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HomeMy WebLinkAboutF12-0066 CALCSBASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 09/19/12 C:\BASINGDA JOB TITLE: Basingdale2.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 30.0 920.0 118.4 104.4 99.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 104.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 104.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 25.0 SOURCE 99.6 104.4 103 31.5 K= 4.90 28.2 26.0 102 31.5 K= 4.90 27.3 25.6 101 31.5 K= 4.90 29.5 26.6 100 31.5 K= 4.90 28.6 26.2 99 32.0 - - - - 30.4 - - - 98 32.0 - - - - 36.2 - - - 97 32.0 - - - - 29.1 - - - 96 32.0 - - - - 35.6 - - - 95 32.0 - - - - 35.6 - - - 94 22.0 - - - - 39.9 - - - 93 32.0 - - - - 41.6 - - - 92 22.0 - - - - 51.1 - - - 91 22.0 - - - - 52.7 - - - 90 22.0 - - - - 53.8 - - - 89 22.0 - - - - 55.6 - - - 88 22.0 - - - - 52.7 - - - 87 9.5 - - - - 57.0 - - - 86 22.0 - - - - 52.5 - - - 85 9.5 - - - - 57.9 - - - 84 22.0 - - - - 53.0 - - - 83 9.5 - - - - 58.2 - - - 82 9.5 - - - - 57.8 - - - 6 10.0 - - - - 65.1 - - - 5 10.0 - - - - 78.1 - - - 4 9.0 - - - - 83.2 - - - 3 9.0 - - - - 96.2 - - - 2 8.0 - - - - 96.8 - - - Page 1 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 09/19/12 JOB TITLE: Basingdale2.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 -26.2 1.055 PL 12.04 PF 2.1 100 31.5 4.9 28.6 26.2 9.6 150 FTG E PE 0.2 99 32.0 0.0 30.4 0.0 0.138 TL 15.06 PV 0.6 Pipe: 2 -26.6 1.055 PL 0.50 PF 1.1 101 31.5 4.9 29.5 26.6 9.8 150 FTG T PE 0.2 99 32.0 0.0 30.4 0.0 0.142 TL 8.06 PV 0.6 Pipe: 3 -52.8 1.055 PL 3.92 PF 5.8 99 32.0 0.0 30.4 0.0 19.4 150 FTG T PE 0.0 98 32.0 0.0 36.2 0.0 0.504 TL 11.48 PV 2.5 Pipe: 4 51.6 1.810 PL 11.54 PF 0.6 98 32.0 0.0 36.2 0.0 6.4 120 FTG ---- PE 0.0 96 32.0 0.0 35.6 0.0 0.053 TL 11.54 PV 0.3 Pipe: 5 -25.6 1.055 PL 12.04 PF 2.0 102 31.5 4.9 27.3 25.6 9.4 150 FTG E PE 0.2 97 32.0 0.0 29.1 0.0 0.132 TL 15.06 PV 0.6 Pipe: 6 -26.0 1.055 PL 0.50 PF 1.1 103 31.5 4.9 28.2 26.0 9.5 150 FTG T PE 0.2 97 32.0 0.0 29.1 0.0 0.136 TL 8.06 PV 0.6 Pipe: 7 -51.6 1.055 PL 3.92 PF 6.5 97 32.0 0.0 29.1 0.0 18.9 120 FTG T PE 0.0 96 32.0 0.0 35.6 0.0 0.731 TL 8.92 PV 2.4 Pipe: 8 0.0 1.810 PL 10.42 PF 0.0 96 32.0 0.0 35.6 0.0 0.0 120 FTG ET PE 0.0 95 32.0 0.0 35.6 0.0 0.000 TL 25.42 PV 0.0 Pipe: 9 -0.0 1.810 PL 16.50 PF 0.0 95 32.0 0.0 35.6 0.0 0.0 120 FTG E PE 4.3 94 22.0 0.0 39.9 0.0 0.000 TL 21.50 PV 0.0 Pipe: 10 -104.4 1.810 PL 8.00 PF 5.4 98 32.0 0.0 36.2 0.0 13.0 120 FTG 2ET PE 0.0 93 32.0 0.0 41.6 0.0 0.194 TL 28.00 PV 1.1 Pipe: 11 -104.4 1.810 PL 16.50 PF 5.1 93 32.0 0.0 41.6 0.0 13.0 120 FTG T PE 4.3 92 22.0 0.0 51.1 0.0 0.194 TL 26.50 PV 1.1 Pipe: 12 -61.9 1.810 PL 11.33 PF 1.6 92 22.0 0.0 51.1 0.0 7.7 120 FTG T PE 0.0 91 22.0 0.0 52.7 0.0 0.074 TL 21.33 PV 0.4 Pipe: 13 -58.6 1.810 PL 11.67 PF 1.1 91 22.0 0.0 52.7 0.0 7.3 120 FTG E PE 0.0 90 22.0 0.0 53.8 0.0 0.067 TL 16.67 PV 0.4 Page 2 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 09/19/12 JOB TITLE: Basingdale2.