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HomeMy WebLinkAbout1315 John Fitch Blvd - Building Plans &amp; HARTFORD SPRINKLER CO. INC. 4 BRITTON ROAD BLOOMFIELD,CT HYDRAULIC CALCULATIONS FOR ANIXTR 1315 JOHN FITCH BLVD. SOUTH WINDSOR, CT. DATE: MAR 26, 2014 -DESIGN DATA- OCCUPANCY CLASSIFICATION: CLASS IV RACK STORAGE TO 27 '-0 DENSITY: . 94 gpm/sq. ft. AREA OF APPLICATION: 1200 sq. ft. COVERAGE PER SPRINKLER: 100 sq. ft. MAX NUMBER OF SPRINKLERS CALCULATED: 12 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 1170.2 gpm TOTAL WATER REQUIRED (including hose) : 1420.2 gpm FLOW AND PRESSURE THE SOURCE \\A ZO 44rfr gpm @ 52 psi SPRINKLER ORIFICE SIZE: 5/8 inch NAME OF CONTRACTOR:HARTFORD SPRINKLER AUTHORITY HAVING JURISDICTION:LOCAL F.M. CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 50080259 ) HRS SYSTEMS, INC. TUCKER, GA 30084 j Q ;6 �a ye 5 � ero ��Qaa,.• SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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 85.0 63.0 1768. 0 70.3 1420.2 51. 6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1420.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0. 0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1170.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 31.0 - - - - 27.8 - - - 2 31.0 K=21.77 20.2 97. 9 3 31.0 K=21.77 19. 9 97. 0 4 31.0 K=21.77 19. 9 97.0 5 31.0 K=21.77 20.3 98.1 6 31.0 - - - - 21.8 - - - 7 31.0 - - - - 27.3 - - - 8 31.0 - - - - 27.8 - - - 9 31.0 K=21.77 20.2 97. 9 10 31.0 K=21.77 19. 9 97.0 11 31.0 K=21.77 19. 9 97. 0 12 31.0 K=21.77 20.3 98.1 13 31.0 - - - - 21.8 - - - 14 31.0 - - - - 27.3 - - - 15 31.0 - - - - 27.8 - - - 16 31.0 K=21.77 20.2 97. 9 17 31.0 K=21.77 19. 9 97.1 18 31.0 K=21.77 19. 9 97.1 19 31.0 K=21.77 20.3 98.2 20 31.0 - - - - 21. 8 - - - 21 31.0 - - - - 27.4 - - - 22 31.0 - - - - 27. 9 - - - 23 31.0 - - - - 27.5 - - - 24 31.0 - - - - 27. 9 - - - 25 31.0 - - - - 27. 6 - - - 26 31.0 - - - - 27. 9 - - - 27 31.0 - - - - 27.8 - - - 28 31.0 - - - - 28.0 - - - 29 31.0 - - - - 27. 9 - - - 30 31.0 - - - - 28.0 - - - 31 31.0 - - - - 28.0 - - - 32 31.0 - - - - 28.1 - - - 33 31.0 - - - - 28.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 3/26/2014RAM FILES\HRS SYS`1'EMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 31. 0 - - - - 28.1 - - - 35 31.0 - - - - 28.2 - - - 36 31. 0 - - - - 28. 1 - - - 37 31.0 - - - - 28.4 - - - 38 31. 0 - - - - 28.2 - - - 39 31.0 - - - - 28.5 - - - 40 31.0 - - - - 28.2 - - - 41 31. 0 - - - - 28. 