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6017 PASEO ACAMPO | 6021 PASEO ACAMPO | 6029 PASEO ACAMPO | 6033 PASEO ACAMPO | 6037 PASEO ACAMPO | 6053 PASEO ACAMPO; ; AS990008; Permit
4/13/26, 9:45 AM AS990008 Permit Data City of Carlsbad Sprinkler Permit Job Address: 6017 PASEO ACAMPO Permit Type: SPRINK Parcel No: Lot#: 0 Permit No: AS990008 Status: ISSUED Applied 5/6/1999 Approved: Reference No.: Issued: PC #: Inspector: Project Title: CARRILLO RANCH APTS Additional addresses, 6021 Paseo Acampo, 6029, 6033,6037,6053 Applicant: Owner: about blank Fees($) 440 Add'I Fees ($) 0 Total($) 440 Balance($) 0 1/1 City of Carlsbad 98350 Fire Department • Bureau of Prevention Plan Review: Requirements Category: Automatic Sprinkler II} Date of Report: Tuesday, June 22, 1999 Contact Name Action Fire Systems Address City, State 9185 Harness St Spring Valley CA Bldg. Dept. No. ______ _ Job Name Carrillo Ranch Apts Job Address Melrose/Poinsettia Planning No. bor7 Pc...seo ftcompo Reviewed by:, __ .... 1//"""'""f='IJ-~/,:::__ Ste. or Bldg. No. ____ _ igi Approved -The item you have submitted for review has been approved. The approval is based on plans; information and/or specifications provided in your submittal; therefore any changes to these items after this date, including field modifica- tions, must be reviewed by this office to insure continued conformance with applicable codes. Please review carefully all comments attached, as failure to comply with instructions in this report can result in suspension of permit to construct or install improvements. D Disapproved -Please see the attached report of deficiencies. Please make corrections to plans or specifications necessary to indicate compliance with applicable codes and standards. Submit corrected plans and/or specifications to this office for review. For Fire Department Use Only Review 1st. __ _ 2nd. __ _ 3rd. __ _ CFD Job#_-=-9=83~5~0 __ File#, ___ _ Other Agency ID 2560 Orion Way • Carlsbad, California 92008 • (619) 931-2121 ACTION FIRE SYSTEMS 91 fltj l .. lflRNEl',i,l ST. SPRING-VALLEY, CA. 91977-3948 HYDICAULlL LALLULATIUNb FiJR RANCHO CARRILLiJ APTS. PALOMAR AIRPORT ROAD FILE NUMBER: 829-3 DATE: '.3·-0'• -'·'l'l BUILDING III PLAl'•l Al ····DEUIGl-.1 Dnrn-- NUMBER OF UPRlNKLERS CALCULnTED: IUTAL SPRINKLER WATER FLOW REQUIRED: 9pm/sq. ft. r □TAL WATER REQUIRED (including hose): 141.0 gpm NAME OF CONTRACTOR: ROEL CONSTRUCTION DESIGN/LAYOUT BY: ELLIOT GATES 141.0 gpm@ 90.0 psi i nc·h ,l,IJTI IOI<! TY H{W I NG Jl.JfH :::,o ! CT [ Dr·l: crrn1. .. ::_,[1/ClD F ! HE DU"T • CALCULATIONS DY HASS C □MPL.JlER PRUGHAN (LICENSE U 802GJ521 HHS S'lb l [J,'iS, J.NL. (lTL/1NliL1 e,n SPRil~~<l-ER SYSTEM HYDf~ALJLlC AN~)L.YSIS Page 1 1J;-.:..te ~ l 1/tZll/91 -C: \Bi::::9---:3 JOB TITLE: RANCHO CARRILLO APARTMENTS BLDG. III PLAN Al PROOF CAL WATER SUPPLY DATA E)OLJF~CE: i'JDDE Tnc bt~CE SHHIC RES ID. FLm~ AVAIL.. PRt~SS. PRESS. (~ PHEGS. (PSI ) (PSI) <GPM) (PSI) 17B. 2 172 .. ti 14~;:_;3. ic\ 17El. 1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STRErlM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ncTIVL SPRINKLERS NODE ANALYSIS DATA i,IUDE TAG J~llh 10~~(., 11Z1i:.~ llZ13 1 1/1A'. • .-~j 11/; ~-3 j_ 1/1(1 1(1/ l UI< BOf< Ubi UGi:~H Ub2(.:l UG~::'. Uh::, t.11..1 1-'► I.Jti'.:\ bHl..,L ELEVATION (FT) 19. 3 19. 3 i:::0. 3 ~!.0 .. 3 .! '). 3 'L 7 9.7 0 .. 5 -3. ,z, -:~. 121 -3. QI ·--3. 0 L~. !ZI 4,. !/I --;::;_;. IL) · <~. t~I NODE TYPE .{;.:;: 2·. 80 h:;;;; 2. 812• HOSE STF<EJ=lM PHEf3SUf-~E o:•~J I ) .-, ,:~ .:~-1::. ,.J. ,.J i::'.1.t. 7 ~:'.t'.:1 .. H t)i.::: .. 6 11.a '/Cj .. 5 'he\. ic\ 93. Qi 1:lli). 3 l 1.3. El 133. ~5 .I. 3121. ~::; 1 ~+c:. ~s Ji~::: ... ~ii i l1.:.:, ~ / l~ TOTAL RED' I) Df~MAND PF~1-=::;s. 1GPM) (Pbl 141. 121 i .(~ ~::i. l'tl. 1,i GPM '.50. 1Z1 GPM 51L"'l. It) G1:::•j·,1 ,, 1. QI GF'M DISCHARGE ,GPM) 13.9 ) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB flTLE: RANCHO CARRILLO APARTMENTS BLDG. Ill PLAN Al PROOF CAL Pl.PE DATA PIPE ·rAG QCGPMl DlAIINl LENGTH PRESS .. END ELEV. NOZ. _PT DISC. VELCFPSl HWICI CFTl SUM. (PSI) NqDLS (FT) • (Kl <PSI) (GPM) F.L./f'.T i~'ll-)E·: 1 Jl/1.lf·I 1..:J.,::; l!b1:::'. 2~~. ::~ Pipe: 2 1 li);':~i="l 1 (.). 3 11Z13 20. 3 Pipe:: 3 11/1.'.tn 19 .. 3 1 tlt5 2Q\. 3 11;~2 102: Pip~?: 5 11z13 20. 3 11z1~-~ i:::'.0. 3 r•ipE•: (::, 11/1::_-:., • ~~IL.l. ~3 .I. i,:1i:.1 2~) .. 3 PipE·: 7 J 1/1~~: f:Q1. 3 i 1/1{:, i::'.Q1. 3 Pipe,: B ~~0. :.3 9.7 r:.i1)e: 9 t1h7 9.7 ·1 u1·j 9. 