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CT 80-15; CARLSBAD COMMERCIAL CENTER; HYDRAULIC ANALYSIS; 1980-12-17
.... --.,; II. STUDY CONSIDERATIONS HYDROLOGY STUDY: DISCUSSION Pipe sizes are determined by using 90 percent of the natural gradient· of the land as approximating the friction slope and assuming non-pressure pipe flow. Each confluence point was evaluated as to· that combination of downstream hydrology occurrences to generate a maximum runoff peak. Consequently, a lower Ittime of concentration" is used in this section of watershed. Sections III and IV of this study includes the detailed computer analysis for the IO-year frequency and two-year frequency storms respectively. HYDROLOGY ANALYSIS: DISCUSSION The program utilized for this study specializes in pressure flow pipe systems where energy losses are determined per LACFCD and OCEMA standard emperical relations. The pipe system is schematically represented by a sequence of nodal points. Each point represents a specific head loss or junction feature, and is notated by a hydraulic station for reference to the computer output. Wherever the pipe unseals, the pressure-flow assumption fails. Accordingly, the next hydraulic station assumes "soffit contror' for the hydraulic grade line (HGL). Both the energy grade line (EGL) and the HGL are included with the provided computer results. Sections V, VI, and VII include hydraulic analysis of the proposed storm drain system. 792~8 2 0 ~ :c 0 en 0' Z <C Z 0 en ~ <C ::i ..J ~ /!' ...; COMPUTER MODEL The computer analysis calculations are referenced to selected points within the watershed by means .of nodal points. All calculations are presented as required for review of the analysis. San Diego County Regional standards are utilized within the model. Hydrology maps' are available which show the nodal point designation scheme, subareas, and other pertinent information. The nodal point designation for hydraulic ana~ysis is shown in Fig. 1. ' 79298 3 0 ~ I () C/) 0 z « Z 0 C/) ~ « ::J ~ 3 " f' .,. ,I. INTRODUCTION PROJECT LOCATION The, development is a commercial development west of 1-5 and south of Cannon Road consisting of approximately 22.7 acres, l,?cated in the City of Carlsbad. This development also includes the completion of the link between Cannon Road and the eXisting northerly end of Avenida Encinas STUDY OBJECTIVE The objective of this study is to develop a computer model of the entire watershed study area in order to evaluate hydrologic responses to storm events. The basis of the model is the Orange County Environmental Management Agency (OGEMA) 1973 Hydrology Manual outline of the "Rational Methodtl, modified to include County of San Diego rainfall intensity/duration information. Included in this primary objective is the ,d~te~mination of peak discharges in cubic feet per second (cfs) at various points, of concentration within the study area. Additionally, pipe size estimates are determined and evaluated for economy and effectiveness of flood control. The watershed is studied with respect to the ten year storm event 'as presented in the San Diego County 1975 hydrology manual. It is the further objective of this study to design the storm drain improvements, based on the data obtained from the hydrology study. STUDY METHOD Determinati?n ,of 'P~ak flows and accommodating pipe sizes for the ten year storm event is based on OCEMA hydrology $tanqards. Solutiqn to the governing hydrology/hydra\llic ~odel equations were made 'on' the Williamson and Schmid Data General "Eclipse" digital cqmputer. ' ' " 79298 ; , ,~ ", 1 • -t • • • • COMPUTER DRAINAGE STUDY AND HYDRAULIC ANALYSIS RATIONAL ME'mOD ANALYSIS OF TEN-YEAR STORM FOR CARLSBAD COMMERCIAL CENTER OUR JOB NO. 79298 DECEMBER, 1980 o :2' I U <f) o z « z o <f) :2' « --' --' ;;; J 0 ~ ::r: () CJ) '0 Z <t Z '" 0 CJ) ~ <t '. ::::l ...J ~ ----""-...... "--~-.;..,;~.~,-~,..,...;~~~,.~ .. ,,.I.:: .. -- sL\-!' • e..Ar\ c.PfR..c s Po . t, ~~ "... ....... --~--------.~ ... ---..... --.. ---.. --.. ----..... --.. ----"-----------------------..... -:-.-----.. "':"----...... -~ .. ----- -RAINFALL INTENSITY DATA INPUT , , ( -_ ...... _. __ ._ .. _-------_._-...... -_ .. _------_ .. _------------------_ .. _ .. _------------_ .. _--_ ...... _--------- RAINFALL INTENSITY INPUT ;;--.. _ .... "'-'-'-'-~ -.. --.~--.. --.. -. ... ---.. -.... - ,c-o "", C; TIME(MIN. ) INTENSITY <INCHES) '-. ;; , 5. 00000 . " . 3. 30000 I f-"-' ----6--:-CHYooo .... --3. 2'0000 .. :,c>., . 7.00000 3.00000 '. '8.00000 2.90000 r---"---~.-_._"----M~~~t-·n -~-------..---.. --.-.. ~ .. "";'''-,..r-, .l"\.M+ 'J 9. u00vO .~. IVO,,-;V C i,; 10.,00000 . 2.60000 ;JL .. __ ... ))=-.99qoo ___ ._ .. ~ ____ . 2. 50QOO ..... '., . ...,_ .... _ ... __ ~ .. , __ ~ __ .... ____ ~._. ____ ._ liol 12. 00000 ' 2. 40000 . . " : C 11'L 13.00000 2.30000 '. . . , 1 ~ ~ "'0 .... 0 ..., .... ) ~ Q ~ ,.. . , . . !;2 _~1'. VV V /:' •• "'-v V ... .J .. . . '. . C, ' "11~'lt ---.::::=.::-.::-==:.:.-=-..:.-::-.:::::..-====:.. =~"'''':':':==:':''''': ...:::....::...: ...:.:-.::..:::.:.-::::..~.:.:.. ....:--:....-..:.--. ,:.:'..:. . .::.:..:._ . ..:.-....::....:.....::..:.....:.::.-:..--:...:.::::...:..-::..-::--.::-= .. ::::..--=-- .. .~---------------------------------------------------------~----------------- 151 . P IPE MASTEI~ PL{~NNING OUTPUT DELETED 1 _.------------.-.---.-.. ------.... , .. -.. --...... -_____ . ___ .... _0_. __ .. _ -------.------.. _-' C ; MINIMUM PIPE SIZE USED IS 1ROO' INCHES la' FHICTIOI',1 SLOPE PERCENTI~GE OF NATURAL SLOPE IS 90.00 . L ____ .... ________ ...... ___ .. __ .. ___ ~_ .. ___ .... _", ...... -. -.. --.. ' .. -... . --......... , ... --.... -.... ~.-_ .. _. __ . ___ -~.~ __ f13;' " . ". -' '. 'C !~~:*******~*~****************************************************************** 12,1'.. PROCESS FliOi'1 NODE l:l TO NODE 12 »CODE :::: 10 <.( . " 1,,(--==:::.:===::..=-=::..::..:.:·;:. .. ::.:.::::.:::::.::--.:=:.:.:..:.:-.:...--=.·.:-------.------.----.. ---....:.:.:...:.~-..::.'-:.:::....--:.:.:..:.::....:.:..:::.:...:::.:.:-:.::..::....:.:.:-.:..-..:::: .. :-:.::=..:.:... ... (' L! DEVEUJPt-1ENT IS COl"If"IERCIAL ' " 'ul ~ I r-.... ----.. -'-------..... -... ---.-----.----........ ,-.. , .. ' -...... -, ..... i2\' (~. INITIAL SUBAREA FLOW-LENGTH = 985,0000 (~ 'l ..... UPST~~~~M ... ELEy0T!_q~~ .. = _" ._57:200°. '. I DOWNSTREAM ELEVATION::::: 47.0000 ( ;7'! EU:::V,t1tTION DIFFEHENCE ::::: 10. 2000 .. 1~"l~C~t/l'<~_ R~! .. ! .. !?}~0~ __ !~1~t19D _ T._!I~:_~._ .. C!C ,CONCENTRATION. :::: r1! '. 11. 709(-:; ( ~i '. RAINFALL INTENSITY FOR RATIONAL METHOD TEN YEAR STORM::::: 2. 4290 . j,.;---'" -_ .. _ .. _-------....... ---_ .......................... _. . ....... .. .. -.. ' ........ -...... "'--' ... ---.. ---- -[I C r' ,3,;_' _ .......... ___ ~.--.. ___ ." ...... _ ._ .... _. ".". __ .-_ ... __ ,. . _____ __ 131 SPECIFIED "ell ::-..:. .850 ( 1'~3i' :;)! . ,:~r-----' -... --.. ~--... -... ---.. -........ --............. -. ( I) U DISCHARGE = "5.7810' r-t----....... ---..... ,--.----........ --' .--..... 2. 8000 ~ ---'--.;'--."~-' . ,'J. t ~Ii **************************************************************************** ';" PROCESS FHOI"1 I',!ODE . 12 TO NODg 12 })CODE ::::: 60 « r .... __ ~_ .. ~-~,_ ....... _~ __ 4_*_~~.__ . -----.-. .. ~.- ------------.-------------------------------~-----------~-------------------- ( ':J ·","1' 2. 4290 SPECIFIED IIC" _ : 85'0 '. , ( f~~. 8905 TOTAL G -.. 8. 6716 TOTAL. p.REp. :::: 4·.2000 (' *****·**~'}**~k*-)r**~Hi··H·*·n·****·*oj~·*********-l"~**********************~"**-1~**'IH~*':i-******** ( PROCESB F~~Oi"l NODE 1~~ TO NODE 12 >)-CODE = 1 <:-.::: ----------------------------------------------------------------------------/:~---__:~*-:R· .. ~~~~*****.Jf***-~-1~ii_1( .. *·**1***·H.*****_3:i.****************~ .. *************·**·u·*~ .. *-**-****·**-·· r ' (~ ,., PROCESS FI~m'J NODE ;2:L TO NODE 22 )-)CODE ::::: 10 -«: .. '\. .. ,J. ----------------------------------------------------------------------------! --"-. -. ~----.---. . .... -~.~-~-\... ----.. ~-.-,~ DEVELOPMENT IS COMMERCIAL C, ; ~ , 1 _. -.. --.-.-'------.. -----------, ----, ", , 17 INITIAL SUBAREA FLm~-LENGTH -520.0000' ( 1<; UPSTREAI'1 ELEVATION == 55.7000 i; ~_ pm~Nl2JRt;:_f\tJL ELEY.bIJ 0,1'1 ::: 48. 0000 :1: ELEVATION DIFFEREf;·lCE =-; 7.7000 C' ill OCEtY1~, RATION.<\L I"IETHOD TIIvlE OF CONCENTHl,TION :;;: 8. 4·434 il 2 !:,---------, --'----"-. '-----------'--_."-:-"' .. " -" ,--. - (. H RAINFALL INTENSITY FOR RAT:[ONt~L I"IETHOD TEN YEAR 11,. ______ ...... ___ ' .,,--------_:;......-------_ .. _-----,---, .;Tt:; '( :11: i r::·-' ----sPEciFYED -IICi-,-,;·---~-~85'(f-~---... ,' --. "","'" I,: ULI i:i I -------.. --'" ,----. . --"-"'" ~ 0 DISCHARGE = (-i~~ !2·; STORN ::::' 2. 2000 --. -... _------,"-- 2.B113 j ~---.--. ----------~-.--. --.-. _ ..... ---._-._ •• +.--.. --... ~ -~--.-. -~I~ **********************************************~******~********************** <. i< PROCESS FROiV! NODE 2~ TO NODE 12 »CODE ::-.: 40 « (;: "'\----~·-'-:;~~i~~~ZL'~i~~~~~y·~'~~:;~~-;~~~-i~~~~~~~~~~~-~~~-~~~;-~~;~~~:-·-~~':b~;;-~~:~=-:-·-: ( ;3:' I . -,---" --" -------. --'-' i,1:~ FLOWTHROUGH SUB,L)REA ,o,S INITIAL ESTIlvlATE ( !"~, 'USING 1''IEAN DISCH.;;-'R(.iE Bf:ISED ON CFS/ACRE , I,,' I -_ ... -----.--------_ ..• ~. ---. I •• e I,,' P' SPECIFIED nc":::: .850 I,? --'"--------, .. ------.. ---... ----.. , -"-' ·c I .. 1'" . . I ' :;"~-_~ ___ !1r;:{.,.N Eq:n-J.. t.--H_T1ifl"L§UJ,1h!=<E.A _ IS.::, i.l!,;: C !"': . l{:" L;---- i 8TREETFLOW HYDRAULICS CVI~lLt!EI.(;'rn-L= __ , __ ,~."OQ _XF,6jLL:::: HALFSTREET WIDTH:::: 24.00 . (. !q NlJi'1BER OF FLOt") COURSES ::::: 1 i·"~ __ ... UPSJJ-?I;;.9!vf ELEYAJJ_QN =:=. ,_ .. 4-8. 00 ,'"' DOWNSTREM'1 ELEV{"TION --47.00 ~. ',; ~ , 1':, WATERCOURSE.LENGTH = :t60.00 7. 39 .0200 ,-----.... , '--' -~- -~--------------------------------------------------------------------------. : (~ DN = .47 V= 2.37 ,.' ·'. __ .. ,.,TRAYEL,. ,T1!"1E ::::= ______ ~,,:l.2, .... _ ~2 SUBAREA ::::: :t. 90 ACRES TIME OF CONCENTRATION' FOR RUNOFF PEAK -9. 5680 c' cm'1!"1.E:r.~C I AL DEVELOPI"IENT ASSUt'IED RAltlf,tiLI.,.. ~.NII;NS-ITY F,OFL BATIQNAL I'JIETHOD TEN YEAR STORI'1 __ =,. c ~ __ ...... .t'~ • .., l.-'\. __ ..... _ "-.. . ,t."-.'"-· .... ____ .. _~ ___ >-... __ .'-: . " -. ..: ..... ~~-.,-.""".,,.~ ........ -..... -~"'"--.--...... -.... --'I~-•• -",...,. ........ ~ ____ ...... ___ • ,. -"' ______ ,' ••••• _ ............... OW> • C', SPECIFIED nell --.850 r,r--. -.----.. '--.. -... -.. " .. - v?' .... \ ( DEL0. ~ " , 4. ;;:688 9. ~;259 TOTr~L AREA ::::: TOTAL Q --. 4. 1000 1';1. _ i~~-'-' . "HALFSTR'EET' F-"LOrJDI j\jG -. ;;·--·-r7'. '3~i-.... . ","·-'1 I --\. 1F' DEPTH X VELOCITY:::: 1. 1.2 ," --; r.L_~ ____ .. _______ ._.....-.~ .. _~_ ~ __ ~ .... _~ _____ ~~ _, ~ ____ . __ . _ . _ ... ~_ .... _ .... __ , __ ~_ ... __._ .... _______ _ !,' ----------------------------------------------------------------------~-----( :0 : J i . I -' ----.--,-.--.•.... ----... . ' ..... _ ...• -...... END OF STHEETFLOW SEG/"IENT HYDRAULICS.: _. '\-. .. --.-_.~.--,--.----.---~----.-. ;IGI FLOOD{rH~TH.::::: 18.73 DN::::: .50 C Pll ' 1121 *·)l·~'i-·***********·**************·~*****1i_***************~.*.'**.'****~.*****.)(-**.*.**.!f._***** 113: ****************"*~*,********.****.**********************·***·**·**:****:li-*1~ .. * .. ******** C. !l':i . PROCESS FROI"l :NODE 1;;? TO NODE 12 >)-CODE:= 1 «: '" ". l15L-=-===--:.~-==-:~::~~~-======::-~===__=_=____=::_=.":::.::.~-_:-~-_=__::.-=_:_:' .. _-:_-::-=:-::-::--~--::--::::-==:.~~-_:.=:.=-::=~-=--.:==-. lIS' • ( 1'71 CONFLUENCE DATA IS] . N DrS'CH~~RGE TC I I .-' -------.----.---~.--~ --.-,.... ... ------.---.--------.. -.-. ~ . -'" .1.. ___ • _____ •• --·--· ..... -r· _______ ····-...,.,.·. 11:1 .' ------------.. ----.------..... -------...... -----.------:--.---....... -.. -....... ---------.. --7--~ .. --..... -------" ... ~ . { '2" • 8 h7 11 71 ~ il '? . I ! . .l '. w .' ~ ... "'W ,!.ll . 2 9. 53 9. 57 2. 64 . . ,.' ' . .,.. I ~-.... -.---_...... ...... • -____ ..... -.... ., . . . "'" .-.-... "'-___ "'_'''' ___ . __ ...... ____ ...... :"'1: a.eEtvfA CONFUJENCE FORlvlULA USED FOR » ~~ <:< PATHS .' .. C" ./:1 I;" VAR IOUS DISCHARGE COI'1B INA/IONS ARE AS FOLLOWS: .... : r-------.. ---~--·~----.----......... -.----.-.------.----- .... i2~ " . 17. 43. 1 7. ll· 9 {'. i:,,;1 . CONFL.UENCE' ES.TJ.I'1ATES ARE AS FOLLm~s: f.' .~... . ":"~" ~ -1?:: ':I:~.? .... TC '"~ 9. 568 SlW//"IATION OF I~REA ::::; 8.300 , ' (.·II~S".'I· *.~***oj( .. }!--l...t..*.I_* .• * ... * ... *., f<-._*~~*~1~*_~*. * .. ~_** .. _'li .• ~.~~_*** .. ************.R-****~~.**'1l-,'***~.*~"****.'*.********-l .. *** ~, PROCESS FR.Ql"l_~~'p!?~ ... 1.~~ "-II:). ~ODE 13 »CODE =-" ~~;;;: « 31: _. __ H .. _____ • _______ .... _. __ ...... _____________ • ___ ..... ________ -.--...--.----.. --::... • .;..:.::=--...::::..