6 - - - 42 31.0 - - - - 28.2 - - - 43 31.0 - - - - 28.8 - - - 44 31.0 - - - - 28.3 - - - 45 31.0 - - - - 29.0 - - - 46 31.0 - - - - 28.3 - - - 47 31.0 - - - - 29.1 - - - 48 31.0 - - - - 28.3 - - - 49 31.0 - - - - 29.3 - - - 50 31.0 - - - - 28.3 - - - 51 31.0 - - - - 29. 6 - - - 52 31.0 - - - - 28.4 - - - 53 31.0 - - - - 29.8 - - - 54 31. 0 - - - - 28.4 - - - 55 31.0 - - - - 30. 1 - - - 56 31.0 - - - - 28.4 - - - 57 31.0 - - - - 30.4 - - - 58 31.0 - - - - 28.4 - - - 59 31.0 - - - - 30.7 - - - 60 31.0 - - - - 28.4 - - - 61 31.0 - - - - 31.1 - - - 62 31.0 - - - - 28.4 - - - 63 31.0 - - - - 31. 6 - - - AV 4.0 - - - - 46.5 - - - BFO 2.0 - - - - 43.2 - - - BFI 2.0 - - - - 48.2 - - - Ri 1.0 - - - - 49.1 - - - S -1.0 SOURCE 51. 6 1170.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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: 1 189.1 2.469 PL 45.00 PF 7. 6 1 31.0 0.0 27.8 0.0 12.7 117 FTG T PE 0. 0 2 31.0 21.8 20.2 97. 9 0.135 TL 56.45 PV Pipe: 2 91.3 2.469 PL 10.00 PF 0.3 2 31.0 21.8 20.2 97. 9 6.1 117 FTG ---- PE 0.0 3 31.0 21.8 19. 9 97.0 0.035 TL 10.00 Pv Pipe: 3 -5.7 2.469 PL 10.00 PF 0.0 3 31.0 21.8 19. 9 97.0 0.4 117 FTG ---- PE 0. 0 4 31.0 21.8 19. 9 97.0 0. 000 TL 10. 00 PV Pipe: 4 -102.7 2.469 PL 10.00 PF 0.4 4 31.0 21.8 19. 9 97.0 6.9 117 FTG ---- PE 0. 0 5 31.0 21.8 20.3 98.1 0.044 TL 10.00 Pv Pipe: 5 -200.8 2.469 PL 10.00 PF 1.5 5 31.0 21.8 20.3 98. 1 13.5 117 FTG ---- PE 0.0 6 31.0 0.0 21.8 0.0 0.150 TL 10.00 PV Pipe: 6 -200.8 2.469 PL 25.00 PF 5.5 6 31.0 0.0 21.8 0.0 13.5 117 FTG T PE 0.0 7 31. 0 0.0 27.3 0.0 0.150 TL 36.45 PV Pipe: 7 189. 1 7. 981 PL 10.00 PF 0.0 8 31.0 0.0 27.8 0.0 1.2 117 FTG ---- PE 0. 0 1 31.0 0.0 27. 8 0.0 0.000 TL 10.00 Pv Pipe: 8 189.1 2.469 PL 45.00 PF 7. 6 8 31.0 0.0 27.8 0.0 12.7 117 FTG T PE 0.0 9 31.0 21.8 20.2 97. 9 0. 135 TL 56.45 PV Pipe: 9 91.2 2.469 PL 10.00 PF 0.3 9 31. 0 21.8 20.2 97. 9 6.1 117 FTG ---- PE 0.0 10 31.0 21.8 19. 9 97.0 0.035 TL 10.00 Pv Pipe: 10 -5.8 2.469 PL 10.00 PF 0.0 10 31.0 21.8 19. 9 97.0 0.4 117 FTG ---- PE 0.0 11 31.0 21.8 19. 9 97.0 0. 000 TL 10.00 Pv Pipe: 11 -102.8 2.469 PL 10.00 PF 0.4 11 31.0 21.8 19. 9 97.0 6. 9 117 FTG ---- PE 0.0 12 31.0 21.8 20.3 98.1 0.044 TL 10.00 Pv Pipe: 12 -200. 9 2.469 PL 10.00 PF 1.5 12 31.0 21.8 20.3 98.1 13.5 117 FTG ---- PE 0.0 13 31.0 0.0 21.8 0.0 0.151 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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 -200.9 2.469 PL 25.00 PF 5.5 13 31.0 0.0 21.8 0.0 13.5 117 FTG T PE 0.0 14 31.0 0.0 27.3 0.0 0.151 TL 36.45 PV Pipe: 14 200.8 6.065 PL 10.00 PF 0.0 14 31.0 0.0 27.3 0.0 2.2 117 FTG ---- PE 0.0 7 31.0 0.0 27.3 0.0 0. 