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7835 RUSH ROSE DR; ; AS050154; Permit
6/14/22, 3:29 PM AS050154 Permit Data City of Carlsbad Sprinkler Permit Job Address: 7835 RUSH ROSE DR Permit Type: SPRINK Parcel No: 2550121900 Lot#: 0 Reference No.: Permit No: AS050154 Status: ISSUED Applied 7/13/2005 Approved: 7/15/2005 Issued: 7/15/2005 PC #: Inspector: Project Title: LA COSTA GLEN UNDGR. FIRE SPRINKLER PLAN CHECK & INSPECTIONS Applicant: Owner: ACTION FIRE SYSTEMS CO., INC. 9185 HARNESS ST SPRING VALLEY, CA 91977-3948 619-462-9210 Fees($) Add'I Fees ($) 250 0 Total($) 250 Balance($) 0 1 /1 ACTION FIRE SYSTEMS CO.,INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR LA COSTA GLEN NORTH BLDG. D 7835 RUSH ROSE DR. CARLSBAD, CA. 92008 FILE NUMBER: 05-1013D3RD-REV2.SDF DATE: 9-23-05 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: CORRIDOR CALC (3RD FLOOR) COVERAGE PER SPRINKLER: 149 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 5 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 80.9 gpm TOTAL WATER REQUIRED (including hose): 180.9 gpm FLOW AND PRESSURE(@ BOR): 80.9 gpm@ 33.9 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: ACTION FIRE SYSTEMS CO., INC. DESIGN/LAYOUT BY: JB AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: LIC. #388160 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4904076910) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC WATER SUPPLY DATA SOURCE NODE TAG SOURCE STATIC PRESS. (PSI) 130.5 RESID. FLOW PRESS.@ (PSI) (GPM) 18.0 4000.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE AVAIL. PRESS. (PSI) 130.1 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 82A 83 83A 84 84A 85 85A 86 86A 87 88 89 90 90A 91 91A 92 92A ELEVATION (FT) 31.5 31.5 31.5 31.5 29.8 31.0 31.0 31.0 31.0 31.0 29.8 31. 5 31.5 31.5 29.8 31. 5 27.8 31. 5 29.0 31.5 29.0 31.5 29.0 31. 5 27.8 31. 5 29.8 29.8 31.0 29.0 31.0 29.0 31.0 29.0 NODE TYPE K= 5.62 K= 5.62 K= 5. 62 K= 5. 62 K= 5. 62 PRESSURE (PSI) 15.5 15.5 15.5 15.5 16.2 15.7 15.7 15.7 15.7 15.7 16.2 15.5 15.5 15.5 16.2 6.2 7.0 7.1 7.3 9.9 9.8 7.6 8.0 9.0 9.5 11.8 16.2 18.6 15.7 16.5 15.7 16.5 15.7 16.5 TOTAL @ DEMAND (GPM) 180.9 REQ'D PRESS. (PSI) 36.3 180.9 GPM 100.0 GPM 0.0 GPM 80.9 GPM DISCHARGE (GPM) 14.9 15.2 17.6 15.9 17.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 93 31.0 15.7 --- 93A 29.0 16.5 --- A 9.8 ----29.3 --- Al 9.8 29.6 --- A2 9.8 ----29.5 --- B 19.8 ----24.9 --- C 29.8 20.5 --- D 29.8 ----19.4 --- E 19.8 ----23.8 --- F 9.8 ----28.1 --- TOR 9.8 ----29.8 --- BOR 0.5 ----33.9 --- DI -3.0 ----35.5 --- UGl -3.0 ----35.7 --- UG2 -3.0 ----38.7 --- BFl 2.0 ----33.5 --- BF2 2.0 36.5 --- SOURCE 2.5 SOURCE 36.3 80.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC 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 0.0 1.049 PL 13.00 PF 0.0 68 31.5 0.0 15.5 0.0 0.0 120 FTG ----PE 0.0 67 31.5 0.0 15.5 0.0 0.000 TL 13.00 PV 0.0 Pipe: 2 0.0 1.049 PL 13.00 PF 0.0 69 31.5 0.0 15.5 0.0 0.0 120 FTG ----PE 0.0 68 31.5 0.0 15.5 0.0 0.000 TL 13.00 PV 0.0 Pipe: 3 0.0 1.380 PL 5.25 PF 0.0 70 31.5 0.0 15.5 0.0 0.0 120 FTG T PE 0.0 69 31.5 0.0 15.5 0.0 0.000 TL 11.25 PV 0.0 Pipe: 4 0.0 1. 380 PL 2.00 PF 0.0 71 29.8 0.0 16.2 0.0 0.0 120 FTG T PE -0.8 70 31. 5 0.0 15.5 0.0 0.000 TL 8.00 PV 0.0 Pipe: 5 0.0 1.610 PL 9.75 PF 0.0 77 29.8 0.0 16.2 0.0 0.0 120 FTG PE 0.0 71 29.8 0.0 16.2 0.0 0.000 TL 9.75 PV 0.0 Pipe: 6 0.0 1.049 PL 2.50 PF 0.0 90 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 72 31.0 0.0 15.7 0.0 0.000 TL 2.50 PV 0.0 Pipe: 7 0.0 1.049 PL 6. 50 PF 0.0 90 31.0 0.0 15.7 0.0 0.0 120 FTG ET PE 0.9 90A 29.0 0.0 16.5 0.0 0.000 TL 13.50 PV 0.0 Pipe: 8 0.0 1.049 PL 7.50 PF 0.0 73 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 90 31.0 0.0 15.7 0.0 0.000 TL 7.50 PV 0.0 Pipe: 9 0.0 1.049 PL 5.33 PF 0.0 91 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 73 31.0 0.0 15.7 0.0 0.000 TL 5.33 PV 0.0 Pipe: 10 0.0 1.049 PL 3.50 PF 0.0 91 31.0 0.0 15.7 0.0 0.0 120 FTG ET PE 0.9 91A 29.0 0.0 16.S 0.0 0.000 TL 10. 