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HomeMy WebLinkAboutF13-0020 Stamped approved calcs.KUPPINGE.TXT  SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 05/20/13 C:\KUPPINGE JOB TITLE: KUPPINGER.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) 1 125.0 11.5 628.0 120.8 106.3 101.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 106.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 106.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 15.0 SOURCE 101.3 106.3 2 1.8 - - - - 99.0 - - - 3 1.8 - - - - 86.0 - - - 4 2.8 - - - - 82.7 - - - 5 2.8 - - - - 69.7 - - - 6 15.1 - - - - 61.3 - - - 7 15.1 - - - - 59.6 - - - 8 15.1 - - - - 59.4 - - - 9 15.1 - - - - 56.9 - - - 10 25.8 - - - - 51.1 - - - 11 15.1 - - - - 54.2 - - - 12 15.1 - - - - 53.5 - - - 13 26.8 - - - - 48.0 - - - 14 15.1 - - - - 53.9 - - - 15 26.8 - - - - 48.6 - - - 16 26.8 - - - - 45.6 - - - 17 29.8 - - - - 40.8 - - - 18 36.8 - - - - 33.8 - - - 19 36.8 - - - - 31.9 - - - 20 36.8 - - - - 31.6 - - - 21 36.8 - - - - 28.6 - - - 100 36.2 K= 4.90 27.4 25.7 101 36.2 K= 4.90 27.3 25.6 102 36.2 K= 4.90 30.4 27.0 103 36.2 K= 4.98 31.7 28.0 Page 1 KUPPINGE.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 05/20/13 JOB TITLE: KUPPINGER.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 -25.7 1.101 PL 7.12 PF 1.4 100 36.2 4.9 27.4 25.7 8.6 150 FTG 2E PE 0.3 21 36.8 0.0 28.6 0.0 0.108 TL 13.16 PV 0.5 Pipe: 2 -25.6 1.101 PL 7.00 PF 1.6 101 36.2 4.9 27.3 25.6 8.6 150 FTG T PE 0.3 21 36.8 0.0 28.6 0.0 0.107 TL 14.56 PV 0.5 Pipe: 3 -51.3 1.101 PL 7.67 PF 3.0 21 36.8 0.0 28.6 0.0 17.3 150 FTG ---- PE 0.0 20 36.8 0.0 31.6 0.0 0.388 TL 7.67 PV 2.0 Pipe: 4 -27.0 1.101 PL 4.79 PF 1.5 102 36.2 4.9 30.4 27.0 9.1 150 FTG T PE 0.3 20 36.8 0.0 31.6 0.0 0.119 TL 12.35 PV 0.6 Pipe: 5 -78.3 1.598 PL 2.33 PF 0.3 20 36.8 0.0 31.6 0.0 12.5 150 FTG ---- PE 0.0 19 36.8 0.0 31.9 0.0 0.138 TL 2.33 PV 1.1 Pipe: 6 -28.0 1.598 PL 7.00 PF 0.5 103 36.2 5.0 31.7 28.0 4.5 120 FTG T PE 0.3 19 36.8 0.0 31.9 0.0 0.031 TL 15.00 PV 0.1 Pipe: 7 -106.3 1.598 PL 1.92 PF 1.9 19 36.8 0.0 31.9 0.0 17.0 150 FTG E PE 0.0 18 36.8 0.0 33.8 0.0 0.244 TL 7.96 PV 1.9 Pipe: 8 -106.3 1.598 PL 10.00 PF 3.9 18 36.8 0.0 33.8 0.0 17.0 150 FTG E PE 3.0 17 29.8 0.0 40.8 0.0 0.244 TL 16.04 PV 1.9 Pipe: 9 -106.3 1.598 PL 2.33 PF 3.5 17 29.8 0.0 40.8 0.0 17.0 150 FTG T PE 1.3 16 26.8 0.0 45.6 0.0 0.244 TL 14.42 PV 1.9 Pipe: 10 -55.8 1.598 PL 7.83 PF 2.4 16 26.8 0.0 45.6 0.0 8.9 150 FTG 2T PE 0.0 13 26.8 0.0 48.0 0.0 0.074 TL 32.01 PV 0.5 Pipe: 11 -31.5 1.598 PL 11.67 PF 0.5 13 26.8 0.0 48.0 0.0 5.0 150 FTG E PE 5.1 12 15.1 0.0 53.5 0.0 0.026 TL 17.71 PV 0.2 Pipe: 12 -24.3 1.598 PL 27.52 PF 0.6 13 26.8 0.0 48.0 0.0 3.9 150 FTG 2E PE 0.0 15 26.8 0.0 48.6 0.0 0.016 TL 39.61 PV 0.1 Pipe: 13 -24.3 1.598 PL 11.67 PF 0.3 15 26.8 0.0 48.6 0.0 3.9 150 FTG E PE 5.1 14 15.1 0.0 53.9 0.0 0.016 TL 17.71 PV 0.1 Page 2 KUPPINGE.