002 TL 10. 00 PV Pipe: 15 378.2 7. 981 PL 10.00 PF 0.0 15 31.0 0.0 27.8 0.0 2.4 117 FTG ---- PE 0.0 8 31.0 0.0 27. 8 0.0 0.002 TL 10. 00 PV Pipe: 16 188.9 2.469 PL 45. 00 PF 7. 6 15 31.0 0.0 27.8 0.0 12.7 117 FTG T PE 0.0 16 31.0 21.8 20.2 97. 9 0.134 TL 56.45 PV Pipe: 17 90. 9 2.469 PL 10. 00 PF 0.3 16 31.0 21.8 20.2 97. 9 6.1 117 FTG ---- PE 0.0 17 31.0 21.8 19. 9 97.1 0.035 TL 10.00 Pv P �' -6.2 2.469 PL 10.00 PF 0. 0 Pipe: 18 17 31.0 21.8 19. 9 97. 1 0.4 117 FTG ---- PE 0.0 18 31.0 21.8 19. 9 97.1 0.000 TL 10.00 Pv Pipe: 19 -103.3 2.469 PL 10.00 PF 0.4 18 31.0 21.8 19. 9 97.1 6. 9 117 FTG ---- PE 0.0 19 31.0 21.8 20.3 98.2 0.044 TL 10.00 Pv Pipe: 20 -201.4 2.469 PL 10.00 PF 1.5 19 31.0 21.8 20.3 98.2 13.5 117 FTG ---- PE 0.0 20 31.0 0.0 21.8 0.0 0. 151 TL 10.00 PV Pipe: 21 -201.4 2.469 PL 25.00 PF 5.5 20 31.0 0.0 21.8 0.0 13.5 117 FTG T PE 0.0 21 31.0 0.0 27.4 0.0 0. 151 TL 36.45 PV Pipe: 22 401.7 6.065 PL 10.00 PF 0.1 21 31.0 0.0 27.4 0.0 4.5 117 FTG ---- PE 0.0 14 31.0 0.0 27.3 0.0 0. 007 TL 10. 00 PV Pipe: 23 567.1 7. 981 PL 10.00 PF 0.0 22 31.0 0.0 27. 9 0.0 3. 6 117 FTG ---- PE 0.0 15 31.0 0.0 27. 8 0.0 0.003 TL 10.00 Pv Pipe: 24 22.5 2.469 PL 110. 00 PF 0.3 22 31.0 0.0 27. 9 0. 0 1.5 117 FTG 2T PE 0.0 23 31.0 0.0 27.5 0.0 0.003 _TL 132. 90 PV Pipe: 25 603.2 6.065 PL 10.00 PF 0. 1 23 31.0 0.0 27.5 0.0 6.7 117 FTG ---- PE 0.0 21 31.0 0.0 27.4 0.0 0.014 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3P26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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: 26 589. 6 7. 981 PL 10.00 PF 0. 0 24 31.0 0.0 27. 9 0.0 3.8 117 FTG ---- PE 0. 0 22 31.0 0.0 27. 9 0.0 0.004 TL 10.00 PV Pipe: 27 18.8 2.469 PL 110.00 PF 0.3 24 31. 0 0.0 27. 9 0.0 1.3 117 FTG 2T PE 0.0 25 31.0 0.0 27. 6 0.0 0.002 TL 132. 90 PV Pipe: 28 580. 6 6.065 PL 10.00 PF 0.1 25 31.0 0.0 27. 6 0. 0 6.4 117 FTG ---- PE 0.0 23 31.0 0.0 27.5 0.0 0.013 TL 10.00 PV Pipe: 29 608.4 7. 981 PL 10.00 PF 0.0 26 31.0 0.0 27. 9 0.0 3. 9 117 FTG ---- PE 0. 0 24 31.0 0.0 27. 9 0.0 0.004 TL 10.00 PV Pipe: 30 14 .2 2.469 PL 110.00 PF 0.2 26 31. 0 0.0 27. 9 0. 0 1. 0 117 FTG 3T PE 0.0 27 31.0 0.0 27.8 0.0 0.001 TL 144.35 PV Pipe: 31 561. 8 6.065 PL 10. 00 PF 0. 1 27 31.0 0.0 27.8 0. 0 6.2 117 FTG ---- PE 0.0 25 31.0 0.0 27. 6 0. 0 0.013 TL 10.00 PV Pipe: 32 622.7 7. 981 PL 10.00 PF 0. 