~::.:=--=-:....~..:::.::..:....._=__=~..:;- ( 132 1 P IPE DISCH~,RGE:= :J. 7:49480 '3:;; ELEVATIOi\! DIFFERENCE ::;:: 1. 00000 I --~-.--.... -.... -. .... . .... --.............. -........ __ ...... ----... . 13'i ~'U\TERCOVHSE U:?NGTH :::: 110. 000 (: ~! 1 PIPES AT 24. OOO-INCH DIAMETER I:;~-' --~-~d:~~0~~~ ·~[~6w-\}r~·~~gi?y··;:--· ··;.r 3f82' FPS ( I::L.._ .. _ .. ~ IPE PE"rEfi!"1 r i"!~I! ... EqR ... ~QN::PR~S.?VRE; FLOW I'l~' ( I:; TR,lWEL lJlvlE IS .2t50t'?::2 I"LtNUTES NEW TIME OF CONCENTRATION IS 9.819 MINUTES . : ( , .. ****************~*********************************************************** -l:.~.******~i-*~.****.*~.*******~.~***************.R_*********.*.ji'**'******-l!-*****,****,***** t --.. __ .. _0 _____ .. _-------------------------_ .. _---.. _---_._-__ ...... ___ .. _. ____________ """:" _______ . _____ _ '" SUBAREA = . 90 ACRES .. ~---~ --_. .'----- ( TIME OF CONCENTRATION FOR. RUNOFF PEAK -9. 8185 !!'I' COMMERCIAL DEVELOPMENT ASSUMED /. I" \.'-" RAINF,6tLL.·il\l'r[~l\isITY FOR R'ATIONAL l'1ETHOD TEN YEAR STDFH1 ::;;: "'~'------2. 6181 ( SPECIFIED "e ll ::. .850 (' ( 2.0029 TOTAL G := 19. iJ.!il77 TOTAL (')REA _. 9. 2000 ****************~*********************************************************** PROCESS FRON NODE 1~_ TO NODE 14· »CODE := 22 « ".../~f--':-~.::''':~_-:-'':'' ____ -._._~ ..... __ ... __ . ____ ._ .. ___ ...... _________ .. __________ . ____ ._ ...... ____ . _____ ... _____ ....:...:.:..._.:::;:...-:---:.::.::.-:.:..-: C~ '" •• 7 ( , PIPE DISCHARGE = 19.49767 ELEVATION DIFFERENCE = , _ :~OOOO WATERCOVl-1SE 'U~NGTH ==' 160. 000 1 PIPES AT 27. OOO-INCH DIAMETER MANNINGS N = .01300 C'Oi'{Pti1-';'ED Fi_otT\iEL.OCT.TY ·~;-·'·-·-5. 9399 FPS C n TRAVEL TllvfE IS . ·1-41:194 I"iINlITES :~. NEW TIME OF 'CONCENTRATION IS 10.267 MINUTES , .---------.--~-----_. __ ._--... ,_ .. ' _." . -----~ IJ~ ( I' ***·'il-**·******~.{_**********_lHH~·*************************~'}****~J-* .. i-**~J-*·It*********.*~* . : :1 **************************************************************************** h----~oR6cE~SS-f:R{:5i'~r'I-iODE' l~f'To' NODE ',j.4 :»CODE';"" 6() <-:.: ....... '-.. ;~..... ..~.-.. ~.-.. ---. C !17' '----.-------.------.,...-------.--------~-.. -------..... ---------------.-----------"---.------------- 1 ' pc SUBAREA = 3. 90 ACr~ES 11"'-·--...::..:...;c ... ,.,_._---_._ .. 1-. i", THiE OF CONCEI\fTHATION FDR RUNOFF PEf\!:\ -10 .. 2675 ;2t. C()i~1t~IE:RC r (sL. ,DEVi::I_OPi"'lEl\lT ?)E1SUMED i";-----'·RArNF~.\LL' It~~r"I~j\fSITY FOR' RATIONAL 1'1ETHOD TEN YEAR STORM -- I (, ,~. !:: . ..;.. . -----.-----_. ~,~) SPECIFIED "Gil _. .850 I-DELG ::::: 8. 5303 TOTAL G·::: 28.0280 TOT,6,L AHEA :::; 13. 1000 . -----, pl. (.-. ******************************************************************~********* :r'-PROCESS FROi'+ NODE 14 TO NODE 15 >:::-CODE ::. 22 « )~; ,-.-=-..:::..:. -::.::::. ::-:--:== -~---:-:. '':': -~.-'-'':'' _.--:::..:..::....:.. ---,..; : . .-.:..:..:.:.. ---------------------------------.• :.. .:::":' :::.-::,.-..:..:-::':'-:.:.:"':":::':':':-:: ==:..:. . ' (. h, PIPE DISCHi\FWE::":: ~?'8. 02798 i~ ELEVATION DIFFERENCE = .70000 13'~---' !~·i;TERCtii]RSE·"L.ENGTl--l ~...... ·i30. '000 ( I;,. 1 PIPES ,6.T 30.00Q"-INCH DU,t1ETER C 1:-----~~~0*~5 ~L·{j~~( .. \iEE·{~~i~~y-·;;-'6. '630'7 FPS ~. PIPE DETERMINED FOR NON-PRESSURE FLOW lj~~-" -..... --''''--' .~--,. -'-"-" '" ---"'-~" .--... ,~ ''--''~'-'.~''''---''-'---, ~--. ~-.--.. - l !', TRAVEL TIME IS .32676 MINUTES ; •. , ____ .. J,j~~_T_U/!E or~-_J~O.!:!.G~_~ITR-'<\TIqN IS '10.594 r-HNUTES .- ( '! **************************************************************************** ****i*********************************************************************** PROCESS F:ROI'1 NODE 15 TO' NODE 15 »CODE == ( '.-~--------------------------------------------------------------------------- .. ! f'\-************************~*************************************************** 31 TO NODE 32 »CODE ~ 10 « ---------------------------------------------------------------------------- . _____ '_'" Dr::V.EL.Qf>,IvIENT IS COl11"IERC I AL c Z ___ . _ .. _ ... ___ ._Il\l~.IIl~L. _§VBAREi-\ FLOhl-LENGTH -700.0000 UPSTREAM ELEVATION = 56.0000 DOWNSTREAt1 ELEVATION -4fJ.0000 ( :ELEVATION DIFFERENCE ~ 8.0000 . OCEMA RATIONAL METHOD TIME OF CONCENTRATION -10.0151 /~ .. -. ""R'A:fNFA[['HH'Ei\}SITYf"OF~ 'RATIONAL' l'-1ETHOD TEN YEAR STORN 1'-'" '-....... * I: ~._ ........... ____ . __ ....... ~_ .. _" ___ ._ .... . " , ( ',3 SPECIFIED lIel!:::: .850 ;:>; DISCHARGE:::: 3. 0922 !.[----_._._----... _----'-'-''"--.~ .... -.... -... ~ ~ : ~ TOTAL f;RE/~ :::: 1.4000 2. 5985-.--------.-.. -.--. { ,11, . Inl *************************************************************~****~*~******* .. . 113~-.-··-·-P-ROCE:SS ""FffoH-NODE-'32"-"fO NODE. 33 »CODE':::: 70 -:::< .... --. ~.-.. -------.--.-. (;:0. ----.--------------.---------------.... ------------....:.----.--------------.--.--'----.------ h' \I-GUTTER HYDRAULICS . c 11;:,----E~·~~r~--::::. ~;-:OO~~~i~~~~·~~~H!·KE: .. ~j,~~·08 . ---......... --..... d CROSSFALL::::: .. 020 ~L~·-----ALLOt~ABLE--MAX:tFiOI'1 ~-JjEP·T"I-i:::! .-50 .~ ----.-... -. . (' ;... UPSTREAI"I ELEW~TION == 48.00 .b; DOWNSTREAM ELEVATION = 46.20 ::t,~' --GUyfEFf-LEN(~TH-:;-·-350:-0cf· '.' C :'" J" ;2'i1 RIUNFALL INTENSITy' FOR. RI~TIONAL 1"1ETHOD TEN YEAR STORl"l :::: >-----.. ----.. ----... ~ .. ---_ .. _-----.--'-"" ----_._--, .' -;,; C !,: ·t;.l '_ ..•.. ~~·L.q~\JT~.R_C?~GH . .sUBAP-Ef; AS rNI~IAL ESTII'-1ATE ~~ USING MEAN DISCHARGE BASED ON CFS/ACRE «: l ... .' 1,)' _H ____ .... ___ ' ____ . __ ... _-' __ ~_. -,.-. __ -,....~ ___ . __ .'~' -,-_. _ .-__ . - ~;I I , ( '''' ~. ~ ... ~. SPECIFI.ED "e ll :::: .850 !,?-3 ~ 1::-' .---.-.-----.-.. ; .... ~ (~ !~5' ! MEAN FLOW WITHIN SUBAREA IS == 3. 78 2. 32;;:~'7 C-:--:-..:·,_:.:.-=:.:..-===::.-=:::.: -~.:.-::...-~-.:.::. =:::.::.:.::.:.::=-.:..::..:...:. :.:.:....:.. -• .:. "~...: -_.------~:.:. -------."--:.....:..::.:.:::.:.::: :':='';:: -.~ • ..:.....:.:.:...:..::.:.:--::::... ::::.:"':::' .. ( L. . J ;"'.. .t"') I '-/ -~ 07 . i". D~ -.. r.:..O. "... t.::.... r. TRAVEL TIME = 2.82 j':'-: --..... _--_ .. _._._ ............. _--_ ...... _._ ......... . ( I::' SUBAREA == . '10 ACHES ~,~ ~ ! -----. .. .... ------tIME--dF-·C·o~fC·ENTRATIOI·{ F'OR RUNOFF PEAK:::: 12. 8328 COMMERCIAL DEVELOPMENT ASSUMED RAINFALL INTENSITY FOR RATIONAL METHOD TEN YEAR STORM =. 2.316"' c·'· l. .'; SPECIFIED "G":::: . 850 DELG -" 1. 3784 TOTAL G -4.4707 TOT AL AHE ... ,\ ::::: . 2. 1000 . --------------" .~ --------. . . . ---.... -"-~ **************************************************************************** (I **************************************************************************** '( ____ .. ____ E.R..9fESS FRO/"I NODE 3~:l TO NODE 33 »CODE == 60 -C< ._---------------------------------------------------------------------------SUBAREA :::: ( ~~ , • --.... : l,.....: _ ...... l. _ _ ~ _ ~., -____ .... ... .. .. ... TIME OF CONCENTRATION FOR RUNOFF PEAK = 12. 8328 COMMERCIAL DEVELOPMENT ASSUMED RAINFALL INTENSITY FOR RATIONAL METHOD TEN YEAR STORM ~ r--~' .---..... _._..... . . -,. ..... , .. I. (C ," .,-, ;.:" I ;...-.~-~~ -._ • -"'-__ ~ ........ _~ __ .• -. -_~.~ ..... ~ SPECIFIED.IIG/I::::: .850 11 I DELG := 2.9538 TOTAL Q ::::: 7.4245 TOT,6,L f~REA _ .. ( : 3"" . · . • :1 -~ . ~ -.. -------~-. . . 3. 6QOO • :-.> ---... --~-----.. ,-----------... • ....... ,._--.... -_. • • --.~ .. ---~----:.- N **************************************************************************** (' 'II PHOCESS FROl"1 NODE 33 TO NODE 34. »CODE :::: 22 {.( P? .. -------_ ..... _---------------------_ ... __ ._----_ .. ---------...... -------------.----.. ------.-...:..---:-~ .:.......-___ ~ ______ "' •• ______ .... __ • __ -.-_ ~ __ ....... ___ " ~~ • 4_'-' __ • _.~_ !D, PIPE DISCH(~RGE ;,., 7.42..'146 C ;1< ELEVATION DIFFERENCE .= 2. 50000 !1,: ___ W~I TEB~_OUR8~ __ br=:NQIt1. =. . _ ;lQQ. 000 JiS! 1 PIPES AT 18.00v ..... INCH DIAI'1ETER C in: t~IANNrNGS N::::: . 0:1.800 :1,:~_~.QMPUTE~.P .. f1.J!!~--V~I""!O~IIY. _=:.:._ .5. ?3S? FPS . ---'-~---,-- 1 • . ( FG PIPE DETERMn',iED -FOR NON.,...PRESSURE FLOW '21· 1 • __ -----.-~ ----_____ --.--________ ._ .. - -.. _. ~ J' .--'-.. ---.~ ~-~ ~ TRAVEL TIME IS .87113 MINUTES C r NEW TIME OF CDf'.ICENTRl"THjN IS 13.704 I'ENUTES ( :?&: ****************~*********************************************************** ____ PfWCESS EB.OI'-1 NODE 3l j. TO NClDE 34 :::·>CODE :::: 60 « (~ ". -.. --.. -.-.-........ --.. ---~-.---....... --.. -""!"-----,-... ------:-------.. ----------------_._---_._----_._---------_.;....-_._-. ( SUBAREA :::: 1..10 ACf~ES i~!·~-.. --.. ---.. --·--TJ:HE-'CfF'-CONCENTRATION . Fo'R RUNOFF PE,6.K :::: ( ~: COMMERCIAL DEVELOPMENT ASSUMED ;3:< Hf..'tINF,\LL INTENBITY FOR Rf\TION.c,L t'lETHOD TEN YE,c\R :.,.,.--.----------_.---... _------------_ ... -. --.-. l~ • i ( j", - . ! '-: 1:;'; t.11r---------------------.. --~-----.---. -.--.. -- e. jJG' SPECIFIED IIGll _. .850 !31; j<o:---'--.---------. -------.----.. ---_ .. . I 'c ;'\ I. ' DFL.Q ::::: TOTl·\L G = 9. 5091 '----_. -,.~ -... _.' :l3. 70ij·O TOTAL AREA 4.7000' ;;~ . ~~{;.~:..;:;.~;,;*~~.;*.~~.*·*:;i_~Z*~~*~~*:;·*~~*·ii*:~****-l;:.*1(-**·;.: .. k·JH.H~**ol",,**·**~~*********·~****·lHi_**·i;**-**-****-- C '.\ PRCh::EEiB FROi"l. NODE ::-)4 TO l'lODE 15 »CODE ::;:: 22 «: :~S; .. __ ...... _ ... __ ....... _ ......... _. ____ .. __ ... _"' .......... _,.. ....... __ ......... _ ..... ___ .... _ ... _ .......... _ .. ___ ....... _ .. _~_ .. ,.. ____ .. ___ ..... _______ ._. ________ ..... _. _____ ""!"" ____ _ : .. s-. ' ( j;, ;!.' "___ .. __ . ,.0,..---_ .. __ . -. --~ --~----. . PIPE DISCHAR~E = 9.50914 ELEVATION DIFFERENCE = . . ;:jOOOO ,. "J;--"-' -~·Jf\TE;R.cour~ l2lE .1·,J:;ij(iTH::: _ _ 40 000 1 PIPES AT 18,OOO-iNCH DIAMETER ( . '" \ .?:. OBHl FPS TRAVEL TIME IS . 09414 MINUTES NEW TIME OF CONCENTRATION IS 13.798 MINUTES -. --~-.--,-. _ .. ~. --. ~ ... ---. . -~ . . '.--. "'*.:~-<~.f,O·;1··r,··l;"·1i-i~*_l~·*****·.'* ... ~****~~*~**·***·~ .. R-*.*****.*'********~"*****.~.~**.l!-*.*****************-l-.<. **~************************************************************************* ( . PRocr:::ss FHDi'1 NODE 1~i TO NODE 15 »CODE =. 1 -C< ----------------------------------------------------------------------------(' CONFLUENCE D(~\TA /0;--. '~-i~--"n I sc r:lAR(~E" "1'c \....,., ____ . _____ ~------.H---------------.......... ---... -.. -.. -------_______ .. __ ..... _-0. __________ • ____ • _____ _ '-. I,. 128. 03 10. 59 ".~. _54 :~,---··--2··-----9. ::51 .. · .. ·· '1'3. BO 2.22 ... _ ....... -'('~'!51 , OCEt-1A CONFLUENCE FOHivlUL4 USED FOf-{ » 2 (<: PATHS ... ·1:;----·-VAR·n)US .. DH:fCHARG,E·-COFH;ffl'~AtI(H~S t)RE f\S FOLLOWS:. {~ ~'1 36. 34 34a 00 JL .. _. CONFLUENCE ESTII'1ATE8 ARE AS FOLLOt.;/S: lJi -''''G ::: ·_ .... 36'. ·33S-·-,.C ":::::--"-rO~"594'--'SUMMATION OF AREA ':;;' .. "'17. 800"'-'''' '-'-"--"-'-"~--'-. (" L I Iii-.. I : 112: ·~·*ll,-~****~·**·R-*************-n,·)f-*******·***************,*,,*******~~***,~************** l;:;--------PROCESS FRbl'1-i\rOI),E---1~r ... to'NODE" '16 ::~>CODE ':::; 22 (:~: .. -....... -.-.. ----'.--.-.--'- ( II": . . T -..-.......... __ • _______ .. ___ ... ___ .. ____ .. ______ .. _______ ...:..... _______ --... -...... -.-.. --.. -----------------... ------...0---, . 1::r-.:··--.. :~l~~~·A-~_}g~Hg~·~~E~ENt-~£;;~37.9~. 26006 - (I~I WATERCOURSE LENGTH::::: 480.000' . t: ___ .!....Y_~ .~ES . ~T ___ ... _.?~~. GO\?=-~J\I_~H D I AI1ETER rn, 1"1ANNINGS N::::: .01300 .( !~, COMPUTED FLOW VELOCITY = 6 .. 8005. FPS II' /ui--o---'-prPE-DEi"ER1-Tfi\iED'-FOR ·-l\iO!'.!"::PRESSURE -FLm4 (. ;23, ~. !z,i . TRAVEL T II"IE IS' 1. 17639 l'1INUTES ... ~12'-. ----N·E!!~TT~1i::-dF-Cf.JNCE!\lTR,6zTt'b'I" IS '1.1. 771 MINUTES (. ;<~: . , , , r'o'. **************************************************************************** \t .:-"*-*~ .. ii-***·*~!'~i-**.***~n-******'li-*'~**-**'~*'***************-).~**~~*'******'********'1!-*'~******** ( ';,: . PRDCESS FRO!"t NODE 16 TO NODE 16 »CODE == 60 « : I~l-. ':-~::§~j~A~·~-~~:-:~':'-""'=i;:-46-~;;~~~~-:-"--'---:--------.----~-... '--:-.":'--:.----~--:-~.==---:~.-=--.. ~~ .. ~--:-.,.~:~ { 1,2: -, . ~; TIME OF CONCENTRATION FOR RUNOFF PEAK = 11.7706 '/0':-"-----.----. -COf'1i"IE!-<Cj:';iS,t: -bEI,}I:tCOP1"1EI\lT' ASSUI'1ED ( H' RAINFf~LL. INTENSITY FOR r~ATIONAL i"IETHOD TEN YEAR STOI~t"l ::::: 106; t ;----------~-----.-. -~-, -------.---~---.--.-~-----, ---lJ1; . ( 13;;. b l 2. 42~~9 . H" ._-.-.. ·----gp·EcTF; I ED-I'C'i!-':;:; .'~ 'i:Y3'o --... (, .. 14l !~L 4i.4592 TOTl~l.. ~)REA "";--... ~ --'-'-'-'--' 23.2000 !'-c_ .. ____ ..... -.... ---...... l}ELG'-';;--i CT:;h 3"-' l'OTAL G " .. , ( ... ): ~. **************************************************************************** . , , .. -.. -...... .