50 PV 0.0 Pipe: 11 0.0 1.049 PL 4.66 PF 0.0 74 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 91 31.0 0.0 15.7 0.0 0.000 TL 4.66 PV 0.0 Pipe: 12 0.0 1.380 PL 7.33 PF 0.0 92 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 74 31.0 0.0 15.7 0.0 0.000 TL 7.33 PV 0.0 Pipe: 13 0.0 1.049 PL 6. 50 PF 0.0 92 31.0 0.0 15.7 0.0 0.0 120 FTG ET PE 0.9 92A 29.0 0.0 16.5 0.0 0.000 TL 13.50 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC 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: 14 0.0 1. 380 PL 2.75 PF 0.0 75 31.0 0.0 15.7 0.0 0.0 120 FTG PE 0.0 92 31.0 0.0 15.7 0.0 0.000 TL 2.75 PV 0.0 Pipe: 15 0.0 1.380 PL 3.33 PF 0.0 76 31.0 0.0 15.7 0.0 0.0 120 FTG T PE 0.0 75 31.0 0.0 15.7 0.0 0.000 TL 9.33 PV 0.0 Pipe: 16 0.0 1.380 PL 1. 50 PF 0.0 77 29.8 0.0 16.2 0.0 0.0 120 FTG T PE -0.5 76 31.0 0.0 15.7 0.0 0.000 TL 7. 50 PV 0.0 Pipe: 17 0.0 1.610 PL 11.00 PF 0.0 81 29.8 0.0 16.2 0.0 0.0 120 FTG ----PE 0.0 77 29.8 0.0 16.2 0.0 0.000 TL 11.00 PV 0.0 Pipe: 18 0.0 1. 380 PL 3.33 PF 0.0 93 31.0 0.0 15.7 0.0 0.0 120 FTG PE -0.2 78 31.5 0.0 15.5 0.0 0.000 TL 3.33 PV 0.0 Pipe: 19 0.0 1.049 PL 7.50 PF 0.0 93 31.0 0.0 15.7 0.0 0.0 120 FTG E2T PE 0.9 93A 29.0 0.0 16.5 0.0 0.000 TL 19.50 PV 0.0 Pipe: 20 0.0 1.380 PL 6.66 PF 0.0 79 31.5 0.0 15.5 0.0 0.0 120 FTG PE 0.2 93 31.0 0.0 15.7 0.0 0.000 TL 6.66 PV 0.0 Pipe: 21 0.0 1.380 PL 3.50 PF 0.0 80 31. 5 0.0 15.5 0.0 0.0 120 FTG T PE 0.0 79 31.5 0.0 15.5 0.0 0.000 TL 9. 50 PV 0.0 Pipe: 22 0.0 1.380 PL 1. 75 . PF 0.0 81 29.8 0.0 16.2 0.0 0.0 120 FTG T PE -0.8 80 31. 5 0.0 15.5 0.0 0.000 TL 7.75 PV 0.0 Pipe: 23 0.0 1.610 PL 8.75 PF 0.0 88 29.8 0.0 16.2 0.0 0.0 120 FTG PE 0.0 81 29.8 0.0 16.2 0.0 0.000 TL 8.75 PV 0.0 Pipe: 24 14.9 1.049 PL 5.83 PF 0.8 82 31.5 0.0 6.2 0.0 5.5 120 FTG T PE 1.6 82A 27.8 5.6 7.0 14.9 0.075 TL 10.83 PV 0.2 Pipe: 25 14.9 1.049 PL 12.00 PF 0.9 83 31.5 0.0 7.1 0.0 5.5 120 FTG ----PE 0.0 82 31.5 0.0 6.2 0.0 0.075 TL 12.00 PV 0.2 Pipe: 26 15.2 1.049 PL 4.00 PF 0.9 83 31.5 0.0 7.1 0.0 5.6 120 FTG ET PE 1.1 83A 29.0 5.6 7.3 15.2 0.078 TL 11.00 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page S DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR SHD PEND CORRIDOR CALC 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: 27 30.1 1.049 PL 10.00 PF 2.8 84 31.S 0.0 9.9 0.0 11.2 120 FTG ----PE 0.0 83 31.S 0.0 7.1 0.0 0.277 TL 10.00 PV 0.8 Pipe: 28 17.6 1.049 PL 4.00 PF 1.1 84 31.S 0.0 9.9 0.0 6.5 120 FTG ET PE 1.1 84A 29.0 5.6 9.8 17.6 0.103 TL 11.00 PV 0.3 Pipe: 29 47.7 1.380 PL 5.33 PF 1.9 87 31.S 0.0 11.8 0.0 10.2 120 FTG T PE 0.0 84 31.S 0.0 9.9 0.0 0.171 TL 11.33 PV 0.7 Pipe: .30 15.9 1.049 PL 4.00 PF 0.7 85 31.S 0.0 7.6 0.0 5.9 120 FTG 2E PE 1.1 BSA 29.0 5.6 8.0 15.9 0.085 TL 8.00 PV 0.2 Pipe: 31 15.9 1.049 PL 16.33 PF 1.4 86 31. S 0.0 9.0 0.0 5.9 120 FTG ----PE 0.0 85 31.S 0.0 7.6 0.0 0.085 TL 16.33 PV 0.2 Pipe: 32 17.4 1.049 PL 5.33 PF 1.0 86 31.S 0.0 9.0 0.0 6.4 120 FTG T PE 1.6 86A 27.8 5.6 9.5 17.4 0.100 TL 10.33 PV 0.3 Pipe: 33 33.2 1.049 PL 3.58 PF 2.9 87 31.S 0.0 11.8 0.0 12.3 120 FTG T PE 0.0 86 31.S 0.0 9.0 0.0 0.333 TL 8. 58 PV 1.0 Pipe: 34 80.9 1. 380 PL 2.00 PF 3.6 88 29.8 0.0 16.2 0.0 17.4 120 FTG T PE -0.8 87 31.S 0.0 11.8 0.0 0.454 TL 8.00 PV 2.0 Pipe: 35 80.9 1.610 PL 3.00 PF 2.4 89 29.8 0.0 18.6 0.0 12.8 120 FTG T PE 0.0 88 29.8 0.0 16.2 0.0 0. 215 TL 11.00 PV 1.1 Pipe: 36 49.3 2.703 PL 257.50 PF 1.9 C 29.8 0.0 20.S 0.0 2.8 120 FTG T3L PE 0.0 89 29.8 0.0 18.6 0.0 0.007 TL 281.50 PV 0.1 Pipe: 37 31.7 2.703 PL 249.50 PF 0.9 D 29.8 0.0 19.4 0.0 1.8 120 FTG 3TL PE 0.0 89 29.8 0.0 18.6 0.0 0.003 TL 289.50 PV 0.0 Pipe: 38 49.3 2.703 PL 10.00 PF 0.1 B 19.8 0.0 24.9 0.0 2.8 120 FTG ----PE -4.3 C 29.8 0.0 20.S 0.0 0.007 TL 10.00 PV 0.1 Pipe: 39 31.7 2.703 PL 10.00 PF 0.0 E 19.8 0.0 23.8 0.0 1.8 120 FTG ----PE -4.3 D 29.8 0.0 19.4 0.0 0.003 TL 10.