Loading...
HomeMy WebLinkAbout31400 CASINO DR_ 97-1130 (3)l r b SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: LAKE CHEVROLET PIPE FITTINGS TABLE 4 \,; Pipe Table Name: STANDARD.PIP Nominal Equivalent Fitting L9ngths in Feet (C =123) Diameter 1n) E T L C d G A D 00 2 00 5 d0 6 00 1 00 10 00 10 001.OG 1.25 2.00 3.00 y 2.00 7.00 8.00 1.00 10.00 1.OG 1.25 2.00 3.00 5. 6.00 2.00 7.00 8.00 1.00 10.00 10.00 1.50 4.00 8.00 2.00 9.00 6.00 1.00 40.00 10.00 2.00 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 2.50 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10.00 3.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 10.00 3.50 8.00 17.00 5.00 19.00 11.00 1.00 14.00 10.00 4.00 10.00 20.00 8.00 22.00 12.00 2.00 20.00 10.00 5.00 12.00 25.00 8.00 27.00 9.00 2.00 21.00 15.00 5.00 14.00 30.00 9.00 32.00 10.00 3.00 28.00 19.00 8.00 18.00 35.00 13.00 45.00 12.00 4.00 35.00 27.00 10.00 22.00 50.00 16.00 55.00 19.00 5.00 40.00 29.00 12.00 27.00 80.00 18.00 85.00 21.00 6.00 49.00 35.00 16.00 35.00 70.00 28.00 66.00 22.00 7.00 83.00 45.00 18.00 39.00 85.00 33.00 98.00 39.00 8.00 70.00 50.00 Fitting Coos Letters: E=stRndard ell T =tee L=1ong turn all Cmcheck valve B =butterfly valve G =gate valve Anaiarm check valve D--dry pipe -valve a st' t ;w f , I S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE ti 120+ 110+ 0 100 +\ t 90+ \ P 80+ \ R ; \ E ; \ S \ S 70+ \ U ; \ E ; \\ e0X \ P ; \ I 50+ \\ t \ 40+ \\ t I ' 301 \ t k 20+ LEGEND t -20.0 psi • 8802 gpm" Flow Test Point" X = Required Water Supply " r ; 60.91 psi 6 622.7 gpm 10+ " 0 = Available Water Supply » 104.37 psi a 822.7 gpm 32004800 6400 8000 9800 11200 12800 14400 16000 j J FLOW (GPM) err rAn 1 I t I,yJ,, ,• r f 1I 1. SINGLETON FIRE PROTECTION f 22559 W. HICKORY PLACE ? SAU1GUS, CALIF. 91350 F palN R,rop" . I MOST NWS Alit r j HYDRAULIC CALCULATIONS i FOR MOST REMOTE AREA JOB LAKE CHEVROLET - 31400 CASINO DRIVE r DATE: 10 -17 -9T DESIGN DATA - OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) 4` f ,r DENSITY: .20 i x: ry.rr AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 130 UP RIGHT SPRINKLERS CALCULATED: 14 mot. SPRINKLER WATER FLOW REQUIRED: 384.2 gpm y TOTAL WATER REQ.(includ+ng hose) 614.2 gpm FLOW \PRESSURE (at base of riser) 364.2 gpm • 052.2 psi 1 ., SPRINKLER ORIFICE SIZE: 1/2" NAME OF CONTRACTOR: SINGLETON FIRE PRO. x" DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 867001 C -18 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE N 9878Z 33 ) HRS SYSTEMS, INC. ATLANTA, GA c fi Cpl 4 l F a s 1 i a st' t ;w f , I S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE ti 120+ 110+ 0 100 +\ t 90+ \ P 80+ \ R ; \ E ; \ S \ S 70+ \ U ; \ E ; \\ e0X \ P ; \ I 50+ \\ t \ 40+ \\ t I ' 301 \ t k 20+ LEGEND t -20.0 psi • 8802 gpm" Flow Test Point" X = Required Water Supply " r ; 60.91 psi 6 622.7 gpm 10+ " 0 = Available Water Supply » 104.37 psi a 822.7 gpm 32004800 6400 8000 9800 11200 12800 14400 16000 j J FLOW (GPM) err rAn 1 I t I,yJ,, ,• r f 1I 1. SINGLETON FIRE PROTECTION f 22559 W. HICKORY PLACE ? SAU1GUS, CALIF. 