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HomeMy WebLinkAboutB24-2812 HYDRAULIC CALCS Hydraulic Calculations Project Information Project Name: Continental Athletics Supply Date 09/17/24 Address: 627 Ohio Street File # 33217 Gridley, CA Index 202 Calculation Area: Remote Area Design Criteria Occupancy Classification: Storage Construction ❑ Combustible ® Non Combustible Density: .40 gpm per sq. ft. Area of Operation: 2,000 sq. ft. 4z,So ok1�� P � Number of Sprinklers Calculated: 23 heads 4 � 22 f:i ran Hose Allowance Rack Allowance 0 gpm inside 0 gpm 0,1 500 gpm outside ''0 coQ- Water Supply Sprinklers Static Pressure: 62 psi Make: Tyco Residual Pressure: 55 psi @ 1,150 gpm flowing Size: K=11.2 Temp: 286° Calculation Summary Total Sprinkler Water Flow: 862.3 gpm Flow& Pressure: (at base of riser): 832.3 gpm @ 34.1 psi (at city connection): 1362.3 gpm @ 45.4 psi Notes: SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) S 62 . 0 55.0 1150. 0 52 .4 1362.3 45. 4 Available pressure is 7 .0 psi (13%) greater than required pressure. AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1362.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 862.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.0 - - - - 14.7 - - - 1A 19.3 K=11.20 12.5 39. 6 1B 19.7 - - - - 12.5 - - - 2 20.7 K=11.20 11.2 37.4 3 22 .2 K=11.20 10.4 36. 1 4 23. 6 K=11.20 9.8 35. 0 5 23. 6 K=11.20 9.8 35. 1 5A 22 .2 K=11.20 10.7 36. 6 5B 20.7 K=11.20 11. 9 38.7 6 18.0 - - - - 17.5 - - - 7 18.0 - - - - 14.8 - - - 7A 19.3 K=11.20 12.5 39. 6 7B 19.7 - - - - 12.5 - - - 8 20.7 K=11.20 11.2 37.5 9 22 .2 K=11.20 10.4 36. 1 10 23. 6 K=11.20 9.8 35. 1 11 23. 6 K=11.20 9. 9 35.2 11A 22 .2 K=11.20 10.7 36.7 11B 20.7 K=11.20 12.0 38. 8 12 18.0 - - - - 17. 6 - - - 13 18.0 - - - - 14. 9 - - - 13A 19.3 K=11.20 12. 6 39. 8 13B 19.7 - - - - 12.7 - - - 14 20.7 K=11.20 11.3 37.7 15 22 .2 K=11.20 10.5 36.3 16 23. 6 K=11.20 9. 9 35.3 17 23. 6 K=11.20 10.0 35.4 17A 22 .2 K=11.20 10.8 36. 9 17B 20.7 K=11.20 12.1 39. 0 18 18.0 - - - - 17.7 - - - 19 18.0 - - - - 15.2 - - - 19A 19.3 K=11.20 14.4 42 .5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 19B 19.7 - - - - 14.4 - - - 19C 20.7 K=11.20 14 .1 42. 