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC 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: 40 14.5 2.203 PL 507.00 PF 1.1 B 19.8 0.0 24.9 0.0 1.2 120 FTG 4T6L PE 0.0 E 19.8 0.0 23.8 0.0 0.002 TL 565.00 PV 0.0 Pipe: 41 63.7 2.703 PL 10.00 PF 0.1 A 9.8 0.0 29.3 0.0 3.6 120 FTG ----PE -4.3 B 19.8 0.0 24.9 0.0 0.011 TL 10.00 PV 0.1 Pipe: 42 17.2 2.703 PL 10.00 PF 0.0 F 9.8 0.0 28.1 0.0 1.0 120 FTG ----PE -4.3 E 19.8 0.0 23.8 0.0 0.001 TL 10.00 PV 0.0 Pipe: 43 17.2 2.203 PL 501.00 PF 1.4 A2 9.8 0.0 29.5 0.0 1.4 120 FTG 2T2L PE 0.0 F 9.8 0.0 28.1 0.0 0.003 TL 527.00 PV 0.0 Pipe: 44 17.2 2.203 PL 8. 50 PF 0.0 Al 9.8 0.0 29.6 0.0 1.4 120 FTG T PE 0.0 A2 9.8 0.0 29.5 0.0 0.003 TL 18.50 PV 0.0 Pipe: 45 63.7 2.703 PL 7.00 PF 0.3 Al 9.8 0.0 29.6 0.0 3.6 120 FTG TL PE 0.0 A 9.8 0.0 29.3 0.0 0.011 TL 23.00 PV 0.1 Pipe: 46 80.9 3.314 PL 20.00 PF 0.2 TOR 9.8 0.0 29.8 0.0 3.0 120 FTG 2L PE 0.0 Al 9.8 0.0 29.6 0.0 0.006 TL 30.00 PV 0.1 Pipe: 47 80.9 3.314 PL 12.75 PF 0.1 BOR 0. 5 0.0 33.9 0.0 3.0 120 FTG 2L PE -4.0 TOR 9.8 0.0 29.8 0.0 0.006 TL 22.75 PV 0.1 Pipe: 48 80.9 4.220 PL 9.00 PF 0.0 DI -3.0 0.0 35.5 0.0 1.9 140 FTG L PE -1.5 BOR 0. 5 0.0 33.9 0.0 0.001 TL 20.00 PV 0.0 Pipe: 49 80.9 4.240 PL 108.00 PF 0.2 UGl -3.0 0.0 35.7 0.0 1.8 150 FTG 2L PE 0.0 DI -3.0 0.0 35.S 0.0 0.001 TL 132.00 PV 0.0 Pipe: so 80.9 6.280 PL 5.00 PF 0.0 BFl 2.0 0.0 33.5 0.0 0.8 140 FTG L PE 2.2 UGl -3.0 0.0 35.7 0.0 0.000 TL 21.00 PV 0.0 Pipe: 51 FIXED PRESSURE LOSS DEVICE BF2 2.0 0.0 36.5 0.0 3.0 psi, 80.9 gpm BFl 2.0 0.0 33.5 0.0 Pipe: 52 80.9 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 38.7 0.0 0.8 140 FTG L PE -2.2 BF2 2.0 0.0 36.5 0.0 0.000 TL 21.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 5HD PEND CORRIDOR CALC 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: 53 80.9 6.080 PL 16.00 PF 0.0 SOURCE 2.5 SRCE 36.3 (N/A) 0.9 150 FTG TLG PE 2.4 UG2 -3.0 0.0 38.7 0.0 0.000 TL 81.00 PV 0.0 NOTES: (1) calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (2) The system has ·been calculated to provide an average imbalance at each node of 0.001 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 17.4 ft/sec at pipe 34. (4) 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 Ell Tee LngEll Chkvlv Bfyvlv Gatvlv Almchk DPVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 4.220 18.00 36.00 11.00 39.00 22.00 4.00 36.00 6. 280 24.00 52.00 16.00 55.00 17.00 5.00 52.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 4.240 19.00 39.00 12.00 43.00 23.00 4.00 39.00 6.080 21.00 46.00 14.00 49.00 15.00 5.00 46.00 N NPTee 5.00 6.00 8.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR SHD PEND CORRIDOR CALC PAGE: F Diameter (in) 2.203 2.703 3.314 MATERIAL: DYNAFL HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 5.00 10.00 3.00 11.00 6.00 1.00 10.00 6.00 12.00 4.00 14.00 7.00 1.00 10.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 D 45ELL 1.80 2.20 2.60 N 0.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV2.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR SHD PEND CORRIDOR CALC WATER SUPPLY ANALYSIS G A u G E p R E s s u R E ( p s i ) 112.0 84.0 56.0 2 28.0 Static: 130.50 psi Resid: 18.00 psi Flow: 4000.0 gpm 80,120<1600 2000 2400 2800 3200 FLOW (GPM) 3600 1 ~ 2 ~ 4000 LEGEND Available pressure 130.13 psi@ 180.9 Required pressure 36.31 psi@ 180.9 gpm gpm ACTION FIRE SYSTEMS CO.,INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR LA COSTA GLEN NORTH BLDG. D 7835 RUSH ROSE DR. CARLSBAD, CA. 92008 FILE NUMBER: 05-1013D3RD-REV1.SDF DATE: 9-23-05 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHTY HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: DWELLING UNIT (3RD FLOOR) COVERAGE PER SPRINKLER: 324 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 145.2 gpm TOTAL WATER REQUIRED (including hose): 245.2 gpm FLOW AND PRESSURE(@ BOR): 145.2 gpm@ 108.8 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: ACTION FIRE SYSTEMS CO., INC. DESIGN/LAYOUT BY: JB AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: LIC. #388160 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4904076910) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC WATER SUPPLY DATA SOURCE NODE TAG SOURCE STATIC PRESS. (PSI) 130.S RESID. FLOW PRESS.