-"·PRcJcEss -F::·Rb.l~f"j\IODE o TO NODE o )·>CODE = o « If" C ,f ------~-------------------------------------------------~-------------------',. ! ..... ,'':;', ( i": \:~:.. _ ... c· ~--------------------------------------~--------------------------------------------------.. (" ~ .. . 10 '" 1 (. 10 ( 2~1 1, 41 3. 9 : .. : 14/~~2115 .I:7tO-L~T.-2·; 40.--5, i3CL ~0T::fo {o '. '-,. ( -.- ( , 1, :2 _.-._" :::i1, 10132 56,48,70011,4,1.4 ::1--"-48'~46~-;;Y; 350} 11 4, ·O~-7 33,60133 jJ' /---i--;-4/-f.--5---_. _. C I·", 33,22,34 :" 44.2,41. 7,300, .0:1.:::1 I .•.• -.......... __ ... -_ ...... -...... __ .- j:: '34,60,34- ro ' /I 1 "i' ·1/ ~I'I 1. 1:~~._~4: .. 2~ !-.~ __ ...... 0,_, __ .0. ;..' 41. 7141.. 2, 401 .OJ3 {. .:1 i5, 11 15 :~~,~_+ _.2! .~ _ _ .. ~_. _ _ _ . _" ...... _ o 1 '3;:}, 22} :1.6 :,. ( ,) ........ :1 . I . ---" . ( , 41.2139,480,.018 16,.601 :1.6 it ,iL 5. 4 0101 0 END ..... -----•. -~- .... -~-.---- _~o...:.. _ < • ...,,_. __ • -il.1 . . - Cl :?! ::c 0 .en Cl z « z --0 en :?! « .,., ::i -l § " .' .' Stir-\\. ~ R.~T '2...fTNS . ~------------~---~--------------------------------------~-------------------RAINFALL INTENSITY DATA INPUT ( \.----------------~--------------~--------------------------------------------RAINFALL INTENSITY INPUT t;"-~ .. --.-.--.-.-----~--.-~-.--.-... -~.-. -~---. _. ~ ........ -.-~-. -. "--_ .. ----_. C:--,.,· TIMEUolIN. ) INTE;NSITY( INCHES) ~, 5.00000' ~.40000 i.; -, _. ·------6:-0'0000-----·--. -'-2:-25'000 -r-~Qu£r-J C ... J . --_. ,-1 ~.-... ------~-, ~t:; ';_. 7. 00000 2. 10000 :.:'.-~r 8. 00000 2. '00000 !) ---------·"9:-·UO,ocro-----··-· , ...... ,'1.'90000 ---:::--.--:--~~--. (,. . .~. 10,00000 '1-, 80000 's --11. 00000 1. 70000 '. ;1':....-·----·-=[2:·-00'0-00·"·-··----·---·---·· .. ---L 65000 ( :11; ·'13.00000 1. 60000 i12! -------14 ... 0-0.00.0.--. -________ ... 1._50000 113~-' =---:C5. OPo{:fO~-. -.-.-----, -1~45000-.---- (, \If.;. :'. '. 16.00000,' . -L 40000 , r:~-=====;:==:-~;;=:=·==~~~~~~::=:==~~=·~;.~~==:=~~~~~~===~~=~=~-;~~;:===:.;;~=~-=====: -C 1171 PIPE to/ASTER PU\NNING OUTPUT DELETED , I I:~I __ ,_, -.. PfmTFiOMPTP-E=-S't-Z~-·(J!jEb'--i8-----i8. ·bO-·thICHES ---~ . . ( 1211 FR ICTION SI.,.OPE PERC-ENTAGl;: OF Nf\TURAL SLOPE IS 90.00 .' 111; . . b,.-' -*~iE·~.*'****·**·.)FJi:*·*·~-**·1i'·~"li-~,}~'f*~·lti~*****~·********·~:j~:·ii:-*-li·****·~:***;~**J,i-*·~:*:*·**·*:-l-.::-*i~·iH~·*1.~'*****-". (~J __ -_ PROCESS FROM NODE -11 TO NODE 12 »CODE = 10 « I • ~ ._--~ ... . !,ll .,._-_-..;..-;..;-..;..;......_....;:..-,;-.-..~...,:o ..... _ .. _ ...... ._;. ___ ..... ____ ..... ______ •. __ • ___________ ---.. -----...... -.--...... --.------.--"!""'-------.. -.. - ~ >.~~-·---~-------:lJE\)'t::L1JI~r:1ENT lS'C'dMI"IERCIAC" ,...... ,'. ..-.-.. ~----.---:: ... -.----.----.. -. C~< , '., . ( .. --~.----.-=-:.:. :.---'11'4 rTri~C" sLJ:En\'RE~~ '''FLm~':''LENGTH -985.0000' ( ~ UPSTREAM ELEVATION = 57_2000 IjJI Dm.1NSTREAt"l ELE:W\TION _. 47. 0000 ::il~E:'CEVA1'rOf\I-iYrF'F-EFrENCE'''-;;':'' -----1."0: 2000 .--. ., .. .. ..... '"'' ( '.; ,OCEt'll'\ RATIONAL l"iETHOD TIME OF CON.CENTRf'lTION ::::: 11.. 7099 . , . l:~;~ ______ .. ~. ___ .. ___ -" ______ ~_ ___ ~ ... ____ w.o ___ _ I~, ~ (i (: i:;~i RI\INFAL.L INTENSITY !=OR RATIONAL l"IETHOD TWO YEAR STORN -.. \:5: .:' '!c1r---I, . ( I"" ... , I IJJ 1':°'1;""-- (' 1.11; ( I·~~--------_. -; -:~-~"--i::'--._ !'. . DitiCHf~"HiE - , ", :''1. 96:t 5 2.8600 1. 664-5 -----*~~*~--::-i"*-*:~~T******~·~·li·**-:i·************~k·***********·**·*****1~**·)~*iHi-****·w~·*'****.~***~j. {: PROCESS FROM NODE 12 TO NODE 12 »CODE = 60 « ---------------------------------------------------------------------------- 1. 40 I~CliES ;, ·TIME OF CONCENTRATION FOR RUNOFF PEAK -11.7099 .... --~----COt1;v1EF<C; I '~L .. DE,/ELOP}y'JENT ASSUtlliED RAINFALL INTENSITY fOR RATIONAL f"1ETHOD TWO YE{~R f3TOF<1"1 :-..: 1.664:3 ( ( c -, DELQ :::" 1.9808 TOT.6,L Q :::: 5.9423 4.-2000 ( ****************~*********************************************************** ~---. ---. PROCESS -Fl~fji'1 NODE 1;':2 -TO' -NODE -1:;! »CODE::: 1 <<:: .. --------.--~--.-- t ~ ----------------------------------------------------------------------------'-. ****~J_***.*******.l'<_*l,: ... ***~-**.l}.l}**********.*******ii"**-i~.**_R.**~L********.*************** --... _-.. ~. ---.--. .. . . --------_ .. - J PROCESS FROM NonE 21 TO NODE 22 »CODE = 10 « ( ---:-------_. __ ._._---_.-._._-_._._--------------_.------------.. -._--------_.-._----,....------.-..... _--- DEVELOPMENT IS COMMERCIAL ,.------------.~-----.-----. -... -. -.-....--... -.----.....--. - 520.0000 8.4434 . -------.... -----_.-.. _--,-----.--..... -----_ .. -----_ .. _, ... -------q., . SPECIFIED DISCHARfiE ::::: ::1. 657:1. ·rOTAL ARE-:.o. _ .. 2. ;;~ooo Ii" ('"-!1": (" ''": ___ *.***·~*:!::**~ .. * .. ****.!H<~H}*:.*:.~.**_*.**~il-**:****.1~**-j:'~***********-l-~*********_1.i·_*~.*~-i(-~·If*-l:i-_·**~_~_~~* __ '( . _ PROCESS FROI~l NODE 22 TO NODE 12 >)-CODE :::: 40 <:<. . r ---------------_____________________________ -______ ~ __ ------_____ ~---------- '-I .~'! RAINFp,LL Ir.ITENSITY FOR RATIONAL NETHOD TVA> YEAR S"rORi"l::= 1. 8318 f _. -. -•• ----.-.-• ----.---. - I"' I (' !Jl FLOWTHROUGH SUBAREA AS INITIAL ESTIMATE -----~-------.. ,-.---. ---'", i~ USING MEAN DISCHARGE BASED ON CFS/ACRE C j}" ·c j"' SPECIFIED "Gil :::: .850 r~. ' (~-_.-----------_. j.;~ ( ., ,. , MEAN FLOW WITHIN SUBAR~A IS = 5. 14 .::. '. STREETFLOW HYDRAULICS f CURB HEIGTH ~ 6. 00 XFALL- _ ._ Jj6Lf$JREET .l,~:rPTH:;:: 24. 00 ., NUMBER OF FLOW COURSES = 1 ':; A:: '-> ( ". UPSTREAM ELEVATION = 48.00 DOWNSTREAM ELEVATION -47.00 WATERCOURSE LENGTH = 160.00 . 0~200 -----------------------------------------------------------~-~---------------~-----DN = .42 V -~31 TRAVEL TII~lE ... 1. i 5 SUBAREA :::: 1. 90 ACHES ( ,----. TH'IE OF CONCEN.Tfl{~TION FOF~ RUNOFF PEAl" -9. '5975. COMMERCIAL DEVE~OPMENT ASSUMED ( RAINFALL It'HENSITY FOR FlI~TIONAL. t"iETHOD TWO YE.AR STORi'''1 = 1. 8403 "T -_ •• ~-_ .... _ .... _ ...... ___ .................... ~ __ ........ ___ ...... , ____ ~._~' ~ ___ • _<o..~. _''';''_ ....... _ (. ( ,r,r:--'-. -"SP'E(C'IFIED "riC-II-==' .850' ,. '''. -..... ~,~r-' ~, . ~ ~ - '-; j"' ,'l.-.~" . ...... (.,I~l .... , : 5! ,:...J 161 HALFSTREET FLOODING:::: 14. 51 6.6291 ' 11 ;---_. 'DEPT1-( X VECo'c:("i-Y""~ --.... -~ 96 ( 3; . 1:1~~-==-~~~=ti'~'-~;:~;~~;~~I~bQ-=-S~6~~N~-=~Y~~A~~~~~;-----.---------~-.--~:-~--~----.::=-=~--=-==- (. lli ' . IIZI __ .E!.09}?W.I12Tt!_::::_L~:~ 6_? .. _ .. __ ~!2!...:~ __ :_ 4~ .. _ __ .. _ . ____ "_ . ___ ._" _. _ ,nl. . (I~ ****~*************************~********************************************* i 1_ .- 1~ PROCESS FROM NODE 12 TO NODE 12 »CODE:::: 1« . 1 15: __ ~*-::::~**":::::-_~:-.*~.~.~.:*_:*~_~'):io,**_*:,~,~:*:):io*~*_***~~*******~.i-*****:R:,:"* .. ):io,:"~~~:~·lt:::::*--:*::.*.-J..~*:~-l~.~!_:*_:.:.~~.:*_ ... -I ' ~ 11 -----------------------------------~----------------------------------------Iwl 11'.' -·ttrNFLlrEi\!CE·~-DAi.;A-~-·----------~-------.--__ 4 __ -:_. __ ,( /: N . DI8CH(~RG~E TC I , . ---------------------------------------------------------------~---------~--- FOR » 2 '-C'::: PATHS VARIOUS DISCHARGE COI'iBIN.4TIONS ARE AS FOLLOHS: -·f .-.:_--... '-I 11. 94 12. 00 C'bi\jr=CUENCE ·EST-j:I'·i.6,TES ARE" AS FOLLOWS: ( i"'t G = 12.004 TC:::: 9.597 SUMMATION OF AREA ~ 8. 300 J,v~L _____ . ____ , __ ._._.~ .. ___ . ____ , __ . ____ .~_. ___ . __ ._ ., _, + ,._. ____ "'. ___ >_ "._. __ ... _.~ :,1! ·1!·*·~*·********·***·)I··~·)t_*·;!·**·*'·!f,·l}****_R·**********·*****·*-li-*****·R-****·l!-·lr{~*_ii_*·*·***Jk*~·****;** ( ~! . ' PROCESS FR~~ NODE 12 TO NODE 13 >:>CODE = 22 « , ;::. ---------------------------------------------------------------~------------:J,j--·----PIPE:----DIf3CHARGE--:::::-.... 12.003-86-· , ' ( !~ ELEVATION DIFFERENCE::::: 1.00000 'J2: WATERCOURSE LENGTH::::: 1:1.0.000 b; --. -----i--pI15 ES---At--2-:C"OOO"::-INCH DrANETER , , . '-i3.: I"1ANNINGS N::;:: .01300 1'33: COMPUTED FLOW VELOCITY' ~ 6. 673:1. FPS I..r--------' .... ------... _ ..... -.. ----.. --... --~ ,--" l·J, ,-;.11' P J PE DETERI"II NED FOR NON-PRESSUHE FLQ[.·J ..... I ! 14J' !:~ .. -----. TRAVEL:. 'i'It1E --I~Y' . . 27474 '!''!INUTES ( ~. NEW TIME OF CONCENTRATION IS 9.872 MINUTES : ... , --.--------...... ---_ .. ' "'. .. -.-.. --.-,.-.. ,--,-... -~ ':, *·***1i-~·.***_lH~··***·~·*****_l:.c*_lt·*·li·li·***·~**·**J~**·***·***·**·li-***-lH~·**_lt'*~·*·*******·*_li_*'_1(·*****·**,~.i- ( " **************************************************************************** ( .: ,I PROCESS FFHJN NODE 13 TO ~,!ODE 13 »CODE' ::: 60 <:( ------.-.---. ---------------------------------------------------------------------------~ SUBAREA :::: .90 lc,.CHES .-.... ---.-.. -_ .. TH1E oi.::· COI\ICENTRATION FOR FWNOFF PE.6J( = 9.8722 COMMERCIAL DEVELOPMENT ASSUMED RAINFALL INTENSITY FOR RATIONAL METHOD Twa YEAR STORM -:t. 8 J. ;;;'!El j ------------.--~~---- '.' (". jf I ' ... :',[ ( SPECIFIED "G ll ::::: .850 ( DEL.G r.::: 1 .. 3868 TOTAL G ::: 13.3906 TOT f\L ~,REA :::~ 9.2000 '. I~r-'-**********~~****:*~:.ii-**-R'***********************·**~~***·li-****·****i~**o!..<"li--l..:.**{.wi****f~*.r;-· .. r-'. (-i'. PROCESS FRm'1 NODE 13 TO NODE 14 )·)·CODl:?: == :;"?2 .(.( . '--' ' 13 ~-.,--:.:-:-::--.::---:-.-::---:-:--,-:-.:----:--:.-:--:---:~----:---.-----:---'--.-.-.:----------.-:--------:----.----~~::::.:...=,-:..=:~,-:--::. :l PIPE DrSCHAI~GE:::: :J.~'?,. 39064 . ( :~,: ELEVATION DIFFERENCE::: '. 80000 I Ir WATERCOURSE LENGTH :::: 160.000 17 ----------"C"P1PES AT'·" "'24.000:::..tli.fcH DI,<.\t1ETER '-! ~ , t-1ANN I N(~S N:::: . O:t 300 )~; COMPUTED FLm-J VELOC :ri'V ::::: I ... -----~~.-, ... -.. -... ---.~--~ -_. "-~.-----~ ." 5. 45~27 FPS jiJ; ( hi' PIPE DETERlvlINED FOR NON-PRESSURE FL.O!~J I I ii:~_" __ ~ ... __ . ___ ." ___ .___ __ ._. ____ ~ __ ~ .. ____ ~ __ .... ~.' __ '4. ___ • ___ ~ !iJ. TRAVEL TIt"IE I8 . 48(;'/05 i"1H.\UTES ( i~:; NEW Tll"lE OF CONCENTRATION IS 10.':361 I'lINUTE8 ' !16:'***-ii.******:ii·i:*-*-*:l!-.~":j~*:~·**:~.~'-it:).Z-**************:~******'R-****'li'*'**'*'li-****'l~*~~'lr:*J,i-****.**** . .. '.'-.,,,--,--,,,,-,,----, --"'""'--,--- ( !17i *.)i.'*********'~*'****'*******'*1-.~*'~**'****'li-**********'l\'***~Jo*~-1!-*-r~**'li-*****'****1t-******** I I • '131 PROCESS FRm'1 NODE 14· TO NDDE 14 :::-}CODE ::::: 60 <{ , !1~ :--::-':"-:::':=-'::::'-"':-:"::::::':"::':::"::::::-':"=::: .. ::::'::':"-:;::==.::'::--:::'.:::":"::-----:: .. :'::":"'--":"-:"'--:--"':---.----':':':'::-'':'':'':'::''-:::::::''':';::''::':'-:'''::'':'':''::'::'::::::::::--:::::::::::::; I : . ,( ~ S~BAREA = 3.90 ACRES I . , '7.1 • .. In-" --, .. -----.. -TI}IE:" OF 'COj\itE:J~TR .. \TrON FOR' RUNOFF PE,4h -'{C. 36.12 ( jn; COI"lt"iERC I f~\L DEVELOPI"IENT ·ASSU!"IED i'·'~_ .. _ .... _I3i"2.1 N~~!.:,= .... ,~ NT5~? I, ~'!~ .. F.(Ji1 .. ,?-.t' 1) O~\1~1.'-: l~lETHOD TyJO YEAR STOR!"l:::; ) :_?~I,~:? ~ ai2j ( .. ..,1., !2t,. I ! , r" , \r -- SPECIFH::D IIG II :::: ,.850 1.1:1 I c __ , ... -.. _--_ .. --- i31 ( . I, ;.11: . DELG ::: 5. 8472 TOTAL G :::: 19.2379 13. 1000 113: . ' t:~****-i!~*********.~-**-*~***,,:f.**~*.******~-*******.*****~"****1i-*****·n:-***·*-;i:***.J~~*-**·***:ji.*-· ( !~S: PROCESS FRDl'i NODE 14 TO NODE 15 »CODE "'" 22 (.::: i . ( I:-:=--:~~~~f~~~~~j~~;:~:~;~;;;~~~~~~::---:-----:-::·-----·-::::--:-:---:--:=--:-:::~::::-::::::::=~ . h-----.-,WA TEl3.g_0Yp'~E .. !:-E;.!::!9 Tl-L := .. ~ ____ 130. _ooq. . . _... ..... __ .... _ ,_', _ ...... ___ ,_ .. ____ .. j'lG! 1 PIPES ;\T 27.000-INCH DUII'1ETER (. ,41' 1"1ANNINGS N::" . 01:300 . 14~~ _____ G.Ot1PU-C~p·.fJ~.Q~L...Y~~Jl.C,L"fy_ .::::: 6. 1297 FPS j" , ( ~. PIPE DETERMINED FOR NON-PRESSURE FLOW :,:3-----' -TR.4VEC-'TII-1E-YS· -.' . 3s:::f47 NINUTES (u NEW TIME OF CONCENTRATION IS 10.715 MINUTES 1., f'.J , .----'.--------,--------.. -, -~-.. --~-.--------.-~ --A~ **************************************************************************** ~~u **********************************~***************************************** ;!l PROCESS FFW!';I NODE 15 TO NODE ,15 >:::-CODE ,:: J .. (.( '-, ...----"_.---_._---_." --.... -~-~-~ ---.. -.-""-"'--''''''-'---'-,~ ---------------------------------------------------------------~------------".r , (", *****************************~********************************************** PROCESS FROM NODE 31 TO NODE 32 »CODE = 10 « , _. _ _ ___ •• __ • __ ., -------. >, .... , •• ~_~_ • __ -<0 ___ ._ i~ -_--------------------------------------------------------------------------DEVELOPNENT IS COI'1I"IEHC I AL ( INITIAL SUBAREA FLOW-LENGTH = 700. 0000 UPi.·rfREAN ELEVf\TJON ::::: 56. 0000 DL1~'JN8TREpl~'1 FLEVl,l I ON .-48. 0000 ( £;LEVr;TION DIFF="ERENCE -8. 0000 'OCEMA RATIONAL METHOD TIME OF CONCENTRATION := 10.·0151 ,/;'------?---------~--". -~----------. ---.-< ----------~ .. --- . (:" ' .. J _ ~ Rf1.1NF~iLL INTENSITY FOR RATIOI\l'!,L t~1ETHOD TWO YEAR STDl-1N = i 4. l,~;--~···-------,-.---" -r'Cl' 1 :~! ~ ,51 L':J' l I € . I, ~.---.