1 20 18.0 - - - - 18.1 - - - 21 18.0 - - - - 15.5 - - - 22 18.0 - - - - 18. 6 - - - 23 18.0 - - - - 15.7 - - - 24 18.0 - - - - 19.2 - - - 25 18.0 - - - - 15.8 - - - 26 18.0 - - - - 19. 9 - - - 27 18.0 - - - - 15. 9 - - - 28 18.0 - - - - 20.8 - - - 29 18.0 - - - - 16.0 - - - 30 18.0 - - - - 24 .8 - - - 31 18.0 - - - - 24 . 9 - - - TR 18.0 - - - - 25.3 - - - BR 2 .0 - - - - 34 .1 - - - PD 2 .0 - - - - 36.2 - - - PS 2 .0 - - - - 0 .4 - - - UG 0.5 - - - - 2.0 - - - RP1 2 .0 - - - - 2.4 - - - RP2 2 .0 - - - - 14.4 - - - 39 -3.0 - - - - 17. 9 - - - 100 -3.0 - - - - 22.0 - - - 101 -3.0 HOSE STREAM 32 .8 500.0 102 -3.0 - - - - 33. 6 - - - 103 -3.0 - - - - 46.4 - - - 104 -3.0 - - - - 36.2 - - - 105 -3.0 - - - - 36. 9 - - - 106 -3.0 - - - - 39. 9 - - - 107 -3.0 - - - - 46. 6 - - - S 0.0 SOURCE 45.4 1362.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 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) FL/FT (PSI) Pipe: 1 120 .3 2.203 PL 1. 67 PF 1 .5 1 18.0 0.0 14 .7 0 .0 10 .1 120 FTG T PE -0 .7 1B 19.7 0.0 12 .5 0 .0 0.097 TL 15.27 PV Pipe: 2 -39. 6 2.203 PL 2. 63 PF 0 .2 lA 19.3 11.2 12 .5 39. 6 3.3 120 FTG T PE -0 .2 1B 19.7 0.0 12 .5 0 .0 0.012 TL 16.23 PV Pipe: 3 80 .7 2.203 PL 6.25 PF 0 . 9 1B 19.7 0 .0 12 .5 0 .0 6.8 120 FTG T PE -0 .4 2 20.7 11 .2 11.2 37 .4 0.046 TL 19. 85 PV Pipe: 4 43.3 2.203 PL 8. 88 PF 0 .1 2 20.7 11 .2 11.2 37 .4 3. 6 120 FTG ---- PE -0 . 6 3 22 .2 11 .2 10.4 36.1 0.015 TL 8. 88 PV Pipe: 5 7 .2 2.203 PL 8. 88 PF 0 .0 3 22 .2 11 .2 10.4 36. 1 0 . 6 120 FTG ---- PE -0 . 6 4 23. 6 11 .2 9. 8 35.0 0.001 TL 8. 88 PV Pipe: 6 -27 .8 2.203 PL 8. 88 PF 0 .1 4 23. 6 11 .2 9. 8 35.0 2 .3 120 FTG ---- PE 0 .0 5 23. 6 11 .2 9. 8 35.1 0.006 TL 8. 88 PV Pipe: 7 -62 . 9 2.203 PL 8. 88 PF 0 .3 5 23. 6 11 .2 9. 8 35.1 5.3 120 FTG ---- PE 0 . 6 5A 22 .2 11 .2 10.7 36. 6 0.029 TL 8. 88 PV Pipe: 8 -99.5 2.203 PL 8. 88 PF 0 . 6 5A 22 .2 11.2 10.7 36. 6 8 .4 120 FTG ---- PE 0 . 6 5B 20.7 11.2 11. 9 38 .7 0.068 TL 8. 88 PV Pipe: 9 -138 .2 2.203 PL 7. 92 PF 4 .4 5B 20.7 11 .2 11. 9 38 .7 11 . 6 120 FTG 2T PE 1 .2 6 18. 0 0 . 0 17 .5 0 .0 0.125 TL 35. 12 PV Pipe: 10 120 .5 2.203 PL 1. 67 PF 1 .5 7 18.0 0.0 14 . 8 0 .0 10 .1 120 FTG T PE -0 .7 7B 19.7 0.0 12.5 0 .0 0.097 TL 15.27 PV Pipe: 11 -39. 6 2.203 PL 2. 