Loading...
HomeMy WebLinkAboutF13-0049 calcs CALC.TXT I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 11/03/13 C:\CALC\SNOWBER2 JOB TITLE: SNOWBER2.TXT WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRE55. PRESS. @ PRESS. @ DEMAND PRE55. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 52.0 6.0 422.0 48.3 107.6 36.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 107.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE O.O GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 107.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 10.0 SOURCE 36.6 107.6 2 1.0 - - - - 32.6 - - - 3 1.0 - - - - 70.6 - - - 4 2.0 - - - - 65.4 - - - 5 2.0 - - - - 52.4 - - - 6 8.4 - - - - 46.0 - - - 7 8.4 - - - - 44.3 - - - 8 8.4 - - - - 44.3 - - - 9 8.4 - - - - 44.3 - - - 10 23.6 - - - - 37.0 - - - 11 8.4 - - - - 43.9 - - - 12 24.1 - - - - 37.1 - - - 13 8.4 - - - - 43.8 - - - 14 8.4 - - - - 43.8 - - - 15 20.1 - - - - 38.7 - - - 16 8.4 - - - - 43. 5 - - - 17 23.7 - - - - 36.1 - - - 18 27.4 - - - - 34.4 - - - 19 13.4 - - - - 40.7 - - - 20 27.4 - - - - 34.4 - - - 21 13.4 - - - - 40.7 - - - 22 13.4 - - - - 40.4 - - - Z3 25.6 - - - - 34.9 - - - 24 13.4 - - - - 40.8 - - - 25 13.4 - - - - 40. 5 - - - 26 25.6 - - - - 34.9 - - - 27 25.6 - - - - 29.7 - - - 28 25.6 - - - - 33. 5 - - - 29 25.6 - - - - 33.6 - - - 30 25.6 - - - - 34.0 - - - 31 25.6 - - - - 34.8 - - - 32 27.6 - - - - 34.0 - - - 33 27.6 - - - - 34.3 - - - 34 27.6 - - - - 34.6 - - - Page 1 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 �ate: 11/03/13 JOB TITLE: SNOWBER2.TXT NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 25.1 - - - - 35.4 - - - 36 25.6 - - - - 33.2 - - - 100 25.1 K= 4.90 27.3 25.6 101 25.1 K= 4.90 32.2 27.8 102 25.1 K= 4.90 28.8 26.3 103 25.1 K= 4.90 32. 5 27.9 Page 2 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 �ate: 11/03/13 JOB TITLE: SNOWBER2.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 16. 50 PF 2.6 100 25.1 4.9 27.3 25.6 9.4 150 FTG E PE 0.2 27 25.6 0.0 29.7 0.0 0.132 TL 19. 52 Pv 0.6 Pipe: 2 -26.3 1.055 PL 0. 50 PF 1.1 102 25.1 4.9 28.8 26.3 9.6 150 FTG T PE 0.2 27 z5.6 0.0 29.7 0.0 0.139 TL 8.06 Pv 0.6 Pipe: 3 -51.9 1.055 PL 0. 