91350 F palN R,rop" . I MOST NWS Alit r j HYDRAULIC CALCULATIONS i FOR MOST REMOTE AREA JOB LAKE CHEVROLET - 31400 CASINO DRIVE r DATE: 10 -17 -9T DESIGN DATA - OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) 4` f ,r DENSITY: .20 i x: ry.rr AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 130 UP RIGHT SPRINKLERS CALCULATED: 14 mot. SPRINKLER WATER FLOW REQUIRED: 384.2 gpm y TOTAL WATER REQ.(includ+ng hose) 614.2 gpm FLOW \PRESSURE (at base of riser) 364.2 gpm • 052.2 psi 1 ., SPRINKLER ORIFICE SIZE: 1/2" NAME OF CONTRACTOR: SINGLETON FIRE PRO. x" DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 867001 C -18 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE N 9878Z 33 ) HRS SYSTEMS, INC. ATLANTA, GA c fi Cpl 4 l F a Y c 11.x£ N ' 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 110+ 0 100 +\ A 90+ P 80+ \\ E ; \ S ; \ 8 70+ \ U \ E ; \\ 80+ \ P i \ I 50X \ 40+ \\ 30+ \\ 20+ LEGEND * < -20.0 psi a 8802 gpm" Flow Test joint" X = Required Water Supply 48.83 psi • 580.2 gpm " 10+ " 0 = Available Water Supply " 104.44 psi A 580.2 gpm " 32004800 6400 8000 9600 11200 12600 14400 16000 FLOW (GPM) J h< tirj ?NrNt.ri. l M of r y y Y i SINGLETON FIRE PROTECTION u 22559 W. HICKORY PLACE SAUGUS, CALIF. 91350 5 RY1I. t¢M 1 r; HYDRAULIC CALCULATIONS FOR MOST REMOTE AREA I 5' JOB rL LAKE CHEVROLET - 31400 CASINO DRIVE DATE :10 -17 -97 4, DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) rM DENSITY: .20 ,5 n AREA OF APPLICATION: 1500 SO. FT. j COVERAGE PER SPRINKLER: 130 UP RIGHT n SPRINKLERS CALCULATED: 14 t SPRINKLER WATER FLOW REQUIRED: 372.7 gpm> TOTAL WATER REQ.(including hose) 822.7 gpm FLOW \PRESSURE (at base of riser) 372.7 gpm a 049.3 psi SPRINKLER ORIFICE SIZE: 1/2" y.y NAME OF CONTRACTOR: SINGLETON FIRE PRO. 1 A. Ue DESIGN \LAYOUT BY: R.S. } AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 887001 C -18 t+ ix ,v CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE >< 9878Z 33 ) ! HRS SYSTEMS, INC. ATLANTA, GA x t' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 JOB TITLE: LAKE CHEVROLET PIPE FITTINGS TABLE CPipe Table Name: STANDARD-PIP Nominal Equivalent Fitting Lengths in Feet C =120) Diar'ster in) E T L C B G A D 1.00 2.00 5.00 2.00 5.00 8.00 1.00 10.00 10.00 1.25 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 1.50 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 2.00 5.00 10.00 3.00 11.00 8.00 1.00 10.00 10.00 2.50 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10-CO 3.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 10.00 t 3.50 6.00 17.00 5.00 19.00 11.00 1.00 14.00 10.00 4.00 10.00 20.00 6.00 22.00 12.00 2.00 20.00 10.00 5.00 12.00 25.00 8.00 27.00 9.00 2.00 21.00 15.00 6.00 14.00 30.00 9.00 32.00 10.00 3.00 28.00 19.00 8.00 18.00 35.00 13.00 45.00 12.00 4.00 35.00 27.00 10.00 22.00 50.00 18.00 55.00 19.00 5.00 40.00 29.00 o - 12.00 27.00 60.00 18.00 65.00 21.00 8.00 49.00 35.00 j 16.00 35.00 70.00 28.00 86.00 22.00 7.00 83.00 45.00 18.00 39.00 85.00 33.00 98.00 39.00 8.00 70.00 50.00 t " Fitting Code Letters: Emstandard ell Tstee L =long turn ell C=check valve B=buttarfly valve G =pate valve A =alarm check valve D =dry pipe valve l n Y c 11.x£ N ' 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 110+ 0 100 +\ A 90+ P 80+ \\ E ; \ S ; \ 8 70+ \ U \ E ; \\ 80+ \ P i \ I 50X \ 40+ \\ 30+ \\ 20+ LEGEND * < -20.0 psi a 8802 gpm" Flow Test joint" X = Required Water Supply 48.83 psi • 580.2 gpm " 10+ " 0 = Available Water Supply " 104.44 psi A 580.2 gpm " 32004800 6400 8000 9600 11200 12600 14400 16000 FLOW (GPM) J h< tirj ?NrNt.ri. l M of r y y Y i SINGLETON FIRE PROTECTION u 22559 W. HICKORY PLACE SAUGUS, CALIF. 