63 PF 0 .2 7A 19.3 11 .2 12 .5 39. 6 3.3 120 FTG T PE -0 .2 7B 19.7 0 .0 12 .5 0 .0 0.012 TL 16.23 PV Pipe: 12 80 .8 2.203 PL 6.25 PF 0 . 9 7B 19.7 0.0 12.5 0 .0 6.8 120 FTG T PE -0 .4 8 20.7 11.2 11.2 37 .5 0.046 TL 19. 85 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 43.3 2.203 PL 8. 88 PF 0 .1 8 20.7 11 .2 11.2 37 .5 3. 6 120 FTG ---- PE -0 . 6 9 22 .2 11 .2 10.4 36.1 0.015 TL 8. 88 PV Pipe: 14 7 .2 2.203 PL 8. 88 PF 0 .0 9 22 .2 11 .2 10.4 36.1 0 . 6 120 FTG ---- PE -0 . 6 10 23. 6 11 .2 9. 8 35.1 0.001 TL 8. 88 PV Pipe: 15 -27 . 9 2.203 PL 8. 88 PF 0 .1 10 23. 6 11 .2 9. 8 35.1 2 .3 120 FTG ---- PE 0 .0 11 23. 6 11 .2 9. 9 35.2 0.006 TL 8. 88 PV Pipe: 16 -63.0 2.203 PL 8. 88 PF 0 .3 11 23. 6 11.2 9. 9 35.2 5.3 120 FTG ---- PE 0 . 6 11A 22 .2 11.2 10.7 36.7 0.029 TL 8. 88 PV Pipe: 17 -99.7 2.203 PL 8. 88 PF 0 . 6 11A 22 .2 11 .2 10.7 36.7 8 .4 120 FTG ---- PE 0 . 6 11B 20.7 11 .2 12.0 38 .8 0.068 TL 8. 88 PV Pipe: 18 -138 .5 2.203 PL 7. 92 PF 4 .4 11B 20.7 11 .2 12. 0 38 .8 11 .7 120 FTG 2T PE 1 .2 12 18.0 0.0 17. 6 0 .0 0.126 TL 35. 12 PV Pipe: 19 121 .0 2.203 PL 1. 67 PF 1 .5 13 18.0 0 . 0 14 . 9 0 .0 10 .2 120 FTG T PE -0 .7 13B 19.7 0 . 0 12.7 0 .0 0.098 TL 15.27 PV Pipe: 20 -39.8 2.203 PL 2. 63 PF 0 .2 13A 19.3 11 .2 12. 6 39.8 3.4 120 FTG T PE -0 .2 13B 19.7 0 .0 12.7 0 .0 0.013 TL 16.23 PV Pipe: 21 81 .2 2.203 PL 6.25 PF 0 . 9 13B 19.7 0 .0 12 .7 0 .0 6.8 120 FTG T PE -0 .4 14 20.7 11 .2 11.3 37 .7 0.047 TL 19. 85 PV Pipe: 22 43 . 5 2.203 PL 8. 88 PF 0 .1 14 20.7 11 .2 11.3 37 .7 3 . 7 120 FTG ---- PE -0 . 6 15 22 .2 11 .2 10.5 36.3 0.015 TL 8. 88 PV Pipe: 23 7 .2 2.203 PL 8. 88 PF 0 .0 15 22 .2 11 .2 10 .5 36.3 0 . 6 120 FTG ---- PE -0 . 6 16 23. 6 11 .2 9. 9 35.3 0.001 TL 8. 88 PV Pipe: 24 -28 .1 2.203 PL 8. 88 PF 0 .1 16 23. 6 11.2 9. 9 35.3 2 .4 120 FTG ---- PE 0 .0 17 23. 6 11.2 10. 0 35.4 0.007 TL 8. 88 PV Pipe: 25 -63.4 2.203 PL 8. 88 PF 0 .3 17 23. 6 11.2 10. 0 35.4 5.3 120 FTG ---- PE 0 . 6 17A 22 .2 11.2 10. 8 36. 9 0.030 TL 8. 88 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 -100 .3 2.203 PL 8. 88 PF 0 . 6 17A 22 .2 11 .2 10. 8 36. 9 8 .4 120 FTG ---- PE 0 . 6 17B 20.7 11 .2 12. 1 39.0 0.069 TL 8. 88 PV Pipe: 27 -139.3 2.203 PL 7. 