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 -45.8 1.810 PL 5.17 PF 0.9 84 22.0 0.0 53.0 0.0 5.7 120 FTG ET PE 0.0 90 22.0 0.0 53.8 0.0 0.042 TL 20.17 PV 0.2 Pipe: 15 -104.4 1.810 PL 4.17 PF 1.8 90 22.0 0.0 53.8 0.0 13.0 120 FTG E PE 0.0 89 22.0 0.0 55.6 0.0 0.194 TL 9.17 PV 1.1 Pipe: 16 -42.6 1.810 PL 7.00 PF 0.4 92 22.0 0.0 51.1 0.0 5.3 120 FTG E PE 5.4 87 9.5 0.0 57.0 0.0 0.037 TL 12.00 PV 0.2 Pipe: 17 -3.3 1.810 PL 12.25 PF 0.0 91 22.0 0.0 52.7 0.0 0.4 120 FTG ---- PE 0.0 88 22.0 0.0 52.7 0.0 0.000 TL 12.25 PV 0.0 Pipe: 18 14.5 1.810 PL 11.75 PF 0.2 88 22.0 0.0 52.7 0.0 1.8 120 FTG 2T PE 0.0 86 22.0 0.0 52.5 0.0 0.005 TL 31.75 PV 0.0 Pipe: 19 14.5 1.810 PL 7.00 PF 0.1 86 22.0 0.0 52.5 0.0 1.8 120 FTG E PE 5.4 85 9.5 0.0 57.9 0.0 0.005 TL 12.00 PV 0.0 Pipe: 20 -17.8 1.810 PL 19.67 PF 0.3 88 22.0 0.0 52.7 0.0 2.2 120 FTG ET PE 0.0 84 22.0 0.0 53.0 0.0 0.007 TL 34.67 PV 0.0 Pipe: 21 28.1 1.810 PL 7.00 PF 0.2 84 22.0 0.0 53.0 0.0 3.5 120 FTG E PE 5.4 83 9.5 0.0 58.2 0.0 0.017 TL 12.00 PV 0.1 Pipe: 22 28.1 1.810 PL 9.00 PF 0.3 83 9.5 0.0 58.2 0.0 3.5 120 FTG T PE 0.0 82 9.5 0.0 57.8 0.0 0.017 TL 19.00 PV 0.1 Pipe: 23 14.5 1.810 PL 1.00 PF 0.1 85 9.5 0.0 57.9 0.0 1.8 120 FTG T PE 0.0 82 9.5 0.0 57.8 0.0 0.005 TL 11.00 PV 0.0 Pipe: 24 42.6 1.810 PL 13.25 PF 0.9 82 9.5 0.0 57.8 0.0 5.3 120 FTG T PE 0.0 87 9.5 0.0 57.0 0.0 0.037 TL 23.25 PV 0.2 Pipe: 25 -104.4 1.810 PL 12.00 PF 4.3 89 22.0 0.0 55.6 0.0 13.0 120 FTG T PE 5.2 6 10.0 0.0 65.1 0.0 0.194 TL 22.00 PV 1.1 Pipe: 26 FIXED PRESSURE LOSS DEVICE 5 10.0 0.0 78.1 0.0 13.0 psi, 104.4 gpm 6 10.0 0.0 65.1 0.0 Page 3 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 09/19/12 JOB TITLE: Basingdale2.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 -104.4 1.810 PL 2.00 PF 4.7 5 10.0 0.0 78.1 0.0 13.0 120 FTG ECB PE 0.4 4 9.0 0.0 83.2 0.0 0.194 TL 24.00 PV 1.1 Pipe: 28 FIXED PRESSURE LOSS DEVICE 3 9.0 0.0 96.2 0.0 13.0 psi, 104.4 gpm 4 9.0 0.0 83.2 0.0 Pipe: 29 -104.4 1.810 PL 1.00 PF 0.2 3 9.0 0.0 96.2 0.0 13.0 120 FTG ---- PE 0.4 2 8.0 0.0 96.8 0.0 0.194 TL 1.00 PV 1.1 Pipe: 30 -104.4 1.985 PL 100.00 PF 10.2 2 8.0 0.0 96.8 0.0 10.8 150 FTG ETG PE 7.4 1 25.0 SRCE 99.6 (N/A) 0.082 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 0.003 gpm and a maximum imbalance at any node of 0.078 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 19.4 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 BASINGDA.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 09/19/12 JOB TITLE: Basingdale2.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 " | 99.60 psi @ 104.4 gpm " 10+ " | 0 = Available Water Supply " | 118.39 psi @ 104.4 gpm " | " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) Page 5