�*+*�*+�*.�.�� FLOW PROCESS FROM NOBE 8103_00 T4 NODE $103.OQ TS CODE = B UPSTREAt+� NODE 8103 . DO ELEVA'I'TON = 249 _ 9�. { FLOW UNSF.AL�S IN RF.ACH} ------------------------------------------------------------------------------- CALCUL.�TE CATCH BASII3 ENTRANCE LOSSES(I�ACFCD): PIPE FLQW = 20.30 CF5 PIPE DIAMETER = 24.00 INCHES � FLpW VELOCITY = 6.60 FEET/SEC. VELOCITY HEAD = 0.677 FEET CATCH BASIN ENERGY LOSS =.2*(VELOCITY HEADi =.2iI fl.677} = 0.135 � ------------------------------------------------------------------------------ �ODE $103.00 : HGL =< 252.613>;EGL= � 252.b13>;FLOWLINE= < 299.910> ��w��+**++*++*****+�+*��+t�+***�*�.**��****+*t**��*+�ww++*+*�*�.**+++**ti�w* UPSTAEAM PIPE FLOW CONTROL DATA: NODE NUMBER ti 6103.00 FLOWLTNE ELEVATION = 249.91 ASS�MED UPSTRF�M CONTRdL HGL = 251.53 FOR DOWNSTREAM RUAT ANAE,YSIS ----------------------- END OF GRAbUALLY VAR�ED FLOW ANALYSIS • . � APPENDIX 4.1�.1� SYSTEM 820Q � � � *trrrar**+rr*�+i�ta�:x+**aw*t�+aa+a+��*+x�iar*�*�***�rw�a�**r*�r*�a**a��r**x+* PTPE--PLpW HYDAAULICS COMPiTTER PROGRAM PAC}CAGE fReference: LAC�'CD, LACRi3, AND OCEMA HYI?RAULICS CRITERTON} (c) Copyright 1982-2002 Advanced Engineering Software faes) Ver. 8.0 Release Date: D1/O1/2002 License ID 15D9 Analysis prepared by: PR0�7ECT DESIGN CONSULTAN3'S 701 'B' STREET. SUTTE BpQ SAN DIEGO, CA 92101 619-235-6471 *i**+*+»++*++�*+***��++*r. DESCRZPTION OF STUDY ti+*++�+tir+*t**�wr+�r*v.**+ * SRESSI RANCH - INTERIM CONDITIdNS * * SYSTEM 82Q0: SD N0. 3& 4 PER SHT 21 OF AWG. 400-8C * * 100-YEAR STORM EVENT * 1! Y�! i f�k Y Y 4YYY4i YYY14*4 rt i�Y * Y�F Y t! Y�kY�Yr**i *t* �*****# ��Yrt**�r+#**** #*�!t***#*irYrYr* FILE NAME: 8204-1T.DAT T�ME/DA'I'E OF S'i`UAX: 19:07 41/21/2003 *****�.*�.+**.,.,..,»*.,,,.�..**.�*«*.**�*,r,.�+****��*.++**+++++�+�r*****+�**++.�*.rt� GRRDIJALLY VARIED FLOW ANALYSIS FOR PIP� SYSTEM NODAL POINT STATiJ5 TAB�,E INote: '*" indicates nodal point data used.) UPSTREAM R[Tl�I DOWT3STREAM AUN NODE MODEL PRESSURE PRESSURE+ FLOW PRESSURE+ NUMBER PROCESS HEAD{FT} MOMF�iTiJMfPOUNDS) DEPTH(FTi MOMENTLTM(POUNDS) . 824d.Q0- 0.97 I3c 106.96 0_44* 215.00 ) FRICTI4N 6200.5Q- 0.97 Dc 106.95 D.42* 226.82 ) �RICTION 8241.4Q- 0.97 Dc 106.35 0.6B* 129.52 ) MAId]IOLE 82a2.OQ- 0.97 Dc 106.95 0_91* 109.47 } FRICTIpN 8203.00-- �.97*Dc 108.95 0.97*De 106_95 } CATCH BASIN 8203.Qa- 1.42* 58.89 0.97 Dc 36.38 MAXIMUM NUMBER OF ENERGY BAiANCES USED �N �ACH PROFILE = 25 ------------------------------------------------------------------------------- NOTE: STEA�Y FLOW HYDRAULIC FiEAD-LOSS COMPUTATIONS BASED dN THE N305T CONSERVATIVE FORMULAE FROM THE CURREN'F LACRD,LACFCD, AND OCEMA DESIGN MANUALS. **#Y� # ik'F Y ik iY � * �l'h��kiF+Y Yiif+i �kf �Fi�'�1tik+Y *�i * YY Y #t #*#t �k t Yr 1i*Y?Yk 4 * Yik*f �kf Yfi �k 1 i *�k * � i� *�F* DQWNSTREAM PIPE FL4W CQNTFtOL bATA: � NODE NUMBER = 8240 .00 F3,C}WLINE ELEVATI013 = 249 _ 00 PIPE FLOW = 7.40 CFS PIPE DIAMETEA = 29.04 INCHES ASSUMED DOWNSTREP.M CONTROL I-1GL = 249.970 FEET ------------------------------------------------------------------------------ NOD� 820a.00 : HGL =< 249.437>;EGL= � 252.746>;FLOWLII3E= < 299.OQ0> .*�*..*.**..*��*.**.,**�....*.*��.,.*.+�*+***+.*.>...,.**..�.***..*.**«******�+ FLaW PROCESS FROi+3 NODE 8200.00 TO NODE 8240.50 IS CODE = 1 UPSTREAT�S NODE $200.5D ELEVATION = 249.04 (FLOW I5 SUPERCRITICALJ CALCULATE FRICTION LOSSESILACFCD}: � PIPE FLOW = 7.40 CFS PIPE DIAMETER = 2q_00 INCHES PIPE LENGTH = 4.04 FEET MANNING'S N= 4.013Q4 � ------------------------------------------------------------------------------ NpRMAL DEPTH{FTJ 0.79 CRITICAL DEPTHIFT) 0_97 ------------------------------------------------------------- ----�__--------- ------------------------------------------------------------------------------ UPSTREAi+3 CON'd'AOL ASSiR+3ED FI,OWDEPTI-3(FT) = 0.42 GRADUALLY VARIID FLOW PROFILE COMPUTED INFORMATION: DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC Pi2�SSURE+ CONTROLIFT) (FT} (FT/5EC] ENERGY{F'P) MOMENTUMSPUUiTNDS) O.Q00 0.419 15.456 9.