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HomeMy WebLinkAbout31400 CASINO DR_ 97-1130 (10)31400 CASINO DR. 97 -1130 4/6 I 7 4Y1f zk `y freer f7 w I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 JOB TITLE: LAKE CHEVROLET JOB TITLE: LAKE CHEVROLET i • WATER SUPPLY CURVE PIPE FITTINGS TABLE rl f )Pipe Table Name: STANDARD.PIP u 120+ Nominal Equivalent Fitting Lengths in Feet C =120) Diameter rr i 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 I 110+ 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 8.00 1.00 10.00 10.00 2.00 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 1002.50 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10.00 00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 10.00 I3.50 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 g0+ \ 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 16.00 55.00 19.00 5.00 40.00 29.00 P 80+ \ 12.00 27.00 60.00 18.00 85.00 21.00 8.00 49.00 35.00 R16.00 35.00 70.00 28.00 86.00 22.00 7.00 63.00 45.00 E 18.00 39.00 85.00 33.00 98.00 39.00 8.00 70.00 50.00 SPRINKLERS CALCULATED: 14 S i \ Fitting Code Letters: E =standard ell Totes L =long turn ell S U 70+ \ C=check valve B= butterfly valve G =gate valve RA =alarm check valve D =dry pipe valve FLOW \PRESSURE tat base of riser) 372.7 gpm A 049.3 psifc E SPRINKLER ORIFICE SIZE: 1/2" w ; NAME OF CONTRACTOR: SINGLETON FIRE PRO. i r` 60+ C1 DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE A, y t CONTRACTOR CERTIFICATION NUMBER: 667001 C -16 P I i S CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE N 9878Z 33 ) jHRSSYSTEMS, INC. I 50X \ ATLANTA, GA r V S' l I 1 40+ \ d r7 J r y r 30+ \ pp 20+ LEGEND • < -20.0 psi A 8802 gpm" Flow Test Point" X = Required Water Supply 48.83 psi ! 580.2 gpm " 10+ " 0 = Available Water Supply j 104.44 psi • 580.2 gpm " 0++-+---+----+-----+------+---'-----+-------- +---------- +------ - - - - -+ j 32004800 6400 8000 9600 11200 12800 14400 16000 FLOW (GPM) 7 4Y1f zk `y freer f7 w icl i4 i • rl u rr i Z 1 I t SINGLETON FIRE PROTECTION 22559 W. HICKORY PLACE SAUGUS, CALIF. 91350 IJMM AMA i. HYDRAULIC CALCULATIONS FOR MOST REMOTE AREA 1 JOB LAKE CHEVROLET - 31400 CASINO DRIVE DATE:10 -17 -97 i i DESIGN DATA- V OCCUPANCY CLASSIFICATION. ORDINARY (GROUP II) l DENSITY: .20 AREA OF APPLICATION: 1500 80. FT. COVERAGE PER SPRINKLER: 130 UP RIGHT SPRINKLERS CALCULATED: 14 III g' SPRINKLER WATER FLOW REQUIRED: 372.7 gpm TOTAL WATER REQ.