91350 5 RY1I. t¢M 1 r; HYDRAULIC CALCULATIONS FOR MOST REMOTE AREA I 5' JOB rL LAKE CHEVROLET - 31400 CASINO DRIVE DATE :10 -17 -97 4, DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) rM DENSITY: .20 ,5 n AREA OF APPLICATION: 1500 SO. FT. j COVERAGE PER SPRINKLER: 130 UP RIGHT n SPRINKLERS CALCULATED: 14 t SPRINKLER WATER FLOW REQUIRED: 372.7 gpm> TOTAL WATER REQ.(including hose) 822.7 gpm FLOW \PRESSURE (at base of riser) 372.7 gpm a 049.3 psi SPRINKLER ORIFICE SIZE: 1/2" y.y NAME OF CONTRACTOR: SINGLETON FIRE PRO. 1 A. Ue DESIGN \LAYOUT BY: R.S. } AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 887001 C -18 t+ ix ,v CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE >< 9878Z 33 ) ! HRS SYSTEMS, INC. ATLANTA, GA x t' G I I I + AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 614.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 384.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION FT) 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: Oct 21, 1997 4 0.0 5 CHEVYS JOB TITLE: LAKE CHEVROLET 7 19.0 8 WATER SUPPLY DATA 9 12.0 10 12.0 r )SOURCE STATIC REBID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 0 PRESS. 0 DEMAND PRESS. TAG PSI) PSI) GPM) (PSI) GPM) PSI) 1 105.0 20.0 8802.0 104.4 614.2 63.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 614.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 384.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION FT) 1 0.0 2 5.0 3 5.0 4 0.0 5 3.0 8 19.0 7 19.0 8 12.0 9 12.0 10 12.0 11 12.0 12 12.0 13 11.0 14 12.0 15 12.0 16 12.0 17 12.0 18 12.0 19 12.0 20 11.0 21 12.0 22 12.0 23 12.0 24 12.0 25 12.0 26 12.0 27 11.0 NODE TYPE PRESSURE DISCHARGE Page 3 PSI) GPM) SOURCE 63.7 384.2 81.3 52.3 53.6 52.2 45.2 CHEVROLETP K= 5.60 18.2 23.9 K= 5.60 19.9 25.0 K= 5.60 28.3 28.7 K= 5.60 27.3 29.3 29.1 30.8 K= 5.60 17.F 23.5 K= 5.60 19.2 24.8 K= 5.60 25.4 28.2 K= 5.60 21.0 25.7 K= 5.60 22.9 26.8 28.1 SUM. 4 30.1 K) K= 5.60 17.6 23.5 K= 5.60 19.1 24.5 K= 5.60 25.3 28.1 K= 5.60 20.9 25.6 K= 5.80 22.8 26.7 28.0 29.9 f1 W t K Yrr"tvC T fYYL1 '•r cifY r zv t g aSt5rt • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE: LAKE CHEVROLET PIPE DATA 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: 1 364.2 6.010 PL 55.00 PF 0.2 1 0.0 SRCE 63.7 (N /A) 4.1 140 FTG - - -- PE 2.2 2 5.0 0.0 61.3 0.0 0.004 TL 55.00 ?V 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 61.3 0.0 9.0 psi, 364.2 gpm 3 5.0 0.0 52.3 0.0 Pipe: 3 384.2 6.010 PL 201.00 PF 0.9 3 5.0 0.0 52.3 0.0 4.1 150 FTG 38.40 PE 2.2 4 0.0 0.0 53.8 0.0 0.004 TL 237.40 PV 0.1 Pipe: 4 384.2 6.010 PL 3.00 PF 0.1 4 0.0 0.0 53.6 0.0 4.1 140 FTG 18.20 PE 1.3 5 3.0 0.0 52.2 0.0 0.004 TL 21.20 PV 0.1 Pipe: 5 384.2 8.357 PL 19.00 PF 0.1 5 3.0 0.0 52.2 0.0 3.7 120 FTG - - -- PE 8.9 6 19.0 0.0 45.2 0.0 0.004 TL 19.00 PV 0.1 Pipe: 6 364.2 4.340 PL 53.50 PF 2.0 t8 19.0 0.0 45.2 0.0 7.9 120 