}.31 226.62 3.412 0.434 14.715 3.798 216.64 4.400 0.437 14.595 3.746 215.D0 --------------------------------------------------------�-------------------- NODE 8200.50 : HGL =< 249.459>;EGL= < 253.173>;FLOWL,INE= < 249.094> yr�k * * � *** i * *i*Yrfik � i�k*'F *4� *# # # f *�k i� �k* �k Yr******i� *1riF* �k Y� }�Y fiYrYrf YrYr**i *tili Y#YYf� f 1 Y�YYi f FLOW PROCESS FRpM NODE 82D0.50 TO AibDE 8201.04 IS CODE = 1 UPSTREAM NpDE 8201.00 ELEVATION = 285.28 {FF�OW IS SCiPERCRITTCAL) CALCULATE FRICTI013 L05SES {I,,ACFCD} ; PIPE FLOW - 7.40 CFS PIPE DIAMETER = 24.D0 INCI-lE5 PIP& LENGTH = $S.OQ FEE�` MANA3ING'S N= O.D2400 ---------------------------_____�______.._____-__--_�_--------------------------- NOAPSI�L DEPTH { FT) = Q. 41 CAITICAL 1)EPTH { FT} - 0. 97 -------------------------------------------------------_-�---------------------- ------------------------------------------------------------------------------- UPSTREAM CON'i'RpL ASSUMED FE,OWDEPTH{FT) = Q.6B ---------------------------__----___--___--__�---__---------------------------------- GRADUALLY VAAIEI� FLOW PROFILE COMPUTED INFORMATI03d: --------------------------------------------------------____----------------- DISTANCE Fi�QM FiOW DEPTH VELOCITY SPECTF�C PRESSUftE+ � CONTRbL(FT) (FT} (F`P/SEC) EIVERGY{FT) MOMENTUM{POUNDS) 0.400 0.678 7.881 1.643 229.52 0.089 0.668 8.D54 1.675 131.38 0.167 0.657 6.233 1.710 133.36 0.294 0.646 6.421 I.748 135.45 D.412 0.536 6.615 1.789 137.67 0.541 0.625 8.819 1.833 140.02 d.684 Q.b14 9.031 1.682 142.5i 0.842 0.6a4 9.252 1.934 145.35 1.fl�5 0.593 9.483 1.990 147.94 1.209 0.562 9.725 2.052 150.9Q 1.424 0.572 9.978 2.1i9 154.03 1.665 0.561 7.0.243 2.191 157.35 �.934 0.551 1Q.52i 2.27Q 160.86 2.238 �.540 10.813 2.357 1fi4.58 2.SB2 0.529 11.119 2.450 15$.53 2.976 0.539 11.441 2.552 172.71 3.430 0.508 11.780 2.66�1 177.15 3.959 Q.497 12.137 2.786 181.85 4.589 a.487 32.514 2.920 186.Sb 5.335 0.476 12.911 3.05b 192.18 6.264 0.465 �3.331 3_227 197.83 7.439 0.455 13.77b 3.944 203.85 9.Q21 0.444 14.248 3.598 210.27 11.343 D.433 14.749 3.813 217.11 15.483 a.423 15.281 9.Q51 224.41 86.000 4.4�9 15.456 9.131 225.82 -------------------------------------------------�--__------------------------ NODE B201.�D : HGL =< 285.958>;EGL= < 286.923>;FLOWLINE= < 285.280> • � k w * * * � * k � i � i * * rt 1 * * * * w i i * * f * Y � + i 1 1 1 # * % ti * # # # W f * * � * * * * * k * * # * t k w f t i * * Y � * � � � * * * * # # � FLOW PROCE55 FROM NODE 82p1.�� TO N�DE 8202.00 IS CODE = 2 UPSTREAM NODE $202.00 ELEVATION = 285_61 {FLpW xS SUPERCRITICAL} ------------------------------------------------------------------------------ CALCULATE I�?AN}•fOLE LOSSES (LACFCD) : PYPE FLOW = 7.40 CFS PIPE DIAMETER = 24.00 INCHES AVERAGED VELOCITY HEAD = Q.699 FEE'i' HMI$ _.05*(AVERAGED VELOCTTY HEAp} _.05*( 0.699) = 0.035 ------------------------------------------------------------------------------ 3VODE 8202.00 : HGL =< 286.525>;EGL= c 286.958>;FLOWL3NE= < 285.61Q� �,.*.*+w.,,,,.,*.**�«*+��.+�.�++***��***+***++»**,.*..�.***+*�*�+*�++++�******�***�« FLOW PROCESS FROt+S NOi]E 8202.00 TO NODE B203.00 IS CODE = 1 [3P5'FRE.