0 28 31.0 0.0 28.0 0.0 4.0 117 FTG ---- PE 0.0 26 31.0 0. 0 27. 9 0.0 0. 004 TL 10.00 Pv Pipe: 33 10.3 2.469 PL 110.00 PF 0.1 28 31.0 0.0 28.0 0.0 0.7 117 FTG 2T PE 0. 0 29 31.0 0.0 27. 9 0. 0 0.001 TL 132. 90 PV Pipe: 34 547. 6 6.065 PL 10. 00 PF 0. 1 29 31.0 0.0 27.9 0.0 6. 1 117 FTG ---- PE 0. 0 27 31.0 0.0 27.8 0.0 0.012 TL 10.00 PV Pipe: 35 633.0 7. 981 PL 10.00 PF 0.0 30 31.0 0.0 28.0 0.0 4.1 117 FTG ---- PE 0.0 28 31.0 0.0 28.0 0.0 0. 004 TL 10.00 PV Pipe: 36 2. 6 2.469 PL 110.00 PF 0.0 30 31. 0 0.0 28. 0 0. 0 0.2 117 FTG 2T PE 0.0 31 31.0 0.0 28.0 0. 0 0.000 TL 132. 90 PV Pipe: 37 537.3 6.065 PL 10.00 PF 0. 1 31 31.0 0.0 28.0 0.0 6.0 117 FTG ---- PE 0.0 29 31.0 0.0 27. 9 0.0 0.012 TL 10.00 PV Pipe: 38 635. 6 7. 981 PL 10.00 PF 0.0 32 31.0 0.0 28.1 0.0 4.1 117 FTG ---- PE 0.0 30 31.0 0.0 28.0 0.0 0. 004 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 3�26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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 -9.2 2.469 PL 110.00 PF 0.1 32 31.0 0.0 28.1 0.0 0. 6 117 FTG 2T PE 0.0 33 31. 0 0.0 28.1 0.0 0. 001 TL 132. 90 PV Pipe: 40 534.7 6. 065 PL 10.00 PF 0.1 33 31.0 0.0 28.1 0.0 5. 9 117 FTG ---- PE 0.0 31 31.0 0.0 28.0 0.0 0.012 TL 10.00 Pv Pipe: 41 626.3 7. 981 PL 10.00 PF 0.0 34 31. 0 0.0 28.1 0.0 4.0 117 FTG ---- PE 0. 0 32 31. 0 0.0 28.1 0.0 0.004 TL 10.00 PV Pipe: 42 -14. 1 2.469 PL 110.00 PF 0.1 34 31.0 0.0 28.1 0.0 0. 9 117 FTG 2T PE 0.0 35 31.0 0.0 28.2 0.0 0.001 TL 132. 90 PV Pipe: 43 543. 9 6.065 PL 10.00 PF 0. 1 35 31. 0 0.0 28.2 0.0 6. 0 117 FTG ---- PE 0. 0 33 31.0 0.0 28. 1 0. 0 0.012 TL 10.00 PV Pipe: 44 612.3 7. 981 PL 10.00 PF 0. 0 36 31.0 0.0 28. 1 0.0 3. 9 117 FTG ---- PE 0.0 34 31.0 0.0 28. 1 0.0 0.004 TL 10.00 PV Pipe: 45 -18. 1 2.469 PL 110.00 PF 0.2 36 31. 0 0.0 28. 1 0.0 1.2 117 FTG 2T PE 0. 0 37 31.0 0.0 28.4 0.0 0.002 TL 132. 90 PV Pipe: 46 558.0 6.065 PL 10.00 PF 0. 1 37 31. 0 0.0 28.4 0.0 6.2 117 FTG ---- PE 0.0 35 31. 0 0.0 28.2 0.0 0.013 TL 10.00 PV Pipe: 47 594.2 7. 981 PL 10.00 PF 0.0 38 31.0 0.0 28.2 0. 0 3.8 117 FTG ---- PE 0.0 36 31.0 0.0 28.1 0. 0 0. 004 TL 10.00 PV Pipe: 48 -21.8 2.469 PL 110.00 PF 0.3 38 31.0 0.0 28.2 0.0 1.5 117 FTG 2T PE 0.0 39 31.0 0.0 28.5 0.0 0.002 TL 132.90 PV Pipe: 49 576.0 6.065 PL 10.00 PF 0.1 39 31.0 0.0 28.5 0.0 6.4 117 FTG ---- PE 0.0 37 31.0 0.0 28.4 0.0 0.013 TL 10.00 PV Pipe: 50 572.4 7. 981 PL 10.00 PF 0.0 40 31.0 0.0 28.2 0.0 3.7 117 FTG ---- PE 0.0 38 31 .0 0.0 28.2 0.0 0.003 TL 10.00 PV Pipe: 51 -25.4 2.469 PL 110.00 PF 0.4 40 31.0 0.0 28.2 0.0 1.7 117 FTG 2T PE 0.0 41 31.0 0.0 28. 