92 PF 4 .5 17B 20.7 11 .2 12. 1 39.0 11 .7 120 FTG 2T PE 1 .2 18 18.0 0 .0 17 .7 0 .0 0.127 TL 35. 12 PV Pipe: 28 15.2 2.203 PL 1. 67 PF 0 .0 19 18.0 0 . 0 15.2 0 .0 1 .3 120 FTG T PE -0 .7 19B 19.7 0 . 0 14 . 4 0 .0 0.002 TL 15.27 PV Pipe: 29 -42 .5 2.203 PL 2. 63 PF 0 .2 19A 19.3 11 .2 14.4 42 .5 3. 6 120 FTG T PE -0 .2 19B 19.7 0.0 14.4 0 .0 0.014 TL 16.23 PV Pipe: 30 -27 .2 2.203 PL 6.25 PF 0 .1 19B 19.7 0.0 14 . 4 0 .0 2 .3 120 FTG T PE -0 .4 19C 20.7 11 .2 14 . 1 42 . 1 0.006 TL 19. 85 PV Pipe: 31 -69. 3 2.203 PL 53. 96 PF 2 .8 19C 20.7 11 .2 14. 1 42 . 1 5 . 8 120 FTG 2T PE 1 .2 20 18.0 0.0 18. 1 0 .0 0.035 TL 81. 16 PV Pipe: 32 -60 .1 2.203 PL 61.21 PF 3 . 1 21 18.0 0 . 0 15.5 0 .0 5.1 120 FTG 4T PE 0 .0 22 18.0 0 . 0 18. 6 0 .0 0.027 TL 115. 61 PV Pipe: 33 -64 .0 2.203 PL 61.21 PF 3 .5 23 18.0 0 . 0 15.7 0 .0 5.4 120 FTG 4T PE 0 .0 24 18.0 0 . 0 19.2 0 .0 0.030 TL 115. 61 PV Pipe: 34 -69.7 2.203 PL 61.21 PF 4 . 1 25 18.0 0 . 0 15 . 8 0 .0 5. 9 120 FTG 4T PE 0 .0 26 18.0 0 . 0 19. 9 0 .0 0.035 TL 115. 61 PV Pipe: 35 -77 .0 2.203 PL 61.21 PF 4 . 9 27 18.0 0 . 0 15. 9 0 .0 6.5 120 FTG 4T PE 0 .0 28 18.0 0 . 0 20. 8 0 .0 0.042 TL 115. 61 PV Pipe: 36 -106.1 2.203 PL 61.21 PF 8 . 9 29 18.0 0 . 0 16. 0 0 .0 8 . 9 120 FTG 4T PE 0 .0 30 18.0 0 . 0 24 . 8 0 .0 0.077 TL 115. 61 PV Pipe: 37 -120 .3 4.310 PL 10. 00 PF 0 .0 1 18.0 0.0 14.7 0 .0 2 . 6 120 FTG ---- PE 0 .0 7 18.0 0.0 14. 8 0 .0 0.004 TL 10. 00 PV Pipe: 38 -240 .8 4.310 PL 10. 00 PF 0 .1 7 18.0 0.0 14 . 8 0 .0 5.3 120 FTG ---- PE 0 .0 13 18.0 0.0 14 . 9 0 .0 0.013 TL 10. 00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -361 .8 4.310 PL 10. 00 PF 0 .3 13 18.0 0 . 0 14 . 9 0 .0 8 .0 120 FTG ---- PE 0 .0 19 18.0 0 . 0 15.2 0 .0 0.028 TL 10. 00 PV Pipe: 40 -377 .0 4.310 PL 10. 00 PF 0 .3 19 18.0 0 . 0 15.2 0 .0 8 .3 120 FTG ---- PE 0 .0 21 18.0 0 . 0 15.5 0 .0 0.031 TL 10. 00 PV Pipe: 41 -316. 9 4.310 PL 10. 00 PF 0 .2 21 18.0 0 . 0 15.5 0 .0 7 .0 120 FTG ---- PE 0 .0 23 18.0 0 . 0 15. 7 0 .0 0.022 TL 10. 00 PV Pipe: 42 -252 . 9 4.310 PL 10. 00 PF 0 .1 23 18.0 0.0 15.7 0 .0 5. 6 120 FTG ---- PE 0 .0 25 18.0 0.0 15. 8 0 .0 0.015 TL 10. 00 PV Pipe: 43 -183.1 4.310 PL 10. 00 PF 0 .1 25 18.0 0.0 15. 8 0 .0 4 .0 120 FTG ---- PE 0 .0 27 18.0 0.0 15. 