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HomeMy WebLinkAboutF14-0004 calcs BUFFEHRC-2 Z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 02/18/14 C:\BUFFEHRC JOB TITLE: BUFFERCREEK.TXT WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRE55. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 100.0 22.0 789.0 98.0 107.7 66.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 107.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 107.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 5.0 SOURCE 66.6 107.7 100 20.8 K= 4.90 31.4 27.4 101 20.8 K= 4.90 27.3 25.6 102 23. 5 K= 4.90 33.3 28.3 103 23. 5 K= 4.90 28.9 26.3 2 1.0 - - - - 59.7 - - - 3 1.0 - - - - 105.0 - - - 4 3.0 - - - - 94.9 - - - 5 3.0 - - - - 79.9 - - - 6 8.8 - - - - 68.8 - - - 7 8.8 - - - - 58.7 - - - 8 8.8 - - - - 50.1 - - - 9 21.2 - - - - 40.6 - - - 10 8.8 - - - - 53.8 - - - 11 8.8 - - - - 53.2 - - - 12 20.6 - - - - 46.9 - - - 13 8.8 - - - - 52.6 - - - 14 23.2 - - - - 45.7 - - - 15 25.2 - - - - 43.7 - - - 16 23.6 - - - - 38.2 - - - 17 24. 5 - - - - 36.4 - - - 18 24.0 - - - - 34.4 - - - 19 24.0 - - - - 29.8 - - - 20 8.8 - - - - 53.0 - - - 21 8.8 - - - - 53.0 - - - 22 23.6 - - - - 39.4 - - - 23 8.8 - - - - 56.1 - - - 24 8.8 - - - - 60.4 - - - 25 8.8 - - - - 53.3 - - - 26 8.8 - - - - 53.0 - - - 27 8.8 - - - - 52.9 - - - 28 8.8 - - - - 53.0 - - - Page 1 BUFFEHRC-2 � SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 �ate: 02/18/14 JOB TITLE: BUFFERCREEK.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 -27.4 1.055 PL 14.38 PF 4.4 100 20.8 4.9 31.4 27.4 10.1 150 FTG 5E PE 1.4 18 24.0 0.0 34.4 0.0 0.150 TL 29.49 PV 0.7 Pipe: 2 -25.6 1.055 PL 14.38 PF 3.9 101 20.8 4.9 27.3 25.6 9.4 150 FTG 5E PE 1.4 19 24.0 0.0 29.8 0.0 0.132 TL 29.49 Pv 0.6 Pipe: 3 -28.3 1.055 PL 0. 50 PF 1. 3 102 23. 5 4.9 33.3 28.3 10.4 150 FTG T PE 0.2 18 24.0 0.0 34.4 0.0 0.159 TL 8.06 PV 0.7 Pipe: 4 -26.3 1.055 PL 0. 50 PF 1.1 103 23. 5 4.9 28.9 26.3 9.7 150 FTG T PE 0.2 19 24.0 0.0 29.8 0.0 0.139 TL 8.06 Pv 0.6 Pipe: 5 -51.9 1.055 PL 9.29 PF 8.2 19 24.0 0.0 29.8 0.0 19.1 150 FTG T PE 0.2 16 23.6 0.0 38.2 0.0 0.490 TL 16.85 Pv 2.4 Pipe: 6 19.2 1.055 PL 15.96 PF 1. 5 16 23.6 0.0 38.2 0.0 7.1 150 FTG E PE 0.4 17 24. 5 0.0 36.4 0.0 0.078 TL 18.98 Pv 0. 3 Pipe: 7 -55.7 1.055 PL 3.88 PF 2.2 18 24.0 0.0 34.4 0.0 20. 5 150 FTG ---- PE 0.2 17 24. 5 0.0 36.4 0.0 0. 558 TL 3.88 PV 2.8 Pipe: 8 -36. 5 1.055 PL 0. 50 PF 2.8 17 24. 5 0.0 36.4 0.0 13.4 150 FTG ET PE 1.4 9 21.2 0.0 40.6 0.0 0.255 TL 11.08 PV 1.2 Pipe: 9 -36. 