FTG 20.00 PE 0.0 7 19.0 0.0 43.1 0.0 0.028 TL 73.50 PV 0.4 Pipe: 7 364.2 3.340 PL 140.50 PF 16.0 7 19.0 0.0 43.1 0.0 13.3 120 FTG 21.00 PE 3.5 13 11.0 0.0 30.6 0.0 0.099 TL 161.50 PV 1.2 Pipe: 8 -23.9 1.087 PL 11.10 PF 1.7 j o 12.0 5.8 18.2 23.9 8.3 120 FTG - - -- PE 0.0 9 12.0 5.6 19.9 25.0 0.152 TL 11.10 PV 0.5 Pipe: 9 -48.9 1.087 PL 11.10 PF 8.4 9 12.0 5.6 19.9 25.0 16.9 120 FTG - - -- PE 0.0 10 12.0 5.6 26.3 28.7 0.572 TL 11.10 PV 1.9 Pipe: 10 -77.6 1.650 PI_ 8.10 PF 2.8 10 12.0 5.8 26.3 28.7 11.8 120 FTG 8.00 PE 0.0 12 12.0 0.0 29.1 0.0 0.176 TL 16.10 PV 0.9 Pipe: 11 -29.3 1.087 PL 3.00 PF 1.8 11 12.0 5.6 27.3 29.3 10.1 120 FTG 5.00 PE 0.0 12 12.0 0.0 29.1 0.0 0.222 TL 8.00 PV 0.7 Pipe: 12 -106.9 2.115 PL 1.00 PF 1.0 12 12.0 0.0 29.1 0.0 9.8 120 FTG 10.00 PE 0.4 13 11.0 0.0 30.6 0.0 0.095 TL 11.00 PV 0.6 1 Pipe: 13 257.3 3.340 PL 10.50 PF 0.5 t 13 11.0 0.0 30.6 0.0 9.4 120 FTG - - -- PE 0.0 20 11.0 0.0 30.1 0.0 0.052 TL 10.50 PV 0.6 r tj 5 x k Y 7'K f P 1ikINtkI F its ¢ 4 r v t,n.x,r•Wf'..•.., -,. .La t:.,K,r!•. $JL., I.ti -x.. F 'n+ ' 7 '•. }J•i'. S" -... +.. nt ., ..t.. -r;. .PJ rt, 1H..:'f 7 h' y. t 1 I 1. 3 a. M r r t xY , t44 ' Lb M+ r*r F .I d ,4 a rte_,. _y a t S F V Y Ni j tt c43. rY tYrG YSIY 5 G'• 4 y 1 .• l J ' 4y r wR. W F SC s a + I 4 Yt oum SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 j.1 JOB TITLE: LAKE CHEVROLETP PIPE DATA cont'd) l )PIPE TAG Q(GPM) OIA(IN) LENGTH PRESS.. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. 4 NODES (FT) K) PSI) GPM) F.L. /FT PSI) ( Pipe: 14 23.5 1.087 PL 11.10 PF 1,.8 14 12.0 5.6 17.8 23.5 8.1 120 FTG PE 0.0 qi 15 12.0 5.8 19.2 24.6 0.147 TL 11.10 PV 0.4 a; Pipe: 15 48.1 1.087 PL 11.10 PF 6.2 15 12.0 5.6 19.2 24.8 16.6 120 FTG PE 0.0 16 12.0 5.6 25.4 28.2 0.554 TL 11.10 PV 1.9 6 Pipe: 18 76.3 1.650 PL 8.10 PF 2.7 16 12.0 5.8 25.4 28.2 11.4 120 FTG 8.00 PE 0.0 19 12.0 0.0 28.1 0.0 0.171 TL 16.10 PV 0.9 Pipe: 17 25.7 1.087 PL 11.10 PF 1.9 17 12.0 5.6 21.0 25.7 8.9 120 FTG PE 0.0 18 12.0 5.8 22.9 28.8 0.174 TL 11.10 PV 0.5'" Pipe: 18 52.5 1.087 PL 3.00 PF 5.2 18 12.0 5.6 22.9 28.8 18.1 120 FTG 5.00 PE 0.0 19 12.0 0.0 28.1 0.0 0.852 TL 8.00 PV 2.2 Pipe: 19 128.6 2.115 PL 1.00 PF 1.5 19 12.0 0.0 28.1 0.0 11.8 120 FTG 10.00 PE 0.4 20 11.0 0.0 30.1 0.0 0.134 TL 11.00 PV 0.9 Pipe: 20 128.5 340 PL 10.50 PF 0.2 20 11.0 0.0 30.1 0.0 4.7 120 FTG PE 0.0 27 11.0 0.0 29.9 0.0 0.014 TL 10.50 PV 0.1 Pipe: 21 23.5 1.087 PL 10.10 PF 1.5 21 12.0 5.8 17.6 23.5 8.1 120 FTG PE 0.0 r 22 12.0 5.8 19.1 24.5 0.148 TL 10.10 PV 0.4 } Pipe: 22 48.0 1.081 PL 11.10 PF 6.1 22 12.0 5.6 19.1 24.5 16.6 120 FTG PE 0.0 23 12.0 5.8 25.3 28.1 0.553 TL 11.10 PV 1.9 Pipe: 23 78.2 1.650 PL 8.10 PF 2.7 23 12.0 5.6 25.3 28.1 11.4 120 FTG 8.00 PE 0.0 26 12.0 0.0 28.0 0.0 0.170 TL 16.10 PV 0.9 Pipe: 24 25.6 1.067 PL 11.10 PF 1.9 Ij 24 12.0 S.6 20.9 25.6 8.8 120 FTG PE 0.0 25 12.0 5.6 22.8 26.7 0.173 TL 11.10 PV 0.5 Pipe: 25 52.3 1.087 PL 3.00 PF 5.2 tr 25 12.0 5.6 22.8 26.7 18.1 120 FTG 5.00 PE 0.0 28 12.0 0.0 28.0 0.0 0.649 TL 8.00 PV 2.2 Pipe: 26 128.5 2.115 PL 1.00 PF 1.5 26 12.0 0.0 28.0 0.0 11.7 120 FTG 10.00 PE 0.4 27 11.0 0.0 29.9 0.0 0.134 TL 11.00 PV 0.9 F V Y Ni j tt c43. rY tYrG YSIY 5 G'• 4 y 1 .