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 05/20/13 JOB TITLE: KUPPINGER.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 -50.5 1.598 PL 34.85 PF 5.1 16 26.8 0.0 45.6 0.0 8.1 150 FTG 6ET PE 0.4 10 25.8 0.0 51.1 0.0 0.061 TL 83.20 PV 0.4 Pipe: 15 -50.5 1.598 PL 11.75 PF 1.1 10 25.8 0.0 51.1 0.0 8.1 150 FTG E PE 4.6 9 15.1 0.0 56.9 0.0 0.061 TL 17.79 PV 0.4 Pipe: 16 -31.5 1.598 PL 16.42 PF 0.7 12 15.1 0.0 53.5 0.0 5.0 150 FTG 2E PE 0.0 11 15.1 0.0 54.2 0.0 0.026 TL 28.51 PV 0.2 Pipe: 17 -24.3 1.598 PL 11.10 PF 0.3 14 15.1 0.0 53.9 0.0 3.9 150 FTG E PE 0.0 11 15.1 0.0 54.2 0.0 0.016 TL 17.14 PV 0.1 Pipe: 18 -55.8 1.598 PL 29.96 PF 5.3 11 15.1 0.0 54.2 0.0 8.9 150 FTG E3T PE 0.0 7 15.1 0.0 59.6 0.0 0.074 TL 72.27 PV 0.5 Pipe: 19 -50.5 1.598 PL 16.85 PF 2.5 9 15.1 0.0 56.9 0.0 8.1 150 FTG 2T PE 0.0 8 15.1 0.0 59.4 0.0 0.061 TL 41.03 PV 0.4 Pipe: 20 -50.5 1.598 PL 2.75 PF 0.2 8 15.1 0.0 59.4 0.0 8.1 150 FTG ---- PE 0.0 7 15.1 0.0 59.6 0.0 0.061 TL 2.75 PV 0.4 Pipe: 21 -106.3 1.598 PL 1.00 PF 1.7 7 15.1 0.0 59.6 0.0 17.0 150 FTG E PE 0.0 6 15.1 0.0 61.3 0.0 0.244 TL 7.04 PV 1.9 Pipe: 22 -106.3 2.003 PL 14.00 PF 3.1 6 15.1 0.0 61.3 0.0 10.8 150 FTG EC PE 5.3 5 2.8 0.0 69.7 0.0 0.081 TL 38.18 PV 0.8 Pipe: 23 FIXED PRESSURE LOSS DEVICE 4 2.8 0.0 82.7 0.0 13.0 psi, 106.3 gpm 5 2.8 0.0 69.7 0.0 Pipe: 24 -106.3 2.003 PL 2.00 PF 2.9 4 2.8 0.0 82.7 0.0 10.8 150 FTG ECB PE 0.4 3 1.8 0.0 86.0 0.0 0.081 TL 35.24 PV 0.8 Pipe: 25 FIXED PRESSURE LOSS DEVICE 2 1.8 0.0 99.0 0.0 13.0 psi, 106.3 gpm 3 1.8 0.0 86.0 0.0 Pipe: 26 -106.3 2.003 PL 75.00 PF 8.1 2 1.8 0.0 99.0 0.0 10.8 150 FTG ETG PE 5.7 1 15.0 SRCE 101.3 (N/A) 0.081 TL 99.18 PV 0.8 Page 3 KUPPINGE.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 05/20/13 JOB TITLE: KUPPINGER.TXT 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 0.159 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 17.3 ft/sec at pipe 3. (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 KUPPINGE.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 05/20/13 JOB TITLE: KUPPINGER.TXT WATER SUPPLY CURVE 180+ | | | 165+ | | | 150+ | | | 135+ | | * P120\0 R |\ E | \ S | \ S105+ \ U |X \ R | \ E | \ 90+ \ ( | \ P | \ S | \ I 75+ \ ) | \ | \ | \ 60+ \ | \ | \ | \ 45+ \ | \ | \ |==============================\ 30+ LEGEND \ " | \ " | X = Required Water Supply\ Page 5