7 Pipe: 10 0.0 2.8 0.0 2.8 121.0 0. 121 o. 0 ,:, . ~:, ~,. e, 0.0 •ZI. 0 1Z1 .. e1 12,. QI 0. \21 0. IZI TOH DDf< '). 7 0. 121 0. 5 H. S. 1-"ip,:,: 11 our~ 0.5 t·t.s. U(il ·--3.0 0.0 i::, i ~· t.:.' ~ 1 i::: l.JLi.l ···,\. ~~I UU,::'.D --:;;. ,Z1 Pipe: 13 23.2 .-,.:;.~ r:;-.::. ,.J. ..... 2 1 •• 7 26.8 25.fa .-,r::-r~· C . .J. ,.J i::::6. 8 62 .. 6 62.b 62. i::> Tl. a Tl. 8 1'3. 1;;.-.. , 79 .. 5 91<). 0 Lll~}~~:B --3. II..~ U62f~ ~-3.0 0.121 11(:).:3 ~,. ~\ 113. L\ --1::::;.c e1~a11t.) Pl .... t:,.1;)1Zt r:ii: 13.b LJ.~ 1~0 FlG ET PE 0.0 0. 148 TL 16.58 ~•V 13.5 0.810 PL 3.00 PF 13.5 8.4 1~0 F""fG 2T PE 0. 0 0. 1'>7 TL Hl. 11 PV --13. ') 0. 810 PL (-.. Q11Z1 pp· 1 -, .,, . 9 [;. 7 1 ~)121 r:·TG ET PE 0. 0 (i). 15~;) TL 16. ::,j3 PV -•. w• l 0. B1QI PL 10. 00 PF 0. 121 ·::, ~-3 1 ~:50 FTG Pl, 0. 0 Ii). !£'ti 3 TL :l0. 00 PV -9.B 0.810 PL 13.50 PF 0.0 b. 1 150 FTG F PE 0.0 0.001 TL lG.52 PV • ·, c:~ 1 .. : .• , .. / ~J • Lt Ii)• ~-J C'. .. 7 11.L Ji. QI .. .l~ Ii~ .. ~;:.j 0. 1 It..~~ 1L) It). Qi 1 .. ,.-:; Ii). 0 1/.L ;:~ ···23.? 0 .. 810 i)L_ 75.50 P~ 35 .. 6 0.0 14.8 150 f~·rG ET PE 0.0 0.0 0.41G -r·L 86.08 PV 1.5 ·-17.3 0.810 PL 146.00 PF 3·7.0 ~:i"1.?1 ilt).b l~;Qi t"·"J"b 2ET Pt~. li.) .. ~~1 0 .. 0 0.2;32 ·r·L 15~.G0 PV 0.8 ····Lt 1,. f/1 1.033 PL 19.67 PF 0 .. 1Z1 lt:i. "/ 150 FTG ET PE 0.0 0.350 1·L 30.25 PV -41.0 1.0~3 PL 2.00 PF 0.0 15.7 150 FTG E PE 0.0 0.350 ·rL 5.02 PV --Lt 1. 0 1. 02;3 PL '.l. ..!,,.!, PF 121. Ii) 15. . .., ' 1 ~512' FTG CG PE :=,;0. Ii) 121. ;35iz1 TL. 18. i.J.Qj PV ·-·01.0 2.04~ J')l_ 5.00 PF 50.0 8.9 1~0 f:1·0 3E PE IZt. Ii) 1Zt. IL/~_)i.1 Tl. 27. 6 7 pt.J 1121~ 6 i.~. C, :l./ 1. 13 iL1. 0 1.7 t~ • .l~ i~ • Q1 1. 7 1 . ~::i 1. ::::; !LI. ~.:j -·11.0 2 .. 041:j G•L. 280.00 PF 17~3 0.0 B.~~ 1~0 l-1·1; 5L P£ 0.w 0.0 0 .. 054 ·rt_ ~17.78 r·v 0.5 ··01.0 2.040 PL 65.00 PF 0 .. 0 8.9 1~0 FTG PE 0.0 0.0~4 ·r·L 65.00 PV 121. Q) 1;~) -~-~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS .JOl3 r I Tl_l::: l<rJNCHO CARH I u_o i'lPAWfMENTS BLDG. I I I PLAN f'l 1 PFWOF CAL. (cont 1 d) PH-•E THG a-m NDL>ES ELEV. <FT> l~OZ. ( K > PT DISC. (PSI) <GPMi QIGPM) DIA(INJ LENGTH VELIFPSl HWCCi CFT) F.L./FT PF<EbS. '.3Ui'I. <PSI) Ul:k:/:i UG~~ Pipe,: 14 -3.QI ···-3. 1Z1 Pipe: 15 UG2 ···3. 0 LIG3 ,,_ 0 Pipe,: 16 LJE,lt Lt. 0 UU .. ·~ ' A. 121 l.J(.;.l.1- Ub:5 1 "/ L~ • Q1 -·-3. ~'I Pip": 18 0. 0. 0. 0. Qi. 1Z1. 121 .. (Ji. 0 1 13. 8 0 133. 5 0 133. 5 0 130. 5 0 i Lt2. r.· .J 1(1_ 130. i:;: ,.J 0 1 i,1-i::'.. ,:::· .. , 0 1.1.t~j. tJ Ub~.:i FlnCE -3.0 0 .. 0 145.5 -3.0 SRCE 145.7 hlUTEb: ··-91. ,o -~ •-· 0Lt\) PL 315. 00 PF Qi. ,zi 8. ~~ 15121 F"fG 4ET PE 0. 0 0. 121~5.lt-TL 36121. 33 PV --91. 0 .lt. 2c:121 PL 8. (%Ii PF 0. 0 ·::, ~-1 1 'tii'I FTG L PE 0. 121 0. QlQl2 TL. 15. 9B Pl) FIXED PHESSURE LOSS DEVICE 0.0 12.0 psi, 91.0 gpm 0.0 --91. 0 Q).Qi ~~-1 Li-.. i::;\:;'.lj) PL 1.:,.11) FTC:, B. e,e, L 15.Slb PF Pl:: Qi. ~-:1 ei. e, ( N/t4) 0. 0(~2 TL PU --½1.0 4.23G PL. 60.00 PF 2. 1 150 FTG TG PE 0.002 ·rL 93.24 PV l '). 6 0.0 IL\. 5 QI. Qi 3. ltl 0.0 !{I • .l ''.J ~ (:) IL) .. I,'.) 111 Calculations were performed by the HASS 5.5.0 computer program und&r license no. 8926J521 granted by Hf<B Systems, Inc. 2193 Ranchwood Dr., N.C. Atlanta, GA 30345 (2) the system has been balanced to provide an average imbalance at each node of 0.006 gpm and a maxin1um imbalance at any node of 0.098 gpm. Vc•locity nut ui;,1~d i,.\j'j '/ p j_ PE' pressures· are printed for in balanci11g tl·1e system. is 1~5. 7 ft/sr,c. infof'mc:1t ion only, c:-1nd are IYl<::1)<irnum v,,::1tc~·1-· velocity in SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB IITLE: RANCHO CARRILLO APARTMENTS BLDG. III PLAN Al PROOF CAL (41 PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP l•(lbL: (1 Di r.:1m et er ( in) MATERIAL: 840 HWC: 120 Equivalent Fitti119 T L. C: l.(ennths B E Ell Tee LngEll Ch~<Vlv BfyVlv in Feet G ri C"JE1tVlv Al1flL:hk D DP'i .I. v SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLC, RANCHO CARRILLO APARTMENfS BLDG. 111 PLAN Al PROOF CAL WAfLR SUPPLY CURVE 1600\\\\\\\\\\\\\\\\\ I \\\\\\\\\\\\\\\\\\ 16'.5+ .l':::il/1+ >: I pl ~~!Zl I- f'{ [" '..~; 11/J'j I u I< L I' L EGEl•,m Reql1irod Water Supply 11►5.bB psi@ 141.0 gpm 0 ~= Availat)le Water Supply 17fL, 13 psi ([:1 li~l .. 121 gpm " " " " l'.•·l••i l·· ····i ........ ····I·,,._ ..