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F13-0019 CALCS.pdf
SNOWBERR.TXT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 01/11/94 C:\CALL\SNOWBERR JOB TITLE: SnowberryEast.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 52.0 6.0 422.0 48. 5 104.1 38.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 104.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 104.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 10.0 SOURCE 38.2 104.1 2 1.0 - - - - 35.2 - - - 3 1.0 - - - - 81.2 - - - 4 2.0 - - - - 76.2 - - - 5 2.0 - - - - 63.2 - - - 6 8.4 - - - - 57.1 - - - 7 8.4 - - - - 54.8 - - - 8 8.4 - - - - 54.1 - - - 9 8.4 - - - - 53.3 - - - 10 8.4 - - - - 54.1 - - - 11 8.4 - - - - 53.8 - - - 12 24.6 - - - - 46.7 - - - 13 8.4 - - - - 52. 5 - - - 14 19.4 - - - - 47.3 - - - 15 19.4 - - - - 46.8 - - - 16 19.1 - - - - 46.0 - - - 17 19.4 - - - - 45.1 - - - 18 19.4 - - - - 47.1 - - - 19 19. 5 - - - - 46.9 - - - 20 29.6 - - - - 41.7 - - - 21 19.4 - - - - 48.1 - - - 22 29.6 - - - - 40.1 - - - 23 29.6 - - - - 40.1 - - - 24 29.6 - - - - 39.1 - - - 25 29.6 - - - - 37.3 - - - 26 29.6 - - - - 38.8 - - - 100 29.1 K= 4.30 35.4 25.6 101 29.1 K= 4.30 36.9 26.1 102 29.1 K= 4.30 36.4 25.9 103 29.1 K= 4.30 37.9 26. 5 Page 1 SNOWBERR.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 01/11/94 JOB TITLE: SnowberryEast.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 12. 50 PF 2.1 100 29.1 4.3 35.4 25.6 9.4 150 FTG E PE 0.2 25 29.6 0.0 37.3 0.0 0.132 TL 15. 52 Pv 0.6 Pipe: 2 -26.1 1.055 PL 12. 50 PF 2.1 101 29.1 4.3 36.9 26.1 9.6 150 FTG E PE 0.2 26 29.6 0.0 38.8 0.0 0.137 TL 15. 52 Pv 0.6 Pipe: 3 -25.9 1.055 PL 0. 50 PF 1.1 102 29.1 4.3 36.4 25.9 9. 5 150 FTG T PE 0.2 25 29.6 0.0 37.3 0.0 0.136 TL 8.06 Pv 0.6 Pipe: 4 -26. 5 1.055 PL 0. 50 PF 1.1 103 29.1 4.3 37.9 26. 5 9.7 150 FTG T PE 0.2 26 29.6 0.0 38.8 0.0 0.141 TL 8.06 Pv 0.6 Pipe: 5 -51. 5 1.055 PL 3.75 PF 1.8 25 29.6 0.0 37.3 0.0 18.9 150 FTG ---- PE 0.0 24 29.6 0.0 39.1 0.0 0.483 TL 3.75 Pv 2.4 Pipe: 6 -51. 5 1.810 PL 8.79 PF 1.0 24 29.6 0.0 39.1 0.0 6.4 120 FTG T PE 0.0 23 29.6 0.0 40.1 0.0 0.053 TL 18.79 Pv 0. 3 Pipe: 7 -52.6 1.810 PL 12. 50 PF 1.2 26 29.6 0.0 38.8 0.0 6.6 120 FTG T PE 0.0 22 29.6 0.0 40.1 0.0 0.055 TL 22. 50 Pv 0. 3 Pipe: 8 0.0 1.810 PL 11. 58 PF 0.0 23 29.6 0.0 40.1 0.0 0.0 120 FTG ---- PE 0.0 22 29.6 0.0 40.1 0.0 0.000 TL 11. 58 Pv 0.0 Pipe: 9 -52.6 1.810 PL 0. 50 PF 0.6 22 29.6 0.0 40.1 0.0 6.6 120 FTG T PE 4.4 17 19.4 0.0 45.1 0.0 0.055 TL 10. 50 Pv 0. 3 Pipe: 10 -52.6 1.810 PL 10.08 PF 0.8 17 19.4 0.0 45.1 0.0 6.6 120 FTG E PE 0.1 16 19.1 0.0 46.0 0.0 0.055 TL 15.08 Pv 0. 3 Pipe: 11 -51.6 1.810 PL 16.25 PF 1.6 23 29.6 0.0 40.1 0.0 6.4 120 FTG ET PE 0.0 20 29.6 0.0 41.7 0.0 0.053 TL 31.25 PV 0. 3 Pipe: 12 -51.6 1.810 PL 10.08 PF 0.8 20 29.6 0.0 41.7 0.0 6.4 120 FTG E PE 4.4 19 19. 5 0.0 46.9 0.0 0.053 TL 15.08 Pv 0.3 Pipe: 13 -52.6 1.810 PL 7.40 PF 0.9 16 19.1 0.0 46.0 0.0 6.6 120 FTG T PE 0.1 15 19.4 0.0 46.8 0.0 0.055 TL 17.40 PV 0. 3 Pipe: 14 -35.8 1.810 PL 2.42 PF 0. 5 15 19.4 0.0 46.8 0.0 4. 5 120 FTG ET PE 0.0 14 19.4 0.0 47.3 0.0 0.027 TL 17.42 Pv 0.1 Page 2 SNOWBERR.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 01/11/94 JOB TITLE: SnowberryEast.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: 15 -35.8 1.810 PL 10.08 PF 0.4 14 19.4 0.0 47.3 0.0 4. 