�hi NQL7E 8203.40 ELEVATION = 286.01 (FLOW �S SLIPERCRITICAL) CALCUI�ATE F}tICTION L055ES (LACFCD) : PIPE FLbW = 7.4a CFS PIPE DIAMETER = 24.Q4 INCHES PIPE LEI+IGTH = 2Q.Q0 FEET MANN�NG'S hF = Q.02400 ------------------------------------------------------------------------------- NORMAL DEPTH(FT} - 0.91 CRIT�CAL DEPTH(F'I') = 0.97 ------------------------------------------------_------------------- UPSTftEAM C0�3'I'ROL A55UMED FLOWDEPTH ( FT} - p. 9'7 ------------------ GRADUALLY VARIED �LOW PROFILE COMPUTED iNl�'ORMATION: DISTA�FCE FROM FLOW DEP'FH VELOC�TY SPECIFIC PRESSURE+ CONTROL ( F"I' } ( FT 1 ( F'i' / SEC 1 EA3ERGY ( FT } MQMENTUM { pQ[JNDS 1 O.d00 Q.966 9.920 1.343 ZO$.95 O.Qa3 0.964 9.934 1.343 1Q8.95 0.011 D.962 9.948 1.343 148.96 . O.Q25 Q.960 4.962 1.343 1d8.96 Q.045 0.958 4.977 1.343 108.97 Q.073 D.956 4.991 1.343 108.97 0.109 ' 0.954 5.006 1.343 108.96 D.153 0.951 5.020 1.343 709.00 0.207 0.949 5.035 1.343 109.D1 _ 0.272 0.947 5.050 1.343 1fl9.02 0.350 0.945 5.054 1.343 109.04 fl.442 0.993 5.079 1.344 109.Ob 0.549 0.941 5.094 �.344 109.08 0.676 0.939 5.�09 �.344 109_IO 0.824 0.936 5.124 1.344 309.22 0.999 0.934 5.14D 1.345 109.15 1.206 0.932 5.155 1.345 1Q9.18 1.452 0.930 5.17D 1.345 109.21 1.748 D.928 5.166 1.346 109.24 2.109 0.92b 5.2�2 1.396 109.27 2.559 �.923 5.217 1.346 109.31 3.�38 0.92�. 5.233 �.397 109.34 3.922 0.919 5.299 L 347 1D4.38 5.D79 Q.917 5.265 1.348 109.92 7.150 Q.915 5.281 1.348 �09.47 . 20.000 d.915 5.283 1.348 �Q9.47 ----------------------------------------------------�_------------------------ NODE 82D3.00 : HGL = � 286.476>;EGL= � 287.353>;FLOWLINE= < 286.010> **rr**a*a�+***yft**��**v�t***+++r�**xwsx*x+xx****+++*x*****�+i.**+xi��,r+wi��+,i.*+x• FLOW PROCE55 FRQ2+1 NODE 6203.00 TO NODE 8203.00 I5 CODE = 8 UPS7'FZEAM NpDE 82p3.40 ELEVATION = 286.01 {�'LOW I5 SUBCRITICAL} ---- --------------------------------------------------__ • CAI_,CllLATE CATCH SASIN EN`iFtANCE LOSSES SLACFCD? : � PYPE FLOW = 7.40 CFS PIPE DIAT'fETER = 24.00 �NCHES FLOW VELOCI'i`Y = 4.92 FEET/SEC. VELOCITY HEAD = 0.375 FEET CA'i'CI3 BASIN ENEAGY LOSS =.2� (�IELOCTTY HEAD) _.2� ( 0.37b) = 0. 075 -----------------------------------------------------------------------------�- � NODE 6203.OQ : HGL =< 287.42$>;EGL= < 287.426>;FLOWL�NE= � 28b.010> ,.*�.*..*.�++t:.*s��.*f++++*+*�*.**.+++��.+.�f*t**r**�.«+:**�*+�*�:�r�r�**�r�. UPSTRE.�M PIP� FLOW CON'9'ROL DATA: NODE NUMBER = 8243.00 FLOWLINE ELEVATION = 286.01 ASSiJr4ED UPSTREAM CQNTROL HGL = 28b.98 FOR �pWNSTREAM RUN AI3ALYSES -----------------------------____--_---_______..__--_----------------------------- ------------------------------------------------------------------------------ EI317 OF GAP.Dl3P.LLY VARiED FLOW ANALY5I5 � • � APPENDIX 4.�,�.6 SYSTEM 8300 s s {. ♦*+w*w>x*w�*wwtx****xxr**r*+***y*w��++****>***++«*+�+xrww«*ti*xr�w��*++t*+x*x*w PiP�-FLQW HYDRAULICS COMPUTER PROGRAM PACKAGE (ReferenCe: LtACFCD,LACRD, AND OCEMA i�YDRALTLICS CRTTERIpN) fc} Copyright 1982-2001 Advanced Engineering Software (aes} Ver. 8.0 Release �ate: O1/O1/20D1 License ID 1549 Analysis prepared by: ProjectDesign Cansultants 741 B StrEet, Suite BDO 5an D�ego, CA 92101 {519} 235-6471 ***r*,r,r**,r*,krw�*******fw*+ BE$CRIPTIObi OF STUDY *«y+..*+fx*+*++***r.*ww*�** * BRESSI P,.ANCH - Ui��'IMATE CONL?ITIONS * * SYSTF�7 8300: SD NO. 5& 6 P�R SHT 21 OF DWG. 444-8C * * 100-YEAF2 STORM EVENF * �r�a�s+�*i�*rtyft****t*f*****rr*xww,ri.*,r++a**a*********�+*++ww+s:ww*rti+**trt+a FILE NAM�: C:12244\8340-1ii.DAT TII�4E/DATE OF STUDY: 14:02 10/23/2002 **t********+*+�**+****«x**�**�*****..*...�.�**�*.*�.�.�>.Wt***.,*******+**....