50 PF 3.9 27 25.6 0.0 29.7 0.0 19.0 150 FTG T PE 0.0 29 25.6 0.0 33.6 0.0 0.488 TL 8.06 Pv 2.4 Pipe: 4 -27.8 1.055 PL 0. 50 PF 1.2 101 25.1 4.9 32.2 27.8 10.2 150 FTG T PE 0.2 36 25.6 0.0 33.2 0.0 0.154 TL 8.06 Pv 0.7 Pipe: 5 -27.8 1.810 PL 16.00 PF 0.3 36 25.6 0.0 33.2 0.0 3. 5 120 FTG ---- PE 0.0 28 25.6 0.0 33. 5 0.0 0.017 TL 16.00 Pv 0.1 Pipe: 6 -27.9 1.055 PL 0. 50 PF 1. 3 103 25.1 4.9 32. 5 27.9 10.2 150 FTG T PE 0.2 28 25.6 0.0 33. 5 0.0 0.155 TL 8.06 Pv 0.7 Pipe: 7 -55.7 1.810 PL 3.66 PF 0. 5 28 25.6 0.0 33. 5 0.0 6.9 120 FTG E PE 0.0 30 25.6 0.0 34.0 0.0 0.061 TL 8.66 Pv 0. 3 Pipe: 8 -51.9 1.810 PL 3. 50 PF 1. 3 29 25.6 0.0 33.6 0.0 6. 5 120 FTG 2T PE 0.0 31 25.6 0.0 34.8 0.0 0.053 TL 23. 50 Pv 0. 3 Pipe: 9 -28.0 1.810 PL 0. 50 PF 0.1 31 25.6 0.0 34.8 0.0 3. 5 120 FTG E PE 0.0 26 25.6 0.0 34.9 0.0 0.017 TL 5. 50 Pv 0.1 Pipe: 10 -28.0 1.810 PL 12.16 PF 0. 3 26 25.6 0.0 34.9 0.0 3. 5 120 FTG E PE 5. 3 25 13.4 0.0 40. 5 0.0 0.017 TL 17.16 Pv 0.1 Pipe: 11 -23.9 1.810 PL 8.75 PF 0. 3 31 25.6 0.0 34.8 0.0 3.0 120 FTG ET PE 0.9 33 27.6 0.0 34.3 0.0 0.013 TL 23.75 Pv 0.1 Pipe: 12 -55.7 1.810 PL 3. 50 PF 0.8 30 25.6 0.0 34.0 0.0 6.9 120 FTG T PE 0.9 32 27.6 0.0 34.0 0.0 0.061 TL 13. 50 Pv 0. 3 Pipe: 13 -23.6 1.810 PL 0. 50 PF 0.1 32 27.6 0.0 34.0 0.0 2.9 120 FTG E PE 0.9 23 25.6 0.0 34.9 0.0 0.012 TL 5. 50 Pv 0.1 Page 3 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 �ate: 11/03/13 JOB TITLE: SNOWBER2.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 -23.6 1.810 PL 12.16 PF 0.2 23 25.6 0.0 34.9 0.0 2.9 120 FTG E PE 5. 3 22 13.4 0.0 40.4 0.0 0.012 TL 17.16 PV 0.1 Pipe: 15 -32.1 1.810 PL 8.33 PF 0. 3 32 27.6 0.0 34.0 0.0 4.0 120 FTG E PE 0.1 18 27.4 0.0 34.4 0.0 0.022 TL 13.33 Pv 0.1 Pipe: 16 -19.2 1.810 PL 0.92 PF 0.0 18 27.4 0.0 34.4 0.0 2.4 120 FTG E PE 0.0 20 27.4 0.0 34.4 0.0 0.008 TL 5.92 PV 0.0 Pipe: 17 -19.2 1.810 PL 14.00 PF 0.2 20 27.4 0.0 34.4 0.0 2.4 120 FTG T PE 6.1 19 13.4 0.0 40.7 0.0 0.008 TL 24.00 PV 0.0 Pipe: 18 -12.9 1.810 PL 0. 50 PF 0.0 18 27.4 0.0 34.4 0.0 1.6 120 FTG ---- PE 1.0 35 25.1 0.0 35.4 0.0 0.004 TL 0. 50 Pv 0.0 Pipe: 19 -1.8 1.810 PL 12.21 PF 0.0 35 25.1 0.0 35.4 0.0 0.2 120 FTG ---- PE l.l 33 27.6 0.0 34.3 0.0 0.000 TL 12.21 Pv 0.0 Pipe: 20 -25.7 1.810 PL 12.92 PF 0. 