@ (PSI) (GPM) 18.0 4000.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE AVAIL. PRESS. (PSI) 129.9 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 82A 83 83A 84 84A 85 85A 86 86A 87 88 89 90 90A 91 91A 92 92A ELEVATION (FT) 31.S 31. 5 31. 5 31.S 29.8 31.0 31.0 31.0 31.0 31.0 29.8 31.S 31. 5 31.S 29.8 31.S 27.8 31. S 29.0 31. 5 29.0 31.S 29.0 31.5 27.8 31.S 29.8 29.8 31.0 29.0 31.0 29.0 31.0 29.0 NODE TYPE K= 5. 50 K= 5. 50 K= 5. 50 PRESSURE (PSI) 64.1 64.1 64.1 64.1 64.9 38.1 40.5 47.9 52.2 58.9 64.9 64.8 65.6 66.9 68.6 73.4 75.0 73.4 74.5 73.4 74.5 73.4 74.S 73.4 75.0 73.4 74.2 81.1 38.1 34.7 42.2 39.3 50.2 45.6 TOTAL @ DEMAND (GPM) REQ'D PRESS. (PSI) 245.2 111.6 245. 2 GPM 100.0 GPM 0.0 GPM 145.2 GPM DISCHARGE (GPM) 32.4 34.5 37.1 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 93 31.0 ----65 .0 --- 93A 29.0 K= 5. 50 56.2 41.2 A 9.8 103.1 --- Al 9.8 103.8 --- A2 9.8 ----103.6 --- B 19.8 ----98.4 --- C 29.8 ----93.9 --- D 29.8 -----89.8 --- E 19.8 94.2 --- F 9.8 ----98.6 --- TOR 9.8 -----104.4 --- BOR 0. 5 ----108.8 --- DI -3.0 110.4 --- UGl -3.0 ----110.9 --- UG2 -3.0 ----113.9 --- BFl 2.0 ----108.8 --- BF2 2.0 111.8 --- SOURCE 2.5 SOURCE 111.6 145.2 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC 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 0.0 1.049 PL 13.00 PF 0.0 68 31.S 0.0 64.1 0.0 0.0 120 FTG ----PE 0.0 67 31.S 0.0 64.1 0.0 0.000 TL 13.00 PV 0.0 Pipe: 2 0.0 1.049 PL 13.00 PF 0.0 69 31.S 0.0 64.1 0.0 0.0 120 FTG ----PE 0.0 68 31.S 0.0 64.1 0.0 0.000 TL 13.00 PV 0.0 Pipe: 3 0.0 1.380 PL 5.25 PF 0.0 70 31.S 0.0 64.1 0.0 0.0 120 FTG T PE 0.0 69 31.S 0.0 64.1 0.0 0.000 TL 11.25 PV 0.0 Pipe: 4 0.0 1. 380 PL 2.00 PF 0.0 71 29.8 0.0 64.9 0.0 0.0 120 FTG T PE -0.8 70 31.S 0.0 64.1 0.0 0.000 TL 8.00 PV 0.0 Pipe: s 0.0 1.610 PL 9.75 PF 0.0 77 29.8 0.0 64.9 0.0 0.0 120 FTG PE 0.0 71 29.8 0.0 64.9 0.0 0.000 TL 9.75 PV 0.0 Pipe: 6 0.0 1.049 PL 2.50 PF 0.0 90 31.0 0.0 38.1 0.0 0.0 120 FTG PE 0.0 72 31.0 0.0 38.1 0.0 0.000 TL 2.50 PV 0.0 Pipe: 7 32.4 1.049 PL 6. so PF 4.3 90 31.0 0.0 38.1 0.0 12.0 120 FTG ET PE 0.9 90A 29.0 5.5 34.7 32.4 0.318 TL 13.50 PV 1.0 Pipe: 8 32.4 1.049 PL 7.50 PF 2.4 73 31.0 0.0 40.S 0.0 12.0 120 FTG PE 0.0 90 31.0 0.0 38.1 0.0 o. 318 TL 7.50 PV 1.0 Pipe: 9 32.4 1.049 PL 5.33 PF 1.7 91 31.0 0.0 42.2 0.0 12.0 120 FTG PE 0.0 73 31.0 0.0 40.5 0.0 o. 318 TL 5.33 PV 1.0 Pipe: 10 34.S 1.049 PL 3.50 PF 3.7 91 31.0 0.0 42.2 0.0 12.8 120 FTG ET PE 0.9 91A 29.0 5.5 39.3 34.S 0.357 TL 10. so PV 1.1 Pipe: 11 66.9 1.049 PL 4.66 PF 5.7 74 31.0 0.0 47.9 0.0 24.8 120 FTG PE 0.0 91 31.0 0.0 42.2 0.0 1.214 TL 4.66 PV 4.1 Pipe: 12 66.9 1.380 PL 7.33 PF 2.3 92 31.0 0.0 50.2 0.0 14.3 120 FTG PE 0.0 74 31.0 0.0 47.9 0.0 0. 319 TL 7.33 PV 1.4 Pipe: 13 37.1 1.049 PL 6. so PF 5.5 92 31.0 0.0 50.2 0.0 13.8 120 FTG ET PE 0.9 92A 29.0 5.5 45.6 37.1 0.408 TL 13.50 PV 1.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC 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: 14 104.0 1. 380 PL 2.75 PF 2.0 75 31.0 0.0 52.2 0.0 22.3 120 FTG PE 0.0 92 31.0 0.0 50.2 0.0 0.723 TL 2.75 PV 3.3 Pipe: 15 104.0 1.380 PL 3.33 PF 6.7 76 31.0 0.0 58.9 0.0 22.3 120 FTG T PE 0.0 75 31.0 0.0 52.2 0.0 0.723 TL 9.33 PV 3.3 Pipe: 16 104.0 1.380 PL 1. 50 PF 5.4 77 29.8 0.0 64.9 0.0 22.3 120 FTG T PE -0.5 76 31.0 0.0 58.9 0.0 0.723 TL 7.50 PV 3.3 Pipe: 17 104.0 1.610 PL 11.00 PF 3.8 81 29.8 0.0 68.6 0.0 16.4 120 FTG ----PE 0.0 77 29.8 0.0 64.9 0.0 0. 