(including hose) 822.7 gpm FLOW \PRESSURE tat base of riser) 372.7 gpm A 049.3 psifc SPRINKLER ORIFICE SIZE: 1/2" w ; NAME OF CONTRACTOR: SINGLETON FIRE PRO. i r` DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE A, y CONTRACTOR CERTIFICATION NUMBER: 667001 C -16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE N 9878Z 33 ) jHRSSYSTEMS, INC. ATLANTA, GA r V S' l I 1 d r7 J r y r pp k SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 1I 110+ 0 100 +\ 1\ 11 \ 1 90+ \ 1 \ 1 P 80+ \ E ; \ S \ S 70+ \ U \ R ; \ E BOX \ 8 \\ I 50+ \ 1 \ 40+ \ 1 \ 11 \ 1 1 \ 30+ \ 1 \ 11 \ 1 20+ LEGEND < -20.0 psi a 8802 gpm" Flow Test Point" X = Required Water Supply " 60.91 psi a 622.7 gpm " 10+ " 0 = Availablb Water Supply " 104.37 psi a 622.7 gpm " M 1 O++-+---+----+-----+------+--------+------ -- +- -- ------ +------ - - - - -+ 32004800 8400 8000 9600 FLOW 11120 12800 14400 18000 t DATE:1O -17 -97 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: LAKE CHEVROLET y M DESIGN DATA- t OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) PIPE FITTINGS TABLE 1r p fn r/ r Pipe Tale Nominal Name: STANDARD.PIP r Equivalent Fitting Lengths in Feet C =120) Diameter 130 UP RIGHT f SPRINKLERS CALCULATED: 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 2.00 9.00 6.00 1.00 10.00 10.00 2.00 5.00 10.00 3.00 11.00 5.00 1.00 10.00 10.00 2.50 6.00 12.00 4.30 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 6.00 22.00 12.00 2.00 20.00 10.00 5.00 12.00 21.00 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 13.10 45.00 12.00 4.00 35.00 27.00 10.00 22.00 50.00 16.00 55.00 19.00 5, 1 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 88.00 22.00 7.00 63.00 45.00 18.00 39.00 86.00 33.00 98.00 39.00 6.00 70.00 50.00 Fitting Code Letters: Eustar.dar6 ell Tutee Wong turn all Cucheck valve Bubutterfly valve Gugate valve Aualarm check valve Dudry pipe valve SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 1I 110+ 0 100 +\ 1\ 11 \ 1 90+ \ 1 \ 1 P 80+ \ E ; \ S \ S 70+ \ U \ R ; \ E BOX \ 8 \\ I 50+ \ 1 \ 40+ \ 1 \ 11 \ 1 1 \ 30+ \ 1 \ 11 \ 1 20+ LEGEND < -20.0 psi a 8802 gpm" Flow Test Point" X = Required Water Supply " 60.91 psi a 622.7 gpm " 10+ " 0 = Availablb Water Supply " 104.37 psi a 622.7 gpm " M 1 O++-+---+----+-----+------+--------+------ -- +- -- ------ +------ - - - - -+ 32004800 8400 8000 9600 FLOW 11120 12800 14400 18000 t J i l LZ DATE:1O -17 -97 r y M DESIGN DATA- t OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) f 1r p fn r/ r 20 r 1500 80. FT. r COVERAGE PER SPRINKLER: 130 UP RIGHT f SPRINKLERS CALCULATED: 14 k 364.2 gpm 7 r' r '1 r•b SINGLETON FIRE PROTECTION Y22559W. HICKORY PLACE i SAUCUS, CALIF. 