�+* GRADUALLY VARIED FLOW ANALYSIS FOR PIPE SYST�t+I NODAL POINT STATUS '�'ABLE (Nate: "*" indicates nodal poin� data used.) UPSTREAM RUN DOWNS`i'REASS RUN NODE I�ODEL PRESSUR� PRE55iTfiE+ FLOW PRE5Si3RE+ NCTt4BER PROC ES S HEAD { FT ) MOi+SENTUM ( PQUNDS } DEP'I'H ( FT ] t+lOMENZ`i73+4 ( POUNDS } 6300.00- 1.b8 Dc 474.9� 0.56' 1335.07 } F1�TCTION 63�1.Q�- 1.58 Dc 474.9� 0.54* ].394.6D } FRICTIbN 8302.00- 1.b8 Dc 474.95 1.26* 530.01 } Mp,NHOLE • 8303.00- 1.68 Dc 474.95 1.41* 495.28 ? FRIC'T'ION 8304.00-- 1.68"Bc 474.95 1.66*Dc 479.95 ? CATCH BASIN 6304.00- 2.SA* 360.09 1.68 Dc 136.18 ------------------------------------------------------------------------------ M.�}CIt+1UM I3iJMBER OF EI3ERGY BA�,ANCES USED IN EACH PROFILE = 50 ------------------------------------------------------------------------------ ?�10TE : S'I'EADY FLOW HYDRAULYC HEP.D-L(}SS COMPiJ'I'ATIONS BASED O�i 7'HE i+IOS`I` CONSERVATIVE FORNIULAE FROM THE CURRENT I.,ACRD,LACFCD, ANA OCEMA DESIGN MANL3ALS. *******+*�***+*+*�+*,.**�«******++�r�+�**«*x*t**t***�+t***+t**+****+,.+****�*+�+ DOWNSTFtEAM PIPE FLOW CON�'ROL DATA: NpDE AiUMBER = B300.00 FidWLINE ELEVATIOF�i = 193.10 P�PE FLOW = 22.2Q CFS PIPE I3IAMETER = 24.00 I3�ICFiE5 ASSUMED DOW�ISTREAM COPPI'ROL HGT.� = 194.780 FEET *NO'�'E: ASSi.iN4ED DOW3dSTREAM COI3TROL DEP'i'H ( 1. 6B F"I'. ) IS LESS Tf-L�id CRI'i`ICAL DEPTH ( 1. 68 FT _} _=_> CRI'FICAL DEPTH IS ASSUMED AS DC3WN5TRF�iM CONTROL DEPTH • -------FOR UPSTREAM Ri.JIV ANALXSIS ---------------------------___--_-------------------------------------- i• NODE B300.00 ; HGL =< 193.661>;EGL= � 2fl8.383>;F�OWLINE= <�93.100> ******�****,t*.�t��*.*k*w***��x��*******.**.***.» ****w**.*.*�«�****w»**. FLOW PROCESS FROM NODE 8300.00 TO NQDE 63fl1.D0 IS CflDE _� UPSTR�a.M NODE B3fl1.00 ELEVATION = 193.14 (FLOW I5 SUPERCRITICAL) ------------------------------------------------------------------------------ CR�CULATE FRiCTION L055E5fLACFCDI: PIPE FLOW = 22.20 CFS PIPE DIAMETER = 24.00 INCHES PIPE LENGTH = 4.04 FEET t+3.�NN�NG'S N� 0.41300 ------------------------------------------------------------------------------ NORMAL DEPTH(FTj = 1.61 CRITICA� DEPTH{FT} = 1,68 LTPSTREP.M CONTROL ASSUMED FLOWDEPTH(FT} � 0.54 GRP.DUALLY VARTEA FLOW PROFiI.�E COMPUTEA INFORMIaTI03d: DISTANCE FROM FLOW DEPTH VEI,OCITY SPECIFIC PRESSURE+ CONFROL ( FT ) ( F'F j ( FT / 5EC } ENERGY ( F'F ) MOMENi'UM ( POLTNDS ) 0.440 0.543 32.183 16.635 1394.60 4.Ob0 0.560 30.782 15.283 1335.07 ----------------------------------..__----------------------------------------- NODE 83D1.00 : HGL =< 193.683>;EGL= < 249.776>,F�OWLINE= � 193.140> t�kt++***w*�+****wx+*+**+*w*w****w**,r*,rw**w+******yt***r***fs�k�*+*w**+i.�r�w+*+** FLOW PROCESS FROM NdD£ 830�.00 TO AiODE $302.00 IS CODE = Z U�STREP.M NODE 8302.OD ELEVATIOAi = 234.39 (FLpW IS SUPERCRITICAL) ------------------------------------------------------------------------------ CALCULATE FRTCTION L055ES(LACFCD}; • PIPE FI,OW = 22.20 CFS PIPE DIAMETER = 24'00 �NCIiES PIPE L�1GTH = 100.00 FEET M.�NNING'S N o.o�3aa ------------------------------------------------------------------------------ NORM.�.L DEPTHfFT) = 0.53 CRITICAL DEPTH(F'i') = 1.6$ ------------------------------------------------------------------------------- UPSTREAi+I CONTROL ASSUMED FLOWDEPTH(FT} - 1.26 GRADUALLY VI�iRIED FLOW PROFILE COMPU�`ED INFORl�i.�TION: ------------------------------------------------------------------------------ DI5'I'ANCE FROM FLOW DEP'I'H VEI,OCI�`Y SPECiFIC PRE55iJRE+ CONTROL(FT} {FT} (FT/SECj ENERGY{FT) MOMENTUM(POUNDS} 0.004 1.258 1a.655 3.025 53D.01 0.0&7 1.243 ].0.&13 3.450 534.44 0.181 1.229 1D.964 3.497 539.10 4.281 1.2�4 11.120 3.236 544.00 4.387 1.200 11.282 3.�77 549.14 0.500 1.185 11.448 3.221 5�4.53 D.621 1.17Q 11.620 3.26$ �64.18 0.750 1.156 11.798 3.3�9 566.11 0.8B8 1.141 11.962 3.372 572.32 1.034 1.127 �2.172 3.429 578.82 1.191 1.112 �2.368 3.489 585.63 1.358 1.097 12.572 3.553 592.76 1.53b 1.083 12.782 3.621 600.22 1.727 3.068 13.040 3.694 50B.