341 TL 11.00 PV 1.8 Pipe: 18 0.0 1.380 PL 3.33 PF 0.0 93 31.0 0.0 65.0 0.0 0.0 120 FTG PE -0.2 78 31.5 0.0 64.8 0.0 0.000 TL 3.33 PV 0.0 Pipe: 19 41.2 1.049 PL 7. 50 PF 9.7 93 31.0 0.0 65.0 0.0 15.3 120 FTG E2T PE 0.9 93A 29.0 5.5 56.2 41.2 0.496 TL 19. 50 PV 1.6 Pipe: 20 41.2 1. 380 PL 6.66 PF 0.9 79 31.5 0.0 65.6 0.0 8.8 120 FTG PE 0.2 93 31.0 0.0 65 .0 0.0 0.130 TL 6.66 PV 0.5 Pipe: 21 41.2 1. 380 PL 3.50 PF 1.2 80 31.5 0.0 66.9 0.0 8.8 120 FTG T PE 0.0 79 31.5 0.0 65.6 0.0 0.130 TL 9. 50 PV 0. 5 Pipe: 22 41.2 1.380 PL 1. 75 PF 1.0 81 29.8 0.0 68.6 0.0 8.8 120 FTG T PE -0.8 80 31.5 0.0 66.9 0.0 0.130 TL 7.75 PV 0.5 Pipe: 23 145. 2 1.610 PL 8.75 PF 5.5 88 29.8 0.0 74.2 0.0 22.9 120 FTG PE 0.0 81 29.8 0.0 68.6 0.0 0.633 TL 8.75 PV 3.5 Pipe: 24 0.0 1.049 PL 5.83 PF 0.0 82 31. 5 0.0 73.4 0.0 0.0 120 FTG T PE 1.6 82A 27.8 0.0 75.0 0.0 0.000 TL 10.83 PV 0.0 Pipe: 25 0.0 1.049 PL 12.00 PF 0.0 83 31.5 0.0 73.4 0.0 0.0 120 FTG ----PE 0.0 82 31.5 0.0 73.4 0.0 0.000 TL 12.00 PV 0.0 Pipe: 26 0.0 1.049 PL 4.00 PF 0.0 83 31.5 0.0 73.4 0.0 0.0 120 FTG ET PE 1.1 83A 29.0 0.0 74.5 0.0 0.000 TL 11.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC 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: 27 0.0 1.049 PL 10.00 PF 0.0 84 31.5 0.0 73.4 0.0 0.0 120 FTG ----PE 0.0 83 31.5 0.0 73.4 0.0 0.000 TL 10.00 PV 0.0 Pipe: 28 0.0 1.049 PL 4.00 PF 0.0 84 31.5 0.0 73.4 0.0 0.0 120 FTG ET PE 1.1 84A 29.0 0.0 74.5 0.0 0.000 TL 11.00 PV 0.0 Pipe: 29 0.0 1. 380 PL 5.33 PF 0.0 87 31. 5 0.0 73.4 0.0 0.0 120 FTG T PE 0.0 84 31.5 0.0 73.4 0.0 0.000 TL 11.33 PV 0.0 Pipe: 30 0.0 1.049 PL 4.00 PF 0.0 85 31. 5 0.0 73.4 0.0 0.0 120 FTG 2E PE 1.1 85A 29.0 0.0 74.5 0.0 0.000 TL 8.00 PV 0.0 Pipe: 31 0.0 1.049 PL 16.33 PF 0.0 86 31.5 0.0 73.4 0.0 0.0 120 FTG ----PE 0.0 85 31.5 0.0 73.4 0.0 0.000 TL 16.33 PV 0.0 Pipe: 32 0.0 1.049 PL 5.33 PF 0.0 86 31.5 0.0 73.4 0.0 0.0 120 FTG T PE 1.6 86A 27.8 0.0 75.0 0.0 0.000 TL 10. 33 PV 0.0 Pipe: 33 0.0 1.049 PL 3.58 PF 0.0 87 31.5 0.0 73.4 0.0 0.0 120 FTG T PE 0.0 86 31.5 0.0 73.4 0.0 0.000 TL 8.58 PV 0.0 Pipe: 34 0.0 1.380 PL 2.00 PF 0.0 88 29.8 0.0 74.2 0.0 0.0 120 FTG T PE -0.8 87 31.5 0.0 73.4 0.0 0.000 TL 8.00 PV 0.0 Pipe: 35 145. 2 1.610 PL 3.00 PF 7.0 89 29.8 0.0 81.1 0.0 22.9 120 FTG T PE 0.0 88 29.8 0.0 74.2 0.0 0.633 TL 11.00 PV 3.5 Pipe: 36 80.7 2.203 PL 257.50 PF 12.8 C 29.8 0.0 93.9 0.0 6.8 120 FTG T3L PE 0.0 89 29.8 0.0 81.1 0.0 0.046 TL 276.50 PV 0.3 Pipe: 37 64.5 2.203 PL 249.50 PF 8.6 D 29.8 0.0 89.8 0.0 5.4 120 FTG 3TL PE 0.0 89 29.8 0.0 81.1 0.0 0.031 TL 282.50 PV 0.2 Pipe: 38 80.7 2.703 PL 10.00 PF 0.2 B 19.8 0.0 98.4 0.0 4.5 120 FTG ----PE -4.3 C 29.8 0.0 93.9 0.0 0.017 TL 10.00 PV 0.1 Pipe: 39 64.5 2.703 PL 10.00 PF 0.1 E 19.8 0.0 94.2 0.0 3.6 120 FTG ----PE -4.3 D 29.8 0.0 89.8 0.0 0.011 TL 10.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC 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: 40 30.1 2.203 PL 507.00 PF 4.2 B 19.8 0.0 98.4 0.0 2.5 120 FTG 4T6L PE 0.0 E 19.8 0.0 94.2 0.0 0.007 TL 565.00 PV 0.0 Pipe: 41 110.9 2.703 PL 10.00 PF 0.3 A 9.8 0.0 103.1 0.0 6.2 120 FTG ----PE -4.3 B 19.8 0.0 98.4 0.0 0.031 TL 10.00 PV 0.3 Pipe: 42 34.4 2.703 PL 10.00 PF 0.0 F 9.8 0.0 98.6 0.0 1.9 120 FTG ----PE -4.3 E 19.8 0.0 94.2 0.0 0.004 TL 10.00 PV 0.0 Pipe: 43 34.4 2.203 PL 501.00 PF 5.0 A2 9.8 0.0 103.6 0.0 2.9 120 FTG 2T2L PE 0.0 F 9.8 0.0 98.6 0.0 0.010 TL 527.00 PV 0.1 Pipe: 44 34.4 2.203 PL 8. 50 PF 0.2 Al 9.8 0.0 103.8 0.0 2.9 120 FTG T PE 0.0 A2 9.8 0.0 103.6 0.0 0.010 TL 18.50 PV 0.1 Pipe: 45 110.9 2.703 PL 7.00 PF 0.7 Al 9.8 0.0 103.8 0.0 6.2 120 FTG TL PE 0.0 A 9.8 0.0 103.1 0.0 0.031 TL 23.00 PV 0.3 Pipe: 46 145. 2 3.314 PL 20.00 PF 0.6 TOR 9.8 0.0 104.4 0.0 5.4 120 FTG 2L PE 0.0 Al 9.8 0.0 103.8 0.0 0.019 TL 30.00 PV 0.2 Pipe: 47 145. 2 3.314 PL 12.75 PF 0.4 BOR 0. 5 0.0 108.8 0.0 5.4 120 FTG 2L PE -4.0 TOR 9.8 0.0 104.4 0.0 0.019 TL 22.75 PV 0.2 Pipe: 48 145.2 4.220 PL 9.00 PF 0.1 DI -3.0 0.0 110.4 0.0 3.3 140 FTG L PE -1.5 BOR 0.5 0.0 108.8 0.0 0.004 TL 20.00 PV 0.1 Pipe: 49 145. 