• M••---·-+· .. - 4L10 b00 800 1000 12Ql/i,) 141l.ll/,) * <-172.8 psi@ 1453 gpm Flo~..,, Test Point 1:0 LOW ( GPM) ACIIDN Fli,E SYSlENS 91 a,; 11nrn,1c::<; :,r. SPRING_VALLEY, CA. <)1<)77-3<)48 HYDRAUL. l C C~1u:uun 1 ONS FOR RANCHO CARRILLO APTS. PAL.OMAR AIRPORT ROnD FILE NUMBER: 829-2 D/ClTC, '5 0t, -')') BUIL..DlHG I I PI..S:1•1 C uccur,nl~CY CLFlSS IF I Cia TI Ol'·l: HF<lcil UF nPPLJ.CATI(.Jl,J: m,rn/sq. ft. NUMBER OF SPRINKLERS CALCULATED: 11nnL f3PRIM,L.ER WfffER FL.ml REUUIRED: 4 sprinklers LLDW AND PRESSURE (@ B□Rl 1 15~.5 QfJm@ 93.6 pisi 11UIIIUHlTY f-1(.WJ.1~13 JLJRib!Jl.CTION: C1'.-lf{l._,jflfll.1 FIHf": uu::,r. uJ1,1T1,ncTIJH CEl-:TIFICfffIOI~ l'•llJMBEI~: C·-16 381'lbl1t CALCULATIONS BY HASS COMPUTER PROGRAM !LICENSE# 8<)26JS21 HRS BY:JTEMS, IMC. rc1TLnr-.rrn, c;;n SPRINKLER SYSTEM HYDRAULIC ANALYSIS D,=tt •~ ~ 11 /1,:11 /91 -L.: \Hi:~<:>· JOB TI TU:.: RANCHO CAfrn I u_o t'IP,rnTMENTS BLDG. I I PLAN C PfWUF I.A\LC WATER SUPPLY DATA uuur,cE NODE ! 1:•·ll:i STATIC F<ESID. FLOW PF<ESS. PHESD" (~ <PSI ) <P1il ) <GPM) 1 }13. -:::, ~-l '/i::~u a 1 L1-~_)::~ .. 1;'.) AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE nvnIL. TOTnL PflE:3S. 1.,, DEl'IAI\ID \PblJ <GPM) flEI::.>' D PF~E:::3Su <PSI) l □lAL HOSE STREnM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES 1 ~)'.5 .. ~S GPl'1I 5Q:1. Q1 GPM ~}0. tll DPN ~55. ~5 GP1·1j lOTAL DISCHARGE FROM ncTIVE SPRINKLERS NODE ANALYSIS DATA r,1unE rr.m l •ZI lH 1 l/.)~~ :l 1/13/:.) l 1t)'-t J 1;:,)~·:_; l 1,)1'.:,(:i j_ 1/1 c., J Ii.I/ i 1liu 11z1•::;1r1 TUH HUH UbJ. UCii?E Lib,:: n Ul:Ji:::: ULi:..S UCJ 1i lJL;~·.=.i ui::t.::L ELEVrn ION (FT} 1 '). 3 .t '). 3 i.~0-;3 l '0 .. ;:3 ~?l'). J, i:::'. 1/1 . ~~ 'L ·; 19. :~ '). 7 1/). t) ·-3. 0 -··J .. tZI -3 .. 0 <L0 Lt. Jl.t ,,. 0 --·3 .. i?:i :.; • Q.\ NODE TYPE f{=-2. 80 !30Ul1CE PRESSURE <PSI) i.~6. ·1 C~1+. 7 i:?.7. Ii.) -::, ; . '•-• I • , • .J Bit. B i::~::s. 1 ') 7. j ]0~~-~\ J.lt)L~~ 6 1 :~~J. Lt 127 MA- DlbCHAf<GE WPM> 13. ') SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RANCHO CARRILLO APARTMENTS BLDG. II PLAN C PROOF CALL P H·'E D,:nn Q(GPM) Dlt-l!IN) LENGTH PHES'.:;;i. 1:•IPE Tf.iG END l',JCi D le S ELE\J. <FT) NOZ. (f() PT DISC. <PSI) (GPM) \JEL(FPS) HW(C) IFT) F.L./FT SUM. <PSI) lilll(-) 1,212 Pip,e: 1 19.3 ~:'.0. 3 i:;:, i pt~·: C: 103A 19. 3 1 Qt.I+ 20. 3 l•)ip~?: 3 ll/tt';,f;\ 19. ;:; l llt'.S i:~ti.). 3 ~)ip<::•!: L~ 11[)9(! 19. :; .l 1/t"/ i.:::1£1. 3 Pipe: ~5 Jilli::: ~:~0 .. :-5 U~1li 20~ 3 Pip£-!: t, l 1/il~ i:::'.0. 3 11/1~::; i.:~ll.l. 3 Pip(.-': '/ 1111~:j i.:'.0. 3 11z1t;;\ 20. 3 j,)i pE:: El 11212 2,21 .. 3 .l IL~ 7 i:~ILL 3 r·t pt,• 1 ') 11;)'/ ~:::It~. 3 .1 iZ11~, ~~iz;. 3 l 1L1(:., .l 1L1b 9.7 Pip,.,: .ll 11l.1l.J 9. 7 TOil 9.7 Pi pt~ : .t 2 2 .. 8 • 23. 2 0. IZI ;;':6. 9 2.8 0.0 0.0 0.0 0.0 121.0 0. 121 0.0 ~). e, Ii). th IZl. 1i1 Qi. ei ll1. 0 ,z,. 0 24.7 27.0 26.9 i~'.7 .. e1 ,~7. 0 29. i.=-:'. 29.2 7 3. 9 26.9 -:,-1 ~., ' ~~-I • ._, I 3. '·J B-'~. 8 EV,. H 86. 2 ··1 CJ P 9,. 7 e,. QI . BL' . 2 LIUF! ll1. ~) H. !:). 93. 6 BUH UG1 Pipe: 13 0. ~:i --:3. 0 H. S. 0. ,z, 93.6 ')7. 1 -13. 5 0. 810 PL 17. ~50 pre 13. 5 8. ,, 150 FTG ET PE 1Z1 .. 0 121. 1'+7 TL 2B. li.\8 PIJ 13.9 0.810 r)L. 7.50 PF 13.9 8.7 150 FTG ET PE 0.0 0. 155 TL 18.08 PV --13.S 0.810 PL 14.00 ~F 13.9 8.7 150 F"T'G E2T PE 0~0 0.155 TL 32. 13 PV --14.2 0.i~l0 ~~L 2.00 PF 14.2 8.8 150 FTG ET PE Ii.\. 0 0. 161 TL. .12. 5B >-'~' 4. 1?11Z1 PF 0.0 3.5 1~0 f.:·1·G PE 0.IZi 0.028 TL 4. ,;,,Zt PV --19. '.:, ('I. 81121 PL. 7. ~)QI Pf~ 0.1Z1 12.1 l'.',0 l"TG PE 0.0 0.2B9 TL 7. 50 PV ···--:,,-:., ~~-'-I· 0. 81,ZI PL 43. 50 PF 0. 0 20. fl 1 ~_:;ei FTG 2ET PE: I~. 0 0. 7t~3 TL. t:i1. 11,) Pl) -7.9 0.810 PL 6.00 PF 0.0 4.9 150 t·Tb ~1E 0.0 0.055 "fl 6.00 PV 1:t u J Ill. .i:,. ILL '.'::i 1Zt. ft 0~ 5 2. e, 1Z1 • .t.1- C1 ~ :,:, 0 . .l. it:I., tZI Q1 •. l IZI. 1/.) 1. 0 i.1-,'.1-~ 7 (). (1 2. () Q1. 2. 0. (ll 0. i::'. ·-22.1 0.810 PL 114.00 Pi= qG.G 0.0 13.8 150 ~TG 2ET PE 0.0 0M0 0.3G~ ~L 12·7.60 PV 1.~ · ~)5. 'j J.. :.~:.(,-1:1-r::,1.__ ;:.:b. l 7 PF. ,'.~ .. v1 .1.i:::: .. ~:~ 1i.i1,:.i 1-TLl c:·r 1:,1::: 0.0 0. 158 ·rL_ 39.77 PV --55.5 1.364 r•L 4.50 Pl~ 0.0 12 .. 2 150 ~TG E PE 0.0 0. 158 TL 9.03 PV -·55.5 1.364 PL 9.33 PF 0.0 12.2 15Q1 Fl"G CG PE 50.0 0 .. iS6 1·L 21n42 PV ·"-10~5. ::i ~,0. 0 1121. 3 ,z,. 0 2.04~ PL 5.00 ~•1~ 150 FTG 3E PE 0.072 TL 27.67 PV .l ., .<+ QI• 1/j l u Iii 3.4 ('.~., If.I 1. 5 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RANCHO CARRILLO APARTMENTS BLDG, II PLAN C PROOF CALC PIPE Di=1Tn (cont' ell PIPE TAG END EUcV. 1•,JUl.JU, <FT> i.::, i pe?: 11.