91350 FLOW \PRESSURE (at base of riser) CpoUNp ' E I MOT IOMS Alma HYDRAULIC CALCULATIONS 4 FOR MOST REMOTE AREA SPRINKLER ORIFICE SIZE: 1/2" JOB LAKE CHEVROLET - 31400 CASINO DRIVE NAME OF CONTRACTOR: J i l LZ DATE:1O -17 -97 DESIGN DATA- t OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) l l DENSITY: 20 AREA OF APPLICATION: 1500 80. FT. COVERAGE PER SPRINKLER: 130 UP RIGHT SPRINKLERS CALCULATED: 14 SPRINKLER WATER FLOW REQUIRED: 364.2 gpm r. r• TOTAL WATER REO.(including hose) 514.2 gpm FLOW \PRESSURE (at base of riser) 364.2 gpm a 052.2 psi SPRINKLER ORIFICE SIZE: 1/2" NAME OF CONTRACTOR: SINGLETON FIRE PRO. DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 667001 C -16 CALCULATIONS BY HASS COMPUTER PROGRAM LICENSE a 98782 33 HRS SYSTEMS, INC. ATLANTA, GA tl J i l LZ 1 r SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: Oct 21, 1997 CHEVY5 JOB TITLE: LAKE CHEVROLET WATER SUPPLY DATA r SOURCE STATIC RESID. FLOW AVAIL. TOTAL REO'D NODE PRESS. PRESS. 0 PRESS. 0 DEMAND PRESS. TAG PSI) PSI) (GPM) PSI) GPM) (PSI) 1 10510 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 364.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 1 0,0 SOURCE 63.7 384.2 2 5.0 81.3 3 5.0 52.3 4 0.0 53.8 5 3.0 52.2 8 19.0 45.2 7 19.0 43.1 8 12.0 K= 5.60 18.2 23.9 9 12.0 K= 5.60 19.9 25.0 10 12.0 K= 5.60 26.3 28.7 11 12.0 K= 5.60 27.3 29.3 12 12.0 29.1 13 11.0 30.6 14 12.0 K= 5.80 17.6 23.5 15 12.0 K= 5.60 19.2 24.6 18 12.0 Kz 5.80 25.4 28.2 17 12.0 K= 5.80 21.0 25.7 18 12.0 K= 5.60 22.9 26.2 19 12.0 28.1 20 11.0 30.1 21 12.0 K= 5.80 17.6 23.5 22 12.0 K= 5.60 19.1 24.5 23 12.0 K= 5.60 25.3 28.1 24 12.0 K= 5.60 20.9 25.6 25 12.0 K= 5.80 22.8 26.7 26 12.0 28.0 27 11.0 29.9 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: 1 334.2 6.010 PL 55.00 PF 0.2 1 0.0 SRCE 83.7 (N /A) 4.1 140 FTG - - -- PE 2.2 2 5.0 0.0 61.3 0.0 0.004 TL 55.00 PV 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 81.3 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 53.6 0.0 0.004 TL 237.40 PV 0.1 Pipe: 4 364.2 6.010 PL 3.00 PF 0.1 4 0.0 0.0 53.8 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 6.9 8 19.0 0.0 45.2 0.0 0.004 TL 19.00 PV 0.1 Pipe: 6 384.2 4.340 PL 53.50 PF 2.0 8 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: 7 354.2 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 ij Pipe: 8 -23.9 1.087 PL 11.10 PF 1.7 8 12.0 5.6 18.2 23.9 8.3 120 FTG - - -- PE 0.0 9 12.0 5.8 19.9 25.0 0.152 TL 11.10 PV 0.5 Pipe: 9 -48.9 1.087 PL 11.10 PF 6.4 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 PL 8.10 PF 2.8 10 12.0 5.6 26.3 28.7 11.6 120 FTG 8.00 PE C.