~---,------- i ( I ~ , SPECIFIED IIC II ::::: 13" .850 h,;-----·---·~ --~-----..... -,----------~-----~------__ A. --".' ---. --, .-- ( ... , DISCHARGE --2. 1402 TOTAL ARE,~ := I I '17' 1.4000 1. 7~785 i :---------,---------------------------------------------------: ----------,---;-----,-----'- L ,::: -***'***********'li-'*'lf'***'******'~*******'*********'li-~'*****************'*:*'li-**~*****~** !IS! PROCESS FRD.i'''i NODE 32 TO NODE 33 »CODE := 70 <-.:: : " II£I--::.-:=-:==--=:...-=-==~::::::==---=::::::-::==:..:'::..::::::.:.:-.:::=-..:.:::..:::::.:.:::...:..:..::----'=.:.:::...=--..:..:..::'=:::':":':':':''=_:':':':-'':'':'::':::::'::::=:.::':'':::'-~==-'':':::::::::::::::::::':'::-' ( :111 V-GUTTER HYm~ ... \ULICS, ' . !,zl WIDTH::: 3. 00 . GUTTER I-III~E:::: . 08 :19~-·~·--Lrp=--. ()3--'-IQ'ANI\lTl\fGF.),1q--:;:---':-Ol::r-----.. -----.. -- ,( t"~ CROSSFI~LL :::: '. 020 ' 121;' ALLOWABLE 1'-lAX Xi'1U(v1 DEPTH::: . 50 12lr-~··-OPSTRE:(~lr ECEV;"\'l" I oKr ;,;--.-·48~OO' ( ~ DOWNSTREAM ELEVATION = 46.20' b:, GUTTER LENGTH ::~ 350.00 ~ • rl>;~. -" --'-,-. ~-'---.--.. -.. ---.. ----------'------.. -"-----._---, -- ('"'i"(;: RAINFALL INTENSITY FOF< RATIONAL !"lETHOD TWO YEAR' STOR/yl ::::: , '~, .. -.. -------. ;-:,-: .. -------~---- ) FUJI"';THROVGH 6UBAHEA AS INITIAL ESTII'-1ATE (Ii::~, USING ME(~N DIBGHf),RGE ,BASE? ON CFBlt)CRE , ' ( '1-,1 ' i "! ""'; . , . r'~ ... -,--·· -------"---.. -.. -----.......:.~.-.-... , /1"/ SPECIFIED IIC II ::::, . 8~50 ( ~:I" ' J"j.--~-["1EAN FLdt~ -tHtH:rI"--sUn;6.RE;\---ts--;;-------2. 6l '-~ll I:~~=:::-~~-:-~-=:~-:::Zii--::-~~-Q:~--=-:~·i~=;;-:-·,-=,~~-.. =-=·--:---:-:---...:----'--~-:----~--=-:=~=--~~,-::=~-~:=:--:~:-::~-=-:--:- <. H TRliVEL TII1E'~:; 3. :l5 -.. . ! ~21 j ,--------------_ .. _--------------.. _--_.. -I" SUBARE.<:'\ :::::. . 70' ACRES ( h ;:~ ~---_ .. TIME OF CONCENTRATION FOR RUNOFF PEAK::::: 13, 1684 --------.. -COl'ilFiEfrC rAC DEVELOPI'1ENT ASSW'IED -.. _-.... ----, .. ----. --.. ---.. ------.... --, .. ( R,.\INFALL INTEI\ISITY FOR RATION/~L 1"1ETHOD T\\)O YEAR STORI'1 -- ~.: '" ,--------------SPECIFtED "C'II -.850 ." .t'0 <', TOTALG ::::: .3.0822 ---2-. fooo , . .", ***************~************************************************************ PROCESS FROM NODE '33 TO NODE 33 »CODE = 60 « • ---------------~------------------------------------------------------------1. 50. ACREE) ( TIME OF CONCENTRATION FOR RUNOFF PEAK = 13. 1684 ~-----.-----'CQI"1l'1Errt-tAL DEVELOPMENT -")SSUt'IED C ___ '" RAINFALL. INTENSITY FOR RATIONAL I"1ETHOD TyJD YE(-\F{ STORN - ; \, I ---..... --.~ _. ____ ----....M __ ._ ~-•. -.--* .. -~ -.----.~. ." ,., .. ---.. I, f 1----"--EWE-C n=IE"t)-'IC II--;"-'-: 850--'-----.--_ ... ( i" i' 1. 58"82 . . '-'-.-~ ~----------... -.----I ---------------, --.-.--.------.. ----.-.. • ---:;' DELQ ~::: 2. 0185 TOTAL Q --5. 1007 TOT p,L AREf>; -" , 3.6000 in -(', ; ill ***·l:H~·************_li·****J.}***-ii_*J.}****·lH~·*****************~i-**~!-*·******·)H************ . I:~-; ~--'--PROCESS-FROl"'l ·i~obE--·33-T(f-NcfPE-34 »CODE ::::: 22-~::;~'''''' -----....... ,'" -... ----,----- (I~' -----~--------~-------~---------------------------------------------------~-I::!---' ~l{~A~-i H~Jj~~ ~~E~ Ei\jCEfi~! 9.9.Z f, '-50000 -. '----_. --. -.-._. .. C in WATERCOURSE LENGTH := 300.000 11;' :( PIPES AT 18. ODD-INCH DIAI"lETER 11J"----l'lANNII\iGS-I~· ';;;--''-61306'-------. . . ( j'~~; COMPUTED FLOW VELOCITY::: 5. 29~j3 FPS _. I;~;-' _.-'VfPE-DE-:'fERMiNED FOR' Ndi~'':PF-<ESSURE FLOl-J C n; ;2~: . 1,·>-'--~ ., j" TRAVEL TIME IS .94423 MINUTES ~iE:W fIME 6F-··(~-:5J\fCEt:il-;;Rkl:IDN IS 14. 113 I"1INUTES ("':2e ( , ****************"~***:*****'*<fi-**************'*'**********·***'R-**·*********1~*{:·****** ' , . ---·-ir****"iZ;-;*";~;;~~*·;~***~'~~·li-**·-",Hi-i*·i*******·li-'R-* R-**'*·***·R-**·R-*".}·l}*******-l~***:j;****·li·***·i*~;** . (. > PROCESS FRD!'I NODE 34 TO NODE 34 »COD£ = 60 <>:: 1 .. ,' \ 1""~ ---....... --.. ---•• ~-.. , .. -.. --":' .. ------.. -----.. ----.---... ------•• ----.------------.. -.--.. ---.-•• --.... -........ -.----... ------...... . 131 ---'----SUBAREt.;--:= . "'L' -1 b ')l)CNES .... _-_.-.,---- <-'~!' V TII'"1E OF CONCENTRr'HIOI\l FOR RUNOFF PEAK·-:l4. 1126 Ic,-------.---·---·-·tm1·1~fEr:i,cTAL· DEVEL.QPi"i"E·NT . ASSUi"!ED ,(. 13" RAINFAL.L INTENSITY FOR RATIONAL NETHGD TWO YEAR STORN :=" 1. 4944 (. i", I , 1:1 :.. __ ._ •• __ , ____ ._ ---.-~--..• ------.-----,"" .• -.. ------- :~, SPECIFIED "e"::::: . 850 (. j~l' I·, 1'-,------.------. -..:.--, . -.. _ .. --. --.--_.-.---... -.. ".-o DELQ = 1.3972 "fOTAf_ G·· ... 6.4979 (. ," -.*************************~**********************************fr*************** r~~--'-~-'-~-"--P-RC)CE'SS'-'F"R'Of~i-f\IODE 3.ll-TO NODE j~5 :».(:ODE == 22 .:::<: . -~-.---'_'4_~. ____ ~ ___ ._._~ €/ ~.. i --. --------~------------------------------~------------------------------------ ;:' _____ eJPE __ D;T-!.?Cljr:"R(;r::.= . 6, _Ll,9795 ~~i ELEVATION DIFFERENCE = .50000 (:'-~.,jATERCOURSE LENGTH ::::-. 40.000 L-.• __ . ____ 1._P I PE:S ... p,T :t 8. 000:-1 NCH D It.,!'~ETER P, MANNINGS N == .01300 ('~ COMPUTED FLOW VELOCITY = 6. 5464 FPS '-~. PIPE ri~tE~MINED FO~-~ON-PRESSURE FLOW Ie TRAVEL TIME IS . 10184 MINUTES NE'W--YiI"IE OF' -CONCEN-TRATION IS 14.2:1.4 I"IINUTES ( ~*~******************************************************~****************** **************************************************************************** PROCESS FROM NODE 15 TO NODE 15 »CODE = 1« -------------------------------------------------------------------------------------_-. .. _---...---~---~. -~--_ .. ---~--~-~-~~ ....,.._ .. ,. ~ ,; .,./:-: ~ ~ . CONFLUENCE DATA ~-l;>!" . N DISCHARGE TC I . .' . ' . .:,g:{~C---~::":.:...:-~~::~~-...:.::=~~~~t.:.~~~=-..::.::::..:..------'----------,.--:..-...:-...:..:--'-::...:.:...:=.:.,.-=---=- 1.i 2 C,. 50 1·'·~, ",~1. 1. 49 . 11r-------·---QC .. ~M/~ ··c·bt\fFL-(fEt'fC'E FORMtJLr~--D8ED -~FOR ).:::.-2 .«: F)A"rl--1S .. -~-~~-----... -..-----.. ---- (" 12i . 191 VARIOUS DISCHARGE COI"IBINATIONS ARE AS FOLLm4S:' 11'J!~-'-" -"-"---" ··-2~+-,·81~--·-··--·-~~3. b't . '.-.-"-'---.--.. --... -. -"'--.... _ .. -. -.. --'---'-'--'- (' lllj CONFLUENCE ESTIl''lATES ARE AS FDL.LOWS: " 'L . 11~l . _____ G ._-=-_ ~ _g:l::_.§l.:~U1._.l~ .. =._~_10·2J.-~-J3UI'1!·1f~TIo.N_ OF t'REA.:,_. _ ._17: __ f~Q9.. __ .~,_~_.,... ____ ~_ 13, { U:· .********************************~******************************************* ,~ I ( ·:i~. --·-~~~~:~m~;~;~:~:::~-~:;;~~f:::::t~~::~~~~~-:-==:~S~:.~=~~~==:_~=~= ____ -::=- ,_._----_ .. _------~ ... -....-_ .. --.-. "_ ... _--------"_. -" -.. .---~. ----~ .. _-_._-------..... -..-..-..--~--~--~----.-~---19;. WATERCOUHSE LENGTH::::: 480,000 . . (;zn: . 1 PIPES AT 30. OOO--INCH DIAlvfETER 'h~ t1ANNINGS N::::: .01300 . lni-···-C-Oi'lPOTED ··FCO~(VELOcfT'Y-;;"'6. '1032 FPS LJI ('.' , 21_. __ ~_rpE ._!?5~~5Rlj..!J'll':::.D. J~q~ _Nq~I-:-f>.Rf::.~SURE FLO\t..I· " .:2\ (-h (,' :;--~- TRAVEL TIME IS 1. 31078.MINUTES NEW TIME OF CONCENTRATION IS 12.025 MINUTES ( li::·L-:~:-;;;,;;.;:::::;;~;~;.::::~;:;;:;.;::~:;-~::::::::::::.::;::;;::;;;;;.~~:::~.;;-~;~;.;-' ~ PROCESS FROM NODE 16 TO NODE 16 »CODE = 60 «. . ( Pi: -------------------------------------------------------------------------~--. h--.. -Sy'~~~~~. ~~ ___ ~:_i±..c~ l\g~~E8 ______ . _ .. ___ . .. . ... __ . __ . .. ..'_ . ,,_,.,, __ ,, _____ . _ ... __ .~._ ( I~ . TIME OF CONCENTRATION FOR RUNOFF PEAK = 12. 0255 110:: CO!'11"1ERC I AL DEVELOPi"iENT ASSUi'"1ED IJ7, ---ffAINF-;t)"LL.--rNtEHi:rtT'\/-FOR RAY(ONAL. !"IETHOD TWO YEAR STORi-.f .~---'-T-:-'64Efi-.... ----- ( I'~i . FJ:_' _____ . ____ . ___ ._. _____ ... __ ..... _ hi I ' {.111: !~;' SPECIFIED HC II :::: .850 ! --'-' •. _._ •. _ ... -.. _ •. -. __ . .. ---.-_._ ..... .... , , .. l-", . ~--_._-DELG ::;: 7. 5676 TOT,t\L. Q :;;: 32.4041. ( :' ;':1 **************************************************************************** PROCESS FROM NODE 0 TO NODE 0 »CODE = 0« ~--' ~ _ ... ----_... .----~ . -----------------------------~---------------------------------------------- '-'/ (' 'J A . .L \.J .\ 1 (" :1.2 5t 6; 7, 8, 9,1.0,11..12, 13J 14, lfJ) 16, c-(~---(f .-_.,._~ ...... , C lB. 90, O. 85 : 11, 10, 1.~~ , i~'----'S?: 2~"47;985.;r;Ji--;·2-:-8' 1-1:':; 12,601 ~2 '~I 1,4 ... 1 . .l} ( . i.1 -'~~'2';' :r/~T 2'--,. ..._ ... " -' ----_. '- ~~ 1 ~ 2 :; ....,.. 1'" ....,") !'1: ~11 Vle.C. :10'1'-' -'55:-1;48, '52'0,'1.; 4~"~.C2-'" · fill; 22, 4·0, :l2 jl~L_4:~_:!?:!..!~O~_~;. ~~: .!~_~. ___ . _____ ... -', ___ . ____ .... -... __ . il:: 6,. 02) 24 .. 1 . .., <. il';~ 1,2, 1, 1~ , tl:i! 2/2-,-, IJ--·~~f'i-:C--·-·-----'-""-'---------,-_ ... ,.. ......... -.. , '" 1101 j, c:.' c:..C:.J ,J.. 3 (17, 43, 42 .. 110, . 013 liS; 13,60" 13 I -----------.. ------------.. -----. " i'". 1, 4·, O. 9 · (::0 13, 22, i4 171~_~ .. ~?1 ... ~~":",,,?!.1.~O, . 9~~_. '''' .... , ___ . __ ' F2; 14,60, 14 (:1.:'1 1, '-1-, 3.9 ..,'24; 1.t.~J22,15 I __ . 00-_' --.--' ._---.. -_. -.. --.,." 4 1 .") (, ~ r.:: 1 r,}o 0" '3' " _1'-': ". c::.l .• ~~.;" •. 1 ,. J., (: ,lS 1,5, it 15 .' I 1 '") (~ ,;-" -8~ :\O~'j2-'" · (.~J: 56, 48, 700, L 4, 1. 4- I:~:< .---~~;--~~-~~~~r50, T; ~r;-(f. '~i" . , -.. ,-" ( I." 3 08 O'? r\ 1 ",.. 0"') "1 1"-: . I • J. '-"} ~ \..r \.:/J.. 't.. __ ,. \..: !~." 33, 60, 33 I . ____ . _____ ... _ .. __ .. -,---------..... .. ....... -----.. -.------' j~l: L 4, 1. 5 <. I:'; 33 .. 22,34 ~. 44.2,41.7,300,.013 hi:---3.c~;-6l1~3-4---------------· .----.------~ ---.-- (b: L 4,1. 1 L I r) Jl '">"), l' 5 , ... ') ,-..J~1 t::::.c:..J I ,-------------. -".--" ',' ----....... -... ---.. i-'. 41. 7,41. 2, ll,O, .. 013 · ( :~ I: 1 5, 1, 15 ( OJ 0, O. bEND ! ':, ---_. -,-----'". ( ( ., ',' ~.--,--. ----.. ,---, ----------~-.------. ,_ ,_ . ______ .-.-____ ·· __ ·,,------1 , •• _ • ______ --._~ ______ ,_~ ___ ... _____ • __ ~l.._,_._ ........... ,_ _. ,----~-----, --, -~-,------.------~ ..... --. o :::1E :r: u CJ) o z « z o (f'j :::1E « -I -I ~ ('. HYDRAULIC CONTROLS 'PIPE FLm,JLINE ::::' DOWNSTREAM CONTROL HGL ::: 34. '70 ...---~ _. {~ . SET AT NODE NVMBER 1. 30. 70 DIAMETER ::::: 3. 00 PIPE DISCHARGE:::: 47. 50 E(iL ::::: 35.40 C', _--------------------------------------------------------------------------------***************'***'J:l-****'l*******************************-It'***'li-*.**************** INP'UT F:i'rPE' FLOtrJLINE FOR NODE 1 = 30. 70 ---~ . ,~--~--.- **************************************************************************** ._---,---"--. ****************************************************************************- ( !'. ----------------------------------------------------------------------------::, INPut D{~TA: DOIA'NSTREAt1 NtJD'E :::: . 1 ! ~----... -- 't. UPSTREAM NODE:::: 2 HYDRAULIC PROCESS CODE -1 '~1? -_____ !"""' ______ .. ___ • ..._ ____ .. _ .. _________ .. ____________________ .. ____ N ____________________ _ ::.-~----HEADLoss FR-Ol'f'N(jDE" f TO NODE 2 EGUt.L8 FRICTION. ,"-OSS,.HF _-0 ..• -.. ---.--------- C '., HF ::::. L 'l~ SF ::,. PIPE DIAi"IETER:::: 3.00 :" ---." ... "-MANNfl\IGS "FR rCT:i:bi~ FACTOR :::: CONVEYANCE FACTOR::::: 666.94 .013 DISCHARGE:::;: 47.500 I ( :1' PIPE LENGTH:::;: 200. 000 SF ... c, ', .. -HF -L * SF :::;: ( 200.000)*< .0050'7240) = 1.014 ;1: -----~ --.----------. .---- Co. I -r: EGL::-.:: 36.41.6 HGL =: 35.714· ~n ____ ~ ___ ~ _~.. _A__ __. .. 0 **************************************************************************** ('~ !zz . -----.~ .. -_ .. _----- :. SOFFIT CONTROL ASSUI"IED AT NODE :tt-2 ( HGL = 36.70 EGL -37.40 :' -'--"'C()i:ff-PRESsDRE-~iE:AD IN SOFFIT CONTROL ( ."1. ASSUMPTION IS) . 99 ::.--_. --,-----------.. -.~ INPUT PIPE FLOWLINE FOR NODE 2 ::: 33. '70 (i •. , I..)~' .. ***************-It************************************************************ f --_ .. " .~.-.-.---._--_. -. ., . •• --~ ~. ---.. _-.... - j'1 *****,*;*.l}****.l}**-It;:i-*******~!-*********.l}*****************'li-***************'******{!-* . <-j3'.; ---...:---;...-.----.-.-------.--.----... ~---.-.--•.• --------.------•• -.--•• -----.-,.---.--...,..-.--.,. •• --.------.... ~. .INPUT DATA: DOWNSTREAM NODE = 2 j11-----' .. ,----UrSTREAi'1 NODE::::: 3 I . ( :11 HYDRAULIC PROCESS CODE -1 ~- ,..' ( ( ( !J,,' 1\",_ !'-. _. _. £. '- ---------------------------------------------------------------------------- HEADLOSS ~ROM NODE 2 TO NODE 3 EQUALS FRICTION LOSS1HF HF= L oU' SF CONVEYANCE FACTOR ::::: -666.94 ...... __ .. __ .. _._. _._ . __ ... F. .I:F.J~. D I AI'1ETER::: ::? 00.- MANNINGS FRICTION FACTOR ~ PIPE LENGTH -15.000 . 013 DISCHARGE.::::: 47.500 SF --(GIlt..) ·**2 :::: « 47. 500) / ( 666, 94) }-I1-*2 _. . 00507240 HF :::: L * SF = ( 15.000)*<. 0050Z240! ~ .. 076 EGL::;;; 37.477 _ ._ __ _ HGL.::::: 36.776_ **************************************************************************** .'---SOFFIT CONTROL ASSUMED AT NODE • 3' HGL = 38.60 EGL -39.30 < LOST PRESSURE HEAD IN SOFFIT CONTROL ( ASSUMPTION IS' 1.82 I{" --"---'INPUj' P'IPE FLm,!LINE FOR NODE 35. 