9 0 .0 0.008 TL 10. 00 PV Pipe: 44 -106.1 4.310 PL 10. 00 PF 0 .0 27 18.0 0.0 15 . 9 0 .0 2 .3 120 FTG ---- PE 0 .0 29 18.0 0.0 16. 0 0 .0 0.003 TL 10 . 00 PV Pipe: 45 -138 .2 4.310 PL 10. 00 PF 0 .0 6 18.0 0 . 0 17 .5 0 .0 3.0 120 FTG ---- PE 0 .0 12 18.0 0 . 0 17 . 6 0 .0 0.005 TL 10. 00 PV Pipe: 46 -276.7 4.310 PL 10. 00 PF 0 .2 12 18.0 0 . 0 17 . 6 0 .0 6. 1 120 FTG ---- PE 0 .0 18 18.0 0 . 0 17 .7 0 .0 0.017 TL 10. 00 PV Pipe: 47 -416.0 4.310 PL 10. 00 PF 0 .4 18 18.0 0 . 0 17 .7 0 .0 9.1 120 FTG ---- PE 0 .0 20 18.0 0 . 0 18. 1 0 .0 0.037 TL 10. 00 PV Pipe: 48 -485.3 4.310 PL 10. 00 PF 0 .5 20 18.0 0 . 0 18. 1 0 .0 10 .7 120 FTG ---- PE 0 .0 22 18.0 0 . 0 18. 6 0 .0 0.049 TL 10. 00 PV Pipe: 49 -545.4 4.310 PL 10. 00 PF 0 . 6 22 18.0 0 . 0 18 . 6 0 .0 12 .0 120 FTG ---- PE 0 .0 24 18.0 0 . 0 19.2 0 .0 0.060 TL 10. 00 PV Pipe: 50 -609.4 4.310 PL 10. 00 PF 0 .7 24 18.0 0.0 19.2 0 .0 13.4 120 FTG ---- PE 0 .0 26 18.0 0.0 19. 9 0 .0 0.074 TL 10. 00 PV Pipe: 51 -679.1 4.310 PL 10. 00 PF 0 . 9 26 18.0 0.0 19. 9 0 .0 14 . 9 120 FTG ---- PE 0 . 0 28 18.0 0.0 20. 8 0 .0 0.091 TL 10. 00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 -756.2 4.310 PL 9. 00 PF 4 . 1 28 18.0 0 . 0 20. 8 0 .0 16. 6 120 FTG T PE 0 .0 31 18.0 0 . 0 24 . 9 0 .0 0.111 TL 36. 90 PV Pipe: 53 -106.1 4.310 PL 1. 00 PF 0 .1 30 18.0 0 . 0 24 . 8 0 .0 2 .3 120 FTG T PE 0 .0 31 18.0 0 . 0 24 . 9 0 .0 0.003 TL 28. 90 PV Pipe: 54 -862 .3 6.357 PL 2.50 PF 0 .4 31 18.0 0 . 0 24 . 9 0 .0 8 .7 120 FTG E PE 0 .0 TR 18.0 0 . 0 25.3 0 .0 0.021 TL 20. 10 PV Pipe: 55 -862 .3 6.357 PL 16. 00 PF 1 .8 TR 18.0 0.0 25.3 0 .0 8 .7 120 FTG ECB PE 6. 9 BR 2 .0 0.0 34 . 1 0 .0 0.021 TL 86.40 PV Pipe: 56 -862 .3 6.357 PL 6. 00 PF 2 .1 BR 2 .0 0.0 34. 1 0 .0 8 .7 120 FTG TCB PE 0 .0 PD 2 .0 0.0 36.2 0 .0 0.021 TL 96.50 PV Pipe: 57 FIRE PUMP Rating: 750.0 gpm @ 60. 0 psi PS 2 .0 0.0 0 .4 0. 0 Avail. : 862 .4 gpm @ 54 .5 psi PD 2 .0 0.0 36.2 0. 0 Req'd. : 862 .4 gpm @ 35.7 psi Pipe: 58 -862 .3 6.357 PL 3. 00 PF 0 . 9 PS 2 .0 0 . 0 0.4 0 .0 8 .7 120 FTG TG PE 0 . 6 UG 0.5 0 . 0 2. 0 0 .0 0.021 TL 44.50 PV Pipe: 59 -862 .3 6.275 PL 16. 00 PF 1 .0 UG 0.5 0 . 0 2.0 0 .0 8 . 9 140 FTG 2E PE -0 . 6 RP1 2 .0 0 . 0 2.4 0 .0 0.017 TL 60. 