• l J ' 4y r wR. W F SC s a + I 4 Yt oum Y . F f! c rte :1, SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 k SPRINKLER SYSTEM HYDRAULIC ANALYSISFSPRINKLERSYSTEMHYDRAULICANALYSTSPage1 Pape 2 Date: Oct 21, 1997 CHEVYI JOB TITLE: LAKE CHEVROLET fJOBTITLE: LAKE CHEVROLETJOBTITLE: LAKE CHEVROLET NODE ANALYSIS DATA (cont'd) PIPE DATA rWATERSUPPLYDATA ) PIPE TAG O(QPM) DIA(IN) LENGTH PRESS. tROURCE STATIC REBID. FLOW AVAIL. TOTAL REQ D ( NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. ;LSD NODE PRESS. PRESS. • PRESS. • DEMANo PRESS. (FT) (PSI) (GPM) NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) ?" TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 35 19.0 - - - - 37,1 _ _ _ I Pipe: 1 372.7 8.010 PL 55.00 PF 0.2 36 19.0 37,1 - _ - 1 0.0 SRCE 60.9 (N /A) 4.2 140 FTG - - -- PE 2.21105.0 20.0 8802.0 104.4 622.7 80.9 37 19,0 - - - - 37.1 - - - 2 5.0 0.0 58.5 0.0 0.004 TL 55.00 PV 0.1 i AGGREGATE FLOW ANALYSIS: Pipe: 2 FIXED PRESSURE LOSS DEVICE t, 2 5.0 0.0 58.5 0.0 9.0 psi, 372.8 gpm f 3 5.0 0.0 49.5 0.0 TOTAL FLOW AT SOURCE 622.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM Pipe: 3 372.7 8.010 PL 201.00 PF 0.9 OTHER HOSE STREAM ALLOWANCES 0.0 GPM 3 5.0 0.0 49.5 0.0 4.2 150 FTG 38.40 PE 2.2 TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 372.7 GPM 4 0.0 0.0 50.7 0.0 0.004 TL 237.40 PV 0.1 . Pipe: 4 372.7 8.010 PL 3.00 PF 0.1 ? NODE ANALYSIS DATA 4 0.0 0.0 50.7 0.0 4.2 140 FTG 18.20 PE 1.3 5 3.0 0.0 49.3 0.0 0.004 TL 21.20 PV 0.1 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE fi ; FT) (PSI) (GPM) Pipe: 5 372.7 8.357 PL 19.00 PF 0.1 5 3.0 0.0 49.3 0.0 3.8 120 FTG - - -- PE 8.9 1 0.0 SOURCE 80.9 372.7 6 19.0 0.0 42.3 0.0 0.005 TL 18.00 PV 0.1 , q 3 5.0 - - - - 49.5 - - - Pipe: 8 214.4 3.340 PL. 53.50 PF 2.5 j e 4 0.0 - - - - 50.7 - - - r 8 19.0 0.0 42.3 0.0 7.9 120 FTG 15.00 PE 0.0 ! 5 3.0 - - - - 49.3 - - - L -7 19.0 0.0 39.8 0.0 0.037 TL 68.50 PV 0.4 F ' 4 ? l.'8 19.0 - - - - 42.3 - 7 19.0 - - - - 39.8 - - - Pipe: 7 214.4 3.340 PL 5.50 PF 0.8 8 19.0 - - - - 39.0 - - - 7 19.0 0.0 39.8 0.0 7.9 120 FTG 15.00 PE 0.0 9 19.0 - - - - 38.8 - 8 19.0 0.0 39.0 0.0 0.037 TL 20.50 PV 0.4 i 3 10 19.0 - - - - 38.8 - - - 11 19.0 - - - - 38.2 - - - Pipe: 8 158.4 3.340 PL 153.50 PF 3.7a 12 13.0 - - - - 37.3 - - - 6 19.0 0.0 42.3 0.0 5.8 120 FTG 22.00 PE 0.0 13 20.0 K= 5.60 21.8 26.2 9 19.0 0.0 38.6 0.0 0.021 TL 175.50 PV 0.2 { - ^- 14 20.0 K= 5.60 20.8 25.6 ' 15 20.0 K= 5.80 20.5 25.4 ! Pipe: 9 6.5 1.650 PL 202.00 PF 0.4 16 20.0 K= 5.60 20.5 25.3 B 19.0 0.0 39.0 0.0 1.0 120 FTG 28.00 PE 0.0 17 20.0 Ka 5.60 20.8 25.4 9 19.0 0.0 38.6 0.0 0.002 TL 230.00 PV 0.0 18 20.0 K= 5.60 21.1 25.7 i 19 19.0 - - - - 37.4 - - - i 9 Pipe: 19.0 0.0 38.6 0.0 164.9 6.0 3 120 FTG 16.00 PE 0.02019.0 - - - - 37.2 - - - 21 20.0 K= 5.60 21.7 26.1 11 19.0 0.0 38.2 0.0 0.023 TL 18.00 PV 0.2 7 22 20.0 K= 5.60 20.8 25.5 + 23 20.0 K= 5.80 20.4 25.3 , Pipe: 11 207.8 3.340 PL 12.00 PF 0.4 y 24 20.0 K= 5.80 20.4 25.3 8 19.0 0.0 39.0 0.0 7.6 120 FTG - - -- PE 0.0 25 20.0 K= 5.80 20.5 25.4 I 10 19.0 0.0 38.6 0.0 0.035 TL 12.00 PV 0.4 y ; 26 20.0 K= 5.60 21.0 25.7 27 19.0 - - - - 37.3 - - - Pipe: 12 5.9 1.650 PL 206.00 PF 0.4 E 28 19.0 - - - 37.1 - - - 10 19.0 0.0 38.8 0.0 0.9 120 FTG 32.00 PE 0.0 I 11 19.0 0.0 38.2 0.0 0.002 TL 238.00 PV 0.02920 t f'^ 0 K =5 80 34.8 32.9 i a 30 20.0 K= 5.60 34.6 32.9 f 31 19.0 r 37.1 + _r! Pipe: 13 170.8 3.340 PL 34.00 PF 0.8 32 19.0 - - - - 37.1 - - - 38.2 0.0 8.3 120 FTG - - -- PE 0.0 w1119.0 0.0 F3318.0 - - - - 37.1 - - - ! 