2 4.240 PL 108.00 PF 0.5 UGl -3.0 0.0 110.9 0.0 3.3 150 FTG 2L PE 0.0 DI -3.0 0.0 110.4 0.0 0.004 TL 132.00 PV 0.1 Pipe: 50 145. 2 6.280 PL 5.00 PF 0.0 BFl 2.0 0.0 108.8 0.0 1.5 140 FTG L PE 2.2 UGl -3.0 0.0 110.9 0.0 0.001 TL 21.00 PV 0.0 Pipe: 51 FIXED PRESSURE LOSS DEVICE BF2 2.0 0.0 111.8 0.0 3.0 psi, 145. 2 gpm BFl 2.0 0.0 108.8 0.0 Pipe: 52 145. 2 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 113.9 0.0 1.5 140 FTG L PE -2.2 BF2 2.0 0.0 111.8 0.0 0.001 TL 21.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC 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: 53 145.2 6.080 PL 16.00 PF 0.1 SOURCE 2.5 SRCE 111.6 (N/A) 1.6 150 FTG TLG PE 2.4 UG2 -3.0 0.0 113.9 0.0 0.001 TL 81.00 PV 0.0 NOTES: (1) calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (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 0.183 gpm. (3) velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 24.8 ft/sec at pipe 11. (4) 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 Ell Tee LngEll chkvlv Bfyvlv Gatvlv Almchk DPVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 4.220 18.00 36.00 11.00 39.00 22.00 4.00 36.00 6.280 24.00 52.00 16.00 55.00 17.00 5.00 52.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 4.240 19.00 39.00 12.00 43.00 23.00 4.00 39.00 6.080 21.00 46.00 14.00 49.00 15.00 5.00 46.00 N NPTee 5.00 6.00 8.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC PAGE: F Diameter (in) 2.203 2.703 3.314 MATERIAL: DYNAFL HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 5.00 10.00 3.00 11.00 6.00 1.00 10.00 6.00 12.00 4.00 14.00 7.00 1.00 10.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 D 45ELL 1.80 2.20 2.60 N 0.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV1.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR 4HD PEND UNIT CALC WATER SUPPLY ANALYSIS G A u G E p R E s s u R E ( p s i ) 140.0 1 112.<2 84.0 56.0 28.0 static: 130.50 psi Resid: 18.00 psi Flow: 4000.0 gpm 80 1120(1600 2000 2400 2800 3200 FLOW (GPM) 3600 1 ~ 2 ~ 4000 LEGEND Available pressure 129.86 psi@ 245.2 Required pressure 111.60 psi@ 245.2 gpm gpm ACTION FIRE SYSTEMS CO.,INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR LA COSTA GLEN NORTH BLDG. D 7835 RUSH ROSE DR. CARLSBAD, CA. 92008 FILE NUMBER: 05-1013D3RD-REV.SDF DATE: 9-23-05 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: 984 sq. ft. (3RD FLR ROOF ATTIC) COVERAGE PER SPRINKLER: 130 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 9 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 169.8 gpm TOTAL WATER REQUIRED (including hose): 269.8 gpm FLOW AND PRESSURE(@ BOR): 169.8 gpm@ 63.4 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: ACTION FIRE SYSTEMS CO., INC. DESIGN/LAYOUT BY: JB AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: LIC. #388160 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4904076910) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC WATER SUPPLY DATA SOURCE NODE TAG SOURCE STATIC PRESS. (PSI) 130.5 RESID. FLOW PRESS.@ (PSI) (GPM) 18.0 4000.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE AVAIL. PRESS. (PSI) 129.7 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 82A 83 83A 84 84A 85 85A 86 86A 87 88 89 90 90A 91 91A 92 92A ELEVATION (FT) 31.5 31.5 31.5 31.5 29.8 31.0 31.0 31.0 31.0 31.0 29.8 31. 5 31.5 31.5 29.8 31. 5 27.8 31.5 29.0 31. 5 29.0 31.5 29.0 31.5 27.8 31.5 29.8 29.8 31.0 29.0 31.0 29.0 31.0 29.0 NODE TYPE K= 5. 60 K= 5.60 K= 5. 60 K= 5. 60 K= 5. 60 K= 5. 60 K= 5. 60 K= 5. 60 K= 5. 