~ LJUJ .... 3. e1 l..Jb.:".::B --3. tZI Ubi:"::'.i=l UGc~ UG2 Ui,2' L.Jt;;.1.,. Ub3 Ut:iL.t Ul.::i~:_:j Pipia: 16 -·<3. 0 --3. ~) Pipe: 17 l''i pe: 18 4, QI 4. IZ, 4. 1Z1 NDZ. OZ> 0. 121 0. 1Z, IZI. 121 0. 0 0. ,ZI 0. 121 0. 0 0. 0 0. e1 0. 121 ~). tZt IL). IZI PT DISC. (PSI ) iGPMl 'cl 7. 1 Ii). IL) 1,~11Zl. 121 0. lb 11,)0. 0 0. IZI 101;. t,\ 0. IZI U,)4. 6 0. e1 130. 4 0. 0 1:30. 4 0. ,;;; 127. ,, 0. 0 139. 1.,. ~). 121 1 ;,'7. 4 0. 0 LY). ,, 0. ti..) 11.•2~ i:;;· __ , 0. 0 G!(GPM) DI/Cl( IN) LENGTH i:.:•RESfj. VEL. ( Fl'.)8) H\..H C) <FTl SUM. F. L. /FT \PSI ) · ·· 1 ti!~.~. 1:..-.-. ()L1') PL. 25. 1/)121 PF , .. _. ,J i:::.. 1 ll1. 2_; 1 :itLI FTG T PE ,ZI. 0. Qi}i:~: TL it II.). 1 1 P\I 1/..\., ---1il'i5. ~'.:i :·, ~--1;:)J'.~ 9 PL 6~:.i. 1210 f:<F .'.~ . 10. .. , 1 t)IZ1 F'TG PE Ii). 0. 072 TL ,-... I:.'\ ,:j, • !lll/.l pl.) 1;,,_1 ~ ..... 10~5 .. 5 ~:, 04() PL 315. ~),Z1 pp: --, '~--~-i:;~,..J. 10. 3 15Q) FTG '•ET PE 0. 0. 072 TL 360 .. .::. ,:, pt) ('i. --1~l5. ~5 '•. 22e1 PL. 8. 00 PF e,. -:-... ~-4 1';0 FTG L PE ··;;• ,J. 0. 00;:: TL 15. 98 P\,' It). FIXED Pf<Et,:3Ul:<E LOBB DEt/ I CE 12. () pt:. l, 1 Q1~:,i. ~~-_, gpm --J. 0~j. :s 4. i.:::20 PL 8. Q11Z, PF 0. -:::., 1+ 14121 !0 TG L PE ..• , ~-_,. (.i.. 1210;::: TL 15. 98 PV e1. ':) tZI I 7 ~~I 7 l.l "i 7 () 1/1 0 () QI 0 !-=•.i~:itc:: 2121 u1;s --3.0 Q1.0 Sli(~~ -3.0 SF~CE It). 0 C::. (1. (N/fl) Li-. i?36 1-:.1__ t.'\li.). Q)IZI :l :.',('1 FTh TG 1L1~ ~%:t,.:~ rL (JJ. t~1.• PF 1-•E PV IL). i::~ 0. 1:!:1 IL) .. 1/1 l\!U 1·L.::i: (1) c:alculations were performed by the HASS 5.5.0 computer program under license no. 8920J521 g1~anted by HRS Bystems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 3034~ (2) Tt1e system t1as been bala11ced to provide an average imb~lance at eact1 node of 0.006 gpm and a maximum imbalance at any node of 0. 111 ~Jpm. (3) Velocity pressures are printed for infc,·,·m.stion only, and are not used 111 balancing tt1e syst8m. l~aximum wate1~ velocity iri a11y pipe is 20.8 ft/sec. SPRINKLER SYSTEM ~IYDRAULIC ANALYSIS PE1BE' 4 JOB TITLE: RANCHO CARRILLO APARTMENTS BLDG. II PLAN C PROOF CALC 14) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP Pi:il3E: n DiaweteY' ( in) M1-HERIAL: s,,ei HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmCl,k DPV!v SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RANCHO CARRILLO APARTMENTS BLDG. II PLAN C PROOF CALC WATER SUPPLY CURVE 180•\\\\\\\\\\\\\\\\\ 10 \\\\\\\\\\\\\\\\\\ I I l t· .. '._·::.,•1 IX r-• 1 ~~1Lt··1 H I''. ::) :.:) l li'.1 ~-~i + LI H (..1/1-1 I LEGEND X --Required Water Supply 0 = {)v~ilat)le Watet~ Suµ~)ly l 7 I.:~ ~ .I. l p :,__ 1 .:;? 1 '.'.:~ ~-:~ . '.'::, q r::. m ···---.. I···· :l i.'.::t2112t " " " " " ··········I. .l i1-1i:11/t -l(. <--l"/i::::M 13 psi (~ 1L►'.:i3 qpm Flo1,,•J Te!::-t Point: .............. , J t'.,!jl/t .1 t':"\ 12ut:1 ACTTON FIRE SYSTEMS COMPANY INC. 9185 HARNESS STREET SPRING VAT,LEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR RANCHO CARRILLO APTS. BUILDING #1 RANCHO CARRILLO VILLAGE "B" LOT 207 FILE NUMBER: C:\830A DATE: 5-4-99 -DESIGN DATA- OCCUPANCY CLASSIFICATION: RESIDENTIAL DENSITY: N/A gpm/sq. AREA OF APPT,TCATION: N/A sq. ft. COVERAGE PER SPRTNKLER: 200 sq. ft. ft. NlJMRER OF SPRINKLERS CALCULATED: 3 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose): F'T,OW AND PRESSURE (@ SRCE: SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: ROEL CONSTRUCTION DESIGN/LAYOUT~¥: JOHNS. MUNA 41.6 141. 6 141.6 3\8 gpm gpm gpm @ inch AUTHORI"l'Y HAVING JURISDICTION: CARLSBAD FIRE DEPT. CONTRACTOR CERTIFICATION NUMBER: C-16 #388160 119.9 Pl3 i CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 8926J52l HRS SYSTEMS, INC. CONTRACTOR CERTIFICATION NUMBER: C-16 #388160 CALCUI,ATIONS BY HASS COMPUTER PROGRAM (LICENSE # 8926J.521 HRS SYSTEMS, INC. ATLANTA, GA SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 830B Date: 11/01/91 ,JOB TITLE: RANCHO CARR TLLO APTS. "BUILDING #1 WATER SUPPLY DATA SOURCE NODE TAG SRCE ST/\TTC RESID. FLOW /\VI\ TT,. PRESS. PRESS. @ PRESS. (PSI) (PST) (GPM) (PSI) 178.2 172.8 1453.0 178. 1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM AT.T,OWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSTS DATA 101A EI.EVATT ON (FT) 19.3 NODE TYPE PRESSURE (PSI) 23.2 @ TOT/\T. REQ'D DEMAND PRESS. (GPM) (PSI) 141.6 119.9 141.6 GPM 100.0 GPM 0.0 GPM 41. 6 GPM DISCHARGE (GPM) 13.