3 33 27.6 0.0 34.3 0.0 3.2 120 FTG 2E PE 0.0 34 27.6 0.0 34.6 0.0 0.014 TL 22.92 Pv 0.1 Pipe: 21 -36.8 1.810 PL 1. 50 PF 0.6 34 27.6 0.0 34.6 0.0 4.6 120 FTG 2ET PE 1.7 10 23.6 0.0 37.0 0.0 0.028 TL 21. 50 Pv 0.1 Pipe: z2 -36.8 1.810 PL 15.16 PF 0.7 10 23.6 0.0 37.0 0.0 4.6 120 FTG T PE 6.6 9 8.4 0.0 44.3 0.0 0.028 TL 25.16 PV 0.1 Pipe: 23 11.2 1.810 PL 15.96 PF 0.2 34 27.6 0.0 34.6 0.0 1.4 120 FTG 3E2T PE 1.7 17 23.7 0.0 36.1 0.0 0.003 TL 50.96 Pv 0.0 Pipe: 24 11.2 1.810 PL 31.62 PF 0.2 17 23.7 0.0 36.1 0.0 1.4 120 FTG 3ET PE 0.6 35 25.1 0.0 35.4 0.0 0.003 TL 56.62 Pv 0.0 Pipe: 25 5.7 1.810 PL 15.60 PF 0.0 11 8.4 0.0 43.9 0.0 0.7 120 FTG E PE 6.8 12 24.1 0.0 37.1 0.0 0.001 TL 20.60 PV 0.0 Pipe: z6 5.7 1.810 PL 36.00 PF 0.1 12 24.1 0.0 37.1 0.0 0.7 120 FTG 5E PE 1.7 15 20.1 0.0 38.7 0.0 0.001 TL 61.00 Pv 0.0 Page 4 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 �ate: 11/03/13 JOB TITLE: SNOWBER2.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: Z7 5.7 1.810 PL 11.75 PF 0.0 15 20.1 0.0 38.7 0.0 0.7 120 FTG E PE 5.1 14 8.4 0.0 43.8 0.0 0.001 TL 16.75 PV 0.0 Pipe: 28 5.7 1.810 PL 14.75 PF 0.0 14 8.4 0.0 43.8 0.0 0.7 120 FTG ---- PE 0.0 13 8.4 0.0 43.8 0.0 0.001 TL 14.75 PV 0.0 Pipe: 29 -19.6 1.810 PL 11.46 PF 0.1 13 8.4 0.0 43.8 0.0 2.4 120 FTG ---- PE 0.0 11 8.4 0.0 43.9 0.0 0.009 TL 11.46 Pv 0.0 Pipe: 30 -25.3 1.810 PL 12.67 PF 0.4 11 8.4 0.0 43.9 0.0 3.2 120 FTG ET PE 0.0 8 8.4 0.0 44.3 0.0 0.014 TL 27.67 PV 0.1 Pipe: 31 -36.8 1.810 PL 0. 50 PF 0.0 9 8.4 0.0 44.3 0.0 4.6 120 FTG ---- PE 0.0 8 8.4 0.0 44.3 0.0 0.028 TL 0. 50 PV 0.1 Pipe: 32 25.3 1.810 PL 17.79 PF 0. 3 13 8.4 0.0 43.8 0.0 3.2 120 FTG ---- PE 0.0 16 8.4 0.0 43. 5 0.0 0.014 TL 17.79 PV 0.1 Pipe: 33 25.3 1.810 PL 33.00 PF 0.7 16 8.4 0.0 43. 5 0.0 3.2 120 FTG 3E PE 2.2 19 13.4 0.0 40.7 0.0 0.014 TL 48.00 PV 0.1 Pipe: 34 6.1 1.810 PL 3.00 PF 0.0 19 13.4 0.0 40.7 0.0 0.8 120 FTG E PE 0.0 Z1 13.4 0.0 40.7 0.0 0.001 TL 8.00 PV 0.0 Pipe: 35 -23.6 1.810 PL 5.62 PF 0.3 22 13.4 0.0 40.4 0.0 2.9 120 FTG ET PE 0.0 21 13.4 0.0 40.7 0.0 0.012 TL 20.62 PV 0.1 Pipe: 36 -17. 