5 1.055 PL 12.92 PF 4.1 9 21.2 0.0 40.6 0.0 13.4 150 FTG E PE 5.4 8 8.8 0.0 50.1 0.0 0.255 TL 15.94 PV 1.2 Pipe: 10 -71.2 1.055 PL 1.38 PF 1.2 16 23.6 0.0 38.2 0.0 26.1 150 FTG ---- PE 0.0 22 23.6 0.0 39.4 0.0 0.877 TL 1.38 Pv 4.6 Pipe: 11 -46.3 1.055 PL 15.25 PF 10.2 22 23.6 0.0 39.4 0.0 17.0 150 FTG ET PE 6.4 23 8.8 0.0 56.1 0.0 0.396 TL 25.83 Pv 1.9 Pipe: 12 -24.8 1.055 PL 33.42 PF 4.9 22 23.6 0.0 39.4 0.0 9.1 150 FTG 2E PE 0.7 15 25.2 0.0 43.7 0.0 0.125 TL 39.46 Pv 0.6 Pipe: 13 -14.3 1.055 PL 10.92 PF 1.2 15 25.2 0.0 43.7 0.0 5.3 150 FTG 2T PE 2.0 12 20.6 0.0 46.9 0.0 0.045 TL 26.03 Pv 0.2 Page 2 BUFFEHRC-2 � SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 �ate: 02/18/14 JOB TITLE: BUFFERCREEK.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 -14.3 1.055 PL 12.08 PF 1.2 12 20.6 0.0 46.9 0.0 5.3 150 FTG 2T PE 5.1 11 8.8 0.0 53.2 0.0 0.045 TL 27.19 PV 0.2 Pipe: 15 -10. 5 1.055 PL 30.29 PF 1.2 15 25.2 0.0 43.7 0.0 3.9 150 FTG 3ET PE 0.9 14 23.2 0.0 45.7 0.0 0.025 TL 46.91 PV 0.1 Pipe: 16 -10. 5 1.055 PL 14.42 PF 0.6 14 23.2 0.0 45.7 0.0 3.9 150 FTG ET PE 6.2 13 8.8 0.0 52.6 0.0 0.025 TL 25.00 PV 0.1 Pipe: 17 -10. 5 1.055 PL 4.21 PF 0. 3 13 8.8 0.0 52.6 0.0 3.9 150 FTG T PE 0.0 27 8.8 0.0 52.9 0.0 0.025 TL 11.77 PV 0.1 Pipe: 18 -5. 5 1.055 PL 7.42 PF 0.1 27 8.8 0.0 52.9 0.0 2.0 150 FTG T PE 0.0 20 8.8 0.0 53.0 0.0 0.008 TL 14.98 Pv 0.0 Pipe: 19 -5.0 1.055 PL 16.63 PF 0.1 27 8.8 0.0 52.9 0.0 1.8 150 FTG ---- PE 0.0 26 8.8 0.0 53.0 0.0 0.006 TL 16.63 Pv 0.0 Pipe: 20 -0.6 1.055 PL 49.17 PF 0.0 26 8.8 0.0 53.0 0.0 0.2 150 FTG E2T PE 0.0 28 8.8 0.0 53.0 0.0 0.000 TL 67.30 Pv 0.0 Pipe: 21 1.8 1.055 PL 2.92 PF 0.0 20 8.8 0.0 53.0 0.0 0.6 150 FTG ---- PE 0.0 28 8.8 0.0 53.0 0.0 0.001 TL 2.92 Pv 0.0 Pipe: 22 -4.4 1.055 PL 49.79 PF 0. 3 26 8.8 0.0 53.0 0.0 1.6 150 FTG 2E PE 0.0 25 8.8 0.0 53.3 0.0 0.005 TL 55.83 PV 0.0 Pipe: 23 -7.3 1.055 PL 13.75 PF 0. 3 20 8.8 0.0 53.0 0.0 2.7 150 FTG T PE 0.0 25 8.8 0.0 53.3 0.0 0.013 TL 21.31 Pv 0.0 Pipe: 24 -11.7 1.055 PL 12.29 PF 0. 5 25 8.8 0.0 53.3 0.0 4.3 150 FTG E PE 0.0 10 8.8 0.0 53.8 0.0 0.031 TL 15.31 Pv 0.1 Pipe: 25 -14.3 1.055 PL 13.04 PF 0.6 11 8.8 0.0 53.2 0.0 5.3 150 FTG ---- PE 0.0 10 8.8 0.0 53.8 0.0 0.045 TL 13.04 PV 0.2 Pipe: 26 -26.1 1.055 PL 18.88 PF 4.9 10 8.8 0.0 53.8 0.0 9.6 120 FTG T PE 0.0 7 8.8 0.0 58.7 0.0 0.206 TL 23.88 Pv 0.6 Page 3 BUFFEHRC-2 � SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 �ate: 02/18/14 JOB TITLE: BUFFERCREEK.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 1.2 1.055 PL 73. 54 PF 0.1 28 8.8 0.0 53.0 0.0 0.4 120 FTG 5ET PE 0.0 21 8.8 0.0 53.0 0.0 0.001 TL 88. 