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 ,JOB 'T'T'T'LE : RANCHO CARRILLO APTS. "BUT I.DING #1 NODE '!'AG ELEVA'T'TON NODE TYPE PRESSURE DTSCHARGE (FT) (PSI) (GPM) 1 02 20.3 ----24. J --- 1 03 20.3 ----25.8 --- 104A 19.3 K= 2.80 24.7 13.9 105 20.3 ----25.6 --- 106A 19.3 K= 2.80 25.8 14.2 107 20.3 ---. -26.7 --- 108 20.3 47.5 --- 109 9.7 69.2 --- TOR 9.7 ----74.6 --- BOR 0.5 100.2 --- UGI -3.0 ----102.0 --- UG2A -3.0 ----103.2 --- UG2 -3.0 ----107.8 --- UG3 4.0 ----104.8 --- UG4 4.0 116.8 --- UG5 -3.0 ----119.8 --- SRCE -3.0 SOURCE 119.9 41.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 ,JOB TITLE: RANCHO CARRILLO APTS. "BUI I.DING #1 PTPE Dl\Tl\ PIPE TAG Q(CPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PST) (GPM) F.I../FT (PSI) Pipe: 1 -13.5 0.810 PL 1.00 PF 1.3 l 011\ 19.3 2.8 23.2 13.5 8.4 150 FTC T PE 0.4 1 07 20.3 0.0 24.l 0.0 0.147 TT. 8.56 PV 0.5 Pipe: 2 -13.5 0.810 PL 4.00 PF 1.7 102 20.3 0.0 24.1 0.0 8.4 150 FTG T PE 0.0 103 20.3 0.0 25.8 0.0 0.147 TL 11. 56 PV 0.5 pjpe: 3 4 . ] 0.810 PL 8.50 PF 0.1 103 20.3 0.0 25.8 0.0 2.5 150 FTG PE 0.0 105 20.3 0.0 25.6 0.0 0.016 TL 8.50 PV 0.0 Pipe: 4 -13.9 0.810 PL 1.00 PF 1.3 104A 19.3 2.8 24.7 13.9 8.7 150 FTC T PE 0.4 105 20.3 0.0 25.6 0.0 0.155 TL 8.56 PV 0.5 Pipe: 5 -9.9 0.810 PL 10.50 PF 1 . J 105 20.3 0.0 25.6 0.0 6 .1 150 FTC E PE 0.0 107 20.3 0.0 26.7 0.0 0.082 TL 13.52 PV 0.3 Pipe: 6 -14.2 0.810 PL 1.00 PF 1.4 106A 19.3 2.8 25.8 14.2 8.9 150 FTC T PE 0.4 107 20.3 0.0 26.7 0.0 0. 161 TL 8.56 PV 0.5 Pipe: 7 -24 . 1 0.810 PL 45.50 PF 20.7 1 07 20.3 0.0 26.7 0.0 15.0 150 FTG E PE 0.0 108 20.3 0.0 47.5 0.0 0.428 TL 48.52 PV 1.5 Pipe: 8 -17.6 0.810 PI, 85.00 PF 21.7 103 20.3 0.0 25.8 0.0 1 0. 9 1 .50 FTC 2E PE 0.0 108 20.3 0.0 47.5 0.0 0.239 TL 91.04 PV 0.8 Pipe: 9 -41 . 6 0.810 PI, 4.00 PF 17.2 108 20.3 0.0 47.5 0.0 25.9 150 FTG ET PE 4.6 109 9.7 0.0 69.2 0.0 1.178 TL 14.58 PV 4.5 Pipe: 10 -41.6 0.810 PL 1. 50 PF 5.3 109 9.7 0.0 69.2 0.0 25.9 150 FTC E PE 0.0 TOR 9.7 0.0 74.6 0.0 1.178 TL 4.52 PV 4.5 Pipe: 11 -41.6 0.810 PL 9.33 PF 21. 7 TOR 9.7 0.0 74.6 0.0 25.9 150 FTG CG PE 4.0 ROR 0.5 0.0 100.2 0.0 1.178 TL 18. 40 PV 4.5 Pipe: 12 -41. 6 2.049 PL 5.00 PF 0.3 BOR 0.5 0.0 100.2 0.0 4.1 150 FTG 2E PE 1.5 UGl -3.0 0.0 1 02. 0 0.0 0.013 TL 20 .11 PV 0.1 Pipe: 1 3 -41. 6 2.049 PI, 70.00 PF 1. 2 UGl -3.0 0.0 102.0 0.0 4 . 1 150 FTG ET PE 0.0 UG2A -3.0 0.0 103.2 0.0 0.013 TT. 97..67 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSTS Page 4 ,JOB TITLE: RANCHO CARRILLO APTS. "BUTT,DJNG #1 PTPF: DATA (cont'd) PIPF: TAG Q(GPM) DIA(TN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODF:S (FT) ( K) (PST) (GPM} F.T,./FT (PST) Pipe: 14 -41.6 2.049 PL 315.00 PF 4.6 UG2A -3.0 0.0 103.2 0.0 4.1 150 FTG 4ET PE 0.0 UG2 -3.0 0.0 107.8 0.0 0.013 TL 360.33 PV 0.1 Pipe: 15 -41.6 4.026 PL 8.00 PF 0.0 UG2 -3.0 0.0 107.8 0.0 1.0 140 FTG L PE 3.0 UG3 4.0 0.0 104.8 0.0 0.001 TL 15.98 PV 0.0 Pipe: 16 FIXED PRESSURE LOSS DEVICE UG4 4.0 0.0 116.8 0.0 12.0 psi, 41. 6 gpm UG3 4.0 0.0 104.8 0.0 Pipe: 17 -41.6 4.026 PL 8.00 PF 0.0 UG4 4.0 0.0 116.8 0.0 1. 0 140 FTG L PE 3.0 UG5 -3.0 0.0 119.8 0.0 0.001 TL 15.98 PV 0.0 Pipe: 18 -41.6 4.026 PL 60.00 PF 0.0 UG5 -3.0 0.0 119.8 0.0 1.0 150 FTG TG PE 0.0 SRCE -3.0 SRCE 119.9 (N/A) 0.000 TL 93.24 PV 0.0 NOTES: ( 1 ) Calculations were performed by the HASS .5. 5. 0 computer program under license no. 8926J521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.009 gpm and a maximum imbalance at any node of 0.142 gpm. (3) Velocity pressures are printed for not used in balancing the system. any pipe is 25.9 ft/sec. information only, and are Maximum water velocity in SPRINKLER SYSTEM HYDRAULIC ANALYSIS ,JOB TITLE: RANCHO CARRILLO APTS. "BUILDING #l (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in ( in) E T L C B Feet. G Ell Tee T.ngEll ChkVlv BfyVlv GatVlv 4.026 10.00 20.00 6.00 22.00 12.00 2.00 Page 5 A D AlmChk DPVlv 20.00 10.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS ,JOB 'T'T'T'T.E: RANCHO CARRTT,I.O APTS. "BUTI.DTNG #1 WA'T'F.R SUPPT,Y CURVF. 