00 PV Pipe: 60 FIXED PRESSURE LOSS DEVICE RP2 2 .0 0 . 0 14 . 4 0 .0 12 .0 psi, 862 .2 gpm RP1 2 .0 0 . 0 2 . 4 0 .0 Pipe: 61 -862 .3 6.275 PL 30. 00 PF 1 .3 RP2 2 .0 0 . 0 14 . 4 0 .0 8 . 9 140 FTG 2EG PE 2 .2 39 -3.0 0 . 0 17 . 9 0 .0 0.017 TL 78.70 PV Pipe: 62 -862 .3 4.155 PL 1. 00 PF 4 .1 39 -3.0 0 . 0 17 . 9 0 .0 20 .4 140 FTG T PE 0 .0 100 -3.0 0 . 0 22. 0 0 .0 0.127 TL 32. 00 PV Pipe: 63 -426. 9 4.155 PL 150. 00 PF 10 .8 100 -3.0 0 . 0 22 . 0 0 .0 10 .1 100 FTG TG PE 0 .0 101 -3.0 H.S. 32 . 8 500 .0 0.064 TL 168.30 PV Pipe: 64 -285.8 6.275 PL 160. 00 PF 0 .8 101 -3.0 H.S. 32 . 8 500 .0 3.0 100 FTG TG PE 0 .0 102 -3.0 0 . 0 33 . 6 0 .0 0.004 TL 187. 80 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -285.8 4.155 PL 400. 00 PF 12 .8 102 -3.0 0.0 33. 6 0 .0 6.8 100 FTG TG PE 0 .0 103 -3.0 0.0 46.4 0 .0 0.031 TL 418.30 PV Pipe: 66 -285.8 6.275 PL 20. 00 PF 0 .2 103 -3.0 0 . 0 46. 4 0 .0 3.0 100 FTG T PE 0 .0 107 -3.0 0 . 0 46. 6 0 .0 0.004 TL 45.27 PV Pipe: 67 -435.4 4.155 PL 250. 00 PF 17 . 9 100 -3.0 0 . 0 22 . 0 0 .0 10 .3 100 FTG TG PE 0 .0 106 -3.0 0 . 0 39. 9 0 .0 0.067 TL 268.30 PV Pipe: 68 -641 .0 6.275 PL 160. 00 PF 3.4 101 -3.0 H.S. 32 . 8 500 .0 6.7 100 FTG TG PE 0 .0 104 -3.0 0 . 0 36.2 0 .0 0.018 TL 187. 80 PV Pipe: 69 -641 .0 10.395 PL 400. 00 PF 0 .7 104 -3.0 0.0 36.2 0 .0 2 .4 100 FTG TG PE 0 .0 105 -3.0 0.0 36. 9 0 .0 0.002 TL 446. 95 PV Pipe: 70 -641 .0 6.275 PL 160. 00 PF 2 . 9 105 -3.0 0.0 36. 9 0 .0 6.7 100 FTG ---- PE 0 .0 106 -3.0 0.0 39. 9 0 .0 0.018 TL 160 . 00 PV Pipe: 71 -1076.4 6.275 PL 140. 00 PF 6.7 106 -3.0 0 . 0 39. 9 0 .0 11 .2 100 FTG ---- PE 0 .0 107 -3.0 0 . 0 46. 6 0 .0 0.048 TL 140. 00 PV Pipe: 72 -1362 .3 6.275 PL 3. 00 PF 0 . 1 107 -3.0 0.0 46. 6 0 .0 14 .1 140 FTG ---- PE -1 .3 S 0. 0 SRCE 45. 4 (N/A) 0.040 TL 3. 00 PV NOTES (HASS) : (1) Calculations were performed by the HASS 2023 D computer program under license no. 64600052 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (2) The system has been calculated to provide an average imbalance at each node of 0. 