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 Pipe: 13 257.3 3.340 PL 10.50 PF 0.5 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 s' AMY/7 h 1 l H ~ y A i 4 i t t lE SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 y JOB TITLE: LAKE CHEVROLET PIPE DATA cont'd) TAG Q(GPM) DIA(IN) LENGTH PRESS.k' PIPE END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. a fir? 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 15 12.0 5.6 19.2 24.8 0.147 TL 11.10 PV 0.4 4 Pipe: 15 48.1 1.087 PL 11.10 PF 8.2; 15 12.0 5.8 19.2 24.8 18.6 120 FTG PE 0.0 J"' 18 12.0 5.8 25.4 28.2 0.554 TL 11.10 PV 1.9 Pipe: 16 78.3 1.850 PL 8.10 PF 2.7 t 18 12.0 5.8 25.4 28.2 11.4 120 FT13 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 28.6 0.174 TL 11.10 PV 0.5 Pipe: 18 52.5 1.067 PL 3.00 PF 5.2 18 12.0 5.8 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: 19 128.8 2.115 PL 1.00 PF 1.5 019 12.0 0.0 28.1 0.0 11.8 120 FTG 10.00 PE 0.4 J 20 11.0 0.0 30.1 0.0 0.134 TL 11.00 PV 0.9 Pipe: 20 128.5 3.340 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 G) r Pipe: 21 23.5 1.087 PL 10.10 PF 1.5 Ht, 21 12.0 5.6 17.6 23.5 8.1 120 FTG PE 0.0 rt 22 12.0 5.8 19.1 24.5 0.148 TL 10.10 PV 0.4 1 =j Pipe: 22 48.0 1.087 PL 11.10 PF 8.1 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 1.850 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 18.10 PV 0.9 er`x Pipe: 24 25.6 1.087 PL 11.10 PF 1.9 I ' 24 12.0 5.6 20.9 25.6 8.8 120 FTG PE 0.0 25 12.0 5.6 22.8 28.7 0.173 TL 11.10 PV 0.5 Pipe: 25 52.3 1.087 PL 3.00 PF 5.2 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 E - 28 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 oo r . i. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: Oct 21, 1997 JOB TITLL: LAKE CHEVROLET WATER SUPPLY DATA Page 1 CHEVYI SOURCE STATIC REBID. FLOW AVAIL. 70TAL REQ'D NODE PRESS. PRESS. 0 PRESS. 0 DEMAND PRESS. TAG (PSI) PSI) (GPM) PSI) GPM) PSI) 1 105.0 20.0 8802.0 104.4 622.7 60.9 AGGREGATE FLOW ANALYSIS: y c, SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET NODE ANALYSIS DATA (cont'd) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGEFT) (PSI) (GPM) 35 19.0 - - - - 37.1 - - - 36 19.0 - - - - 37.1 - - - 37 19.0 - - - - 37.1 - - - Page 2 y . kFN %J ut ri c' xl u s f F xR a f Mfr r R L rh F SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 SitiF JOB TITLE: LAKE CHEVROLET PIPE DATA 1, )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) i Pipe: 1 372.7 8.010 PL 55.00 PF 0.2 1 0.0 SRCE 80.9 (N /A) 4.2 140 FTG - - -- PE 2.2 2 5.0 0.0 58.5 0.0 0.004 TL 55.00 PV 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 58.5 0.0 9.0 psi, 372.8 gpm 3 5.0 0.0 49.5 0.0 Pipe: 3 372.7 8.010 PL 201.00 PF 0.9 3 5.0 0.0 49.5 0.0 4.2 150 FTG 36.40 PE 2.2 4 0.0 0.0 50.7 0.0 0.004 TL 