1800\\\\\\\\\\\\\\\\\ \\\\\\\\\\\\\\\\\\ Page 6 * <-172.8 psi@ 1453 gpm Flow Test Point 165+ 1 5 0 ➔ 135+ P120X R E s 8]05+ u R E 901 ( p s T 75+ ) 60> 45+ 30+ 1 5+ LEGEND X = Required Water Supply 119.88 psi@ 141.6 gpm 0 = Available Water Supply 178.13 psi@ 141.6 gpm 011-1----1----1------t-------1----------t---------1---------i-------------1 400 600 800 1000 1200 1400 1600 1800 2000 FT.OW (GPM) ATT,ANTA, GA ACTION FIRE SYSTEMS COMPANY INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR RANCHO CARRILLO APTS. REC.BUILDING RANCHO CARRILLO VILLAGE "B" LOT 207 FILE NUMBER: C:\830A DATE: 5-4-99 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: RECREATION BUILDING .10 gpm/sq. ft. 1500 sq. ft. COVERAGE PER SPRINKLER: NUMBER OF SPRINKJ:,ERS CALCULATED: TOTAL SPRINKI,ER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (tncluding hose): FLOW AND PRESSURE (@ SRCE: SPRTNKT.RR ORTFTCR STZE: NAME OF CONTRACTOR: ROEL CONSTRUCTION DESTGN/LAYOUT BY: JOHNS. MUNA 78 18 182.2 282.2 282.2 1 \?. sq. ft. sprinklers gpm gpm gpm @ 93.9 inch AUTHORITY HAVING JURISDICTION: CART,SBAD FTRE DEPT. psi SPRTNKT.ER SYSTEM HYDRAULTC ANALYSTS Date: 11/01/91 JOB TITLE: RANCHO CARRILLO APTS. "REC. RUTT.DING" WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ PRESS. @ TAG (PSI) ( PSI) (GPM) (PSI) SRCE 178.2 172.8 1453.0 177.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG ET.EVATT ON NODE TYPE PRESSURE (FT) (PSI) 1 01 A 15.0 K= 5.60 1. 6 1 02 16.0 ----1. ] 1 03 ]6.0 ----1. 3 1 04A 15.0 K= 5.60 1.7 105 16. 0 ----1.2 J 06 16.0 ----1.4 1 07 A 15.0 K= 5.60 l.9 108 16.0 ----1. 5 109 16.0 ----1.6 110A 15.0 K= 5.60 2.0 111 16.0 ----1.6 112 16.0 ----1. 8 113 16.0 ----2.2 114 16.0 ----2.8 11 5A 15.0 K= 5.60 2.8 116 16.0 ----2.4 117 16.0 ----2.8 118A 15.0 K= 5.60 3.1 119 16.0 ----2.7 120 16.0 ----2.9 121A 15.0 K= 5.60 3.2 122 16.0 ----2.8 123 16.0 ----3.3 124 A 15.0 K= 5.60 3.6 17.5 16. 0 ----3.2 126 16.0 ----3.6 127A 15.0 K= 5.60 2.5 128 16.0 ----2.1 129A 15.0 K= 5.60 2.5 130 16.0 ----2.2 131 16.0 ----2.3 132 16.0 ----3.3 133A 15.0 K= 5.60 2.9 134 16.0 ----2.5 TOTAL DEMAND (GPM) 282.2 282.2 100.0 0.0 182.2 DTSCHARGE (GPM) 7.0 --- --- 7.2 --- --- 7.7 --- --- 7.9 ------ --- --- 9.4 --- --- 9.8 --- --- 10.0 ------ 10.7 --- --- 8.9 --- 8.9 --- --- --- 9.6 --- Page 1 830A REQ'D PRESS. (PSI) 93.9 GPM GPM GPM GPM I SPRINKLER SYSTEM HYDRAULIC ANALYSTS Page 2 ,JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" NODE TAG F.LEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 135 16.0 ----2.8 --- 1361\ 15.0 K= 5.60 2.6 9.1 137 ]6.0 ----2.3 --- 138 16.0 ----2.7 --- 1391\ 15.0 K= 5.60 2.2 8.4 140 16.0 ----2.0 --- 141 l\ 15. 0 K= 5.60 2.4 8.7 142 16.0 ----2.2 --- 143 16.0 ----2.6 --- 144A 15.0 K= 5.60 1. 9 7.7 1 4 .5 16.0 ----l.6 --- 14 61\. 15.0 K= 5.60 1.9 7.7 147 16.0 ----1.5 --- 148 16.0 ----1. 7 --- J49A 15.0 K= 5.60 2.5 8.8 150 16.0 ----2.1 --- 151 16.0 ----2.3 --- 152 16.0 ----2.9 --- 1.53A 15.0 K= 5.60 19.6 24.8 154 16.0 ----19.3 --- 155 16.0 ----21. 0 --- 156 16.0 ----4.0 --- 157A 15.0 K= 5.60 3.2 10.0 158 16.0 ----2.8 --- 159 16.0 ---3.1 --- 160 16.0 ---3.2 --- 161 16.0 ----50.6 --- 162 11. 0 ----57.8 --- TOR 11.0 ----66.4 --- BOP 0.5 ----79. 1 --- UG1 -3.0 ---80.7 --- UG2 -3.0 81. 0 --- UG3 4.0 78.1 --- UG4 4.0 ---90.1 UG5 4.0 ---90.2 SRCE -3.0 SOURCE 93.9 182.2 SPRINKLER SYSTEM HYDRAULIC ANALYSTS Page 3 JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" PIPE DATA PIPE TAG Q(GPM) DIA ( IN) T,ENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PST) (GPM) F.I,./FT (PST) Pipe: 1 -7.0 1.104 PL 1.00 PF 0.0 101A 15.0 5.6 1.6 7.0 2.3 120 FTG PE 0.4 J 02 16.0 0.0 1.1 0.0 0.015 TL 1 . 00 PV 0.0 Pipe: 2 -7.0 1.104 PL 0.50 PF 0.1 102 16. 0 0.0 1.1 0.0 2.3 120 FTG ET PE 0.0 103 16.0 0.0 1.3 0.0 0.015 TL 7.50 PV 0.0 Pipe: 3 -7.0 1.104 PL 10.00 PF 0. 1 J 03 16.0 0.0 1.3 0.0 2.3 120 FTG PE 0.0 106 16.0 0.0 1.4 0.0 0.015 TL 10.00 PV 0.0 Pipe: 4 -7.2 1.104 PL 1.00 PF 0.0 1 041\ 15.0 5.6 1.7 7.2 2.4 120 FTG PE 0.4 105 16.0 0.0 1.2 0.0 0.015 TL 1.00 PV 0.0 Pipe: 5 -7.2 1.104 PL 0.50 PF 0.2 105 16.0 0.0 1.2 0.0 2.4 120 FTG 2T PE 0.0 106 16.0 0.0 1.4 0.0 0.015 TL 10.50 PV 0.0 Pipe: 6 -14.2 1.104 PL 13.00 PF 0.8 106 16.0 0.0 1.4 0.0 4.8 120 FTG E PE 0.0 l13 16.0 0.0 2.2 0.0 0.054 TL 15.00 PV 0.2 Pipe: 7 -29.9 1.452 PL 2.00 PF 0.6 113 16.0 0.0 2.2 0.0 5.8 120 FTG T PE 0.0 114 16.0 0.0 2.8 0.0 0.056 TL 10.00 PV 0.2 Pipe: 8 -7.7 1.104 PL 1.00 PF 0.0 107A 15.0 5.6 1.9 7.7 2.6 120 FTC PE 0.4 108 16.0 0.0 1. 5 0.0 0.017 TL 1.00 PV 0.0 Pipe: 9 -7.7 1.104 PL 0.50 PF 0.1 108 16.0 0.0 1 . 5 0.0 2.6 120 FTG ET PE 0.0 109 16.0 0.0 1. 6 0.0 0.017 TL 7.50 PV 0.0 Pipe: 10 -7.7 1.104 PL 10.00 PF 0.2 109 16.0 0.0 l. 6 0.0 2.6 120 FTG PE 0.0 112 16.0 0.0 l.8 0.0 0.017 TL 10.00 PV 0.0 Pipe: 11 -7.9 1.104 PL 1.00 PF 0.0 l]0A 15.0 5.6 2.0 7.9 2.7 120 FTG PE 0.4 ] l l 16.0 0.0 1.6 0.0 0.018 TL 1.00 PV 0.0 Pipe: 12 -7.9 l. 104 PL 0.50 PF 0.2 111 16.0 0.0 1.6 0.0 2.7 120 FTC 2T PE 0.0 112 16.0 0.0 1.8 0.0 0.018 TL 10.50 PV 0.0 Pipe: 13 -15.7 1.104 PL l. 50 PF 0.4 112 16.0 0.0 1.8 0.0 5.2 120 FTG T PE 0.0 113 16.0 0.0 2.2 0.0 0.064 TL 6.50 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" PIPE DATA (cont'd) - PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES ( FT) ( K) (PST) (GPM) F.T../FT (PST) Pipe: 14 -29.9 1 . 