19 19.0 0.0 37.4 0.0 0.024 TL 34.00 PV 0.3 34 19.0 - - - - F 1 % s k. r r ' R: I .9 V'4 ` . • its` 'y' .r wt •1' 1ra i' FQ tii. t 4r t n' i. yynu' `1.fF. vj. S1tMaT' i4+' Xr I V i r Itd ra 6 e i i N U r V ./ i k SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: LAKE CHEVROLET NOTES: 1 1) Calculations were performed by the HASS 6.0.0 computer program 9878Z 33 granted by HRS Systems, Inc. 2193 Ranohwood Dr., N.E. Atlanta, GA 30345 i 2) The system has been balanced to provide an average imbalance at each node of 0.011 gpm and a maximum ir•.balance at any node of 0.138 gpm. 3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pip is 18.1 ft /sec. I t { 1. SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET PIPE FITTINGS TABLE Page 5 Pipe Table Name: STANDARD.PIP a ppii 4 .. .. ..... .i... 3 - p..., .. JY,y i1h Sfln ` A`W' i t.a .`r7 : err .,r.'R° Y irPw; .. Nominal Equivalent Fitting Lengths in Feet C =120) 4 Diameter I t in) E T L C B G A D 1.00 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.25 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 1.50 4.00 8.00 2.90 9.00 6.00 1.00 10.00 10.00 2.00 5.00 10.00 3.00 11.00 8.00 1.00 10.00 10.00 2.50 8.00 12.90 4.00 14.00 7.00 1.00 10.00 10.00 3.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 10.00 3.50 8.00 17.00 5.00 19.00 11.00 1.00 14.00 10.00 4.00 10.00 20.00 8.00 22.00 12.00 2.00 20.00 10.00 5.00 12.00 25.00 8.00 27.00 9.00 2.00 21.00 15.00 6.00 14.00 30.00 9.00 32.00 10.00 3.00 28.00 19.00 6.00 18.00 35.00 13.00 45.00 12.00 4.00 35.00 27.00 10.00 22.00 50.00 16.00 55.00 19.00 5.00 40.00 29.00 12.00 27.00 60.00 18.00 65.00 21.00 6.00 49.00 35.00 16.00 35.00 70.00 28.00 86.00 22.00 7.00 83.00 45.00 18.00 39.00 85.00 33.00 98.00 39.00 8.00 70.00 50.00 Fitting Code Letters: E= standard ell T =toe L =long turn all C =check valve B= butterfly valve G =gate valve A =alarm check valve D =dry pipe valve SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE Page e 120+ 1 110+ 0 100 +\ i \ 90+ \ 1 \ 1 P 80+ \\ R i \ S S 70+ \ R \\ E 60+ \\ 1 \ P ' 1 S i \ I 60+ \ i \ i \ i \ 40+ \\ 71 i \ 1 \ 30+ \ 1 \ 11 \ 1 20+ LEGEND s < -20.0 psi • 8802 gpm" Flow Teat Point" X = Required Water Supply Flow. Teat psi • 614.2 gpm 10+ " 0 = Available Water Supply 104.38 psi • 614.2 gpm u 1 32004800 8400 8000 9600 FLOW ` 11 20 12800 14400 ltwd0 k d at h 1 I r. 5 r „ S .. r - .-.;rs : ..:: ., a ppii 4 .. .. ..... .i... 3 - p..., .. JY,y i1h Sfln ` A`W' i t.a .`r7 : err .,r.'R° Y irPw; .. i t_....r 4 I t V. 1 y 1 f,i1'. i iY r",y1 U t.. 4: 3. r r. t r 1 3 far •.. fy. Ypp1r1 r ti1 r 1 , , 1 ., ,.. r.arrL :', .r ,..: i,.r 5, tr.. '. . 1r 1. ,. ," .. , .. a t ... ,,: W 5 .- r. ,F .. .4 .., j' i . r C.t V .. • 1. Y ... :. , ... -. ., i -fcr, X, .,: .w ' -f. yLy y _ / j' y.., a :K.1 ..:M l , ,A.i1. '•i 'r rE`.c. .'l.I?: -i, 41 yj.J.''W1ti •:E>.yR VFt'r i fi..' +:W'i LT1- Y .i 6' 1 i „' i M• -ikl4 ;,i. 7f r r: _.: ' 1 - • , , r. 1 l (1 >M 4:•' 'S4 f.'i illr 4i•v6f!