237.40 PV 0.1 s Pipe: 4 372.7 8.010 PL 3.00 PF 0.1 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 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 8 19.0 0.0 42.3 0.0 0.005 TL 19.00 PV 0.1 Pipe: 8 214.4 3.340 PL 53.50 PF 2.5 F 8 19.0 0.0 42.3 0.0 7.9 120 FTG 15.00 PE 0.0 7 19.0 0.0 39.8 0.0 0.037 TL 88.50 PV 0.4 Pipe: 7 214.4 3.340 PL 5.50 PF 0.6 7 19.0 0.0 39.8 0.0 7.9 120 FTG 15.00 PE 0.0 8 19.0 0.0 39.0 0.0 0.037 TL 20.50 PV 0.4 Pipe: 8 158.4 3.340 PL 153.50 PF 3.7 6 19.0 0.0 42.3 0.0 5.8 120 FTG 22.00 PE 0.0 9 19.0 0.0 38.6 0.0 0.021 TL 175.50 PV 0.2 i Pipe: 9 8.5 1.650 PL 202.00 PF 0.4 p 8 19.0 0.0 39.0 0.0 1.0 120 FTG 28.00 PE 0.0 9 19.0 0.0 38.8 0.0 0.002 TL 230.00 PV 0.0 Pipe: 10 104.9 3.340 PL 18.00 PF 0.4 9 19.0 0.0 38.6 0.0 6.0 120 FTG - - -- PE 0.0 '1 11 19.0 0.0 38.2 0.0 0.023 TL 16.00 PV 0.2 ^w Pipe: 11 207.8 3.340 PL 12.00 PF 0.4 8 19.0 0.0 39.0 0.0 7.6 120 FTG - - -- PE 0.0 r 10 19.0 0.0 38.6 0.0 0.035 TL 12.00 PV 0.4 i Pipe: 12 5.9 1.650 PL 208.00 PF 0.4 10 19.0 0.0 38.6 0.0 0.9 120 FTG 32.00 PE 0.0 11 19.0 0.0 38.2 0.0 0.002 TL 238.00 PV 0.0 Pipe: 13 170.8 3.340 PL 34.00 PF 0.8 ; 11 19.0 0.0 38.2 0.0 8.3 120 FTG - - PE 0.0 h' 19 19.0 0.0 37.4 0.0 0.024 TL 34.00 PV 0.3 i y TOTAL FLOW AT SOURCE 622.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE. SPRINKLERS 372.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 1 0.0 30URCE 80.9 372.7 2 5.0 58.5 3 5.0 49.5 4 0.0 50.7 5 3.0 49.3 13 19.0 42.3 7 19.0 39.8 8 19.0 39.0 9 19.0 38.6 10 19.0 38.6 11 19.0 38.2 12 19.0 37.3 13 20.0 K= 5.60 21.8 25.2 14 20.0 K= 5.60 20.8 25.6 15 20.0 K= 5.60 20.5 25.4 18 20.0 K= 5.60 20.5 25.3 17 20.0 K= 5.60 20.6 25.4 i8 20.0 K= 5.60 21.1 25.7 19 19.0 37.4 20 19.0 37.2 21 20.0 K= 5.60 21.7 26.1 22 20.0 K= 5.60 20.8 25.5 23 20.0 K= 5.80 20.4 25.3 24 20.0 K= 5.60 20.4 25.3 25 20.0 K= 5.60 20.5 25.4 26 20.0 K= 5.60 21.0 25.7 27 19.0 7.3 28 19.0 37.1 29 20.0 K= 5.60 34.6 32.9 30 20.0 K= 5.60 34.8 32.9 1 ;31 19.0 37.1 32 19.0 37.1 3P 19.0 37.1i3419.0 37.1 y c, SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET NODE ANALYSIS DATA (cont'd) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGEFT) (PSI) (GPM) 35 19.0 - - - - 37.1 - - - 36 19.0 - - - - 37.1 - - - 37 19.0 - - - - 37.1 - - - Page 2 y . kFN %J ut ri c' xl u s f F xR a f Mfr r R L rh F SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 SitiF JOB TITLE: LAKE CHEVROLET PIPE DATA 1, )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) i Pipe: 1 372.7 8.010 PL 55.00 PF 0.2 1 0.0 SRCE 80.9 (N /A) 4.2 140 FTG - - -- PE 2.2 2 5.0 0.0 58.5 0.0 0.004 TL 55.00 PV 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 