6 0.0 0.003 TL 132. 90 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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: 52 597.8 6.065 PL 10.00 PF 0.1 41 31. 0 0.0 28. 6 0.0 6. 6 117 FTG ---- PE 0.0 39 31.0 0.0 28.5 0.0 0.014 TL 10.00 PV Pipe: 53 547.1 7.981 PL 10.00 PF 0.0 42 31.0 0.0 28.2 0.0 3.5 117 FTG ---- PE 0.0 40 31.0 0.0 28.2 0.0 0.003 TL 10. 00 PV Pipe: 54 -29.0 2.469 PL 110.00 PF 0. 6 42 31.0 0.0 28.2 0.0 1. 9 117 FTG 2T PE 0.0 43 31. 0 0.0 28.8 0.0 0.004 TL 132. 90 PV Pipe: 55 623.2 6.065 PL 10.00 PF 0.2 43 31.0 0.0 28.8 0.0 6. 9 117 FTG ---- PE 0. 0 41 31.0 0.0 28. 6 0.0 0.015 TL 10.00 PV Pipe: 56 518. 1 7. 981 PL 10.00 PF 0. 0 44 31.0 0.0 28.3 0.0 3.3 117 FTG ---- PE 0.0 42 31.0 0.0 28.2 0.0 0.003 TL 10.00 PV Pipe: 57 -31.3 2.469 PL 110.00 PF 0.7 44 31.0 0.0 28.3 0.0 2.1 117 FTG 3T PE 0. 0 45 31.0 0.0 29.0 0.0 0.005 TL 144.35 PV Pipe: 58 652.2 6. 065 PL 10.00 PF 0.2 45 31.0 0.0 29.0 0.0 7.2 117 FTG ---- PE 0.0 43 31.0 0.0 28.8 0.0 0.017 TL 10.00 PV Pipe: 59 486.8 7. 981 PL 10.00 PF 0.0 46 31.0 0.0 28.3 0.0 3.1 117 FTG ---- PE 0. 0 44 31.0 0.0 28.3 0.0 0.003 TL 10.00 PV Pipe: 60 -34. 9 2.469 PL 110.00 PF 0. 9 46 31.0 0.0 28.3 0.0 2.3 117 FTG 3T PE 0.0 47 31. 0 0.0 29.1 0.0 0.006 TL 144.35 PV Pipe: 61 683.5 6.065 PL 10.00 PF 0.2 47 31.0 0.0 29. 1 0.0 7. 6 117 FTG ---- PE 0.0 45 31.0 0.0 29.0 0.0 0.018 TL 10.00 PV Pipe: 62 451.9 7. 981 PL 10.00 PF 0.0 48 31.0 0.0 28.3 0.0 2. 9 117 FTG ---- PE 0.0 46 31.0 0.0 28.3 0.0 0.002 TL 10.00 PV Pipe: 63 -40.4 2.469 PL 110.00 PF 1.0 48 31.0 0.0 28.3 0.0 2.7 117 FTG 2T PE 0.0 49 31. 0 0.0 29.3 0.0 0.008 TL 132. 90 PV Pipe: 64 718.4 6.065 PL 10.00 PF 0.2 49 31.0 0.0 29.3 0.0 8.0 117 FTG ---- PE 0.0 47 31.0 0.0 29.1 0.0 0.020 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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: 65 411.5 7. 981 PL 10.00 PF 0.0 50 31.0 0.0 28.3 0.0 2. 6 117 FTG ---- PE 0.0 48 31.0 0.0 28.3 0.0 0.002 TL 10.00 PV Pipe: 66 -44.5 2.469 PL 110.00 PF 1.2 50 31.0 0.0 28.3 0.0 3.0 117 FTG 2T PE 0.0 51 31.0 0.0 29. 6 0.0 0.009 TL 132. 90 PV Pipe: 67 758.8 6.065 PL 10.00 PF 0.2 51 31.0 0.0 29. 6 0.0 8.4 117 FTG ---- PE 0.0 49 31.0 0.0 29.3 0.0 0.022 TL 10.00 PV Pipe: 68 366. 9 7. 981 PL 10.00 PF 0.0 52 31.0 0.0 28.4 0.0 2.4 117 FTG ---- PE 0.0 50 31.0 0.0 28.3 0.0 0.002 TL 10.00 PV Pipe: 69 -48. 9 2.469 PL 110.00 PF 1.5 52 31.0 0.0 28.4 0.0 3.3 117 FTG 2T PE 0.0 53 31.0 0.0 29.8 0.0 0.011 TL 132. 