5 120 FTG E PE 4.8 13 8.4 0.0 52. 5 0.0 0.027 TL 15.08 Pv 0.1 Pipe: 16 -16.7 1.810 PL 23.27 PF 0.2 15 19.4 0.0 46.8 0.0 2.1 120 FTG T PE 0.0 18 19.4 0.0 47.1 0.0 0.007 TL 33.27 Pv 0.0 Pipe: 17 -51.6 1.810 PL 2.33 PF 0.1 19 19. 5 0.0 46.9 0.0 6.4 120 FTG ---- PE 0.0 18 19.4 0.0 47.1 0.0 0.053 TL 2.33 Pv 0. 3 Pipe: 18 -68.3 1.810 PL 2.00 PF 1.1 18 19.4 0.0 47.1 0.0 8. 5 120 FTG T PE 0.0 21 19.4 0.0 48.1 0.0 0.089 TL 12.00 Pv 0. 5 Pipe: 19 -51.8 1.810 PL 3.42 PF 0.4 21 19.4 0.0 48.1 0.0 6. 5 120 FTG E PE 4.8 9 8.4 0.0 53.3 0.0 0.053 TL 8.42 Pv 0. 3 Pipe: 20 -51.8 1.810 PL 10.08 PF 0.8 9 8.4 0.0 53.3 0.0 6. 5 120 FTG E PE 0.0 8 8.4 0.0 54.1 0.0 0.053 TL 15.08 Pv 0. 3 Pipe: 21 -16.6 1.810 PL 52.09 PF 0.8 21 19.4 0.0 48.1 0.0 2.1 120 FTG 8E3T PE 2. 3 12 24.6 0.0 46.7 0.0 0.006 TL 122.09 Pv 0.0 Pipe: 22 -16.6 1.810 PL 15.17 PF 0.1 12 24.6 0.0 46.7 0.0 2.1 120 FTG E PE 7.0 11 8.4 0.0 53.8 0.0 0.006 TL 20.17 Pv 0.0 Pipe: 23 -16.6 1.810 PL 24.71 PF 0. 3 11 8.4 0.0 53.8 0.0 2.1 120 FTG E2T PE 0.0 10 8.4 0.0 54.1 0.0 0.006 TL 49.71 Pv 0.0 Pipe: 24 -35.8 1.810 PL 31.19 PF 1.6 13 8.4 0.0 52. 5 0.0 4. 5 120 FTG 3T PE 0.0 10 8.4 0.0 54.1 0.0 0.027 TL 61.19 Pv 0.1 Pipe: 25 -52.4 1.810 PL 1.67 PF 0.6 10 8.4 0.0 54.1 0.0 6. 5 120 FTG T PE 0.0 7 8.4 0.0 54.8 0.0 0.054 TL 11.67 PV 0. 3 Pipe: 26 -51.8 1.810 PL 1.71 PF 0.6 8 8.4 0.0 54.1 0.0 6. 5 120 FTG T PE 0.0 7 8.4 0.0 54.8 0.0 0.053 TL 11.71 PV 0. 3 Pipe: 27 -104.2 1.810 PL 7.08 PF 2. 3 7 8.4 0.0 54.8 0.0 13.0 120 FTG E PE 0.0 6 8.4 0.0 57.1 0.0 0.193 TL 12.08 PV 1.1 Pipe: 28 -104.2 1.810 PL 1.27 PF 3.3 6 8.4 0.0 57.1 0.0 13.0 120 FTG EC PE 2.8 5 2.0 0.0 63.2 0.0 0.193 TL 17.27 Pv 1.1 Page 3 SNOWBERR.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 01/11/94 JOB TITLE: SnowberryEast.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: 29 FIXED PRESSURE LOSS DEVICE 4 2.0 0.0 76.2 0.0 13.0 psi , 104.2 gpm 5 2.0 0.0 63.2 0.0 Pipe: 30 -104.2 1.810 PL 1. 50 PF 4. 5 4 2.0 0.0 76.2 0.0 13.0 120 FTG ECB PE 0.4 3 1.0 0.0 81.2 0.0 0.193 TL 23. 50 Pv 1.1 Pipe: 31 FIRE PUMP Rating: 105.0 gpm @ 46.0 psi 2 1.0 0.0 35.2 0.0 Avail . : 104.2 gpm @ 46.0 psi 3 1.0 0.0 81.2 0.0 Req'd. : 104.2 gpm @ 46.0 psi Pipe: 32 -104.1 1.985 PL 40.00 PF 6.9 2 1.0 0.0 35.2 0.0 10.8 120 FTG ETG PE 3.9 1 10.0 SRCE 38.2 (N/A) 0.123 TL 56.00 Pv 0.8 NOTES: (1) Calculations were performed by the HASS 5.7.0 computer program under license no. 4163187 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 0.075 gpm. (3) velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 18.9 ft/sec at pipe 5. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: SO HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G S D Ell Tee LngEll ChkVIV BfyVIV Gately 45Ell DPVIV Page 4 SNOWBERR.TXT g SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 01/11/94 JOB TITLE: SnowberryEast.txt WATER SUPPLY CURVE 60+ I I I 55+ I 50\ 10 1\ 1\ 45+ \ I \ I \ I \ P 40+ \ R IX \ E I \ S I \ S 35+ \ U I \ R I \ E I \ 30+ \ C I \ P I \ S I \ 125+ \ I \ I \ I \ 20+ \ I \ I \ I \ 15+ \ I \ I \ 10+ \ LEGEND " 1 X = Required water Supply\ " 1 38.19 psi @ 104.1 gpm* <-6.0 psi @ 422 gpm" 5+ Flow Test Point" 1 0 = Available water Supply " 1 48.54 psi @ 104.1 gpm " I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) Page 5