�2 �.930 �.fl54 13.225 3.771 616.19 2.147 1.039 13.459 3.854 624.73 • 2.379 1.424 13.701 3.941 633.57 2.628 1.010 13.953 4.035 643.42 �• • � 2.899 3.179 3.485 3.819 4.1b7 4.546 4.956 5.397 5.879 6.390 6.950 7.5�8 8.221 8.943 9.734 10.643 11.559 12.616 13.794 15.100 16.569 18.229 20.116 22.285 24 . B04 27.772 31.333 35.712 .41 .2B2 48.74B �9.693 79.193 100.000 �.995 0.98� o.s�� 4.952 0.937 4.922 d.908 0.893 4.879 0.864 0.849 �.$35 0.820 0.806 fl.79� 0.777 0.7b2 4.797 4.733 0.73$ 0.704 Q.589 4.574 4.56Q 0.645 0.531 O.b16 0.602 0.587 0.572 0.558 0.543 0.543 1A.213 �4.484 19.755 15.057 15.360 15.57fi 15.405 16.347 1b.703 17.075 �7.453 17.858 18.291 18.734 19.197 19.582 2D.�9D 20.723 2�.283 21.$71 22.490 23.142 23.829 24.5�4 25.320 26.131 26.990 27.90� 28.&59 29.898 30.995 32.165 32.183 9.134 4.240 4.353 4.479 4.603 4.741 4.866 �.045 5.214 5.394 5.586 5.796 5.019 5.259 6.517 6.795 7.096 7.420 7.771 8.151 8.563 9.010 9.497 10.028 10.607 11.240 11.935 12.697 13.536 �4.451 i5.484 �6.518 �6.536 552.81 663_a4 673.�5 584.96 695.74 7Q8.98 72Z.85 735.32 744.45 754.25 779.77 796.06 813.15 831.�0 844.9b 669.79 B90.55 912.6Q 935.73 96R.1� 985.84 1013.4Q 1041.71 1072.Q9 1104.25 1138.35 1174.55 1213.02 1253.95 1297.56 1344.09 1393.83 1394.6� NODE 8302.00 : HGL =< 235.59B>;EGL= < 237.365�;FLOWLINE= � 234.34a> * 1r * f� Yr Yr f Yr Yr Yr yr k�F Y� Yr Yr Yr k k* i*** ir *�r #* i t t�t t�k t t** tk �t *�Jr 4* Yr yr ** t�t i�Ir i* Y�1 ** yr f yr yr y� t y� yr yr t�k #*# yr yr ## Yr FLOW PROCESS FROM NODE 83D2.00 TO NODE $303.00 IS CObE = 2 UP5'i'REP.M NODE 8303 . DO ELEVATI033 = 234 . 67 (FLOW IS Si3PERCRIT�CAi) ------------------------------------------_-_---------------------------------- CALCULATE MANHOLE LpSS�SILACFCD}: PIPE FLOW = 22.20 CF5 PIPE DIRM£TEFi = 24.00 INCHES AVERAGED VELOCiTY HEAD = 1.565 FEET HMN =.05*(AVE�iAGED VELOCITY HEAD) =.05*( 1.565) = 4.0�8 ---------------------------------------------------------------____------------- NODE 8303.00 : HGL =< 23b.682>;EGL= < 237,444>;FLpWT,irrE= < 234.670> �*....�*+*t.�+*.w�t++*****>�.**.*.**�+**�»******+****»*.*.,-**.**********.****** FLOW PROCESS FROI�i NODE 8343.00 TO NODE 6304.00 IS CODE = 1 UPSTREAM NODE 8309.OD �LEVATION = 234.99 (FLOW IS SUPERCI��TICALi CA�,CULATE FRICT'ION LOSSES{�p�FCDj: PIPE FLOW - 22.20 CFS PIPE DIAMETER = 24.00 iNCHES PIPE LENGTH = 16.00 FEET MANNING'S N= 0.41300 -------------------------------.._________.._----______------------------------- NORMAL DEPTIi{��) = 1.23 CRi'iiCAL DEPTH(F'Fj = 1.68 � --UPSTREAM-CONPROL-ASSUMED-FLOWDEPTH(F�1-----==1=68========--vT^F--"==_______ GRADUA%,LX VARIED FLOW PROFILE COMPUTED T13F'ORMATION: ----------------------------------------------------------------_____---------- DISTANCE FROM FLOW DEPTH VELOCITY SPECIFIC PRESSURE+ CONTROL(FT} (FTj (FT/SEC) ENERGY(FT} MOMEN'I'UM(POT3NDSj 0.000 i.b81 7.872 2.644 474.95 0.011 Z.672 7.914 2.644 474.98 0.045 1.663 7.948 2.645 475.04 D.102 1.654 7.988 2.645 475.14 0.163 1.545 8.D28 2.646 475.29 0.289 1.536 8.468 2.647 475.48 0.422 1.527 $.110 2.549 475.71 Q.582 1.618 8.153 2.650 475.99 �.770 1.6�8 8.196 2.652 476.31 0.9B8 1.599 8.240 2.654 476.68 1.238 1.590 8.285 2.657 477.69 1.520 1.5$1 8.331 2.660 477.55 1.837 1.572 8.378 2.663 478.45 2.190 1.553 8.426 2.656 478.51 2.581. 1.554 8.474 2.674 479.21 3.012 1.545 8.524 2.674 479.85 3.4B6 1.535 8.574 2.678 484.55 4.005 1.525 8.625 2.683 481.34 4.571 1.517 $.678 2.b88 482.14 5.189 1.508 8.732 2.693 482.95 5.Bfi1 1.499 8.785 2.599 483.85 6.591 1.490 8.842 2.705 484.80 . 