90 PV Pipe: 70 803.3 6.065 PL 10.00 PF 0.2 53 31.0 0.0 29.8 0.0 8.9 117 FTG ---- PE 0.0 51 31.0 0.0 29. 6 0. 0 0.025 TL 10.00 PV Pipe: 71 318.0 7. 981 PL 10.00 PF 0.0 54 31.0 0.0 28.4 0.0 2.0 117 FTG ---- PE 0.0 52 31.0 0.0 28.4 0.0 0.001 TL 10.00 PV Pipe: 72 -53.4 2.469 PL 110.00 PF 1.7 54 31.0 0.0 28.4 0.0 3. 6 117 FTG 2T PE 0.0 55 31.0 0.0 30.1 0.0 0.013 TL 132. 90 PV Pipe: 73 852.2 6.065 PL 10.00 PF 0.3 55 31.0 0.0 30. 1 0.0 9.5 117 FTG ---- PE 0.0 53 31.0 0.0 29.8 0.0 0.027 TL 10.00 PV Pipe: 74 264. 6 7. 981 PL 10.00 PF 0.0 56 31.0 0.0 28.4 0.0 1.7 117 FTG ---- PE 0.0 54 31.0 0.0 28.4 0.0 0.001 TL 10.00 PV Pipe: 75 -58.2 2.469 PL 110.00 PF 2.0 56 31.0 0.0 28.4 0.0 3. 9 117 FTG 2T PE 0. 0 57 31.0 0.0 30.4 0.0 0.015 TL 132. 90 PV Pipe: 76 905. 6 6.065 PL 10.00 PF 0.3 57 31.0 0.0 30.4 0.0 10.1 117 FTG ---- PE 0.0 55 31.0 0.0 30.1 0.0 0.031 TL 10.00 PV Pipe: 77 206.4 7. 981 PL 10.00 PF 0.0 58 31.0 0.0 28.4 0.0 1.3 117 FTG ---- PE 0.0 56 31.0 0.0 28.4 0.0 0.001 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R 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: 78 -63.3 2.469 PL 110.00 PF 2.4 58 31.0 0.0 28.4 0.0 4.2 117 FTG 2T PE 0.0 59 31.0 0.0 30.7 0.0 0.018 TL 132. 90 PV Pipe: 79 963. 9 6.065 PL 10.00 PF 0.3 59 31.0 0.0 30.7 0. 0 10.7 117 FTG ---- PE 0.0 57 31.0 0.0 30.4 0.0 0.034 TL 10.00 PV Pipe: 80 143. 1 7. 981 PL 10.00 PF 0. 0 60 31.0 0.0 28.4 0.0 0. 9 117 FTG ---- PE 0. 0 58 31.0 0.0 28.4 0.0 0.000 TL 10.00 PV Pipe: 81 -68.7 2.469 PL 110.00 PF 2.7 60 31.0 0.0 28.4 0.0 4. 6 117 FTG 2T PE 0. 0 61 31.0 0.0 31.1 0.0 0.021 TL 132. 90 PV Pipe: 82 1027.2 6.065 PL 10. 00 PF 0.4 61 31.0 0.0 31.1 0.0 11.4 117 FTG ---- PE 0.0 59 31.0 0.0 30.7 0.0 0.039 TL 10. 00 Pv Pipe: 83 74.4 7. 981 PL 10.00 PF 0. 0 62 31.0 0. 0 28.4 0.0 0.5 117 FTG ---- PE 0.0 60 31.0 0.0 28.4 0.0 0.000 TL 10. 00 PV Pipe: 84 -74.4 2.469 PL 110.00 PF 3.2 62 31.0 0.0 28.4 0. 0 5. 0 117 FTG 2T PE 0.0 63 31.0 0.0 31. 6 0. 0 0.024 TL 132. 90 PV Pipe: 85 1095. 9 6.065 PL 10. 00 PF 0.4 63 31.0 0.0 31. 6 0. 0 12.2 117 FTG ---- PE 0.0 61 31.0 0.0 31.1 0.0 0.044 TL 10.00 PV Pipe: 86 -1170.2 7. 981 PL 93.00 PF 3.3 63 31.0 0.0 31. 6 0.0 7.5 117 FTG SETBA PE 11.7 AV 4.0 0.0 46.5 0.0 0.013 TL 253.31 PV Pipe: 87 -1170.2 7. 981 PL 3.00 PF 0. 8 AV 4.0 0. 0 46.5 0.0 7.5 120 FTG 3EG PE 0. 9 BFI 2.0 0.0 48.2 0.0 0.012 TL 61.00 PV Pipe: 88 FIXED PRESSURE LOSS DEVICE BFI 2. 0 0.0 48.2 0.0 5.0 psi, 0. 0 gpm BFO 2.0 0.0 43.2 0. 0 Pipe: 89 -1170.2 7. 