54 PV 0.0 Pipe: 28 -36. 5 1.055 PL 2. 58 PF 2.9 8 8.8 0.0 50.1 0.0 13.4 120 FTG T PE 0.0 21 8.8 0.0 53.0 0.0 0.385 TL 7. 58 PV 1.2 Pipe: 29 -35.3 1.055 PL 20.96 PF 5.7 21 8.8 0.0 53.0 0.0 13.0 150 FTG E PE 0.0 7 8.8 0.0 58.7 0.0 0.240 TL 23.98 PV l.l Pipe: 30 -61.3 1. 527 PL 3. 54 PF 1.7 7 8.8 0.0 58.7 0.0 10.7 150 FTG T PE 0.0 24 8.8 0.0 60.4 0.0 0.110 TL 15.63 Pv 0.8 Pipe: 31 -46.3 1.055 PL 3.42 PF 4. 3 23 8.8 0.0 56.1 0.0 17.0 150 FTG T PE 0.0 24 8.8 0.0 60.4 0.0 0.396 TL 10.98 Pv 1.9 Pipe: 32 -107.7 1. 527 PL 8. 58 PF 8. 3 24 8.8 0.0 60.4 0.0 18.9 150 FTG ET PE 0.0 6 8.8 0.0 68.8 0.0 0.312 TL 26.71 Pv 2.4 Pipe: 33 -107.7 1. 527 PL 8.00 PF 8.6 6 8.8 0.0 68.8 0.0 18.9 150 FTG EC PE 2. 5 5 3.0 0.0 79.9 0.0 0.312 TL 27.64 Pv 2.4 Pipe: 34 FIXED PRESSURE LOSS DEVICE 4 3.0 0.0 94.9 0.0 15.0 psi , 107.7 gpm 5 3.0 0.0 79.9 0.0 Pipe: 35 -107.7 1. 527 PL 1.00 PF 9. 3 4 3.0 0.0 94.9 0.0 18.9 150 FTG ECB PE 0.9 3 1.0 0.0 105.0 0.0 0.312 TL 29.71 Pv 2.4 Pipe: 36 FIRE PUMP Rating: 110.0 gpm @ 44.0 psi 2 1.0 0.0 59.7 0.0 Avail . : 107.7 gpm @ 45.3 psi 3 1.0 0.0 105.0 0.0 Req'd. : 107.7 gpm @ 45.3 psi user �efined Pump Curve: gpm psi gpm psi 10.0 60.6 120.0 41.6 40.0 58.9 145.0 31.2 80.0 53.7 Pipe: 37 -107.7 1.985 PL 75.00 PF 8.6 2 1.0 0.0 59.7 0.0 11.2 150 FTG ETG PE 1.7 1 5.0 SRCE 66.6 (N/A) 0.087 TL 99.18 PV 0.8 Page 4 BUFFEHRC-2 � SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 �ate: 02/18/14 JOB TITLE: BUFFERCREEK.TXT NOTES: (1) Calculations were performed by the HASS 5.7.0 computer program under license no. 4167187 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 0.004 gpm and a maximum imbalance at any node of 0.118 gpm. (3) velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 26.1 ft/sec at pipe 10. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: 540 HWC: 120 �iameter Equivalent Fitting �engths in Feet (i n) E T L C B G S D E11 Tee LngEll ChkVlv BfyVlv GatVlv 45E11 DPVIv Page 5 BUFFEHRC-2 � SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 �ate: 02/18/14 JOB TITLE: BUFFERCREEK.TXT WATER SUPPLY CURVE 120+ I I I 110+ I I I ioo-�� Io\ I \\ I \ 90+ \ I \\ I \ I \ P 80+ �� R I \ E I \ s I \\ s 70+ \ u Ix � R I \\ E I \ 60+ �\ C I \ P I \ s I \\ I 50+ \ ) I \ I \\ I \ 40+ \ I \\ I \ I \ 30+ �� I \ I \ 1______________________________ �� <-22.0 psi @ 789 gpm 20+ LEGEND �� Flow Test Point I �� � x = ►zequired water Supply " � 66. 56 psi @ 107.7 gpm " 10+ " � 0 = Available water supply " � 98.04 psi @ 107.7 gpm " I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) � Page 6