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HomeMy WebLinkAboutF12-0094 hydraulic calcsBASINGDA.TXT  SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 11/12/12 C:\BASINGDA JOB TITLE: Basingdale.txt WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 120.0 30.0 920.0 118.4 105.0 94.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 105.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 105.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 25.0 SOURCE 94.2 105.0 2 7.5 - - - - 91.5 - - - 3 8.5 - - - - 90.9 - - - 4 8.5 - - - - 77.9 - - - 5 9.5 - - - - 73.9 - - - 6 9.5 - - - - 60.9 - - - 7 19.0 - - - - 54.0 - - - 8 19.0 - - - - 50.0 - - - 9 12.5 - - - - 51.1 - - - 10 12.5 - - - - 50.7 - - - 11 25.0 - - - - 44.6 - - - 12 19.0 - - - - 47.9 - - - 13 21.0 - - - - 46.4 - - - 14 25.0 - - - - 44.0 - - - 15 25.0 - - - - 44.0 - - - 16 37.0 - - - - 38.9 - - - 17 30.0 - - - - 42.4 - - - 18 30.0 - - - - 42.3 - - - 19 41.0 - - - - 37.5 - - - 20 25.0 - - - - 43.4 - - - 21 25.0 - - - - 43.4 - - - 22 26.8 - - - - 29.6 - - - 23 26.8 - - - - 31.3 - - - 100 26.2 K= 4.90 27.3 25.6 101 26.2 K= 4.90 28.8 26.3 102 26.2 K= 4.90 28.3 26.1 103 26.2 K= 4.90 30.4 27.0 Page 1 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 11/12/12 JOB TITLE: Basingdale.txt 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 -25.6 1.055 PL 10.25 PF 2.6 100 26.2 4.9 27.3 25.6 9.4 150 FTG 3E PE 0.3 22 26.8 0.0 29.6 0.0 0.132 TL 19.32 PV 0.6 Pipe: 2 -26.1 1.055 PL 1.00 PF 1.6 102 26.2 4.9 28.3 26.1 9.6 150 FTG ET PE 0.3 22 26.8 0.0 29.6 0.0 0.137 TL 11.58 PV 0.6 Pipe: 3 -26.3 1.055 PL 10.75 PF 2.8 101 26.2 4.9 28.8 26.3 9.7 150 FTG 3E PE 0.3 23 26.8 0.0 31.3 0.0 0.139 TL 19.82 PV 0.6 Pipe: 4 -27.0 1.055 PL 0.50 PF 1.2 103 26.2 4.9 30.4 27.0 9.9 150 FTG T PE 0.3 23 26.8 0.0 31.3 0.0 0.146 TL 8.06 PV 0.7 Pipe: 5 -51.7 1.055 PL 17.75 PF 13.0 22 26.8 0.0 29.6 0.0 19.0 150 FTG 3E PE 0.8 20 25.0 0.0 43.4 0.0 0.484 TL 26.82 PV 2.4 Pipe: 6 -51.7 1.810 PL 1.75 PF 0.6 20 25.0 0.0 43.4 0.0 6.4 120 FTG T PE 0.0 14 25.0 0.0 44.0 0.0 0.053 TL 11.75 PV 0.3 Pipe: 7 -53.3 1.055 PL 8.42 PF 11.3 23 26.8 0.0 31.3 0.0 19.6 150 FTG 2ET PE 0.8 21 25.0 0.0 43.4 0.0 0.514 TL 22.02 PV 2.6 Pipe: 8 -53.3 1.810 PL 11.83 PF 1.2 21 25.0 0.0 43.4 0.0 6.6 120 FTG T PE 1.7 13 21.0 0.0 46.4 0.0 0.056 TL 21.83 PV 0.3 Pipe: 9 -61.2 1.810 PL 8.50 PF 0.6 13 21.0 0.0 46.4 0.0 7.6 120 FTG ---- PE 0.9 12 19.0 0.0 47.9 0.0 0.072 TL 8.50 PV 0.4 Pipe: 10 -12.0 1.810 PL 2.58 PF 0.1 14 25.0 0.0 44.0 0.0 1.5 120 FTG ET PE 0.0 15 25.0 0.0 44.0 0.0 0.004 TL 17.58 PV 0.0 Pipe: 11 -12.0 1.810 PL 12.00 PF 0.1 15 25.0 0.0 44.0 0.0 1.5 120 FTG E PE 5.2 16 37.0 0.0 38.9 0.0 0.004 TL 17.00 PV 0.0 Pipe: 12 -12.0 1.810 PL 47.25 PF 0.3 16 37.0 0.0 38.9 0.0 1.5 120 FTG E4T PE 1.7 19 41.0 0.0 37.5 0.0 0.004 TL 92.25 PV 0.0 Pipe: 13 -12.0 1.810 PL 11.00 PF 0.1 19 41.0 0.0 37.5 0.0 1.5 120 FTG E PE 4.8 18 30.0 0.0 42.3 0.0 0.004 TL 16.00 PV 0.0 Page 2 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 11/12/12 JOB TITLE: Basingdale.txt PIPE DATA (cont.) 