60 E ~t i I ,. **************************************************************************** : ;---'*****-ti*'*****-li'*'*i~ *******'IHi-********'~***********'li-*******'~*********1!-**.*********' ~(~~ ---------------------------~------------------------------------------------J INPUT DATA: DOWNSTREAI'1 NODE ::: 3 '----;'-----.. '---.. --tjPSTREAI'-1 NODE:.::: 4 ( HYDRAULIC PROCESS CODE -3 ---------------_._-------_ .. _-----------_ ...... _-----------------------------------~ . . -:-.--....... . }-IEADLOSS -FROl"1 NODE (3 TO NODE 4 EGUALS FRICTION LOSS~S . . ( , PLUS BEND LOSSES j ~ ;n--'-''tnSCHARGE--:.::: , .. 41~ 500 PIPE DIAMETER::: 3: 00 ( ,I" PIPE AREA::: 7.07 VELOCITY:.::: 6.720 i . I'd VELOCITY HEAD:.::: ; '701 f'<·'---·-----P-[PE'LEr;IG-fH--;,;·--6.-bocr--· ','MANNINGS FRICTION FACTOR'-;"" "":-613'" --".--.. -,. ( ",pi . CONVEYANCE FACTOR::: 66.6.94· I": ________ .... SF .= (G/KH!-*2 itJ SF . 00507240 ,( Ii; HF -L. * SF 'll' HF:.::: .030. !:-c,-'-'-RAD'I'AC' DELTA';;'-' 8.. 00 BEND COEFFICIENT:;: .075 BEND LOSS ::: ·c· .13, , '~1 ... . I..,. %_ ___ M -~.--.--:. ------ EGL ::::: .' HGL-= 39.384 88:683 .052 I!o I." ~. I ~ '?' '\ .. t-*********************************~****************************************** • I, ~ 2:· I . _. ""'_ ... , ___ . ( . SOFFIT CONTROL ASSUMED AT NODE # 4 ;o·. __ , __ .. _J~GL _=' ______ ~9~ .. ~.Q.. .. EGL:::: 39. 80 (J'. LOST PRESSURE HEAD IN SOFFIT CONTROL Ass0MPTION IS .42 INPUT PIPE FLOWLINE FOR NODE 4 ::: 36, 10 " ~ 13" --**************:j~*-********·~·li:·********·I!_***·I!_******************-It.*****************~~i (_ I.. **************************************************************************** I • . II"'~_._.::,:::::::.~::.-::-:--~.-:-:--::-::-.:-:-.---":------"".~---'--.. -.-:----------------------::-.:-:.-:-:-..... -----:-.-:-.:-:-.:---:::.-:--:::=::-::-... I~ INPUT DATA: DOWNSTREAM NODE::: 4 (: :,. UPSTREAlvl NODE::::: 5 . . 4" 'L ~ f ~ ( ( • HYDRAULIC PROCESS CODE ~ 1 .'. ,-. ., --.. -...... ------------.. ~------------........ --------.-... -----------_ .. _--------_ .. _----------_._---.. ""!""- HEADLOSS FROM NODE 4 to NODE 5 EQUALS FRICTION LOSS~HF HF :;: L * SF --.. -· .. ·---.. PIPE DItf.\I"IETER·::: 3.00 CONVEYANCE F,~CTOR --666 .. 94 MANNINGS FRICTION FACTOR::: .013 DISCHARGE -47.500 PIPE LENGTH --22. 000 SF -CG/K>**2 ::: « 47; SOO)/( 666.94»**2 -.00507240 HF .-L ·u, SF ::: . .11~~ EGL::: 89.91.3 HGL:::: 39.21.2 ( '. ****************':i-*******'I!_*******************{.~***':i-**************-1!-************ (' '. SOFFIT CONTROL A;38UI"IED AT NODE *I: 5 ( -. HGL ::::: ; 42. 10 EGL := 42. 80 , ( LOST PRESSURE HEAD IN SOFFIT CONTROL A8S~~PTION IS 2.89 INPUT PIPE FLOWLINE FOR NODE 5 ::::: 39. 10 • I ___ • _ ****************~*********************************************************** e -*********************~**************************************************~*** ( ------------------------------------------------------------------------~---INPUT DATA: DO!;..!N~'1TREAM NODE ::::: 5 UPSTREAM NODE::::: 6 HYDRAULIC PROCESS CODE -1 ------------------------------------------------------------~---------------( .. HEADLOSS FROi"1 NODE 5 TO NODE 6 EG,UALS FR I CTI ON LOSS~ HF ';11~_~ ___ •• _HF ::= .. _L __ ~ .. SF ........ _ ........ ' ....... ,_ ... _ .. ". ' ... __ . _____ .. )'. PIPE DIAMETER:::::' :;3. 00 CONVEYANCE FACTOR:::: 666. 94 ( I" t1ANNINGS FfU'CrION FACTOR::: . 013 DI8CHf~RGE --47. 500 ,"_. __ .... _ ..... EIPE L,ENGTH. =-....... 5.000 SF -(O/K)**2 -« 47.500)!( 666. 94»**g ::::: '.00507240· :1; '--~'--~ ...... ---~--.---_. . . HF - L * SF ::::: ( 5.000>*( .00507240) = .025 . ( [7 . EGL:;;:; ,42.827: I-K~L::::: 42. 125 (' **************************************************************************** ___ .. __ Ihll?UT_.F:lPE FLO["'!LJNE Fot1 NODE 6 := 39. 10 . '_'_' ___ . (~" **********************************************************************~*****' ".~ ~.:**-:lt*i!'.*-~****.)i-***.):!-*******.)i-*************.~********,****~i-****-l}******'****11'*****:*** --------------------------------------------------------------------~-------( INPUT DATA: DOWNSTREAM NODE = 6 { ( " UPSTREAM NODE:= 7 :, HYDRAULIC PROCESS CODE -3 : _ ... , _._._ ... _HEADLOSS FRON NODE 6 TO NODE PLUS BEND LOSSES 7 EQUALS FRICTION LOSSES .. _. ___ .. " DISCHl\RGE :;:._ 47 .. 500 PIPE DIAMETER:::: 3. 00 PIPE AREA:;;:; 7.07 VELOCITY::::: 6.720 ( VELOCITY HEAD:;;:; .701 :; __ . __ ........ Y_reE .. LENGTH:::: '3.5. 000 .1"1.<~NNINGS FRICTION Ft;CTOR :;;:; ( c (. ( .0:1.3 ,'. CONVEYANCE FACTOR::::: 666. 94 1"" SF SF HF HF ._RADIAL DELTA::::: ... 90. 00 .BEND COEFFICIENT ::::: :::: :::: ::::: ::::: (G/I-\) {i-*;;! .00507;;:!40 L '·Ii· SF . 178 .250 EGL:;;:; 43. 1.79 HGL --4·2 . .478 .**************************************************************************** INPUT PlPE FLOWLINE FOR NODE 7 ::::: 39.30 ***************11***********************************************************~ **************************************************************************** ----------------------------------------------------------~------------------. . " '-",'.' -' ~ ~ - 7 INPUT DATA: DOWNSTREAM NODE = UPSTREAM NODE = 7 HYDRAULIC PROCESS CODE -8 ----------------------------------------------------------------------------HEAD LOSS .FROM NODE 7 TO NODE 7 EQUALS ~UNCTION LOSSES .... --.-._-.-.-. -. ------. -.-.-. -. -..... -... -,-.0 -... -.-.. -_-.. -. ----------------~_;_-.;;:. ~--. . _.'~. __ ~ .... _'" • ( PLUS NEAN FRICTION LOSSES c ,~O .. DISCHARGE DIAMETER . AREA VELOCITY DELTA .. HV 1 36.300 3.00 7.069 5.135 .000 .410 ('" . 2 47.500 3.00 7.069 6.720 .701 ~ 11. 200 L 50 1. 767 6.338 90.000 ... __ , __ .. _ .. ___ . " ':' . 4 . 000 . 00 . 000 . 000 . 000 I' -( . DELY :::: (Q2*V2-Q1*Vl*COS (DELTA2)-Q3*V3*COS(DELTA3)-Q4*V4*COS (D ELTA4» ._ ...... ~ __ /JO. 5.'1f:G.Jl.'31-i.1+A2» .. ___ ' '_.~~ __ HJ ::;: .292 (' FRICTION LOSSES :::: L * SF J _ F:R I CT I ON LOSSES::;: 6. 000* . 0040 :l737 _. .".024 1\ C :\ EGL =: 43.495 -I' I ___ ~" ___ •• ____ ~ HGL :::: 43. 086 ..... _____ .. ___ _ **************************************************************************** ( /1: . INPUT PIPE FLOWLINE FOR NODE 7 :::: 39. 30 I . i1:;' I :--------"-.' ....... --.. , ........... --.-............. -.. •.. , ... -....... "'-" .-...... ---.. -... .. l~ **************************************************************************** ('1'1 *'li'*****************************************.Jl'**********·I:H~*·******~~**·~H\-******{~*. ____ "':-___ .. _ .. ___ • _______ .. _____ • _________ ..... ________________ • ______ ...... _______ .. _-.. ____ H _____ ._ ~ .. ----.~ --... -.----~ .~~ .. ~-.---~.--.. -, .~-INPUT DATA: DOWNSTREAM NODE ::::: 7 ( :. UPSTREAM NODE:= 8 HYDRAULIC PROCESS CODE ::::: ( .. . ' , .. I ,. ( I .. t1 .. (. ,-- ( 1 ---------------_._----------------------------------------------------------HEADLOSS FROM NODE 7 TO NODE 8 EGUALS FRICTION L08S,HF _ .. _ ............. _ .HF :::: .~ '*: S~. .. . PIPE DIAMETER:= 3.00 CONVEYANCE FACTOR:= 666.94 MANNINGS FHICTION FACTOR::::: . 013 DISCH{~f-{GE -36.300 PIPE LENGTH:= 220.000 S~ -(Q/K)**2 -« 36.300)/( 666.Q4)}**2 -.00296238 HF::::: L * SF:= ( 220.000)*( .00296238) := .652 EGL:= 44. 147 HGL.::::: 4':3. 737 **************************************************************************** ___ . _~t.,fPUT _~IPE FLm'JLINE FOR NODE 8 ::: 40. 40 (. ****************.Jl*********************************************************** ( ( (. ,~- ( "" ( :; **************************************************************************** I " ______ ,. . .. ~ .. _ .. "_ . • .•.. .. . .... " ----------------------------------------------------------------------------INPUT DATA: DOWNSTREAM NODE ::::: 8 UPSTREAM NODE = ~ HYDRAULIC PROCESS CODE -3 ----------------------------------------------------------------------------HEADLOSS FROM NODE ' 8 TO NODE PLUS BEND L.OSSES 9 EGUALS FRICTION LOSSES DISCHARGE = 36. 300 PIPE DIAMETER -3.00 PIPE AREA = 7.07 VELOCITY:= 5. 135 VELOCITY HEAD =: .410 PIPE LENGTH = 21.000 ,MANNINGS FRICTION FACTOR - CONVEYANCE FACTOR:::: 666.94 SF = (G/KHI-·*2 .00296238 :::: L * SF SF :::: . 013 (. .. HF HF ::;: .062 137 RADIAL DELTA :::: 27.00' BEND COEFFICIENT = BEND LOSS .-.056 c EGL:::: 44.265 c HGL::::: 43.856 ***·**********'**')i-.I}'Ii-*******')i.*************it-*****************·)i-·!i·********1i-********·. ( INPUT PIPE FLOWLINE ~OR NODE 9 ::::: 40.40 *******************.)i-********************'~*****************.*******.**.********* " .,. ***********'li-***':i-'*********-n'******************~'***'li-**'li-*'li-**********.~********.**{i. ( ------.. ------.. -----------.... !"'""---...... -.. --~----............... -------.-_ .. _ .. _----""---------------------- INPUT DATA: DOWNSTREAM NODE::::: 9 UPSTREAM NODE::::: 10 HYDRAULIC PROCESS CODE ::::: 3 HEADLDSS' FROI-' NODE 9 TO NODE 10 EQUALS FI~ ICTHJN LOSSES PLUS BEND LOSSES ( ,. D:rSCHAR(~E::::: 36.300 PIPE DIAMETER:= 3.00 ( ·( ( ,·· _____ ... __ £}~E ... AREA .. =:: .... 7.07 VELOCITY == 5. 135· ,.' 1" I,s ~ ., i' VELOCITY HEAD::::: .410 PIPE LENGTH::::: 21.000 ,MANNINGS FRICTION FACTOR ::::: .O:l3 __________ C.QNyr;:yANCE FACTOR::::: 6-66.94 R AD I.AL DEL. T A .-27.00 BEND SF ::::: SF - HF ::::: HF :::: COEFFICIENT :::: (Q/j,O~i-*2 .00296238 L .Ii-SF .062 1.'37 BEND LOSS _. EGL .. ::::; HGL ::::: 44.383 43.974 .056 **************************************************************************** ---·--·~····I·NPOT--PI'I:;)E FLO~\ILJ:f\jE FOR' l\IODE 10 = 40. S() .-~-____ .w_ (" .' (: _ .~~*~*~_~~********-li'***.*.*.***********'******'****************************1('**'****** . **i~***'*****1~*****#****'*********'~*******{Hi-**'*~~*ii,**·********i}*·*******·tH}-!'-"******* ------------------------------------------------------------------~---------" ....J !I}~t!I _ D,t~ 'fA: DOhfNSTREAIV! NODE:::: 10 UPSTREAM NODE = 10 HYDRAULIC PROCESS CODE - 2 -----------------------------------------------------------------------------'--'-'--'--'HEADLOSS FHOI"{ !~ODE 10 TO NODE 10 EGUALS MANHOLE LOSSES ( ;'-DISCHf~RGE = 36.300 PIPE DIAMETER _. 3.00 PIPE AREA = 7.07 VELOCITY:::: 5.14 -----------VELOCITY· HE~AD, /-IV,:::: .410 if' .. ~. LOSS -C.OB*VELOCITY HEAD { ,.1 LOSS ::::: .020 <. .-!. ( ( c. ;", -_. --------.... -------. EGL:::: 4 Li. 40'4 - H(;}L _. 43. 991.1· i:-***************~~*********~k*****_k<.*******·*****_h-_x·*****.)~******.li-****.*****~~****** ----~ --. ~. ----. ~ ~ -.-~ -INPUT PIPE FLOWLINE FOR NODE 10 = .40.50 . ___ * __ *.*~.li_***~*.*******i!-*******·n·**·*********·*******it****·*·**·********************.**~*_ **********************************************************~***************** -----------------------------~----------------------------------------------"'._. __ " _ ~NPUT DATA: DOWNSTREA!1 NODE::::: 10 UPSTREAM NODE ~ 30 HYDRAULIC PROCESS CODE -1 -' --------------------------------~-----~---------------------------------------. HEADLOSS FROM NODE 10 TO NODE 30 EGUALS FRICTION LOSS,HF HF ::::: L * SF P~PE DIAMETER::::: a 00 CONVEYANCE FACTOR::::: 666.94 MANNINGS FRICTION FACTOR -.. 013 DISCHARGE::::: 36.800 PIPE LENGTH = 185.000 ( ( .. --... _.. .. .... ~ M..... ___ "... -................ ... SF == (Q/K)**2 -« 3~300)/( 666.'94»**2 -.00296238 HF == L * SF = ( 185.000>*< .00296238) = . 5"48 EGL ::: HGL ::::: 44.952 44'.542 .-'**************'*'~*******{!'****'I**'I**~'*********'I****'l*******ii-***.jH'*****-ll-**********~~' --( INPUT PIPE FLOWLINE FOR NODE 30.::::: 41. 50 c ~, . -. -,--.-" .. ~-...-~ "'-**************************************************************************** **************************************************************************** --.-----------~-.. --.......... -~-.. ----------.-------~ ......... ---------"-"---.--~--"'!-'!""'--------:'~---"":"" ..... -".-~-,~-'--------.... -~ ~-. C I' tNPut' 'DII.\TA:--D0l4NS"rREAI'1 NODE == 30 UPSTREAM NODE -11 HYDRAULIC PROCESS CODE ::::: 3 ,--_._--. ---.-~----" .. -.---_. ---.~-.-~ ." .".-.~--.--------~ ..... ---~1 ----------------------------------------------------------------------------( :. HEADLOSS FHfJI-l' NODE 30 TO NODE 11 EGUALS FR I CT I ON LOSSES i' PLUS BEND LOSSES ;la:-------.----------... ~ --,,----~ . --,._- ( ;1,1 DISCHARGE::::: 36.300 PIPE DUil"lETER --3.00 ( I:, PIPE AREA = 7.07 VELOCITY::::: 5.135 F ------'.----, "'---VELOC ttY-HEAD ::::: --, . -410 . -._-- PIPE LENGTH:::: 18.000 ',MANNINGS FRICTION FA.CTOR - CONVEYANCE FACTOR -666.94 -"-.-,-.~ .. ~ -_. --. ----.----_ .. - SF __ SF == HF == HF - ( G/.li\) **:;~ , .00296238 L * SF ,053 t> ': , , .013 ( i' RADIAL'DELTA :::: il·5.00 BEND COEFFICIENT .::::: . 177 BEND LOSS -.072 EGL -45.678 ( HGL. -4'-1-. 668 , ****************~*************************************************~********* : .. ,'-----.-----~ -- (' :. , , ,-.sOFFIT CONTROL ASSU1"IED AT NODE 4t 11 .,----, 'HGC-':;:;-' --44. 70 EGL ':;:; , 45.:1.1 LOST PRESSURE HEAD IN SOFFIT CONTROL :J,i-·------ASSTJlvi'PTION,--rS· ,--. 