7.383 1.481 8.898 2.711 485.81 8.241 1.472 8.955 2.71$ 48b.87 9.172 1.4b3 9.Q14 2.725 487.99 10.180 1.454 9.a74 2.733 4$9_15 11.271 1.444 9.135 2_74� 49�.39 12.454 1.435 9.197 2.750 49�.58 13.736 1.425 9.264 2.758 493.03 15.126 1.417 9.324 2.76$ 494.44 16.000 1.412 9.362 2.774 495.28 NODE 8304.�0 : HGL =< 236.571>;�GL= � 237.534>;�'LOWI,IN�= � 234.990> �,.****.**««**�**«**.*************«**********�*********«**�***�*****�****«�**** FLOW PROCE55 FROM NODE $304.40 TO NODE $304.40 i5 CQDE _$ UPSTREANi NODE 8304.00 ELEVATION = 234.99 (FLOW I5 AT CRITICAL DEPTH} ------------------------------------------------------------------------------ CALCULATE CATCH BASTN EN'I'RANCE LOSSES{LACFCD): P�PE FLOW = 22.2D CFS PIPE DIAMETER = 24.D4 INCHES FLOW VELOCITX = 7.87 FEET/S�C. VELOCTTY HEAD = 0.963 FEE'I' CATCH BASIN EIdERGY L05S =.2*(VELOCITY HEAD) =.2*( 0.963) = 0.�93 ------------------------------------------------------------------------------ NOAE 83DA.00 : HGI� _< 237.827>;EGL= < 237.827>;FLOWLINE= < 234.990> ,-************.**��*t*********�***********«**�**�*�**�*********.*********«**** UPSTREP.M PIPE FLOW CON'I'ROL DATA: NODE NEJMBER = 8304.OD FLOWLINE ELEVATTON = 234.99 ASSUMED UPSTREP.M CONTROL HGL = 235.67 FOR DOWNSTREAiI RUN AI+I�LYSIS � ------------------------------- i � � ! � r****�r*****xx+xr�**�*��*�***��rx*�x+++*+rtt*�i��wx�*+w*++ax++**ry:trtrti*ty**+ PIPE-FLOW HYDRAULICS COMPUTER PROGRASyI PACKAGE (R�ference: LACFCD,LACR]], AND OCEMA HYDRAULICS CRITERIONj (cj Copyright 19B2-2002 Advanced Engineering Software {aesl V�r. 8.0 Release Date: O1/O1/2002 Lfcense ID 1509 Analysis prepared by: PROJECT DESIGN CbNSULTAN'FS 701 'B' STREET, SUITE 8Q0 SAN DIEGO, CA 92101 619-235-6471 �f�**+�++��.�,r+++++«++.+�� DESCRIPTION dF STUDY <*<**.�.��*.*..�..***.�.+. * VELOCITY CHECIC QN ST�EP i�AT�RAL PIPES * * * „ + �1YrtlYY�i�!**f f*i �rt 1� tY� *Yr #*********ikik*1rYrY•**!� i�f*##'M t t� i ik�L��i*#*1 Y� i***Y 1 Y Y� f i! 1YYY FILE NAME: 2244VEL.DA`i' TIME/bATE OF STUl7Y: 15:57 Ol/21/2403 �F*YrYrik??Yr1r*Yr?*YriF*i�i*Yc*i� i� * * *�1�##ii **�� ** 4 YY * #tii! * i� Yr #'kir# �F * �k **Yi Y� f1r**ikiF1� *YrY� Y� YrYr?*Yr* GRADi3ALLY VAKIE� Fi�OW ANALYSiS FOR PIPE SYSTEM NODAL PO�NT STATUS 'iABLE (DIote: "*' indicates nodal point data used.} UP5'�'REAM RUN D[?WNSTREAM RUN NQDE MODEE, PRESSURE PRESSURE+ FLOW PRESSURE+ NUMB�R PROCE$S HEAD{FT} MOMENTUM{p0UND5} pEPTH(F'i) MOMENTi3M(POUNDS) . zaaa.oa- i.is Dc 154.85 Q.67* 2�8.49 } FRzcTxo� ioa�.oa- 1.��*Dc 154.86 1.16*Dc 154.86 ) CATCH BASIt+i 100I.04- 1.85* 122.50 1.16 Dc 47.87 MAXIMUM NLTMBER OF F.1�3ERGY SAL.ANCES USED �N EACH PRpFILE = 25 NOTE: STEADY FF,OW HYDRAULTC HEAD-LOSS COMPU'i'ATIOi�i5 BASED ON TiiE MOST CONSERVATEV� FORN4CTLAE FRQM THE CURRFNT LACRD,LACFCD, AND OCEMA DESIGN MANUALS. t*t*YrYrYr*YrYr�FYriF*f Yr*�h *�h f1# k** k iF ***i� *Yi'� f f 11 f'k i i t##* 1� �***ir* i� i� *'k***� i� ****Yr*Yrf YrYr�Jr*#* DOWNSTREAM PIPE FLOW CON'i'ROL AATA: NODE I3UMBER = 1000.00 FLOWLIl�TE ELEVATI033 = 311.88 PIPE FLOW = 9.OD CF5 P�PE DIAMETER = 18.D0 INCHES ASSUMED DOWI3STREAM CONTAOL HGL = 3� 2. 0 DQ FEB'1' *I30TE: ASSiiD4ED DOWfVSTREAM CQNFRQL DEP'FH { 0. 12 FT. ) I5 LESS Tl-IAEV CRI'f`ICAL DEP'FI-3 ( �.� 6 FT .} ___> CRTTICAL DEPTH IS ASSUMEB A5 DOWNSTREAM CONTROL DEPTH FOR UPSTRF.AM RUN RN7�LYSIS ------------------------------------------------------------------------------- NODE 1000.00 : HGL =< 312.551>;EGL= � 314.b96>;FLOWLINE= < 311.$$0> +*+++++.�+**++.,�+*.�v�,+,��.�.�,�.*+*�****..**�**.*.*+**,,**�.�+**+++**+**++.w�*.