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JAFFE SECONDARY HOME.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 01/06/12 C:\HASS57\JAFFE2ND JOB TITLE: JAFFE2ND.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 99.0 26.7 868.0 97.6 103.5 86.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 103.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 103.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 13.5 SOURCE 86.1 103.5 2 27.9 K= 4.90 27.3 25.6 3 27.9 K= 4.90 28.2 26.0 4 27.9 K= 4.90 27.7 25.8 5 27.9 K= 4.90 28.2 26.0 6 30.4 - - - - 28.8 - - - 7 30.4 - - - - 28.8 - - - 8 30.4 - - - - 30.8 - - - 9 30.4 - - - - 29.8 - - - 10 30.4 - - - - 29.8 - - - 11 24.0 - - - - 38.6 - - - 12 24.0 - - - - 38.6 - - - 13 24.0 - - - - 39.3 - - - 14 11.5 - - - - 45.7 - - - 15 29.1 - - - - 36.1 - - - 16 11.5 - - - - 44.8 - - - 17 24.0 - - - - 38.6 - - - 18 12.0 - - - - 48.8 - - - 19 11.5 - - - - 46.5 - - - 20 11.5 - - - - 49.0 - - - 21 3.0 - - - - 54.0 - - - 22 3.0 - - - - 67.0 - - - 23 1.0 - - - - 82.9 - - - 24 1.5 - - - - 69.6 - - - 25 1.5 - - - - 82.6 - - - Page 1 JAFFE SECONDARY HOME.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 01/06/12 JOB TITLE: JAFFE2ND.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 5.71 PF 2.6 2 27.9 4.9 27.3 25.6 9.4 150 FTG 2ET PE 1.1 6 30.4 0.0 28.8 0.0 0.132 TL 19.31 PV 0.6 Pipe: 2 -25.8 1.055 PL 5.21 PF 2.1 4 27.9 4.9 27.7 25.8 9.5 150 FTG ET PE 1.1 7 30.4 0.0 28.8 0.0 0.134 TL 15.79 PV 0.6 Pipe: 3 -26.0 1.055 PL 5.71 PF 2.6 3 27.9 4.9 28.2 26.0 9.6 150 FTG 2ET PE 1.1 10 30.4 0.0 29.8 0.0 0.136 TL 19.31 PV 0.6 Pipe: 4 -26.0 1.055 PL 5.71 PF 2.6 5 27.9 4.9 28.2 26.0 9.6 150 FTG 2ET PE 1.1 9 30.4 0.0 29.8 0.0 0.136 TL 19.31 PV 0.6 Pipe: 5 1.2 1.055 PL 7.79 PF 0.0 6 30.4 0.0 28.8 0.0 0.5 150 FTG ---- PE 0.0 7 30.4 0.0 28.8 0.0 0.000 TL 7.79 PV 0.0 Pipe: 6 -24.6 1.055 PL 2.83 PF 2.0 7 30.4 0.0 28.8 0.0 9.0 150 FTG 2ET PE 0.0 8 30.4 0.0 30.8 0.0 0.123 TL 16.43 PV 0.5 Pipe: 7 -26.8 1.055 PL 30.75 PF 7.0 6 30.4 0.0 28.8 0.0 9.8 150 FTG E2T PE 2.8 12 24.0 0.0 38.6 0.0 0.144 TL 48.88 PV 0.7 Pipe: 8 1.4 1.055 PL 8.25 PF 0.0 10 30.4 0.0 29.8 0.0 0.5 150 FTG ---- PE 0.0 9 30.4 0.0 29.8 0.0 0.001 TL 8.25 PV 0.0 Pipe: 9 -24.7 1.055 PL 0.50 PF 1.0 9 30.4 0.0 29.8 0.0 9.0 150 FTG T PE 0.0 8 30.4 0.0 30.8 0.0 0.123 TL 8.06 PV 0.6 Pipe: 10 -27.4 1.055 PL 26.38 PF 6.0 10 30.4 0.0 29.8 0.0 10.1 150 FTG 2ET PE 2.8 11 24.0 0.0 38.6 0.0 0.150 TL 39.98 PV 0.7 Pipe: 11 -49.2 1.055 PL 4.75 PF 4.8 8 30.4 0.0 30.8 0.0 18.1 150 FTG 2E PE 0.6 15 29.1 0.0 36.1 0.0 0.443 TL 10.79 PV 2.2 Pipe: 12 -49.2 1.810 PL 17.62 PF 1.1 15 29.1 0.0 36.1 0.0 6.1 120 FTG E PE 7.6 16 11.5 0.0 44.8 0.0 0.048 TL 22.62 PV 0.3 Pipe: 13 27.4 1.810 PL 1.54 PF 0.0 12 24.0 0.0 38.6 0.0 3.4 120 FTG ---- PE 0.0 11 24.0 0.0 38.6 0.0 0.016 TL 1.54 PV 0.1 Page 2 JAFFE SECONDARY HOME.