0:-:1 , (' : . __ . ______ .!l\!~.YI .!~IPE FLQ\.\lLINE FDR NODE U. ::::: 41. 70 I( '. ****'li-*********'li-*')}********'i!'**'l$*********************************************** (' 'f \ .. ~: ( ... i·:,_. __ ,~*!~~~ __ ~,~~*-l********-J{'**·)!-*~-*~**-ii·********'*-J{'****************************'l$'*****~~_~~~,~ ---------------------------------------------------------------------------- . : INPUT DATA: DOWNSTREAM NODE = 11 UPSTREAM NODE:::: 11 HYDRAULIC PROCESS CODE = 8 ----~-----~--~--------------------------------------------------------------HEADLOSS FROM NODE 11 TO NODE 11 EGUALS JUNCTION 'LOSSES PLUS MEAN FRICTION LOSSES DISCHARGE DIAMETER AREA VELOCITY HV C I NO . 1 ,28.000 3.00 7.069 3.961 DELTA .000 .244 . 4-10 " " ( ... ,/ , ( 2 3 36.300 3.00 7.069 5.135 8.800 2.00 3.142 2.642 ,30.000 . 000 . 00 . 000 . 000 ~ 000 4 DEL.Y = (G2~V2-G1*Vl*COS(DELTA2)-G3*V3*COS(DELTA3)-G4*V4*COS(DELTA4» / (0. O'I*G* (.<\ 1 +A2) ) HJ ::::: .08;2 ( FRICTION LOSSES -L FRICTION LOSSES =: -Ii. SF 8.000* .00236245 ~I EGL = HGL :::: 45.211- 44.9(. .... 7 (! ,.. **************************************************************************** ( IN.PVT PIPE FLOlAJLINE FOR ·NODE 11:::: 41. 50 *·ii-******it·******·lt--n ****~~****************.**.)i-************.)i-***********.lt--:i-***.lt-***** **************************************************************************** ..,-.-.~-~.~ --~---... ~. . ~ -------. . _--_._--.... _-------------.. ---.-------~--.. ----.--.. -----.--..... --.. -.. -..... ----------"---_._--------_. INPUT DATA: DOi.-JNSTREAI1 NODE:::: 11 UPSTREAM NODE =: 12 HYDRAULIC PROCESS CODE = 3 (" ----------------------------------------------------------------------------i·;: .. _. __ .... __ ri~ADl..OSS .F:R.Oi'·1 NODE 11 TO .NODE 12 EQUALS FRICTION LOSSES :,' PLUS BEND L.OSSES ;l·. __ ._._. ___ .. ~ .. _P~.SC.H{iRGE.::= ... 28. 000.. .PIPE DIAi'1ETER :::: ;1' PIPE AREA." 7.07 VELOCITY =: 3.961 C '1' VELOCITY HEAD:= .244 :'~ .. _____ .. _J~:I.P~ .. LENGJH =, .18.000 . J MANNINGS FRICTION Ff\CTOR _=.. . ()~3 CONVEYANCE FACTOR -666. 94 ,( , SF :::: I _.-..... ----.. --. SF :::: j .. .. ?' , .. . , . ( HF := !-IF ::::: BEND COEFFICIENT = (0/1,(,) *1!-2 .00176256 L * SF .032 177 BEND LOSS -... ' .043 '._ . __ ( '" EGL "'" HGL == 45.286 45.04·2 " ( ( (" (. <- <- ( ,. <.: ( ( (' " 1"-' 1 ... __ ~_. . !'.! .2, i'" I :'" !- . ... , .. -. ***~************************************************************************ INPUT PIPE FLOWLINE FOR NODE 12:::: 41.70 ************************************************************************~*** **************************************************************************** --------------------------~------------------------------------------------- INPUT DATA: DOWNSTREAM NODE = 12 UPSTREf~M NODE:::: 13 --" . --...... ~-.------_.-.-~. _ .. J-(YI)RAtJL_IC PROCESS CODE :::: 1 ----------------------------------------------------------------------------HEADLOSS FReJl'1 NODE :t2 TO NODE la EGUALS FRICTION LOSS) HF . ___ .. __ .. Jjf_:::::: .J ..... * $F .. PIPE DIAMETER -3.00 MANNINGS FRICTION FACTOR - ....... _erPE LENGTH _ .. ,72.0.00 CONVEYANCE FACTOR::::: 666.94 .013 DISCH.<\RGE .. · 28. 000 « 28.000)/( 666.94»**2::::: .00176256 . _ __ .~ .. _~. _. _____ R~_. HF - L * SF =: ( 72.000)*( ~00176256) :::: 127 EGL::::: 45.412 HGL:::: 45. 169 **************.~l_*****_n.*****_li .. 1l_.1l_***********************.***~~**.)i-****~!_,~**~!.*.******* IJ\lPUT.. PIPE. FLmt.lLINE FOR NODE 13::: 41. 90 ... _ ... __ .. ' . **************************************************************************** _ .. *.*~*:lt-*.*~*.~***~·*·)Hi'·li-*******·"·**-1l-*****.*********'~'**************:*************.****~ ----------------------------------------------------------------------------INPUT DATA: DOWNSTREAM NODE = 13 UPSTREAM NODE = 14 HYDRAUL.IC PHOCESS CODE::::: ::1 ~------------.---------..--..... --~--..... ------.. ---.. ---.. ---.-.--.----.. ---............ -----~ .. ------.-.----"- ( ~-.-.-- " HEADLOSS FROIYJ NODE -13 '10 NODE PLUS BEND LOSSES 14 EGUALS FRICTION LOSSES DISCHARGE = 28.000 PIPE DIAMETER == 3.00 PIP-E-AREA~' 7.07 VEL.OCITY;::: 3.961 E,.i, VELOCITY HEAD:::: .244 PIPE LENGTH == 13.000 ,MANNINGS FRICTION FAGTOI~ -.013 CONVEYANCE FAcTOR =: 666. 94 -(-. SF SF -- --(QlKHH('2 .00176256 ( RADIAL DELTA --: ---.~--.~. 17.00 HF :;:: HF == BEND COEFFICIENT ::: L * SF .. 023 . 109 BEND LOSS ; .026. ( " EGL:::: 45.462 ;;! ______ . ____ • ____ .. _ .. _._ ... ____ , ... , . _ HGL::::: 45.21El "_ .. _., __ . ___ ._ .... __ 'I: ****************.~********************.J}*****~.**************'******1i'il-********** C :1.: INPUT PIPE FLOv.JLINE FOR NODE 14::: 42.00 I 1I4 ! ----_._------~--.. -~ ------.--.. _-..... -----_ .. -. .. -. ~---._._---*---_. ~_.- :1'i *************·J}**·I;-*******·*~·***~·***************·*******'J}*********************** C-I . 'I; : . ***************'*'*'J}*************************-lfo****'J}***~.************,********.J}~.* ,'''' ----------------------------------------------------------------------------!;,'----·fNPuf··DATA":· --Dtf~fi\isTREAi"1 NODE == 14 . ( .. UPSTREAl"1 NODE::: 14 i1r~._.___ HYPRAULIC PROCESS CODE :::: 8 '. ( HEADLOSS FROM NODE 14 TO NODE 14 EGUALS 0UNCTION LOSSES ,. ( " ( ( .. ' PLUS I"IF,:AN FRICTION LOSSES I --.-------•. ----.• '., -. I;; ,"' i ,NO. DISCHARGE DIAMETER AREA VELOCITY i'-19.500 2.50 4.909 3.973 2 28.000 3.00 7.069 3.961 DELTA .000 3 8.500 1.50 1.767 4.810 45.000 HV .245 . ~!4·4· .------.----.-------. _. . 4 . 000 . 00 . 000 . 000 . 000 DELY :::: (G2*V2-G1*Vl*COS(DELTA2)-G3*V3*COS(DELTA3)-Q4*V4*COS(DELTA4») / (0. 5*Gii-(Al+A2» ---'---HJ:::: .025. ( . FRICTION LOSSES -L * SF j_. '---'-'----_._.-.-.. FRICTION LOSSES -6.000* .00201150 :::: ·.Ol2 1~7 ( b; , EGL:= 45. 499 h.; HGL = 45.254 I -.-.. --.. _.------. . --. :': *********,*·]}****·l"Ht·**,*·R-****·Il-*****·**~·**~r***·*****.J}****.********~.*****.J}.J}*.********* <. i" INPUT PIPE FLIJWLINE Fon NODE 14::::: 42.00 ,' . ( ( ~~ <- ( ( (. . ~**_li.***.!t:********.*-H.*****.***************.*,********'*************'l(-**']}*'**-*****1fo**** **************************************************************************** ----------------------------------------------------------------------------INPUT DAT/~: DOWNSTREAM NODE::::: 14 UPSTREAM NODE::::: 15 HYDRAULIC PROCESS CODE = ·3 ------------------------------------------------~---------------------------HEADLOSS FROM NODE 14 TO NODE 15 EGUALS FRICTION LOSSES PLUS BEND LOSSES DISCHARGE:::: 19.500 PIPE DIAMETER = 2.50 PIPE AREA = 4.91 VELOCITY = 3.973 VELociTV HEAD = .245 PIPE LENGTH = 24.000 ,MANNINGS FRICTION FACTOR -.013 CONVEYANCE FACTOR -410. 15 SF :::: (Q/K)·**2 SF -.00226046 , . ( RADIAL DELTA::::: 30.00 HF ::::: L. 'R-SF /-IF == .054 BEND COEFFICIENT::::: 144 BEND LOSS::::: .035 (. .,.. EGL·~ 45 .. 588 HGL -45.343 c; - C· **************************************************************************** •• _0_. "INPUT' PIPE FLQl.\tLINE FOR NODE 15::::: 42. 10. _. "'-' -.--".- **************************************************************************** '*******·***·It*****·lHl-*******~··lt*************************·***·*-It**·**.!i.***********'*-**''- --~-----------------------------------------------------------~----~--------INPUT DATA: DOWNSTREAM NODE::::: 15 --.--. _..... UPSTREAI1 NODE::::: 16 -._..:. __ ..-__ .-0. : .. ~~ ~ ( HYDRAULIC PROCESS CODE ::::: 3 --------------------------------------------------------------------------------_._---.-_ .. ~ -~.---.--". HEADLOSS FROH NODE 15 TO NODE 16 EQUALS FRICTION LOSSES (' 1: PLUS BEND LOSSES '.,----------DISCHAHGE' ;,---19.500 PIPE DIAJVIETER _. 2.50 C 1) PIPE AREA::= 4.91 VELOCITY == 3.973 ... VELOCIT\l f-IEAD:::: .245 .. -----'--PfPETENGTH:::: 115.000 I MANNINGS FRICTION FACTOR:::: .013 .( CONVEYANCE FACTOR -410.15 . ( ----... ------~--. RADIAL DELTA -28.00 SF ::::: (Gn<.)**2 SF::::: .00226046 HF -L * SF HF:::: .260' BEND COEFFICIENT:::::· 139 BEND LOSS :::: EGL -45.883 HGL == 45.637 .034 ( **************************************************************************** .INPUT PIPE FLOWLINE FOR NODE 16 = 42.80 ( **********·R-"l*-***1H"lt******,Ht-***************·***·*****'~f-'*****'****'***~i-'***1i-***-li'1l-**** c I,' , ****************':i-************'**'***********************1}*************~;'******·* INPUT DATA: DOWNSTREAM NODE = 16 UPSTREAM NODE:::: 16 ~YDRAULic PROCESS CODE = 8 ( .. ----------------------------------~-------------------------------~--------~ j:: HEADLOSS FR.Oi"l NODE 16 TO NODE 16 EGUALS .JUNCTION LOSSES I --------.• --.. -. _______ ~ __ • ---,"------____ -.-.. -____ _ i-PLUS NEAN FI~ICTION LOSSES l .. .. :: . ( -.' .-:.. ( • NO. DISCHARGE DIAMETER AREA VELOCITY 1 17. 500 2. 50 4. 909 3. 565 2 19.500 2.50 4.909 3.973 DELTA .000 3 1.000 1.25 1.227 .815 90.000 4 1.000 1.25 1.227' .815 90.000 -. . .. _. , -----, ~-,--. HV . 197 .245 DELY_~ (Q2*V2-Gl*Vl*COS(DELTA2)-G3*V3*COSCDELTA3)-G4*V4*COS(DELTA4» / (G. 5*G* (.<\1 +A2) ) HJ = .048 FRICTION LOSSES - L * SF FRICTION LOSSES::::: 6.000* .00204049 -.012 EGL == 45.942 H(:}L::;: 45. 745 ( ****************'~***'**'***'lf-*-*-********************************.**.***********.*** . .~ __ . IJ\iP~T. i=>.IPE FLOhlLINE Fm1 NODE 16::::: 42. 80 ( **************************************************************************** ( ( /t ***********************.***************************.&-*****·&-*-U·*il-***oJHi··y..·li-****il-*** '-. ------------"""'t"'--------______ ..... _____ ..... _____________________ .---.... .,.--.. --.. --...,.. ______ . ____ _ , . INPUT DATA: DOWNSTREAM NODE:::: 16 UPSTI1EAI"I NODE:::: 1 7 HYDRAULIC PROCESS CODE :::: 1 -.. -.-..... " ---.-'.1 (Jl --------------------------------------------------------------------------~- ( ( . i , . , . HEADLOSS FROi"f NODE 16 TO NODE 17 EGUALS FRICTION LOBSI HI·:- HF'::::L* SF PIPE DIAMETER:::: 2. 50 CONVEYANCE FACTOR:::: 410. 15 , MANNINGS FRI'CTION FACTOR:::: . 018 DI8CH/~RGE --17. 500 -··-· .. ~-·-PIPE-·'LENG·rH _.. 107.000' _. -------.-.. ---.~~ SF ::;: (G/~O*'*2 ::: « 17.500)/( 410.15) >-**2:::: .00182055 HF - L * SF:::: ( 107.000)*< .00182055) :::: 195 , ---... ------..... __ . ------... -. -~ -, ... -~--EGL == 46-. " 137 HGL == 45.940 _ ************************-U*************************************************** 11',:-_ .... _ .... -tl'fpU'r 'P"IPE-FLt)14LrNE: FOR 'NODE"17 :::: 43.30 '-" .--.. -.... -.......... -.---.. -.. , , . ( .,:' . **·****·****·*****·)}********·lfo**·***********************************.*****.********* :1' --. *****-******.*****.l****.*******************************.*****************'******** . ('" -_.-.---_. __ ._------_._-_ ...... _------------_ ..... _---_._--------------------._-----------_ .... -'- .1' INPUT DATA: DOlA.lNSTREAM NODE:::: 17 i?~-' .. --~.-....... -... -.-'-'-~"(JP8TREAtvl NODE:= 17 ( .' HYDRAULIC PROCESS CODE ::: 9 "'"":"'"._-_ .. _-------..... _-...... --------------_._-_._---..... _----_ .. -----------~-.---.-.--.. ------------- .... ------·HEA1)[08f:f FffOi"l NODE' 17 TO NODE 17 EGUALS ENTRi·\NCE I":OSSES DISCHARGE:::: 17.500 PIPE DIAMETER:;:: 2.50 PIPE AREA -4.91 VELOCITY:::: 3. 565 VELOCITY HEAD:::: . 197 -.. -.. _ .. ·-------· .. ENTRANCE LOSSES --0.20 -Ii-HV ENTRANCE LOSSES :::: . 039 (. .... " ! ~ -_. E('}L :::: <. o3? I HGL :;:: 46. 177 _ ********·**i(-*********************************·li-*·**********'**-1i-*.*.***-ti-**.li-******** i~, --------INP-Ot P IPE ~ Fl~ .. (JtAJ[INE FOF< I"{JDE 0 == 43. 30 ( I" I'" ,.. -li'**********'li-*-li-~'**'*******~~**************************'IH-!-****1i-*************~~**** '.1 c_--*-****************-l-!-***************'*************************·1l·****1}***:l****·*****· . ( .. (, ( c ( ( .( (" ' .. L 30. 7,36,34.7,47. :5 L 1'/2 ( 200,.013~36,47. 5,33.7 2,1,3 -15, . Oi3, 36, 47. 5,3~i. 6 C-.. 3,3,4 ~7. 5,36.~,.013,8,36. 1 4, 1,5 ~ ~ 22,.013,36,47.5,39.1 5, L~ 5, '. 013~'36.-47. 5,39. 1 C '6,3.7 47.5,36,35,.013,90,39.3 --~ ~---. - « 7,8,7 ( " ,47.5,36.3,11.2,0,36,36.18,0,0,90,0,6.89.3 :':' 71 1,8 J:"--220;":'of3,"36; 36:-3,4·0.4 (II:' 8,3,9 I :1" 36. 3,361 21, . 0:l3, 27, 40. 4 ;tf'-cl,'3-1' 10 ~ .. ~~ .. (in 36.3,36,21,.013,27,40. 5 I !1". 10J 2J 10 ! -_.,. --~ ---.-----~ - 'I: 36. 3, 36, 40. 5 ( 10,.1, 30 _J_E!5L:. 013,36,36, 3,4·1. 5 " ", 30, 3, 11 ( ,", 36.3,36,18,. 013~45,41. 7 11,8,11 j,",'" ,,-. 36'-3~-·2Ef/·8. 3,0; 36,'-36,24,0,0,30,0,8,41. 5, 'iii 1:h3,1~~ 28136,18, .013/45,41. 7 12;' (~ f3"" 72,.013,36,28,41.9, , 13,3,14 i -------. -, .. --- )3' 28, 36, j.3, . 013. 1""-. . .42 ((" 14,8,14 ," 28, 19. 5, 8. 5, 0, 36, 80, 18,0,0,45,0, 6, L~;;~ , -i4J 3;'fs--.-- t· 19. 5,30,24, . 013130, 42. 1 t5, 3,> 16 -'--19. 5,"30~'Tf5, : dl:3.~28, • 4·2. 8 ( 16,8,16 19.5,17,5,1,1,30,30, 15, 15,O,90,90,6~42.8 :---f 6~/-i ";-i 7--.~ .. -. . , .. ( 107,.013,30,17.5,43.3 17,9,17 • __ • _____ w. 17. 5,301 4~.:L 3 c ( ( ,( ( , " 0 ~ :c u (f) 0 z « z ~ 0 (f) ~ « -' ..J ..J ~ c· HYDRAULIC CONTROL$ SET AT NODE NUMBER 11 'p IPE FLOWLI.NE :::: 41. 