+ FLOW PROCESS FR4M NOdE 1000.00 TO NODE 1001.Q0 IS COBE = 1 UPSTREAM NODE iaai.ao ELEVATTON = 313.09 (FLOW IS SUPERCRITICAL) --------------------------------------------__--_-_----------------------------- CALCULATE FRICTION LOSSES(LACFCDf: PIPE FLOW = 9.00 CFS PIPE DIAP3ETER = 18.00 INCHES PIPE LENGTii = 9.84 FEET MAI�I3ING'S N = 0.01300 � ---------------------------------------------- -------------------------------- � �^NORMP.L-DEPTH(FT)========0=�2===^^^=====CRITxCAL-DEPTHIFT)===^„YV'1^16=====__ UPSTR.EAM CONTRpL ASSi.73+3ED FLOWDEPTH(FT) = 1.16 GRADUALLY VARIED FLOW PROFILE COMPUTED ENFORMATIOd3: ------------------------------------------------------------------------------- DISTANCE FROi�7 FLOW DEP'FH VELOCI7'Y SPECIFIC PRESSURE+ CON'I'AOL ( FT ) ( FT } { F'P / SEC ) ENERGY ( FT ) MpMEAI7'UM ( PQ[7i�IDS f O.Q00 1.151 fi.133 1.745 154.66 0.407 �.131 6.245 1.747 155.01 0.428 1.101 6.47fl 1.752 155.47 0.066 �.072 6.660 1.761 156.25 0.124 1.092 6.866 1.775 157.39 0.202 1.D12 7.089 1.793 158.90 0.306 0.983 7.332 1.828 160.82 0.438 0.953 7.595 1.899 163.18 D.605 0.924 7.881 3..889 166.02 a.810 D.894 8.192 1.937 169.38 1.063 0.864 8.532 1.996 173.32 1.371 0.$35 8.904 2.067 177.90 i.747 D.805 9.312 2.152 i$3.I9 2.205 0.776 9.760 2.255 189.2b 2.764 0.746 10.254 2.379 19b.2� 3.449 D.716 16.8Q0 2.529 204.i7 4.293 D.687 11.407 2.708 213.26 4.840 Q.b7� 11.75Q 2.816 218.49 -------_--___---------------------------_-------------------------____----------- NODE 1001.00 : HGL =� 3�4.251>;EGL= t 314.835�;FLOWLINE= < 313.090> yi*+a*+**�wx*+w+*+**�tt�t*yv�*�t*+r**axx***iftiti��***ers++*+rt*f*t***a+**w*,ti�f,��l.* � FLOW PROCESS FROM NODE 1001.00 TO NODE 1001.00 IS CODE _$ UPSTREAM NdDE iaai.oa ELEVATION = 313.d9 (FIAW UNSEALS IN REACHj ----------------------------------------------------------------_--------------- CALCE]LATE CATCH BASFN ENTRP.NCE LOSSES{LACFCD): P�PE FLOW = 9.00 CFS PiPE DIAMETER = 18.00 INCHES FLOW VELOCTTY = 6.13 FEET/SEC. VELOCITY HEAD = 0.584 FEET CATCH BASIN �1VEAGY LQSS =.2*IVELOCITY HEADj =.2*{ 4.584) = 0.1].7 -------------------------------------------------------------------------�__-- PFODE 1001.Q0 : HGL =< 314.952>;EGL= < 314.952>;FLOWLIi3E= < 313.090> *}y� #�Jrti i Y?#tY� # t**1r* *?'kYrYr iF M' *'kYr*it�'tY1 �k y i***'M Yi'k iF'k'!r *# Y�1� *# i#yY y�#*#**i Y� 1 YY Y***�r*Yr�1rYi #Y� UPSTREAM PIPE FLOW CONTRbL DATA: . IVODE NUMBER = 1Q0�.00 FLOWLINE ELEVA'I`ION = 313.09 ASSUMED UPSTREAM CONTROL HGL = 314.25 FQR DOWNSTRF�AM RUN ANALYSIS END OF GRADUALLY VARIED FLAW Ai�iALYSIS � I � t * * * k % * * * * * * * t * Y � * 4 w i t * � * * * � # i 1 t k * # t * * * * * * � * f * * * * * * * � t * * * } # * * k # � * k 4 * * * * * * * * * * * PTPE-FLOW HYI?RAULICS C�MPUf'EF2 PROGRAI� PACKAGE (Reference: LACFCD,LACRD. AND OCEMA HYbRALFLIC5 CRITERION) (c) Copyright 1982-2042 Advanced Engineering Software (aes) Ver. 8.0 Release Date: 01/O1/2002 License ID 1509 Analysis prepared by: PROJECT DESIGN CONSULTAN'I'S 70i 'B' STREET, SUiTE 800 SAN DIEGO, CA 9210i 619-235-6471 +***��***��*ww*++w�,rww**** DESCRIPTZON OF STUDY �+++,r*+*a**�*��*****a****� * VELOCITY CFiECK ON STEEP LATERAL PIPES * �, . * * �li Y t 1 i�i 4f f*ik*+Y*#+i � f�1 �kiY 4�k! Y Y* t Y� Y t#i! Y Yt*t t* * i i!*�!**Yt # f�**Y�k�Y4Yf #�!*i t**♦ FILE NAME: 2294VEL3.DAT TIME/DATE OF STUDY: 16:39 Oi/21/2003 **��**�***.*******.*****,�,.*�.****��„�,,��**+�**++*�*..�*+.*.,.,.*.**.�**�*x**++* GRADUALLY VARIED FLOW ANALYSYS FOR PIPE SYSTEM NODAL POI�PI' STATUS �'ASLE (Note: "*" indicates nodal point data used.l UPSTRE.�M RUN DOWNSTREADS RUN NODE MODEL PRESSURE PRESSURE+ FLAW PRESSURE+ NLTMBER PROCESS HEP.D ( FT} MOMENT�I'M ( POUNDS J DEPTH ( F'f' j M0�7EN'I`UM ( POCTNDS ? •' 1000.00- 1.22 Dc 179.35 D.54* 384.98 ) FRICTION 104�.OQ- 1.22*Dc 179.35 1.22*Dc 179.35 ) CATCH BASIN ioai.ao- z.oi* �38.58 1.22 Dc 53.33 �+3AXIMUM NUMBER OF ENERGY SAI,ANCES i3SED 3N EACH PROFILE = 25 I30TE: STEAFIY FT..OW iiXDRAULIC HFR.D-LOSS COMPUTATIObTS BASED O�I THE MOST COI3SERVA�'�VE FORhEULAE FROM 'FHE CURRENT LACRD, iaACFCD, ANU OCEMA DESIGN MAN[JALS . f*i Y Y fYrt*** ** *�k # tM k tk�k *1r�k*}1r * t****Yr** * k k fi* fr **YrYr**MYrf Y� �k k Y�1r fYrYr*Y� k k k Yr�M 1rikYi fYr*YrYr! ***# DOW?