5 1.810 PL 13.73 PF 0.1 21 13.4 0.0 40.7 0.0 2.2 120 FTG ---- PE 0.0 24 13.4 0.0 40.8 0.0 0.007 TL 13.73 Pv 0.0 Pipe: 37 -28.0 1.810 PL 5.00 PF 0. 3 25 13.4 0.0 40. 5 0.0 3. 5 120 FTG T PE 0.0 24 13.4 0.0 40.8 0.0 0.017 TL 15.00 PV 0.1 Pipe: 38 -45. 5 1.810 PL 13. 50 PF 1.4 24 13.4 0.0 40.8 0.0 5.7 120 FTG 2ET PE 2.2 7 8.4 0.0 44.3 0.0 0.042 TL 33. 50 PV 0.2 Pipe: 39 -62.1 1.810 PL 1.00 PF 0.1 8 8.4 0.0 44.3 0.0 7.7 120 FTG ---- PE 0.0 7 8.4 0.0 44.3 0.0 0.074 TL 1.00 PV 0.4 Page 5 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 �ate: 11/03/13 JOB TITLE: SNOWBER2.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: 40 -107.6 1.810 PL 3.30 PF 1.7 7 8.4 0.0 44.3 0.0 13.4 120 FTG E PE 0.0 6 8.4 0.0 46.0 0.0 0.205 TL 8.30 Pv 1.2 Pipe: 41 -107.6 1.810 PL 1.27 PF 3. 5 6 8.4 0.0 46.0 0.0 13.4 120 FTG EC PE 2.8 5 z.0 0.0 52.4 0.0 0.205 TL 17.27 Pv 1.2 Pipe: 42 FIXED PRESSURE LOSS DEVICE 4 2.0 0.0 65.4 0.0 13.0 psi , 107.6 gpm 5 2.0 0.0 52.4 0.0 Pipe: 43 -107.6 1.810 PL 1. 50 PF 4.8 4 2.0 0.0 65.4 0.0 13.4 120 FTG ECB PE 0.4 3 1.0 0.0 70.6 0.0 0.205 TL 23. 50 Pv 1.2 Pipe: 44 FIRE PUMP Rating: 110.0 gpm @ 38.0 psi 2 1.0 0.0 32.6 0.0 Avail . : 107.6 gpm @ 38.0 psi 3 1.0 0.0 70.6 0.0 Req'd. : 107.6 gpm @ 38.0 psi Pipe: 45 -107.6 1.958 PL 40.00 PF 7.8 2 1.0 0.0 32.6 0.0 11. 5 120 FTG ETG PE 3.9 1 10.0 SRCE 36.6 (N/A) 0.140 TL 56.00 Pv 0.9 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 0.001 gpm and a maximum imbalance at any node of 0.042 gpm. (3) velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 19.0 ft/sec at pipe 3. Page 6 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 �ate: 11/03/13 JOB TITLE: SNOWBER2.TXT (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting �engths in Feet (i n) E T L C B G S D E11 Tee �ngEll Chkvlv Bfyvlv Gatvlv 45E11 oPVlv Page 7 CALC.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 �ate: 11/03/13 JOB TITLE: SNOWBER2.TXT WATER SUPPLY CURVE 60+ I I I 55+ I \ 50\ lo I\ I\ 45+ \ I \ I \ I \ P 40+ \ R I \ E I \ s Ix � S 35+ \ u I \ R I \ E I \ 30+ \ C I \ P I \ s I \ I 25+ \ ) I \ I \ I \ 20+ \ I \ I \ I \ 15+ \ I \ I \ 1______________________________\ 10+ \ LEGEND �� � � �� � X = Required Water Supply\ " � 36. 56 psi @ 107.6 gpm�° <-6.0 psi @ 422 gpm" Page 8