50 DIAMETER :::: 2.00 DOWNSTREAM CONTROL PIPE DISCHARGE == 9. 50 Ii r---.---HGL._ .. = __ . --44. 64 .. ---EGL ==. -44. 78 --.-...... --- -(~ -I,! . ---,-------------:--------------------------.,.----.,..-----..... -----.--------.-.---.:..------- , -; *·********·********.********it-********************************-n.******.*********** -!:;-,. INPUT' PIPE FLm.JLINE FOR NODE 1:1.:::; 41. 50 -. -- (,,( : 'i _. __ **.***_*_*~********.*-*******************************************************-It*** ._ 1 i ***'************'~:l}************1::'************.**********************.************ (' ;i -----~~------------------------~-----------------.-----------------~---------,~ : 1 L-.. _ ... (. I'::: .• I INPUT_.DATA: DD.WNSTREAM NODE::: 11 UPSTREAM NODE:::; 20 HYDRAULIC PROCESS, CODE --1 i1ZL_::.::..::"_-:=::_-:.:=::-_:::=_~--::::-_:-~·--:--:-::--:-~-:.~:-::::-... -::~~~-:-----------------------~-_~-_--_~_:::-:--:~~~-:-."7~:::.~~-=-=:::::".-_ '[1!1 ' HEAD LOSS FROl-1' NODE 11 TO NODE 20 EGUALS FR I CT I ON LOSS, ·!-iF ( I't':j HF :::: L .* SF· . 1°1-' ____ P.IF:E .. _DIAMETER_?=: ___ 2 .. 00 ._ ... _CONVEYANCE FACTOR =. 226._2.1 _' .. _ ...... ~ __ ~. __ . ____ _ Ilci, . MANNINGS FRICTION FACTOR:::: .013 DISCHARGE -~ 9. 500 C I::; PIPE LENGTH:::: 24. 000 .;. i '."----.-.------.-----------.------.------.-.. --~ rs; SF ::: (G/~O **2 :::: « 9. '500) / ( 226. 21) ) **2:::: . 00176371 .( In, ~ I· . ;n; __ , ______ ._._. __ . __________ . ____ . HE __ ::::_. L.* ,SF = .. (. 24. 000) * ( . 00176371). =? __ ._._. 04~2 ...... _ .... ~ ___ . (' p?: . . EGL =: 44·. 824 ~: I::: *;;;f~;~;*;~;~*;~~~f;~~*;~;*~~~~**;;":**';*:~~:~***~~;*:**!!;.::;**,,******;;*,,* . : .. : ,7" . I ~-... ---.. ---.. --.---.--~.~--.. ----------~.------... . --. -~ -. -;.--. ---~--. -->~ • --.--.---~-.---•• ,:'1: *.)i-**~~**,**********.'****.)i-**-)i-***.************************'******'l~'***************** ( **************************************************************************** .,' j.;, '--'=--=-=;~~~~='~~~~7:-;~~~~~~~~~'~~'~~~-:-'-;;--'--'---------~-------.---------~~----~--.~~ .. (' i~!i UPSTREAM NODE;:::: 20 :"31• __ ._ .. ___ ... ______ • .HYDRAULIC.PROCESS CODE"'" 5 .... __ .. _. ___ .. __ . c. !~~: -----~~~~~~;~-;~;~-~~~~--;;-~~-~~~~--;;-~~~~~;-:~~~~~~~-~~~S~;--'------------ :~\ ___ . ___ ... _____ .. ____ PLVS_ ENTRANCE. LOSSES DUE. TO G5 __ ...... _____ .. __ . __ . ___ .. __ . :~I : ( ~ NO. DISCHARGE DIAMETER AREA VELOCITY 1,'or--.----~-----~. 450000 ------2.00 3. 142 2.355 . . I c:;. -:~. 2.00 3. 142 3.024 c.. ill; 3 .000 .00 . 000 . 000 l~zL_. __ .. . ".-4 _____ .. _ ... 000 _ ...... . 00 _ . 000 . 000 DELTA .000 .000 .000 HV ... 086 __ ..... _____ .. _._ ..... __ .. .142 i;3 5 2. 100::::::::::::05 EGVALS BASIN INPUT::;::::::::: «: :; 'i DEL Y == {Q2·*V2 ..... 0 1 *V 1 *COS (DEL TA2) -Q3*V3*COS ( DEL TA3) -G4*V4*COS (DEL TA4 n /"i _ .. _.j (0~5*G*.( I~l ~I-A2) ) .---... .. ___ . ____ ...... ___ . ,ie, ENTRANCE LOSSES :::: O. 2 * HV2 ( -:,; TOTAL LOS.SES::::: --. 084· '·:'~ .. _WI-IER·E _.II:lE ENTR1~}\JCE LOSSES -. 028 . I" ." EGL. ::::: HGL :::: 4l.k 909 1.~4. 822 **************************************************************************** i (~. J~:'-: INPUT PIPE FLOWLINE FOR NODE . 20 :::: 41. 60 l,t;- I ,-' -. . .. ------... -.. . ---. -.... --- I~' **************************************************************************** ( ~ **************************************************************************** . . ---------------------------------------------------------------------------- INPUT DATA: DOWNSTREAM NODE:::: 20 UPSTREAM NODE:::: 21 ( HYDRAULIC PROCESS CODE:: 1 . -------------------~--------------------------------~------~----------------(~ HEADLOSS FROM NODE 20 TO NODE 21 EGUALS FRICTION LOSS,HF HF .. ::::: L *Sf. __ .. . -(:"-" -----PIPE DIAMETER:= 2.00 1"1ANNINGS FRICTION FACTOR =: (-r.' . ._ PIPE. LENGTH .:::: _ 28. 000 CONVEYANCE FACTOR ::::: 226.21 . 0"1.3 Dr SCHARGE --7.400 (,U '.. ,:,' SF ~ (Q/K)**2 ::::: « 7.400)/( 226.21) ) **2 .. -. 0010'7015' .... "" -----_._- !-iF ~ L * SF ::::: ( 28.000)*< .00107015) ::::: .030 ( j3 . , '9. ___________ ..... _ • __ .... _ . __ .. __ •. _ ... .' .,. . • EGL::::: 44. 938. . .. _ ~ ________ . :i~ HGL:::: 44a • 852- C' ~l **************************************************************************** , . ;I' _____ !.NF:V.c.T_EJPE.FLOWLINE _FOR NODE; 21::::: 41. 70 .... " . __ .. _ .. II: I " (;1:: ********************.****.1:1-'**,*************************************************. I I . 115 . ****************************************************.J:!-***********.1:1-*********** ! .----~-.-.-.. --_.. --.. -_. --.. ~ ." . .. -. . .--~--.-.----.-. --------------------------------------------------~----------~--~------------11£ ~. I I -i. p7; . INPUT DATA: nD.WNSTREAi'1 NODE::::: 23.' , i::, UPSTREAI'1 NODE:= 22 !1'. --.. -----.-------... -. ·-------HyDRAULIC PROCESS CODE == 3 ,(' :"e . . ----------------------------------------------------------------------------, 12 , ________ .: __ J"U;:.ARLQSS:FBOI'1'. NODE 21 1'0 NOPE 22 EGUALS FR I CT I ON LOSSES • ;zo, PLUS BEND LOSSES .r '.'_ I;", .. , ,_,_ ...... _. __ .. __ .... __ .DISCHl-'iRGE ==... 7. 400 PIPE DIAMETER -2. 00 ---1'< PIPE AREA:::: 3. 14 VEL.OCITY:::: 2.355 ( ;" VELOCITY I-lEAD:::: . 086 ( " 21__ .. P.IPE LENGTH:::: _. .24.000 II"'IANNINGS FRICTION FACTOR:::: . 013 CONVEYANCE FACTOR -226.21 j~" ;3!,-.. __ RAJ2.I_e~ DELTA -6l. 00 . BEND • i.!_!' , SF -. (G/K) *·*2 SF ::::: HF :::: HF -- COEFFICIENT :::.~ .. 0010701.5 L * SF .026 .206 .' 0 l EL _____ . __ ( j!" EGL:::: 44.982' ;;';' ______ . ________ . _ HGL .. __ 44,_.a96 .. ~ ..... __ .. _._~ .. _~ __ ... ,_. :3,' ***********************·li-**·~*1~******·li_****************************1-:'*********** C lj,· iNPUT PIPE FLOWLINE FOR NODE 22 == 41. 80 U9 i !------------~------~--"-.' --._--_.. ---. ..,. ~ .. --. -.. -.-..... -,-~.-.. ---. r· **************************************************************************** **************************************************************************** -------------------------------------------------------------~--------------, ____ •• •• _~ ._~ _ ~_4 _. ~ _ • ~ • __ ._ INPUT DATA: DOWNSTREAM NODE :=. 22 UP~TREAM NODE = 23 HYDRAULIC PROCESS CODE ::::: 3 ----------------------------------------------------------------------------HEAD LOSS FROM NODE 22 TO NODE PLUS BEND LOSSES 23 EGUALS FR~CTION LOSS~S I "'"<:.. ~.;: I( DISCHARGE ::: ... '~ ___ .... __ .PIPE AREA == 3.14 VELOCITY HEAD ::::: t, PIPE LENGTH == 24.000 .013 . ·. __ . ___ . ___ .. CONVEYANCE FACTOR := _ 226.21 SF = (Q/I"'HHi-2 (. SF ::::: .00107015 ~,' 1 HF-::::: L * SF -~--.---. HF -.02& { RADIAL DELTA ::::: 61.00 BEND COEFFlCIENT ::::: .206 BEND LOSS :::: .018 <. c· EGL := HGL == 45.025 44.939 **************************************************************************** :.~ rr'-: INPUT' PIPE FLOt.JL.INE FOR NODE 23::: 41. 90 . . ( i'" . I J ~ __ *~****i!"~***'l****.lt'*:******'***********'*,-l::-****************************************. *************************.~******************.~********************'li-*ie-******** ~ ....,..t. t . • ~ ! ---------------------------------------_ .. _-------------.......... -------------------~-! : G· 1-- ] . ( .': I _ .. INF:\J.T.DATA: DOWNSTREAI"I NODE:::· 23 UPSTREAM NODE =: 24 HYDRAULIC PROCESS CODE =: 1 'J. ~ ____ ~_-:::::_:-::::::--:::'_~: .. :::~.-------";*---------.-~_:"".~---~-..... -----_:'" _______ ...... ________ ._ ....... ___ "":"_ .. __ "":'_-_-::-::-:::::--:'.:':::_ .. I:, HEADLOSS FRON NODE 23 TO NODE 24 EGUALS FRICTION LOSS, HF (. II HF == L * SF jl< __ ._ .... ____ .E.IJ:l.E ... D!AMETER_ =: 2. 00. CONVEYANCE FACTOR::: 226.21... !lJ MANNINGS FRICTION FACTOR::: .613 ·DISCHARGE -7.400 ( if'i PIPE LENGTH:::::: 198. 000 \1,: __ . _ .... _ .. _____ ...... .. j!';; SF ::: (G/K)**2 --« 7.400)/( 226.21»**2 =: .00107.015 . C.' i 1 :11 I. Il~':.. __ . ___ _ _' .. __ . ___ . ___ HF _::::: L _ .~. SF 1)"0 i' .( , EGL := HGL ::::: 45.237' 45. 151 .. , -- ";21 ***************.~.************************************~i-********');.*****'********* £-if. INPUT 'PIPE FLO'4LINE FOR NODE 24::::: 42.90 . ********************.~***.)t_**********,l********************·~*********i."·~******1i-** C ***********1i.*****************.******.~*****************.***.********.***.********* ---------------------------------------------------------------------------- ( .... -... ., INPUT DATA: DOWNST~EAM NODE::::: 24 . UPSTRE/~M NODE::::: 25 .HY:DRAULIC PROCESS CODE ::: 3 --------------_ ..... --------------------_ .. _-------------------------------..... ------ ( (,. HEADLOSS FROI-1 NODE 24 TO NODE 25 EGUALS FRICTION LOSSES . 1"_-,-.. ",_ .. __ ._. __ ... _. PLUS. B.END. LOSSES. :3:, ( ~ DISCHARGE. =: 7.400 PIPE DIAMETER == 2.00 11.' ____ .. _._ P.IPE.AREA. ==, .... 3. 14 ....... VELOCITY::::: 2.355 /37 VELOCI TY HEAD:::: . '086 C i3'! PIPE LENGTH::::: 60. 000. I MANNINGS FR ICTION FACTOR ::= . I'J:'~ __ .-._ .. ___ CONVEY.ANCE_ fACTOR:::: 226. 21 « ( I~I: . L,l !' ~-.. , --... ..---.. -- 1'1, SF -(0/1-\)**2 .001070:1.5 SF := HF :::: HF ::: L * SF .064 .013 ( I;". RADIAL DELTA === 76.00 BEND COEFFICIENT =: .230 BEND LOSS = il):---.. -. ----~-~ .. , ( " EGL = HGL := 45.321 45.235 .020 i _._~*~*.*_lf.***.**.~**************-R.***********************.~*****************.!i'*:*1i'**** ::j ( , :'(1 ,1 .SOFEIT. CONTROL ASSUMED AT NODE # 25 ~ HGL = 45.40 EGL = .45.49 . _ ..... .LOST. PRESSUHE .HEAD _IN SOFFIT CONTROL ASSUMPTION IS ·:ib ( :', ".' i ',I " INPUT.~PIPE FLOWLINE FOR NOD~ 25 =: 43. 40 **************************************************************************** (" . ~*t************************************************************************* ~------------:------------.. -----.... ---------.----------------....... _---_ ..... _---.-----------(., ' I;~--.. INPUT D'.~TA: DO~INSTREAM NODE::: 25 UPSTREAM NODE == 25 HYDRAt)LIG PROCESS CODE =: 9 C· I ~. ----------------------------------------------------------------------------'-. f-~ . _'.:...i . .1 If" , "" " .HEADLOSSF~OI·l NODE 25 TO NODE 25 EGUALS ENTRANCE LOSSES DISCHARGE:::: 7.400 PIPE DIAMETER:::: 2.00 PIPE AREA = VELOCITY:::: 2.355 VELOCITY HEAD:::: .086 . __ ... __ _ _ ...... _. __ .. , .. , ENTI1ANCE LOSSES :::: O. 20 *' HV ENTRANCE LOSSES:::: .017 I, I' _ ....... " .. _. __ . ____ _ EGL :::: 45. 503 45. 503 J:'" HGL :::: 3. 14 4(.,1~ Tc... .. ··4~:&s-~- (. , ;1:. *.~*******************************************************-li:**************'*'*** ;12._. _____ . _.JNE.UI .. PIPE _F,I.,.O.WL,.INE F,QR."NODE 0 = 43. 40 . .. ____ -.'" ..... __ ._~_. __ ',. I': ( ;1" . **************************************************************************** , .. l~ . **************************************************************************** I ------.-.. --..... --. --.. ---.-----..... - ----'---.-----.. -. . ... ----... . ..... _ .... __ .-.. --." 11:; ( :1;: I,,' I' IH ,til., '?' . Il I 1":---.. '-.-----" ;f p; ri" J.2! i --" -----, . -----.. --- )-. ,. I . -( ;1:. !z'" : • ~_~ __ r _____ ~ ___ ; ___ .. tf,-. ~:. ' I'" -" ------.... ------.--. ·1;; {. 'j' . l:~:-~-.. · ----.. - -I'" ( I~': ,- I --.---'" -.---------" C := b~ I. ---_ ... _--._-. -.. -. .. ..... ,,---. j"" ( ':1 I. .. , ( 1(, (: ( ,- ,.-I '.' , (" ·11~41. 5,24,44. 64,9. 5 1'1, 1,20 24,.013,24,9.5,41.6' ____ .20, 5120_. . ... e 9. 5,7. 4.0.0,2. 1124,24·, O. O. O. 0, 0, 41. 6 C;-. '-20,1,21 ;: _. _28, .. 013,24,7.4,41.. 7. 2:L,3,22 7.4,24124 •. 013,61.41.8 :; _._ 221.3, 23... "". __ .. _-.. -. _. _ ... 7.4,24,24,.013.61,41.9 (, 23,1,24 l~-: _198.1 . D13, 24, 7.. 41.42.-.9. (; 24, 3" 25 ' (Ill, 7. 4,24,60, . 013. 76, 43. 4 !12~ __ 25,. 9.1.25 ____ ... ___ ... __________ .. _ .. _ ....... . 113 7. 4/241 43. 4 (H 0,0,0 IL:_END . ___ . _ .... ___ . ___ .. __ d';' . I ' (. 117: l'~~----~-------·---" ~.-------.----.. ------.. -----~. :l~ . I ' ,(~ ,0 " , ! 1.1' ; : __ H ______ .~ ~ _____ _ ;.?2: f'~· --,!:,,:' :~,1r-'-----'----------_ .. ----------.--~.-- (. IL; lZ! ___ . __ ... ______ ._. ___ ._ ( " L .. 1·" ___________ -... ~. I:: ' , \. !: i~~ ---_. --.-----._. -. C b;; 1,3; ----~~--------.. ( . I i~~ ; I '~ ___ ..... ____ . __ .. i·:" . , ' C jll; )'21 j ,--_ .. -. -----.---.... I" ~: ,. t" : ~---~-_. ---,----~ -- ( (, .. --.. ... , , ( ;" I;'!, I ' 1.--.--;::.:1 . ( ?' ~~, -.: ~ ...... ---~--'- '- ,,1 c:l ~ :r: u (f) 0 z ,. « z ~ -0 (f) ~ « ... ..J ..J §; c ( H Y D R A U L I C PROGRAlvlS DATE 12/17/80 AT 7: 46: 11 '. CIRCULAR PIPE HYDRAULIC DATA ~ ---~------~ ... -~----•• --""f'--~-----. . . Q:::: 47. 500 n ::= .0130 Diam::::: 86.000 8 :;::: .02000 . ~ .. ; --NbRivrAC-b"EPTH _·····-1.50636· .... .. ( ': K'::;:: . 23324 '" Dep/Diam::.:;. 50212 A::::: 3. 55336 V::: 13.36761 i:. -",.-.. ---. __ .. -.... -·HE .. ·;;-... ·~4. ;;~8196' -~p ::::: . 4.72510' R::::: . 75202 V212G:::: 2. '17t=J60 K -1.4.6443·:....-- ( ,1: '. FN::::; 2. 16473 Ii;' :,~--~-cRf-;.fI-cAI.:-DEPTj:J -;;~·--2. 