-I N%.'...!., Wf. I.YJF 1 rr: Y# k d at h 1 I r. 5 r „ S .. r - .-.;rs : ..:: ., a ppii4 .. .. ..... .i... 3 - p..., .. 4w - q y - -n, r ... ,.,. t .. .. ...... Sfln ` A`W' i t.a .`r7 : err .,r.'R° Y irPw; .. i t_....r I t r 1 y t.. 4: t is r r. t r 1 3 far •.. fy. Ypp1r1 r ti1 r 1 , , 1 ., ,.. r.arrL :', .r ,..: i,.r 5, tr.. '. . 1r 1. ,. ," .. , .. a t ... ,,: W 5 .- r. ,F .. .4 .., j' i . r C.t V .. • 1. Y ... :. , ... -. ., i -fcr, X, .,: .w ' -f. yLy y _ / j' y.., a :K.1 ..:M l , ,A.i1. '•i 'r rE`.c. .'l.I?: -i, 41 yj.J.''W1ti •:E>.yR VFt'r i fi..' +:W'i LT1- Y .i 6' 1 i „' i M• -ikl4 ;,i. 7f r: _.: ' 1 - • , , r. 1 l (1 >M 4:•' 'S4 f.'i illr 4i•v6f!-I N%.'...!., Wf. I.YJF r SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA(IN) i.ENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 40 -1.8 3.340 PL 38.00 PF 0.0 32 19.0 0.0 37.1 0.0 0.1 120 FTG - - -- PE 0.0 34 19.0 0.0 37.1 0.0 0.000 TL 38.00 PV 0.0 Pipe: 41 -0.9 1.550 PL 98.00 PF 0.0 34 19.0 0.0 37.1 0.0 0.1 120 FTG 32.00 PE 0.0 35 19.0 0.0 37.1 0.0 0.000 TL 130.00 PV 0.0 Pipe: 42 0.9 3.340 PL 12.00 PF 0.0 35 19.0 0.0 37.1 0.0 0.0 120 FTG - - -- PE 0.0 37 19.0 0.0 37.1 0.0 0.000 TL 12.00 PV 0.0 Pipe: 43 -0.9 3.340 PL 12.00 PF 0.0 34 19.0 0.0 37.1 0.0 0.0 120 FTG - - -- PE 0.0 36 19.0 0.0 37.1 0.0 0.000 TL 12.00 PV 0.0 Pipe: 44 '-0.9 1.650 PL 98.00 PF 0.0 36 19.0 0.0 37.1 0.0 0.1 120 FTG 32.00 PE 0.0 37 19.0 0.0 37.1 0.0 0.000 TL 130.00 PV 0.0 NOTES: 1) Calculations were performed by the HASS 6.0.0 computer program 9878Z 33 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 0.008 gpm and a maximum imbalance at any node of 0.152 gpm. 3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 12.8 ft /sec. t f1 r h I 1 k r f tt LJrt Z i •" R t SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS P , 5age JOB TITLE: LAKE CHEVROLETJOBTITLE: LAKE CHEVROLET PIPE DATA cont'd) PIPE DATA cont'd) PIPE r TAG Q(GPM) DIA(IN) LENGTH PRESS, PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) F SUM. j END ELEV. NOZ. PT DISC !EL(FPS) HW(C) F7) SUM. NODES (FT) K) PSI) GPM) F.LL. ./F/FT PSI) NODES FT) K) PSI) GPM) F.L. /FT PSI) Pipe: 14 201.9 3.340 PL 38.00 PF 1.3 Pipe: 27 8.1 1.650 PL 9.00 PF 0.0 10 19.0 0.0 38.8 0.0 7.4 120 FTG PE 0.0 23 20.0 5.8 20.4 25.3 1.2 120 FTG PE 0.0 12 19.0 0.0 37.3 0.0 0.033 TL 38.00 PV 0.4 24 20.0 5.8 20.4 25.3 0.003 TL 9.00 PV 0.0 Pipe: 15 85.3 1.850 PL 58.00 PF 15.1 Pipe: 28 17.L 1.650 PL 9.00 PF I 0.1 12 19.0 0.0 31.3 0.0 12.8 120 FTG 18.00 PE 0. 24 20.0 5.8 20.4 25.3 2.8 120 FT'3 PE 0.0 13 20.0 8.8 21.8 28.2 0.210 TL 72.00 PV 1.11 i 25 20.0 5.8 20.5 25.4 0.011 TL 9.00 PV 0.0 Pipe: 16 59.1 1.650 PL 9.00 PF 1.0 Pipe: 29 42.5 1.650 PL 9.00 PF 0'.5 13 20.0 5.8 21.8 2 8.9 120 FTG PE 0.0 2 S 20.0 5.8 20.5 25.4 6.4 120 FTO PE 0.0 14 20.0 5.8 20.8 2 26i.8 0.108 TL 9.00 PV 0.5 28 20.0 3.6 21.0 25.7 0.058 TL 9.00 PV 0.3 Pipe: 17 33.5 1.880 PL 9.00 PF 0.3 Pipe: 30 88.2 1.650 PL 102.00 PF 15.8 14 20.0 5.6 20.8 25.6 5.0 120 FTG PE 0.0 28 20.0 5.6 21.0 25.7 10.2 120 FTG 12.00 PE 0.4 15 20.0 5.8 20.5 25.4 0.037 TL 9.00 PV 0.2 27 19.0 0.0 37.3 0.0 0.139 TL 114.00 PV 0.7 Pipe: 18 8.2 1.850 PL 9.00 