004 gpm and a maximum imbalance at any node of 0 .129 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 20 .4 ft/sec at pipe 62. (4) The Minimum pump suction pressure under maximum calculated demand is 0.44 (psi) (5) Items listed in bold print on the cover sheet SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 are automatically transferred from the calculation report. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD PAGE: B MATERIAL: S10 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D F Ell Tee LngEll ChkVly BfyVly GatVly AlmChk DPVly FlowSw 6.357 17 . 60 37 .70 11.30 40 .20 12 . 60 3.80 35.20 39.00 20.10 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G Ell Tee LngEll ChkVly BfyVly GatVly 4 . 155 15.50 31 .00 9.30 34 .10 18. 60 3.10 6.275 22.00 47 .10 14 . 10 50 .20 15.70 4.70 10.395 35.00 79.50 25.40 87 .50 30.20 8.00 PAGE: P MATERIAL: EddyF HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D F Ell Tee LngEll ChkVly BfyVly GatVly FlowSw 2.203 6.80 13. 60 4. 10 15.00 8.20 1.40 19.10 0. 00 0 .00 4.310 13. 90 27 . 90 8.40 30 .70 16.70 2.80 41 .80 0. 00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 9/10/2024 : \DWG\MISC\FOX COMPANY\CAS BUILDING\CALCULATIONS\33217 .SDF JOB TITLE: .40/2000 0 0 0 I N I 1 0-1 0 ,� CO 0 I '-0 U) O '-0 I 04 o in 0 E H I v U ) a) -H I o 3▪ a $4 a al +J I C H H o f a°i E E E A\ 0 0 U > a) Cl) +-) a, a, E O E CO E 4 E ro I -H ro 0) -k-) 0-) Lk a, aH a,--I a, 0) 0 a co 0al 0 0' w 0-) 0 0 01 U U 0 1 H • -0 • H a' a' > a' a) a' 4 a) a O A N 0 N A • a) • cci • • >1 U 0 'd O al w S4 w al ("\ -I N N N ,-I CO 4 l a--) I Hr) -Hr) HW -HW a) W (I) W a -H ozi ccl cci inn cci 0" rd H -H CO b" 0 0 Q 0 a) a) I O a) C > C a) C co C co C u) 0, CO U H I o -▪ w •H •H •H •H 0 •H 0 •H Cl) 2 as I H HC CO 0 0 04a CO U)�, w +°- H I 0 w a) a U) N CO O CO W U) M H N H I— 0 a) >1 > 1 U) a' U) sr CO ' m ro C ro H v) Z a u) FC -H 0 • 0 • a) • a) • 4) • 4) • I U) N 7r LO O H O W • a u) Pa a' Pa u) a r) H w H r) r.0 m U C] 4., I u) I H O 0 U) O• � 7 7 7 7 7 I A CD sr 7�] 7��/ z A 7 0 U , N CO s' ,1) LO N / W c7 +, O a ro H c I / o O m ,_ u) I / o ,-a o +-) a a I / H w -P Hu ro • o o o • U CD w o H CO •0 • E a 0 g E o If) ') � 0 Cb ce -kJ C 03 CC) O ° o o LC) I o 0 m 0 0 U 0 I U 1 1 � 1 1 Q � � -H CO O O O 0 0 O O O 0 7r' CO a) O 0 0 0 0 0 0 0 0 l_C) d' N 0 CO l0 G' N -H CO H H 0fr:0w aawU) u) aw - a, CO -H ---- 7 O C o