60 PRESSURE (PSI) 7.7 8.8 12.9 15.2 17.5 7.0 7.7 10.6 12.3 15 .4 18.5 19.0 19.5 21.2 23.4 30.0 31.6 30.0 31.1 30.0 31.1 30.0 31.1 30.0 31.6 30.0 30.8 40.1 7.2 8.1 9.3 10.1 11.9 12.7 TOTAL @ DEMAND (GPM) 269.8 REQ'D PRESS. (PSI) 66.4 269.8 GPM 100.0 GPM 0.0 GPM 169.8 GPM DISCHARGE (GPM) 15.6 16.6 20.1 14.8 15.6 18.2 19.7 24.4 24.7 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 93 31.0 ----19.4 --- 93A 29.0 20.3 --- A 9.8 ----57.0 --- Al 9.8 ----58.0 --- A2 9.8 57.8 --- B 19.8 52.3 --- C 29.8 ----47.7 --- D 29.8 ----43.5 --- E 19.8 48.0 --- F 9.8 52.3 --- TOR 9.8 58.8 --- BOR 0.5 ----63.4 --- DI -3.0 65 .0 --- UGl -3.0 65.7 --- UG2 -3.0 ----68.7 --- BFl 2.0 ----63.5 --- BF2 2.0 ----66.5 --- SOURCE 2.5 SOURCE 66.4 169.8 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC 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 15.6 1.049 PL 13.00 PF 1.1 68 31.5 5.6 8.8 16.6 5.8 120 FTG ----PE 0.0 67 31.5 5.6 7.7 15.6 0.082 TL 13.00 PV 0.2 Pipe: 2 32.2 1.049 PL 13.00 PF 4.1 69 31.5 5.6 12.9 20.1 12.0 120 FTG ----PE 0.0 68 31.5 5.6 8.8 16.6 o. 314 TL 13.00 PV 1.0 Pipe: 3 52.3 1.380 PL 5.25 PF 2.3 70 31.5 0.0 15.2 0.0 11.2 120 FTG T PE 0.0 69 31.5 5.6 12.9 20.1 0.203 TL 11.25 PV 0.8 Pipe: 4 52.3 1.380 PL 2.00 PF 1.6 71 29.8 0.0 17.5 0.0 11.2 120 FTG T PE -0.8 70 31.5 0.0 15.2 0.0 0.203 TL 8.00 PV 0.8 Pipe: 5 52.3 1.610 PL 9.75 PF 0.9 77 29.8 0.0 18.5 0.0 8.2 120 FTG PE 0.0 71 29.8 0.0 17.5 0.0 0.096 TL 9.75 PV 0. 5 Pipe: 6 14.8 1.049 PL 2.50 PF 0.2 90 31.0 0.0 7.2 0.0 5.5 120 FTG PE 0.0 72 31.0 5.6 7.0 14.8 0.075 TL 2.50 PV 0.2 Pipe: 7 0.0 1.049 PL 6. 50 PF 0.0 90 31.0 0.0 7.2 0.0 0.0 120 FTG ET PE 0.9 90A 29.0 0.0 8.1 0.0 0.000 TL 13.50 PV 0.0 Pipe: 8 14.8 1.049 PL 7.50 PF 0.6 73 31.0 5.6 7.7 15.6 5.5 120 FTG PE 0.0 90 31.0 0.0 7.2 0.0 0.075 TL 7.50 PV 0.2 Pipe: 9 30.4 1.049 PL 5.33 PF 1.5 91 31.0 0.0 9.3 0.0 11.3 120 FTG PE 0.0 73 31.0 5.6 7.7 15.6 0.282 TL 5.33 PV 0.9 Pipe: 10 0.0 1.049 PL 3.50 PF 0.0 91 31.0 0.0 9.3 0.0 0.0 120 FTG ET PE 0.9 91A 29.0 0.0 10.1 0.0 0.000 TL 10. 50 PV 0.0 Pipe: 11 30.4 1.049 PL 4.66 PF 1.3 74 31.0 5.6 10.6 18.2 11.3 120 FTG PE 0.0 91 31.0 0.0 9.3 0.0 0.282 TL 4.66 PV 0.9 Pipe: 12 48.6 1.380 PL 7.33 PF 1.3 92 31.0 0.0 11.9 0.0 10.4 120 FTG PE 0.0 74 31.0 5.6 10.6 18.2 0.177 TL 7.33 PV 0.7 Pipe: 13 0.0 1.049 PL 6. 50 PF 0.0 92 31.0 0.0 11.9 0.0 0.0 120 FTG ET PE 0.9 92A 29.0 0.0 12.7 0.0 0.000 TL 13.50 PV 0.0 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC 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: 14 48.6 1. 380 PL 2.75 PF 0. 5 75 31.0 5.6 12.3 19.7 10.4 120 FTG PE 0.0 92 31.0 0.0 11.9 0.0 0.177 TL 2.75 PV 0.7 Pipe: 15 68.3 1.380 PL 3.33 PF 3.1 76 31.0 0.0 15.4 0.0 14.6 120 FTG T PE 0.0 75 31.0 5.6 12.3 19.7 0.332 TL 9.33 PV 1.4 Pipe: 16 68.3 1. 380 PL 1. so PF 2.5 77 29.8 0.0 18.S 0.0 14.6 120 FTG T PE -0.S 76 31.0 0.0 15.4 0.0 0.332 TL 7. so PV 1.4 Pipe: 17 120.6 1.610 PL 11.00 PF 4.9 81 29.8 0.0 23.4 0.0 19.0 120 FTG -----PE 0.0 77 29.8 0.0 18.5 0.0 0.448 TL 11.00 PV 2.4 Pipe: 18 24.4 1. 380 PL 3.33 PF 0.2 93 31.0 0.0 19.4 0.0 5.2 120 FTG PE -0.2 78 31.5 5.6 19.0 24.4 0.050 TL 3.33 PV 0.2 Pipe: 19 0.0 1.049 PL 7.50 PF 0.0 93 31.0 0.0 19.4 0.0 0.0 120 FTG E2T PE 0.9 93A 29.0 0.0 20.3 0.0 0.000 TL 19. so PV 0.0 Pipe: 20 24.4 1.380 PL 6.66 PF 0.3 79 31.5 5.6 19.S 24.7 5.2 120 FTG PE 0.2 93 31.0 0.0 19.4 0.0 0.050 TL 6.66 PV 0.2 Pipe: 21 49.2 1. 380 PL 3.50 PF 1.7 80 31. 5 0.0 21. 2 0.0 10. 5 120 FTG T PE 0.0 79 31.5 5.6 19.S 24.7 0.181 TL 9. so PV 0.7 Pipe: 22 49.2 1.380 PL 1.75 PF 1.4 81 29.8 0.0 23.4 0.0 10.S 120 FTG T PE -0.8 80 31. 5 0.0 21. 2 0.0 0.181 TL 7.75 PV 0.7 Pipe: 23 169.8 1.610 PL 8.75 PF 7.4 88 29.8 0.0 30.8 0.0 26.8 120 FTG PE 0.0 81 29.8 0.0 23.4 0.0 0.844 TL 8.75 PV 4.8 Pipe: 24 0.0 1.049 PL 5.83 PF 0.0 82 31. 5 0.0 30.0 0.0 0.0 120 FTG T PE 1.6 82A 27.8 0.0 31.6 0.0 0.000 TL 10.83 PV 0.0 Pipe: 25 0.0 1.049 PL 12.00 PF 0.0 83 31. 5 0.0 30.0 0.0 0.0 120 FTG ----PE 0.0 82 31.5 0.0 30.0 0.0 0.000 TL 12.00 PV 0.0 Pipe: 26 0.0 1.049 PL 4.00 PF 0.0 83 31.5 0.0 30.0 0.0 0.0 120 FTG ET PE 1.1 83A 29.0 0.0 31.1 0.0 0.000 TL 11.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC 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: 27 0.0 1.049 PL 10.00 PF 0.0 84 31. 