�iSTRF.AM PIPE FLOW CQNFRQi� DATA: NpDE NLTMBEA = 1000.00 FLOWLINE ELEVATION = 140.fl0 P�PE FLOW = 1d.00 CFS PIPE DIAF7ETER = 18.00 INCHES ASSUMED DpWNSTREAM CONTRdL HGE� = 101.000 FEET *NO'I'E: ASSUMED DOWNSTREAM CONTROL DEPTH( 1.00 FT_) IS LESS THAN CRITICAL DEPTH( 1.22 FT.) -__> CR�TICAL 1]�PTH IS ASSUi�E]] AS DUWNSTRF,AM CON'PRQL DEP'I'H FOR E3PSTREAM RUN ANALYSIS ------------------------------------------------------------------------------ NODE 100D.fl0 : HGL =< 100.498>,EGL= < lOb.418>;FLOWLINE= < 100.000> *,-+�***.�***+�+*****�**�*�***�++**++#***+#��tt++**��.+,�+�.+*�++�****w�*�*.�..+ FLOW PROCESS FROM NODE 1040.04 TO FIODE iaot.oa IS CODE = 1 UPSTRF.AM NdDE 1001.00 ELEVA'i'30N = 107.54 (FLOW �S 5l3PERCRI'i`ICAL} ------------------------------------------------------------------------------ CALCiFLATE FRICT�ON LOSSES(LRCFCDI: P�PE FLOW = ZQ . DO CFS PIPE DIAME'I'EK = 18 . 04 T33CHES PFPE LENGTH = 30.00 FEET --MP.NNING'S N= 0.01300 • ----------- ---------------------------------- ---------------------------- NO�L DEPTH(FTj---_____0_49___ CR�TZCAL DEPTH{FT} = f.zZ � -------------��-�-�----------------------- -------------------------------- " UP57'RF.AM CONTROL ASSLTMED FLOWDEPTH (FT} = 1.22 -------------------W--_----------- GAADUALLY VARIED FLOW PROFiLE COMPUTEb INFORMATION: D�STANCE FROM FLOW DEPTH VELOCI�'Y SPECIFIC PRESSURE+F` ` CONTROLIFT} (FTj (F'I'/SEC} ENERGY(FT) MOMENT[3I�(POUNDS} O.00D 1.219 6.50Z 1.875 179.35 4.008 1.188 6.66i 1.677 174.52 O.d3Z 1.157 6.835 1.883 180.45 0.073 1.126 7.027 1.893 180.95 0.136 1.095 7.235 1.9Q8 �82.26 Q.222 1.064 7.460 �.928 184.00 0.335 1.�33 7.706 I.955 186.2D 6.48D �.002 7.973 Z.989 188.91 0.660 0.971 8.26A 2.032 192.17 D.8B4 0.940 8.581 2.a89 19b.02 1.157 Q.909 8_926 2.147 2Q0.53 1.491 �.878 9.307 2.224 2D5.77 1.895 0.847 9.723 2_316 211.80 2.390 0.816 10.�83 2_426 218.73 2.99Z 0.785 10.686 2.559 226.67 3.727 0.754 11.245 2.71$ 235.74 4.634 0.723 11.866 2.910 246.10 5.762 0.692 12.558 3_142 257.93 7.162 0.661 13.334 3.923 271.46 9.001 0.63� 14.206 3.765 285.97 11.3$5 Q.599 1�.194 4.185 304.80 14.519 0.558 �6.3i8 4.7D5 325.37 19.239 4.537 17.508 5.354 349.22 i 26.456 0.506 19.Q97 6.172 377.05 30.aa0 0.498 19.520 6.416 384.98 --------_-----------------------------------------------------______------------- NODE 1441.DD : HGL =< 108,719>;EGL= � 109.375>,FLOWLINE= < 107.540> ***«*****�,..��+�.*�.��****.��..*.**�*t*+++�+..*w.��**+*****�**.�***.«�t*��*... FLOW PROCESS FRpM NODE 1001.00 'I`0 1VODE 10Q1.00 IS CODE = 6 UPSTRF�M NODE �00�.4� ELEVAT�OIV = 147.50 (FLOW UI3SEALS IN REACH) ------------------------------------------------------------------------------ CALCUIsATE CAi'CH BASIN ENTRPNCE i,QSSES {I,ACFCDj : PIPE FLOW � 1D.OD CFS PIPE DIAMETER = 18.Q0 TNCHES FLOW VELOCTTY = 6.50 FEET/SEC. VEiOCITY fiEAD = 0.657 FEH'f' CATCH BASZN k�7ERGY L05S =.2*(VELOCITY HEAD) _.2"'f D.657) = 0.131 __---_------------------------------------------------------------------------- NODE 1001.00 : HGL =< 109.507>;EGL= � 109.507>;FLOWLZNE= < 107.500> ,,*.*****.*.�*�...**�.�.******...****..***�..:�+ti.+.*******.*��**+*.��.*�..�*+t i3PSTAEAM PIPE FLOW CONTROL DATA: NODE NLTMBER = 1p01.00 FLpWLINE ELEVATIOI3 = 107.50 ASS[TI�iEL7 �PSTR�P„I�4 CONTROL HGL = 108.72 FOR DOWidSTREAN3 RUN ANALXSIS ____�------------------------ END OF GRAUUALLY VARIED FLOW ANALYSIS � �� . u