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 01/06/12 JOB TITLE: JAFFE2ND.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 -54.2 1.810 PL 1.50 PF 0.7 12 24.0 0.0 38.6 0.0 6.8 120 FTG 2E PE 0.0 13 24.0 0.0 39.3 0.0 0.058 TL 11.50 PV 0.3 Pipe: 15 -54.2 1.810 PL 12.50 PF 1.0 13 24.0 0.0 39.3 0.0 6.8 120 FTG E PE 5.4 14 11.5 0.0 45.7 0.0 0.058 TL 17.50 PV 0.3 Pipe: 16 0.0 1.810 PL 29.67 PF 0.0 12 24.0 0.0 38.6 0.0 0.0 120 FTG E PE 0.0 17 24.0 0.0 38.6 0.0 0.000 TL 34.67 PV 0.0 Pipe: 17 -49.2 1.810 PL 24.58 PF 1.7 16 11.5 0.0 44.8 0.0 6.1 120 FTG T PE 0.0 19 11.5 0.0 46.5 0.0 0.048 TL 34.58 PV 0.3 Pipe: 18 -54.2 1.810 PL 4.46 PF 0.8 14 11.5 0.0 45.7 0.0 6.8 120 FTG T PE 0.0 19 11.5 0.0 46.5 0.0 0.058 TL 14.46 PV 0.3 Pipe: 19 -103.5 1.810 PL 3.08 PF 2.5 19 11.5 0.0 46.5 0.0 12.9 120 FTG T PE 0.0 20 11.5 0.0 49.0 0.0 0.191 TL 13.08 PV 1.1 Pipe: 20 -0.0 2.067 PL 58.75 PF 0.0 18 12.0 0.0 48.8 0.0 0.0 120 FTG 5ET PE 0.2 20 11.5 0.0 49.0 0.0 0.000 TL 93.75 PV 0.0 Pipe: 21 -103.5 2.067 PL 8.50 PF 1.4 20 11.5 0.0 49.0 0.0 9.9 120 FTG E PE 3.7 21 3.0 0.0 54.0 0.0 0.100 TL 13.50 PV 0.7 Pipe: 22 FIXED PRESSURE LOSS DEVICE 22 3.0 0.0 67.0 0.0 13.0 psi, 103.5 gpm 21 3.0 0.0 54.0 0.0 Pipe: 23 -103.5 2.067 PL 3.00 PF 1.9 22 3.0 0.0 67.0 0.0 9.9 120 FTG EC PE 0.6 24 1.5 0.0 69.6 0.0 0.100 TL 19.00 PV 0.7 Pipe: 24 FIXED PRESSURE LOSS DEVICE 25 1.5 0.0 82.6 0.0 13.0 psi, 103.5 gpm 24 1.5 0.0 69.6 0.0 Pipe: 25 -103.5 2.067 PL 0.50 PF 0.1 25 1.5 0.0 82.6 0.0 9.9 120 FTG ---- PE 0.2 23 1.0 0.0 82.9 0.0 0.100 TL 0.50 PV 0.7 Pipe: 26 -103.5 1.985 PL 75.00 PF 8.6 23 1.0 0.0 82.9 0.0 10.7 150 FTG 2ETG PE 5.4 1 13.5 SRCE 86.1 (N/A) 0.081 TL 106.73 PV 0.8 Page 3 JAFFE SECONDARY HOME.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 01/06/12 JOB TITLE: JAFFE2ND.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 0.005 gpm and a maximum imbalance at any node of 0.113 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 18.1 ft/sec at pipe 11. (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 2.067 5.00 10.00 3.00 11.00 6.00 1.00 2.00 10.00 Page 4 JAFFE SECONDARY HOME.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 01/06/12 JOB TITLE: JAFFE2ND.TXT WATER SUPPLY CURVE 120+ | | | 110+ | | | 100*\ |0\\ | \\ | \ 90+ \\ | \\ |X \\ | \ P 80+ \\ R | \\ E | \ S | \\ S 70+ \\ U | \\ R | \ E | \\ 60+ \\ ( | \\ P | \ S | \\ I 50+ \\ ) | \ | \\ | \\ 40+ \\ | \ | \\ | \\ 30+ \ | 26.7 psi @ 868 gpm-> * | Flow Test Point |============================== 20+ LEGEND " | " | X = Required Water Supply " | 86.06 psi @ 103.5 gpm " 10+ " | 0 = Available Water Supply " | 97.59 psi @ 103.5 gpm " | " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) Page 5