981 PL 3.00 PF 0.5 BFI 2.0 0.0 48.2 0.0 7.5 120 FTG 2E PE 0.4 RI 1.0 0.0 49.1 0. 0 0.012 TL 39.00 PV Pipe: 90 -1170.2 8.390 PL 100. 00 PF 1.7 RI 1.0 0.0 49.1 0.0 6.8 140 FTG 2ETG PE 0. 9 S -1.0 SRCE 51. 6 (N/A) 0. 007 TL 228.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R NOTES (HASS) : (1) Calculations were performed by the HASS 8.4 computer program under license no. 50080259 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 0.003 gpm and a maximum imbalance at any node of 0.180 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 13.5 ft/sec at pipe 20. (4) a. System remote area HAS been proven or 'peaked' . b. Minimum pressure at any sprinkler: 19.853 psi c. Minimum pressure with remote area shifted one sprinkler space toward left cross main: 19.881 psi d. Minimum pressure with remote area shifted one sprinkler space toward right cross main: 19. 995 psi (5) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (6) Available pressure at source node S under full flow conditions is 66.00 psi compared to the minimum required pressure of 20.00 psi. (7) 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 A D N Ell Tee LngEll ChkVly BfyVly GatVly AlmChk DPVly NPTee 2.469 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10.00 12.00 6.065 14.00 30.00 9. 00 32.00 10.00 3.00 28.00 28.00 30.00 7. 981 18.00 35.00 13.00 45.00 12.00 4.00 31.00 31.00 35.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 3/26/2014RAM FILES\HRS SYSTEMS\HASS83\HASS FILES\2013\ANIXTRI2 .SDF JOB TITLE: ANITXR12R PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVly Bfyvly GatVly NPTee 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 C-4 d o > WATER SUPPLY ANALYSIS y Static: 85 . 00 psi Resid: 63 . 00 psi Flow: 1768 . 0 gpm y , H H w 100 . 0 N ' 1LEGEND Available pressure 70.33 psi @ 1420.2 gpm if >Z o H I-° 2 x � Required pressure �C Z0 51.61 psi @ 1420.2 gpm F A. Source Supply Curve N 80 . 0 B. System Demand Curve H G Ln H A / z U 1 G x m E CD F< H3 CO ■��'••••••• M H p 60 . 0 ••••••'••••..... x M •■■.. / R > F< E 2 cn U S w > S / r x H U > n m co R 40 . 0 E H r Cn H N p CD r� s u' / i > 20 . 0 H i-3 F-` N ro w � t7 m H w 0 . 0 -14 . 7 4 0 6 0 8 0 1 00 12700 1 00 1600 1 00 2 00 Utilities Report Equivalent K-Factor Calculator Node Sprinkler Press. Dia. Pipe Ftgs. Total H-W Equivalent Name K-Factor (psi) (in) Len. (ft) Len. (ft) coef. K-factor ------------------------------------- A 25.20 7.00 1.380 1.50 2E 7.50 120.00 21.77 End of Utilities Report