24·~t61 ~. "'-~-'--. 1 , (" ill' K'C ::::: 11~. Cr i '!;Dep IDiam ==' • 74820 AC ::::: 3.04713 5.67263 6.27074 . VC := RC ::::: 8.37353 VC2/2G'::::: 1.08910 11s.--------... _.-.-.. HEe ·-;~·--·3. ~33370 PC . 90462 . ..... ... ~{c"-';---"-.-91287 --. (. i~~. FNC == . 99993 SC--.00613 /." .. -.---.---... ----~---....... " '-'-'---_., --.. . ... --. CtRCULAR PIPE HYDRAULIC DATA' . --------------------------~- 47.500 .0130 Diam::: 86.000 s .. -. 10200 ( NORI'1!~L DEPTH ::::: .9628:l K I __ :.,-~"" ·----DeiiID"iarh"';;,;---. 32094' A :::: ( ~ HE ~ 10. 10546 p::;:: FN :;-.::' 5.11434 ; ... , ( i, CRITICAL DEPTH:::::' 2.24461 K'C ::::: , .... -·--t-rI-tDeplb'fam--;,;;--'-. 74820 Ac :::: HEC::::: 3.33370 PC ::: :~: FNC::::: . 9<;'993 SC ::::: l~· -_._.---.--------.. -.. -~ .. --~.-".-----... , . 10328 1.95786 3.61360 3.04713 5. 67~!63 6.27074, .00613 v -24. 2611c) R:::: . 54180 VC :::: RC :::- 8. 37353 .90462 ( CIRCULAR PIPE HYDRAULIC DATA ---------------------------- V212G ~ "9. ·14265--------· , K:::: 2. 13922 VC2/2G :::: ---1:08910---' ,- . I'<'C:::: • 91287 .00520 .0130 s :;::: ... n --Diam --36. 000 ~: ( ( '. ( '. NORI'1I~L DEPTH -- Dep/D:iam ;:::: HE .- FN ::::: 2. 11-2599 .80866 3.36045 .84862 CRITICAL DEPTH -2.24461 CritDep/Diam ::::: HEC - FNC - .74820 3.~3370 .99993 1:<' J' :;::: f\ ::::: p - K/C - AC ::;:: PC == SC == .. 45742 6. 12408 6. 70841 3:04713 5.67263 6.27074 .00613 V :::: R = VC ::: RC == 7. 75633 .91289 8.37353 .90462 V2/2G ~\ := VC2/2G - ~\C = .93/1-46 .80593 1.089:l0 .91287 c ~ . CIRCULAR PIPE HYDRAUL1C DATA (~-.. ------------------------------- t!'i-" G:::: 36.300 n == .0130 Diam == 36.000 S ::::: .00520 .. : t. -NORMA'L'--DEPT'H = 1 .. 94683 f ..01 ( . ~\ '._ • 34956 _______ I?~p/Diam .:: ____ : 64!394... A::::: 4. 85469 V 7. 47731 . V;;U20 -. 86844 2 HE = 2.81527 P -5.61983 R:::: . 86385 ~" -'-L--10736-----'- ( FN == 1.01215 '..!. c··, ~\ Ie ::::: 2. 32865 AC PC SC -4.88994 ~. -, 5: 64568 -.00511 VC ::::: RC ::::: ---------------------------- 7.42341 .86614 . .. --------_ . ..,......!.-----'--- VC2/2G ::::: l\C :::: .85596 ,~ _____ "0 •• ___ •• ___ __ 1.09866 .C G:::: 28.000 n ::::: .0130 Diem :::: 36.000 . 00520 __ . ____ ~ ___ _ S - "' r-· C .-NORMAL DEPTH = 1. 64379 .' I i~' -----Dein:fiam--;;-· --. 54793. j,{, I ••• A ::: p ::::: .26964 3.96500 5.00041 i,./ ::::: 7.06178--'V2/2G --;"---'--7'71;-60'''------' HE::::: 2.41839 FN ~ 1.08009 R ::::: . 79294 K :I.. 3·~1-121 .,., ( CRITICAL DEPTH = 1.71151 ~\ ~e ::::: -c'-r. i t-De-p ID-lam' ';'''--. : -5'7050 AC::::: HEC::::: 2. 41293 PC::::: : 3 FNC = .99990· Be ::::: !,.--------------_ .. _-,,, ~, C. I:, . , i:. 1. 79620 4. 16672 VC = 5. 13683 RC = .004-57 ., I:: .----.:----.--------'---.. _. ----.- ( , .. _ . CIRCULAR PIPE HYDR,~ULrC DATA 6. 71992 .811:1.5 1:,;-.-----.-----.. -._.--. -.. ---.---.::-:-.-------------------.--------!':~;' G.::: 19. 500 n::::: .. '0130 Dif'3m -~ 30 .. 000 S = ;.t 1 .. 1 • tS__ ! I :;' NORMAL DEPTH:::: 1.. 48171 I ----.-.---.. ---.---- ;( .-' j • -~---,-'!' .. ' , ... " ( ',: I. --'-' -- ( -. !,: . Dep/Diam .. ~ HE .- Ff\! - eritDep/Diam ::::: HEC - FNC :::: .59268 ~. l2491 1. 02114 A ::::: p ::::: ~,/C :::: .59924 AG::::: 2. 12456 PC·- .99986 se-:::::. .30535 3.03032 4-.39311 1.97326 3.07049 4.42648 .00503 V :::: R - ve ::::: RC ::::: 6.43497 .68979 6. 35077 .69366 CIRCULAR PIPE HYDRAUl~C DATA ---------------------------- VC2/2G --::;;-. i6:Cif2'- KC ~ 1.28489- V2/2G ::::: . . 643:t 9 ~\ __ = __ .: .. J.. ~:23g9_t_ .. __ ... VC2/2G -- ~\C - .62647 1. 21662 c Q:::: 1'7.500 n :::: . 0130 Diam::::: 30.000 s :=: : 00520 '" c. L NO~MAL DEPTH = ( !;r------ ~ ! t:...".! Dep/Diam HE FN 1.38364 . . ~\ I ::::: ::::: . 55346 A:::: ::;:--'1'.-99570 '--'p - .-1.04464 ! 1;---'CRrrICAL 'DEPTH-;;" '1. 41570 , -, .... , /.<./C _. .27404 2. 78784 4. 19479 1.77088 v :::: R :::: 6. 27726 .66460 V2/2(,J = ~\ :;; .. .. . 61:205 1. 32717---.---~-. _. -------_ ... .0---"--- .. ~{ : , ~ . ..:~ i, CritDep/Diam::::: .56628 AC :::: 2.86741 VC :::: 6. 10307 VC2/2G ::::! 57856 . ~ 1 ;-----~ -~~"'--~---._-'l-fEC '=~""-' 1. 99·426 PC :::: 4.259::m RC ::: .67320 ~\C---"i~-2cj523-'---. (, ! < FNC::::: . tj>t7<191 Be :::: .00483 L 11"L-,.-----·-· .. · .. · --_ .... _ ..•.. _ .. _-........ -.-.,--->--.. C I,,' I :~~.---, .. -. -. '-'--'---.... _._...... CIRC-UL~,RP IPE HVDRAULIC DATA ( !'" .I" Q:: 32.400 n::: .0130 Diam:: 36.000 1--· -.------.--.-... -_.-._-.-.. ,.---------....... -.... --..... -. c l~ NORMAL DEPTH::::: 1.21259 ,1$) K I == • 15909 IE'-"--'--"--'-~n~p/Diam"'f:-"-''-L~()420-' l\"'; "'-'2;-67738 V:::: 12. 10140 ( i2' • • HE :::::. 3. 48727 p:::: 4. 13400 R:::: . 64765 Ir FN::::: 2.~23662 ----------------------------s ::; i ---------.--.---~ .. --~ - ,. 117, ~f 12:, CRITICAL DEPTH --1. 846'r8 ---+~~ ...................... .....,.........---...........-. . ' .02000 V2/2G --;;--'2. ·2746fr-----·-· .. -·-· '" == 1. 78t21 I,; ~\ 'C :::: .~ 11", ------C'; i ftfep7 D i a'm ,; .... -. --. -6'1566 ---AC" ( Iz: . HEC -2. 6?913 PC:::: 2.07846 '-'"4": 56586 5. ll·1269 .00484 VC ::::: RC ::: 7.096f4 .84355 vc~9;;iG-';;" --:-782fb ~<'C:=. 1. 17955 12' FNC .:::: . 9(;:)991 SC--I . 'f ~ : - ( i,., I' i ----.. ---.--... -.--131 , • ( !n' CIRCULAR PIPE HYDRAULIC DATA '< i __ . ___________________ ------------ t:>~-Q .. -:...;~--.. 32. 4'00' ---n·-·;..:-·--·· .0180 Diam -36. '000 ,1 oJ"..' ( I.: .. -13~: . NOFH4AL DEPTH::::: . 79082 13/----· ---~-----.-.. -........ _-.. -.... .. . ~~;::::: .-07045 t !l' Dep/Diam:::: .26361 A -1.48892 V:::: 21.76073 ... , .46025 :,~' HE:::: 8. 14605 P:::::. 3. 23505 R == j,oL_ .. _._ ... __ . __ , __ ._ .... FN =5-.-11024 ( I;; i 1~2 CRI"rICAL DEP"rH :::: 1.84698 I ;---.-~--_~_. ____ 4 -~\ iC '--~C07846 _. V2/2G = i" :::: 7.35522 2.46606 -.. ----. --,... ... ~------..... -- . . ~. "' \..1 I t~ Cl'itDep/Diam ::: !-lEG :::: .--.--.. ---_. --''''--FNC---;;- .61566 AC :::: 4. 56586 VC -7.09614 VC2/2G = .78216 .. 2.62918 PC --5.41269 He :::: . 84355 .. _ _ .. __ .:.~~. =_. 1_~._1??_~ .. ~.~ __ ". 99991 BC :::: .00484 (.,. <. CIRCULAR PIPE HYDRAULIC DATA ---------------------------- (-" G == 32. 400 .0130 Diam -36.000 S :::: .00520 ~ ---~"----~ ~ -NORMAL DEPTH:::: 1.80305 . Pep/Diam:::: --. --HE :.. - K' _. .31201 .60102 A -4.43721 V ::::: 7.30188 V2/2G -.82817 .83364' - 2.63122 P ...,. 5.32269 R -K ::: 1. 21273 ( " ( '" FN :;;: 1. 04719 ( .4-C'R I TICAL DEPTH ::= e- Cr'i tDep IDiam ::=. <:-_._ ..... -'-'-" ..... 'HEC" ;.."," ,~>; FNC ::::: !:1 ! .--._ .. __ .... . , 1.84698 .61566 2. -62cl1:3 .99991 .------.. ~, _.!-...-_--_ .. --'-.---.. -..--~---~ ,- ~" I C = AC :::: PC :::: se = 2.07846 4. 56586 5.41269 .00484 VC :::: RC ::: 7.09614 VC~/2G:::: .84355 KC :::: . _~]13::?~6 __ . 1. 17955 ;1' CIRCULAR PIPE HYDRAULIC DATA C' /.. , ·1 '~L_ . .9 .=: .. g.1-_!_j~90 Diam ::::: 36.000 Il~ , ! . (;n NORMAL DEPTH::::: 1. 52750 " ~,,' _ 1'-:.....---·_--_··_---_·· ... ----,-----.. ---.-.... -. C . 113, Dep IDiam::::: .50:17. A :::: 1\ " HE::::: 2. 25181 p:::: .23882 . 3.61679 4. 76740 i I'~ ___ .. _. ___ fi\'---=-__ l ~ _..1. oq 5.3 ... _.. __ P'l; C 117; CR I T rCAL DEPTH::::: 1. 60616 h.) K 'C::::: 1. 59092 v :::: R'::: s -- ., ,---------... _. ----------------_. 6. 85691 V2/2G':::: . 7303-1 .75865 K:::: . 1.44462 I l ____ . ______ -........... --.------.. _ .... ---.---' j". Cr i tDep ID:i.am::: . 53539 AC:::: 3. 852BO 4.92488 .00440 VC ::::: 6.43738 .78225 VC2/2G-;;-'--:'64368 --. . ( ;20; HEC::: 2. 24983 PC::::: RC ::::: ~\C::;: 1. 37370 ;2!: ____ .. ___________ FN.G. __ := .. ___ ~. 99992 ... SG. =. 4 i~:, . (" ""! ~. · i~~-----·---------*--.--.. ------.. -~.-~.--. '-', ~ ,"", (., k: · ;4'-: CIRCULAR PIPE HYDRAULIC DATA • Gi _. 19. 200 . n:::: .0130 ( .. ~ ~:,.:' NORMAL DEPTH == .. X 31810. ." 1-;, ,-_____ .. A ----• ---- ! (. 1", Dep/Diam:::. 4·3937 ,"": HE::::: 1. 95861 i<'-'--'-------"---···.···Ft\i-~-;,· .. i. 3.29.<1-6: 12" (. i~l' CRITICAL DEPTH::," 1. 404'78 tll------·--·---·· _ ... "~ ~-_ .. -.. ~ ....... ~ . <. !3.:, C-r i tDep IDiam:::: . 46826 I~): . _HEC .. -::'.'-__ 1. 94728 4a~-'-----FNC'::::: --. 99987 j,V ::::: PI - P - It. 'C AC PC SC , ( :"1: ;';2 ~ __ . ~._ .... _ . ___ . ~ .. ~.!~ .. Diam::::: 36.000 ::::: ::::: ::::: :::: . 18489 2.98993 4.34769 1. 23168 3.24883 .4 .. 5~182 .00415 'vi ::: R ::: VC RC ::: ::: -. ... --~---~-.-.. -_ .... -~._-----~--~ .. -. S ::::: .00520 6.42156 . 68771 5. 90983 .71848 V2/2G::: .64052 )". ::-_. .1.. 6:5Z~? _____ ...... ~ .... ,.~_. , ____ 0-.~. __ . ____ . ___ ..... ______ . __ ._ VC2J2G:::; . 54250 KG:::; 1. 56458 . -.. ------~.-._-... ~-.--. ---. ---.--~ .. ,- ( i~~;' ;::, l·,~------CIRCULAR PIPE HYDRAULIC DATA f' (~" G::::: 13.400 n == '. OJ.30 ~ . ., -!, .. ...._____ ~ ___ -_-0 ___ . ". ,..',;, , NORMAL DEPTH -' ( '31; • 1----- te,!, (~, t~-l -.' ... ___ Qe p .(Di am HE FN L 18024 _. .47210 -1. 71674- = 1. 08374 (:----.. . .......... -. ---.~. . !,,!. CRITICAL DEPTH -1. 231.07 ( ., . . ,( C-ri~p.epfDiarn := HEC ::-.:: FNC ::::: .: 49243 :I.. 7124-5 .99985" Diam:::: 30.000 K' :::: A - P -~ ~\ 'C _ AC == PC :::: se := .20983 2.28006 3.78740 1.35598 2.40704 3.88913 .00"'150 v :::: R - VC RG - s -.00520 V212G ::::: . 5364~ __ . ___ . 5.87703 .60201 K ::::: 1. 55279 5. 56699 .61892 VC2/2Q.= J.\G :::: .481.38 . . 1.49224 C' 9 .•. (" CIRCULAR PIPE I':IYDRAULIC DATA .0:1.30· Diam -~ 30. 000 S :::: .00520 .-~ .~: ~_~~~R.~i~~~ .. ~E.~TH. -' .... ~'~.p1.~843 !I Dep/Diam:::::. 44337 ~'\ I -18791 :A :::: .2: 10121 ( i,. . . HE::::: 1. 6:1.504 !,; i . FN::::: 1. 09435 I -'-'-.. _--._ .. ,... ...--_ ..... -p == 3.64324 ( I:':: CRITICAL DEPTH::: 1. 1,6192 i", 11\ IC::: 1. 21431 !1'r----'C1' :i:bDejilI5:L.3Cn . ;';;'-"" :4647'7'" At-::::: 2. 23435 ( !1';; HEC::::: 1. 60995 PC:::: 3. 75069 liS FNC:::: . 99('799 se:::: . 00440 I _ .. _ .. _ ... ______ . _ ..... --........... -••••.•• --------........ . 111~;i,' ('. '" p:; ii, ____ ... _____ ........ ____ ... _____ ... V :::: R ::::: VC :::: RC :::: 5.71101 .57674 5. 37068 .59572 ;1::- .' ( I~~ CIRCULAR PIPE HYDRAULIC DATA ---------------------------- V2/2G -K = 1.644-06 VG2/2G' .;;. --'-: 4480tr-:--' KC::::: :J.. 57541 .~ ~-.. -----~-.---.-: .... --.---~.--.-' L·: n::::: :0130 24,.000 S ::::: .00520· NORMAL DEPTH == .87775 Dep/Diam ~ .43888 HE::::: 1. 2~5048 . FN ""; ~"i:0559!..j· 1:'1' CRITICAL DEPTH :::i -~---~ ----.. -.------.--.- (. ~., , . I CritDep/Diam HEC ;~::-... -._-_._._-_. FNC ( j.~ " f ,,--_ ... --.. -------_. --_ . ., .. :::: 90310 -45155 ::::. 1. 24905 .. -99994- K'i A P j·VC AC PC se .. '18455 -, --1. 32692 V =: 4. :::: 2. 89649 R _. :::: 'i~ 14905 :::: 1. 37729 VC :::: --2. 94748 RC :::: :::: 00470 ~ I;:, ~.~ CIRCULAR PIPE HYDRAULIC DATA t --------.----~----.---~.~ ----.--~ .• -.---- '~'~'---'-~-.. -....... -........ 89858 V2/2G .-. 37273 45811 K := 1. 65901 " ---_. __ w -. ._--.-------.. - ----.. ------. ~ ______ ,_..... __ ..--.w_ 4. 71 {")40 VC212G :::::. 34.596 . 46728 ~\C .... 1. 61735 -----.-.-. --~----.-------.. -- ~, ----------------------------(.' :.,1: G== 5. 100 n:::: . 0130 Diam == 24.000 S ::.~ .00520 :t? . . . '" ·---·f~ORMA1=-·DEPTH :::: . '76800 ' .. Dep/Diam , --._--.-.. -------... -.... HE ~" _. 14480 == .38400 A :::: 1. 11099 V :::: 4. 59049 .. 1. 09532 2.67333 R .41558 -P :::: :::: V2/2G:::: .32732 '. ~( ;; "1.' 85l::i69" ... --._-, .. - c " t "',,' FN --1.07059 ~.' CR I TfcAT: DEPTH ::::: (. " Ci'itDep/Diam ::::: til _ ... -.-. ., HEG::::: .79578 K'C -.90156 .39789 AC :::: 1. 16521 ve :::: 4.37691 ·1.09334 PC _. 2.73025' RC :::: .42678 , ~ ----, -.--:----~ VC2/2G:::: .29757 ~\C· -~.--'f:. "80487 ( FNC -. 99r:t92 SG ::::: .00456 ( ..... , '-~~RCULAR PIPE HYDRAULIC DATA _ ....... --------:""""'--_.----_ .. _-------- . e'~ . \" G :::: 8.300 n ::::: .0130 \ .~ .. NORMAL DEPTH ::: ~.01040 -----De-p IDiam .;; . 50520 HE::= 1.43~82 j ... ---. _ ._ . __ . _ FN ._~ ___ . ~: 03025 '. • I (~:, CRITICAL DEPTH:::: 1. O::.;!638 . . , (,~. , .;,j 1 1'----" (. " Cr-{ tDeiP/Dia:m---;;' -'--. 51319 HEC::;:: 1.43233 ._ _ .. ____ .... _ FJ~~ ___ == ____ .. .9 9983 {Ham::;; 24.000 K' ::= A == P - 1-,\ 'C . :::: AC :::: PC; ::: Be ::: .23565 1. 59160 3. 16239 1.46725 '1.62356 3. 19437 .00493 v ::: R ::= VC RC ---:-:-'._.~'--'-----'-----' --." --. ::.:: ::: 8 :::;; .00520 5.21489 .50329 5. 11~123 .50826 V2/2G K :::: VC~.2/2G KC . 422'42---'--"-' 1.45573 o ~ __ ~_. ___ _M __ ••• ' ..... :::: ~ 40595 ::= 1.:4·3345 .. ------~- CIRCULAR PIPE HYDRAULIC DATA e ]J t!-I' , • CRITICAL DEPTH = .96648 'III I',·:· (iI, ::,.: I :r I .----. " fI,. ( , : --- ,." ir . I. (" -I" ~ i I :~. r .:: '-: i'·' j, ~.---~ i L' , ( ... ::. ~I ••. _ .. _ .•. OJ II ::!' ~ "-'" !)~ , ..... :.1 1-··.· "J c CritDep/Diam:::: .48324 HEC:::: 1.34262 --------~----Ff\fC .. ~-~ ~---: -99992 ,(/C :::;. AC -- PC :::: SC':: 1. 30815 1. 50377 3.074:34 .00481 V ::::: R ::: VC ::: RC =: 5.06618 . 4818:3 4. 92098 .48910 V2/2G == l\ - . ~~tt867 1.. 551..70 VC2/2G ::.: .. 37614 ~\C:::::. 1. 51922