58.5 0.0 9.0 psi, 372.8 gpm 3 5.0 0.0 49.5 0.0 Pipe: 3 372.7 8.010 PL 201.00 PF 0.9 3 5.0 0.0 49.5 0.0 4.2 150 FTG 36.40 PE 2.2 4 0.0 0.0 50.7 0.0 0.004 TL 237.40 PV 0.1 s Pipe: 4 372.7 8.010 PL 3.00 PF 0.1 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 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 8 19.0 0.0 42.3 0.0 0.005 TL 19.00 PV 0.1 Pipe: 8 214.4 3.340 PL 53.50 PF 2.5 F 8 19.0 0.0 42.3 0.0 7.9 120 FTG 15.00 PE 0.0 7 19.0 0.0 39.8 0.0 0.037 TL 88.50 PV 0.4 Pipe: 7 214.4 3.340 PL 5.50 PF 0.6 7 19.0 0.0 39.8 0.0 7.9 120 FTG 15.00 PE 0.0 8 19.0 0.0 39.0 0.0 0.037 TL 20.50 PV 0.4 Pipe: 8 158.4 3.340 PL 153.50 PF 3.7 6 19.0 0.0 42.3 0.0 5.8 120 FTG 22.00 PE 0.0 9 19.0 0.0 38.6 0.0 0.021 TL 175.50 PV 0.2 i Pipe: 9 8.5 1.650 PL 202.00 PF 0.4 p 8 19.0 0.0 39.0 0.0 1.0 120 FTG 28.00 PE 0.0 9 19.0 0.0 38.8 0.0 0.002 TL 230.00 PV 0.0 Pipe: 10 104.9 3.340 PL 18.00 PF 0.4 9 19.0 0.0 38.6 0.0 6.0 120 FTG - - -- PE 0.0 '1 11 19.0 0.0 38.2 0.0 0.023 TL 16.00 PV 0.2 ^w Pipe: 11 207.8 3.340 PL 12.00 PF 0.4 8 19.0 0.0 39.0 0.0 7.6 120 FTG - - -- PE 0.0 r 10 19.0 0.0 38.6 0.0 0.035 TL 12.00 PV 0.4 i Pipe: 12 5.9 1.650 PL 208.00 PF 0.4 10 19.0 0.0 38.6 0.0 0.9 120 FTG 32.00 PE 0.0 11 19.0 0.0 38.2 0.0 0.002 TL 238.00 PV 0.0 Pipe: 13 170.8 3.340 PL 34.00 PF 0.8 ; 11 19.0 0.0 38.2 0.0 8.3 120 FTG - - PE 0.0 h' 19 19.0 0.0 37.4 0.0 0.024 TL 34.00 PV 0.3 i y 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: LAKE CHEVROLET NOTES: 1) Calculations were performed by the HASS 8.0.0 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 0.0:1 gpm and a maximum imbalance 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 pipe is 18.1 ft /sec. A. ti. SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 1 110+ 0 100 +\ i\ i \ 90+ \ i \ i \ P 80+ \ R ; \ E \ S ; \ S 70+ \ R ; \\ E 8 + P \\ I 50+ \ i \ i \ 40+ \ i \ i \ i \ 30+ \ 20+ LEGEND 4-20.0 psi 0 8802 gpm" Flow Test Point" X = Required Water Supply " 83.72 psi • 814.2 gpm " 10+ " 0 = Available Water Supply " 104.38 psi S 814.2 gpm " 1 32004800 8400 8000 9800 11200 12800 14400 18000 FLOW (GPM) Ya aS r1 X7.'7artb ddA 57^ I s AFB SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: LAKE CHEVROLET PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP Nominal Equivalent Fitting Lengths in Feet C =120) Diameter in) E T L C B G A D 1100 2.00 5.00 2.00 5.00 8.00 1.00 10.00 10.00 1.25 3.00 8.00 2.00 7.00 8.00 1.00 10.00 10.00 1.50 4.00 8.00 2.00 9.00 8.00 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 12.00 4.00 14.00 7.00 1.00 10.00 10.00 3.00 7.00 15.00 5.00 18.00 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 