PF 0.0 Pipe: 31 34.3 3.340 PL 101.00 PF 0.1 15 20.0 5.8 20.5 25.4 1.2 120 FTG PE 0.0 27 19.0 0.0 37.3 0.0 1.3 120 FTG 14.00 PE 0.0 31 19.0 0.0 37.1 0.0 0.001 TL 115.00 PV 0.0 Pipe: 19 17.2 1.650 PL 9.00 PF 0.1 Pipe: 32 31.6 3.340 PL 28.50 PF 0.0 20.0 5.8 20.5 25.3 2.8 120 FTG PE 0.0 X20 19.0 0.0 37.2 0.0 1.2 120 FTG 14.00 PE 0.0 C)18 17 20.0 5.6 20.6 25.4 0.011 TL 9.00 PV 0.0 28 19.0 0.0 37.1 0.0 0.001 TL 42.50 PV 0.0 la Pipe: 20 42.8 1.850 PL 9.00 PF 0.5 Pipe: 33 34.4 1.650 PL 41.50 PF 2.1 17 -• 20.0 5.8 20.6 25.4 8.4 120 FTG PE 0.0 28 19.0 0.0 37.1 0.0 5.2 120 FTG 12.00 PE 0.4 18 20.0 5.8 21.1 25.7 0.058 TL 9.00 PV 0.3 i 29 20.0 5.8 34.6 32.9 0.039 TL 53.50 PV 0.2 Pipe: 21 88.3 1.650 PL 102.00 PF 15.9 Pipe: 34 1.4 1.850 PL 9.20 PF 0.0 18 20.0 5.8 21.1 25.7 10.3 120 FTG 12.00 PE 0.4 29 20.0 5.8 34.6 32.9 0.2 120 FTG PE 0.0 19 19.0 0.0 37.4 0.0 0.139 TL 114.00 PV 0.7 30 20.0 5.8 34.8 32.9 0.000 TL 9.20 PV 0.0 Pipe: 22 102.5 3.340 PL 12.60 PF 0.1 Pipe: 35 31.5 1.650 PL 47.00 PF 2.1 19 19.0 0.0 37.4 0.0 3.8 120 FTG PE 0.0 30 20.0 5.8 34.6 32.9 4.7 120 FTG 18.00 PE 0.4 27 18.0 0.0 37.3 0.0 0.010 TL 12.80 PV 0.1 3 1 19.0 0.0 37.1 0.0 0.033 TL 83.00 PV 0.2 Pipe: 23 118.8 3.340 PL 12.80 PF 0.2 Pipe: 38 2.8 3.340 PL 12.30 PF 0.0 12 18.0 0.0 37.3 0.0 4.3 120 FTG PE 0.0 31 33 19.0 19.0 0.0 0.0 37.1 0.0 0.1 120 FTG PE 0.0 20 19.0 0.0 37.2 0.0 4.012 TL 12.60 PV 0.1 37.1 0.0 0.000 TL 12.30 PV 0.0 Pipe: 24 85.1 1.650 PL 56.00 PF 15.0 Pipe: 37 2.8 3.340 PL 12.30 PF 0.0 20 19.0 0.0 37.2 0.0 12.8 120 FTG 18.00 PE 0.4 28 19.0 0.0 37.1 0.0 0.1 120 FTG PE 0.0 21 20.0 5.6 21.7 28.1 0.209 TL 72.00 PV 1.1 32 19.0 0.0 37.1 0.0 0.000 TL 12.30 PV 0.0 1 i Pipe: 25 59.0 1.0 PL 9.00 PF 1.0 Pipe: 38 1.0 1.650 PL 98.00 OF 0.0 1 p 21 20.0 5.8 21.7 28.1 8.8 12120 FTG PE 0.0 32 19.0 0.0 37.1 0.0 0.1 120 FTG 28.00 PE 0.0 22 20.0 5.8 20.8 25.5 0.108 TL 9.00 PV 0.5 33 19.0 0.0 37.1 0.0 0.000 TL 126.00 PV 0.0 i Pipe: 28 33.4 1.850 PL 9_00 PF 0.3 Pipe: 39 1.8 3.340 PL 38.00 PF 0.0 22 20.0 5.8 20.8 25.5 5.0 120 FTG PE 0.0 33 19.0 0.0 37.1 0.0 0.1 120 FTG PE 0.0 1 23 20.0 5.6 20.4 25.3 0.037 TL 9.00 PV 0.2 35 19.0 0.0 37.1 0.0 0.000 TL 38.00 PV 0.0 r SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA(IN) i.ENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 40 -1.8 3.340 PL 38.00 PF 0.0 32 19.0 0.0 37.1 0.0 0.1 120 FTG - - -- PE 0.0 34 19.0 0.0 37.1 0.0 0.000 TL 38.00 PV 0.0 Pipe: 41 -0.9 1.550 PL 98.00 PF 0.0 34 19.0 0.0 37.1 0.0 0.1 120 FTG 32.00 PE 0.0 35 19.0 0.0 37.1 0.0 0.000 TL 130.00 PV 0.0 Pipe: 42 0.9 3.340 PL 12.00 PF 0.0 35 19.0 0.0 37.1 0.0 0.0 120 FTG - - -- PE 0.0 37 19.0 0.0 37.1 0.0 0.000 TL 12.00 PV 0.0 Pipe: 43 -0.9 3.340 PL 12.00 PF 0.0 34 19.0 0.0 37.1 0.0 0.0 120 FTG - - -- PE 0.0 36 19.0 0.0 37.1 0.0 0.000 TL 12.00 PV 0.0 Pipe: 44 '-0.9 1.650 PL 98.00 PF 0.0 36 19.0 0.0 37.1 0.0 0.1 120 FTG 32.00 PE 0.0 37 19.0 0.0 37.1 0.0 0.000 TL 130.00 PV 0.0 NOTES: 1) Calculations were performed by the HASS 6.0.0 computer program 9878Z 33 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 0.008 gpm and a maximum imbalance at any node of 0.152 gpm. 3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 12.8 ft /sec. t f1 r h I 1 k r f tt LJrt Z i •" R t