682 PT. 2.50 PF 0. 1 114 16.0 0.0 2.8 0.0 4.3 120 FTC PE 0.0 11 7 16.0 0.0 2.8 0.0 0.027 TT. 2.50 PV 0. 1 Pipe: 15 -9.4 l.104 PL 1.00 PF 0.1 115A 15.0 5.6 2.8 9.4 3.1 120 FTG E PE 0.4 116 16.0 0.0 2.4 0.0 0.025 TL 3.00 PV 0.1 Pipe: 16 -9.4 1 . 104 PL 10.50 PF 0.4 116 16.0 0.0 2.4 0.0 3.1 120 FTG T PE 0.0 117 16.0 0.0 2.8 0.0 0.025 TL 15.50 PV 0.1 Pipe: 17 -39.2 1.682 PL 2.50 PF 0.1 117 16.0 0.0 2.8 0.0 5.7 120 FTG PE 0.0 120 16.0 0.0 2.9 0.0 0.045 TL 2.50 PV 0.2 Pipe: 18 -9.8 1.104 PL 1.00 PF 0.0 1181\ 15.0 5.6 3.1 9.8 3.3 120 FTC PE 0.4 119 16.0 0.0 2.7 0.0 0.027 TL 1.00 PV 0.1 Pipe: 19 -9.8 1.104 PL 1.00 PF 0.3 119 16.0 0.0 2.7 0.0 3.3 120 FTG 2T PE 0.0 120 16.0 0.0 2.9 0.0 0.027 TL 11. 00 PV 0. 1 Pipe: 20 -49.0 1.682 PL 3.00 PF 0.2 120 16.0 0.0 2.9 0.0 7.1 120 FTG PE 0.0 160 16. 0 0.0 3.2 0.0 0.069 TL 3.00 PV 0.3 Pipe: 21 -59.0 1.682 PL 2.00 PF 0.2 160 16.0 0.0 3.2 0.0 8.5 120 FTC PE 0.0 123 16.0 0.0 3.3 0.0 0.097 TL 2.00 PV 0.5 Pipe: 22 -10.0 1.104 PL 1.00 PF 0.0 1217\ 15.0 5.6 3.2 10.0 3.3 120 FTG PE 0.4 122 16.0 0.0 2.8 0.0 0.028 TL 1.00 PV 0.1 Pipe: 23 -10.0 1.104 PL 10.50 PF 0.6 122 16.0 0.0 2.8 0.0 3.3 120 FTG 2T PE 0.0 123 16.0 0.0 3.3 0.0 0.028 TL 20.50 PV 0.1 Pipe: 24 -69.0 1.682 PT, 5.00 PF 0.6 123 16. 0 0.0 3.3 0.0 10.0 120 FTC PE 0.0 156 16.0 0.0 4.0 0.0 0.129 TL 5.00 PV 0.7 Pipe: 25 88.4 1.682 PL 2.00 PF 0.4 156 16.0 0.0 4.0 0.0 12.8 120 FTC PE 0.0 l 7. 6 16.0 0.0 3.6 0.0 0.204 TI, 2.00 PV 1 . 1 Pipe: 26 -10.7 l . 104 PL 1.00 PF 0.0 1247\ 15.0 5.6 3.6 10.7 3.6 120 FTC PE 0.4 125 16.0 0.0 3.2 0.0 0.037. TT. 1 . 00 PV 0.l SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE : RANCHO CARRILLO APTS. "REC. BUTLDTNG" PIPE DATA (cont'd) -· PIPE TAG Q(GPM) DIA ( TN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -10.7 l.104 PL 1.00 PF 0.3 125 16.0 0.0 3.2 0.0 3.6 120 FTG 2T PE 0.0 126 16.0 0.0 3.6 0.0 0.032 TT. 11.00 PV 0. 1 Pipe: 28 77.8 l.682 PL 2.00 PF 0.3 126 16.0 0.0 3.6 0.0 11.2 1.20 FTG PE 0.0 132 16.0 0.0 3.3 0.0 0.161 TL 2.00 PV 0.8 Pipe: 29 -8.9 l. 104 PL 1.00 PF 0.0 127A 15.0 5.6 2.5 8.9 3.0 120 FTG PE 0.4 128 J 6. 0 0.0 2.1 0.0 0.023 TL 1.00 PV 0.1 Pipe: 30 -8.9 l.101 PL 0.50 PF 0.2 128 16.0 0.0 2.1 0.0 3.0 120 FTG ET PE 0.0 131 16.0 0.0 2.3 0.0 0.023 TT. 7 .. 50 PV 0. 1 Pipe: 31 -8.9 J . J 01 pr, 1.00 PF 0.1 129A 15.0 5.6 2.5 8.9 3.0 120 FTG E PE 0.4 130 16.0 0.0 2.2 0;0 0.0?.3 TL 3.00 PV 0. 1 Pipe: 32 -8.9 1.104 PL 0.50 PF 0.1 130 16.0 0.0 2.2 0.0 3.0 120 FTG T PE 0.0 1 3 J 16.0 0.0 2.3 0.0 0.023 TL 5.50 PV 0.1 pjpe: 33 -17.8 1.104 PL 7.00 PF l. 0 131 16.0 0.0 2.3 0.0 6.0 120 FTG T PE 0.0 132 16.0 0.0 3.3 0.0 0.082 TL 12.00 PV 0.2 Pipe: 31 60.0 1 . 682 PL 4.00 PF 0.4 132 16.0 0.0 3.3 0.0 8.7 120 FTG PE 0.0 152 16.0 0.0 2.9 0.0 0.099 TL 4.00 PV 0.5 Pipe: 35 35.7 1.682 PL 2.00 PF 0. 1 152 16.0 0.0 2.9 0.0 5.2 120 FTG PE 0.0 135 16.0 0.0 2.8 0.0 0.038 TL 2.00 PV 0.2 Pipe: 36 -9.6 l. 1 04 PL 1.00 PF 0.0 133A 15.0 5.6 2.9 9.6 3.2 120 FTG PE 0.4 ] 3~ 1 6. 0 0.0 2.5 0.0 0.026 TT. 1 . 00 PV 0. 1 Pipe: 37 -9.6 1.101 PL l.00 PF 0.3 134 16.0 0.0 2.5 0.0 3.2 120 FTG 2T PE 0.0 135 16.0 0.0 2.8 0.0 0.026 TL 11.00 PV 0.1 Pipe: 38 26.2 1.682 PL 2.50 PF 0. 1 135 16.0 0.0 2.8 0.0 3.8 120 FTG PE 0.0 138 16.0 0.0 2.7 0.0 0.021 TL 2.50 PV 0.1 Pipe: 39 ~9.1 1.101 PL 2.00 PF 0.0 136A 15.0 5.6 2.6 9.1 3.1 120 FTG PE 0.4 137 16.0 0.0 2.3 0.0 0.024 TL 2.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSTS Page 6 JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" PIPE DATA (cont'd) - PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PST) (GPM) F.L./FT (PSI) Pipe: 40 -9. 1 l.104 PL 10.00 PF 0.5 137 16. 0 0.0 2.3 0.0 3.l 120 FTG 2T PE 0.0 138 16.0 0.0 2.7 0.0 0.0:>4 TL 20.00 PV 0.1 Pipe: 41 17.0 1.682 PL 9.50 PF 0.l 138 1 6. 0 0.0 2.7 0.0 2.5 120 FTG PE 0.0 1113 16.0 0.0 2.6 0.0 0.010 TI. 9.50 PV 0.0 Pipe: 42 -8.4 l.104 pr, 2.50 PF 0.2 139A 15.0 5.6 2.2 8 . l[ 2.8 120 FTG ET PE 0.4 140 16.0 0.0 2.0 0.0 0.020 TL 9.50 PV 0.1 Pipe: 43 -8.4 1.104 PL 9.00 PF 0.2 140 16.0 0.0 2.0 0.0 2.8 120 FTG PE 0.0 147. 