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: 14 -12.0 1.810 PL 19.25 PF 0.1 18 30.0 0.0 42.3 0.0 1.5 120 FTG 2E PE 0.0 17 30.0 0.0 42.4 0.0 0.004 TL 29.25 PV 0.0 Pipe: 15 -7.9 1.810 PL 13.42 PF 0.1 17 30.0 0.0 42.4 0.0 1.0 120 FTG 4E PE 3.9 13 21.0 0.0 46.4 0.0 0.002 TL 33.42 PV 0.0 Pipe: 16 -4.1 1.810 PL 28.50 PF 0.0 17 30.0 0.0 42.4 0.0 0.5 120 FTG 3ET PE 2.2 11 25.0 0.0 44.6 0.0 0.000 TL 53.50 PV 0.0 Pipe: 17 -39.6 1.810 PL 19.71 PF 0.6 14 25.0 0.0 44.0 0.0 4.9 120 FTG ---- PE 0.0 11 25.0 0.0 44.6 0.0 0.032 TL 19.71 PV 0.2 Pipe: 18 -43.8 1.810 PL 12.50 PF 0.7 11 25.0 0.0 44.6 0.0 5.5 120 FTG E PE 5.4 10 12.5 0.0 50.7 0.0 0.039 TL 17.50 PV 0.2 Pipe: 19 -43.8 1.810 PL 0.92 PF 0.4 10 12.5 0.0 50.7 0.0 5.5 120 FTG T PE 0.0 9 12.5 0.0 51.1 0.0 0.039 TL 10.92 PV 0.2 Pipe: 20 -60.4 1.810 PL 13.82 PF 1.7 9 12.5 0.0 51.1 0.0 7.5 120 FTG 2E PE 2.8 8 19.0 0.0 50.0 0.0 0.071 TL 23.82 PV 0.4 Pipe: 21 16.6 1.810 PL 41.63 PF 0.5 9 12.5 0.0 51.1 0.0 2.1 120 FTG 2E2T PE 2.8 12 19.0 0.0 47.9 0.0 0.006 TL 71.63 PV 0.0 Pipe: 22 -44.6 1.810 PL 38.33 PF 2.1 12 19.0 0.0 47.9 0.0 5.6 120 FTG ET PE 0.0 8 19.0 0.0 50.0 0.0 0.040 TL 53.33 PV 0.2 Pipe: 23 -105.0 1.810 PL 5.25 PF 4.0 8 19.0 0.0 50.0 0.0 13.1 120 FTG ET PE 0.0 7 19.0 0.0 54.0 0.0 0.196 TL 20.25 PV 1.2 Pipe: 24 -105.0 1.810 PL 9.50 PF 2.8 7 19.0 0.0 54.0 0.0 13.1 120 FTG E PE 4.1 6 9.5 0.0 60.9 0.0 0.196 TL 14.50 PV 1.2 Pipe: 25 FIXED PRESSURE LOSS DEVICE 5 9.5 0.0 73.9 0.0 13.0 psi, 105.0 gpm 6 9.5 0.0 60.9 0.0 Pipe: 26 -105.0 1.810 PL 2.00 PF 3.5 5 9.5 0.0 73.9 0.0 13.1 120 FTG EC PE 0.4 4 8.5 0.0 77.9 0.0 0.196 TL 18.00 PV 1.2 Page 3 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 11/12/12 JOB TITLE: Basingdale.txt PIPE DATA (cont.) 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: 27 FIXED PRESSURE LOSS DEVICE 3 8.5 0.0 90.9 0.0 13.0 psi, 105.0 gpm 4 8.5 0.0 77.9 0.0 Pipe: 28 -105.0 1.810 PL 1.00 PF 0.2 3 8.5 0.0 90.9 0.0 13.1 120 FTG ---- PE 0.4 2 7.5 0.0 91.5 0.0 0.196 TL 1.00 PV 1.2 Pipe: 29 -105.0 1.985 PL 100.00 PF 10.3 2 7.5 0.0 91.5 0.0 10.9 150 FTG ETG PE 7.6 1 25.0 SRCE 94.2 (N/A) 0.083 TL 124.18 PV 0.8 NOTES: (1) Calculations were performed by the HASS 5.7.0 computer program under license no. 416J187 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 0.007 gpm and a maximum imbalance at any node of 0.188 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 19.6 ft/sec at pipe 7. (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 S D Ell Tee LngEll ChkVlv BfyVlv GatVlv 45Ell DPVlv Page 4 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 11/12/12 JOB TITLE: Basingdale.txt WATER SUPPLY CURVE 120*\ |0\\ | \ | \\ 110+ \ | \\ | \ | \\ 100+ \ | \\ |X \\ | \ 90+ \\ | \ | \\ | \ P 80+ \\ R | \ E | \\ S | \\ S 70+ \ U | \\ R | \ E | \\ 60+ \ ( | \\ P | \ S | \\ I 50+ \\ ) | \ | \\ | \ 40+ \\ | \ | \\ | \ 30+ 30.0 psi @ 920 gpm-> * | Flow Test Point | |============================== 20+ LEGEND " | " | X = Required Water Supply " | 94.25 psi @ 105.0 gpm " 10+ " | 0 = Available Water Supply " Page 5