8.00 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 8.00 49.00 35.00 18.00 35.00 70.00 28.00 88.00 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 =tee L =long turn ell Cacheck valve B =butterfly valve Gagate valve A =alarm i check valve D =dry pipe valve SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE 120+ 1 110+ 0 100 +\ i\ i \ 90+ \ i \ i \ P 80+ \ R ; \ E \ S ; \ S 70+ \ R ; \\ E 8 + P \\ I 50+ \ i \ i \ 40+ \ i \ i \ i \ 30+ \ 20+ LEGEND 4-20.0 psi 0 8802 gpm" Flow Test Point" X = Required Water Supply " 83.72 psi • 814.2 gpm " 10+ " 0 = Available Water Supply " 104.38 psi S 814.2 gpm " 1 32004800 8400 8000 9800 11200 12800 14400 18000 FLOW (GPM) Ya aS r1 X7.'7artb ddA 57^ I s AFB SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 j. JOS TITLE: LAKE CHEVROLET PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA(IN) LENGT14 PRESS. ENO ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 14 201.9 3.340 PL 3F.00 PF 1.3 10 19.0 0.0 38.6 0.0 7.4 120 FTG - - -- PE 0.0 12 19.0 5.0 37.3 0.0 0.033 TL 38.00 PV 0.4 Pipe: 15 85.3 1.650 PL 58.00 PF 15.1 12 19.0 0.0 37.3 0.0 12.8 120 FTG 18.00 PE 0.4 13 20.0 5.8 21.8 26.2 0.210 TL 72.00 PV 1.1 Pipe: 18 59.1 1.650 PL 9.00 PF 1.0 13 20.0 5.8 21.8 26.2 8.9 120 FTG - - -- PE 0.0 14 20.0 5.6 20.8 25.8 0.108 TL 9.00 PV 0.5 Pipe: 17 33.5 1.850 PL 9.00 PF 0.3 14 20.0 5.6 20.8 25.6 5.0 120 FTG - - -- PE 0.0 15 20.0 5.8 20.5 25.4 0.037 TL 9.00 PV 0.2 Pipe: 18 8.2 1.650 PL 9.00 PF 0.0 15 20.0 5.6 20.5 25.4 1.2 120 FTG - - -- PE 0.0 18 20.0 5.6 20.5 25.3 0.003 TL 9.00 PV 0.0 Pipe: 19 -17.2 1.850 PL 9.00 PF 0.1 C 16 20.0 5.6 20.5 25.3 2.6 120 FTG - -- PE 0.0 17 20.0 5.6 20.6 25.4 0.011 TL 9.00 PV 0.0 Pipe: 20 -42.8 1.850 PL 9.00 PF 0.5 17 20.0 5.6 20.6 25.4 8.4 120 FTG - - -- PE 0.0 18 20.0 5.6 21.1 25.7 0.058 TL 9.00 PV 0.3 Pipe: 21 -68.3 1.650 PL 102.00 PF 15.9 18 20.0 5.8 21.1 25.7 10.3 120 FTG 12.00 PE 0.4 19 19.0 0.0 37.4 0.0 0.139 TL 114.00 PV 0.7 Pipe: 22 102.5 3.340 PL 12.60 PF 0.1 19 19.0 0.0 3T.4 0.0 3.8 120 FTG - - -- PE 0.0 27 19.0 0.0 37.3 0.0 0.010 TL 12.80 PV 0.1 Pipe: 23 116.6 3.340 PL 12.60 PF 0.2 12 19.0 0.0 37.3 0.0 4.3 120 FTG - - -- PE 0.0 20 19.0 0.0 37.2 0.0 0.012 TL 12.60 PV 0.1 Pipe: 24 85.1 1.850 PL 56.00 PF 15.0 20 19.0 0.0 37.2 0.0 12.8 120 FTG 16.00 PE 0.4 21 20.0 5.6 21.7 26.1 0.209 TL 72.00 PV 1.1 i i Pipe: 25 59.0 1.650 PL 9.00 PF 1.0 21 20.0 5.6 21.7 26.1 8.8 120 FTG - - -- PE 0.0 20.0 5.6 20.8 25.5 0.106 TL 9.00 PV 0.5 Pipe: 26 33.4 1.650 PL 9.00 PF 0.3 22 20.0 5.6 20.8 25.5 5.0 120 FTG - - -- PE 0.0 j 23 20.0 5.6 20.4 25.3 0.037 TL 9.00 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: LAKE CHEVROLET PIPE DATA ( cont'd) PIPE TAG END ELEV. NODES (FT) Pipe: 27 23 20.0 24 20.0 Pipe: 28 24 20.0 25 20.0 Pipe: 29 25 20.0 28 20.0 Pipe: 30 28 20.0 27 19.0 Pipe: 31 27 19.0 31 19.0 Pipe: 32 20 19.0 26 19.0 Pipe: 33 28 19.0 29 20.0 Pipe: 34 29 20.0 30 20.0 Pipe: 35 30 20.0 31 19.0 Pipe: 36 31 19.0 33 19.0 Pipe: 37 28 19.0 32 19.0 Pipe: 38 32 19.0 33 19.0 Pipe: 39 33 19.0 35 19.0 Q(GPM) DIA(IN) LENGTH PRESS. NOZ. PT DISC. VEL(FPS) OW(C) (FT) SUM. K) (PSI) (GPM) F.L. /FT (PSI) 8.1 1.650 PL 9.00 PF 0.0 5.6 20.4 25.3 1.2 120 FTG - - -- PE 0.0 5.6 20.4 25.3 0.003 TL 9.00 PV 0.0 17.2 1.650 PL 9.00 PF 0.1 5.6 20.4 25.3 2.6 120 FTG - - -- PE 0.0 5.6 20.5 25.4 0.011 TL 9.00 PV 0.0 42.5 1.650 PL 9.00 PF 0.5 5.6 20.5 25.4 8.4 120 FTO - - -- PE 0.0 5.6 21.0 25.7 0.058 TL 9.00 PV 0.3 88.2 1.650 PL 102.00 PF 15.8 5.8 21.0 25.7 10.2 120 FTG 12.00 PE 0.4 0.0 37.3 0.0 0.139 TL 114.00 PV 0.7 34.3 3.340 PL 101.00 PF 0.1 0.0 37.3 0.0 1.3 120 FTG 14.00 PE 0.0 0.0 37.1 0.0 0.001 TL 115.00 PV 0.0 31.6 3.340 PL 28.50 PF 0.0 0.0 37.2 0.0 1.2 120 FTG 14.00 PE 0.0 0.0 37.1 0.0 0.001 TL 42.50 PV 0.0 34.4 1.850 PL 41.50 PF 2.1 0.0 37.1 0.0 5.2 120 FTG 12.00 PE 0.4 5.8 34.6 32.9 0.039 TL 53.50 PV 0.2 1.4 1.650 PL 9.20 PF 0.0 5.6 34.8 32.9 0.2 120 FTG - - -- PE 0.0 6.6 34.6 32.9 0.000 TL 9.20 PV 0.0 31.5 1.650 PL 47.00 PF 2.1 5.8 34.8 32.9 4.7 120 FTG 16.00 PE 0.4 0.0 37.1 0.0 0.033 TL 63.00 PV 0.2 2.8 3.340 PL 12.30 PF 0.0 0.0 37.1 0.0 0.1 120 FTG - - -- PE 0.0 0.0 37.1 0.0 0.000 TL 12.30 PV 0.0 2.8 3.340 PL 12.30 PF 0.0 0.0 37.1 0.0 0.1 120 FTG - - -- PE 0.0 0.0 37.1 0.0 0.000 TL 12.30 PV 0.0 1.0 1.650 PL 88.00 PF 0.0 0.0 37.1 010 0.1 120 FTG 28.00 PE 0.0 0.0 37.1 0.0 0.000 TL 126.00 PV 0.0 1.8 3.340 PL 38.00 PF 0.0 0.0 37.1 0.0 0.1 120 FTG - - -- PE 0.0 0.0 37.1 0.0 0.000 TL 38.00 PV 0.0 y tf f xd i ors•. 1.,'J, rIFy t i "Y f F f K dY i f SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 f'f w F JOB TITLE: LAKE CHEVROLET PIPE DATA ( cont'd) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.9 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 36.00 PF 0.0 u- 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 1.850 PL 98.00 PF 0.0 34 19.0 0.0 37.1 0.0 0.1 170 FTG 32.00 PE 0.0 35 19.0 0.0 37.1 0.0 0.000 TL 130.00 PV 0.0 ff: 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 7- 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 r: Pipe: 44 -0.9 1.650 PL 98.00 PF 0.0 38 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 98787 33 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. 4 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; y tf f xd i