16.0 0.0 2.2 0.0 0.020 TL 9.00 PV 0.1 Pipe: 44 -8.7 1.104 PT, 1.00 PF 0.2 141A 15.0 5.6 2.4 8.7 2.9 120 FTG 2T PE 0.4 142 16.0 0.0 2.2 0.0 0.022 TT, 11 .00 PV 0.] Pipe: 45 -17.0 1.104 PL 1.00 PF 0.5 142 16.0 0.0 2.2 0.0 5.7 120 FTG T PE 0.0 143 16.0 0.0 ;> . 6 0.0 0.075 TL 6.00 PV 0 . ;> Pipe: 46 -7.7 1.104 PL 1.00 PF 0.1 144A 15.0 5.6 1 . 9 7.7 2.6 120 FTG ET PE 0.4 145 16.0 0.0 1.6 0.0 0.017 TT. 8.00 PV 0.0 Pipe: 47 -7.7 l.104 PL 1.00 PF 0.1 145 16.0 0.0 1.6 0.0 2.6 120 FTG 2E PE 0.0 148 16.0 0.0 1.7 0.0 0.017 TL 5.00 PV 0.0 Pipe: 48 -7.7 1.104 PL l.00 PF 0.0 11167\ 15.0 5.6 1.9 7.7 2.6 120 FTG PE 0.4 147 16.0 0.0 1.5 0.0 0.017 TL 1.00 PV 0.0 Pipe: 49 -7.7 1.104 PL 1.00 PF 0.2 147 16.0 0.0 1.5 0.0 2.6 120 FTG 2T PE 0.0 1118 16.0 0.0 1.7 0.0 0.017 TL 11.00 PV 0.0 Pipe: 50 -15.4 l.104 PL 10.50 PF 0.7 ],18 16.0 0.0 1.7 0.0 5.2 120 FTG PE 0.0 151 16.0 0.0 2.3 0.0 0.063 TT. 10.50 PV 0.2 Pipe: 51 -8.8 1,104 PT, 1 . 00 PF 0.0 149A 15.0 5.6 2.5 8.8 3.0 120 FTG PE 0.4 150 16.0 0.0 2. 1 0.0 0.022 TL l.00 PV 0.l Pipe: 52 -8.8 1.104 PT, 1 . 00 PF 0.2 150 16.0 0.0 2 . 1 0.0 3.0 120 FTG 2T PE 0.0 1 51 16.0 0.0 2.3 0.0 0.022 TI. ll . 00 PV 0. 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" PTPF: DATA (cont'd) PIPE TAG Q(GPM) DIA (IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 53 -24.2 1.452 PL 6.00 PF 0.5 151 16.0 0.0 2.3 0.0 4.7 120 FTG T PE 0.0 152 16.0 o.6 2.9 0.0 0.038 TL 14.00 PV 0.] Pipe: 54 -24.8 1.104 PL l.00 PF 0.2 153A 15.0 5.6 19.6 24.B 8.3 120 FTG PE 0.4 154 16.0 0.0 19.3 0.0 0.151 TL 1.00 PV 0.5 Pipe: 55 -24.8 1.104 PL 1.00 PF 1.7 154 16.0 0.0 19.3 0.0 8.3 120 FTG 2T PE 0.0 155 16.0 0.0 21.0 0.0 0.151 TL 11.00 PV 0.5 Pipe: 56 157.5 1.452 PL 6.00 PF 17.0 155 16.0 0.0 21.0 0.0 30.5 120 FTG T PE 0.0 156 16.0 0.0 4.0 0.0 1.215 TL 14.00 PV 6.3 P:ipe: 57 -10.0 l. 1 04 PT, l.00 PF 0.0 157A 15.0 5.6 3.2 10.0 3.4 120 FTG PE 0.4 1 58 16.0 0.0 2.8 o:o 0.028 TL 1 . 00 PV 0.l Pipe: 58 -10.0 1.104 PL l.00 PF 0.3 1 .58 16.0 0.0 2.8 0.0 3.4 120 FTG 2T PE 0.0 159 16.0 0.0 3.1 0.0 0.028 TL 11.00 PV 0.1 Pipe: 59 -10.0 l. 682 PL 6.00 PF 0 . l 159 16.0 0.0 3.1 0.0 1.4 120 FTG T PE 0.0 160 16.0 0.0 3.2 0.0 0.004 TL 14.00 PV 0.0 Pipe: 60 -182.3 1.682 PL 32.00 PF 29.6 155 16.0 0.0 21.0 0.0 26.3 120 FTG 3L PE 0.0 161 16.0 0.0 50.6 0.0 0.778 TL 38.00 PV 4.7 Pipe: 61 -182.3 l. 682 PL 4.50 PF 5.l 161 16.0 0.0 50.6 0.0 26.3 120 FTG L PE 2.2 162 11.0 0.0 57.B 0.0 0.778 TL 6.50 PV 4.7 P:ipe: 62 -182.3 1.682 PI, 9.00 PF 8.6 162 11. 0 0.0 57.8 0.0 26.3 120 FTG L PE 0.0 TOR 11.0 0.0 66.4 0.0 0.778 TL 11 . 00 PV 4.7 Pipe: 63 -182.3 l.682 PL 10.50 PF 8.2 TOR 11. 0 0.0 66.4 0.0 26.3 120 FTG PE 4.5 BOR 0.5 0.0 79.1 0.0 0.778 TL 10.50 PV 4.7 Pipe: 64 -182.3 4.026 PL 4.50 PF 0.1 BOR 0.5 0.0 79.1 0.0 4.6 140 FTG L PE l. 5 UGl -3.0 0.0 80.7 0.0 0.008 TL 12.48 PV 0.1 Pipe: 65 -182.3 4.026 PL 15.00 PF 0.2 UGl -3.0 0.0 80.7 0.0 4.6 150 FTG 2T, PE 0.0 UG2 -3.0 0.0 Bl. 0 0.0 0.007 TL 33.13 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSTS JOB TITLE: RANCHO CARRILLO APTS. "REC. BUILDING" PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA(JN) LENGTH END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) NODES (FT) (K) (PSI) (GPM) F.I../FT Pipe: 66 -182.3 4.026 PL 8.00 UG2 -3.0 0.0 81.0 0.0 4.6 140 FTG L UG3 4.0 0.0 78.l 0.0 0.008 TL 15.98 Page 8 PRESS. SUM. (PST) PF 0. 1 PE 3.0 PV 0. 1 Pipe: 67 FTXED PRESSURE LOSS DEVICE UG4 4.0 0.0 90.l 0.0 12.0 psi, 182.3 gpm UG3 4.0 0.0 78.l 0.0 Pipe: 68 -182.3 4.026 PL 8.00 PF 0.1 UG4 4.0 0.0 90.l 0.0 4.6 140 FTG I, PE 0.0 UG5 4.0 0.0 90.2 0.0 0.008 TL 15.98 PV 0.1 Pipe: 69 -182.2 4.026 PL 60.00 PF 0.7 UG5 4.0 0.0 90.2 0.0 4.6 150 FTG TG PE 3.0 SRCE -3.0 SRCE 93.9 (N/A) 0.007 TL 93.24 PV 0.1 NOTES: ( 1) Calculations were performed by the HASS 5.5.0 computer program under license no. 8926J52l granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (~) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.077 gpm. ( 3 ) Velocity pressures are printed for not used in balancing the system. any pipe is 30.5 ft/sec. information only, and are Maximum water velocity in (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 D DPVlv 10.00 SPRINKJ,ER SYSTEM HYDRAULIC ANALYSTS JOB TITJ.E: RANCHO CARRILLO APTS. "REC. BUTLDTNG" WATER SUPPLY CURVE 180*\\\\\\\\\\\\\\\\\ 0 \\\\\\\\\\\\\\\\\\ Page 9 * <-172.8 psi@ 1453 gpm Flow Test Point 165+ 150+ ]351 Pl20+ R E s 8105+ u R E X 90+ p s I 75+ ) 60+ 30+ X = 15+ 0 = LEGEND Required Water Supply 93.90 psi @ 282.2 gpm Available Water Supply 177.94 psi @ 282.2 gpm " " " " " " " " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)