5 0.0 30.0 0.0 0.0 120 FTG ----PE 0.0 83 31.5 0.0 30.0 0.0 0.000 TL 10.00 PV 0.0 Pipe: 28 0.0 1.049 PL 4.00 PF 0.0 84 31.5 0.0 30.0 0.0 0.0 120 FTG ET PE 1.1 84A 29.0 0.0 31.1 0.0 0.000 TL 11.00 PV 0.0 Pipe: 29 0.0 1.380 PL 5.33 PF 0.0 87 31.5 0.0 30.0 0.0 0.0 120 FTG T PE 0.0 84 31.5 0.0 30.0 0.0 0.000 TL 11.33 PV 0.0 Pipe: 30 0.0 1.049 PL 4.00 PF 0.0 85 31. 5 0.0 30.0 0.0 0.0 120 FTG 2E PE 1.1 85A 29.0 0.0 31.1 0.0 0.000 TL 8.00 PV 0.0 Pipe: 31 0.0 1.049 PL 16.33 PF 0.0 86 31. 5 0.0 30.0 0.0 0.0 120 FTG ----PE 0.0 85 31. 5 0.0 30.0 0.0 0.000 TL 16.33 PV 0.0 Pipe: 32 0.0 1.049 PL 5.33 PF 0.0 86 31.5 0.0 30.0 0.0 0.0 120 FTG T PE 1.6 86A 27.8 0.0 31.6 0.0 0.000 TL 10.33 PV 0.0 Pipe: 33 0.0 1.049 PL 3.58 PF 0.0 87 31. 5 0.0 30.0 0.0 0.0 120 FTG T PE 0.0 86 31.5 0.0 30.0 0.0 0.000 TL 8. 58 PV 0.0 Pipe: 34 0.0 1. 380 PL 2.00 PF 0.0 88 29.8 0.0 30.8 0.0 0.0 120 FTG T PE -0.8 87 31. 5 0.0 30.0 0.0 0.000 TL 8.00 PV 0.0 Pipe: 35 169.8 1.610 PL 3.00 PF 9.3 89 29.8 0.0 40.1 0.0 26.8 120 FTG T PE 0.0 88 29.8 0.0 30.8 0.0 0.844 TL 11.00 PV 4.8 Pipe: 36 103.3 2.703 PL 257.50 PF 7.6 C 29.8 0.0 47.7 0.0 5.8 120 FTG T3L PE 0.0 89 29.8 0.0 40.1 0.0 0.027 TL 281.50 PV 0.2 Pipe: 37 66.5 2.703 PL 249.50 PF 3.5 D 29.8 0.0 43.5 0.0 3.7 120 FTG 3TL PE 0.0 89 29.8 0.0 40.1 0.0 0.012 TL 289.50 PV 0.1 Pipe: 38 103.3 2.703 PL 10.00 PF 0.3 B 19.8 0.0 52.3 0.0 5.8 120 FTG ----PE -4.3 C 29.8 0.0 47.7 0.0 0.027 TL 10.00 PV 0.2 Pipe: 39 66.5 2.703 PL 10.00 PF 0.1 E 19.8 0.0 48.0 0.0 3.7 120 FTG -----PE -4.3 D 29.8 0.0 43.5 0.0 0.012 TL 10.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC 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: 40 30.4 2.203 PL 507.00 PF 4.3 B 19.8 0.0 52.3 0.0 2.6 120 FTG 4T6L PE 0.0 E 19.8 0.0 48.0 0.0 0.008 TL 565.00 PV 0.0 Pipe: 41 133.7 2.703 PL 10.00 PF 0.4 A 9.8 0.0 57.0 0.0 7.5 120 FTG ----PE -4.3 B 19.8 0.0 52.3 0.0 0.044 TL 10.00 PV 0.4 Pipe: 42 36.1 2.703 PL 10.00 PF 0.0 F 9.8 0.0 52.3 0.0 2.0 120 FTG ----PE -4.3 E 19.8 0.0 48.0 0.0 0.004 TL 10.00 PV 0.0 Pipe: 43 36.1 2.203 PL 501.00 PF 5.5 A2 9.8 0.0 57.8 0.0 3.0 120 FTG 2T2L PE 0.0 F 9.8 0.0 52.3 0.0 0.010 TL 527.00 PV 0.1 Pipe: 44 36.1 2.203 PL 8. so PF 0.2 Al 9.8 0.0 58.0 0.0 3.0 120 FTG T PE 0.0 A2 9.8 0.0 57.8 0.0 0.010 TL 18.50 PV 0.1 Pipe: 45 133.7 2.703 PL 7.00 PF 1.0 Al 9.8 0.0 58.0 0.0 7.5 120 FTG TL PE 0.0 A 9.8 ,o.o 57.0 0.0 0.044 TL 23.00 PV 0.4 Pipe: 46 169.8 3.314 PL 20.00 PF 0.8 TOR 9.8 0.0 58.8 0.0 6.3 120 FTG 2L PE 0.0 Al 9.8 0.0 58.0 0.0 0.025 TL 30.00 PV 0.3 Pipe: 47 169.8 3.314 PL 12.75 PF 0.6 BOR 0.5 0.0 63.4 0.0 6.3 120 FTG 2L PE -4.0 TOR 9.8 0.0 58.8 0.0 0.025 TL 22.75 PV 0.3 Pipe: 48 169.8 4.220 PL 9.00 PF 0.1 DI -3.0 0.0 65.0 0.0 3.9 140 FTG L PE -1.S BOR 0.5 0.0 63.4 0.0 0.006 TL 20.00 PV 0.1 Pipe: 49 169.8 4.240 PL 108.00 PF 0.7 UGl -3.0 0.0 65.7 0.0 3.9 150 FTG 2L PE 0.0 DI -3.0 0.0 65 .0 0.0 0.005 TL 132.00 PV 0.1 Pipe: so 169.8 6.280 PL 5.00 PF 0.0 BFl 2.0 0.0 63.5 0.0 1.8 140 FTG L PE 2.2 UGl -3.0 0.0 65.7 0.0 0.001 TL 21.00 PV 0.0 Pipe: 51 FIXED PRESSURE LOSS DEVICE BF2 2.0 0.0 66.S 0.0 3.0 psi, 169.8 gpm BFl 2.0 0.0 63.5 0.0 Pipe: 52 169.8 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 68.7 0.0 1.8 140 FTG L PE -2.2 BF2 2.0 0.0 66.5 0.0 0.001 TL 21.00 PV o.o SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC 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: 53 169.8 6.080 PL 16.00 PF 0.1 SOURCE 2.5 SRCE 66.4 (N/A) 1.9 150 FTG TLG PE 2.4 UG2 -3.0 0.0 68.7 0.0 0.001 TL 81.00 PV 0.0 NOTES: (1) Calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (2) The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.079 gpm. (3) velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 26.8 ft/sec at pipe 23. (4) 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 Ell Tee LngEll chkvlv Bfyvlv GatVlv Almchk DPVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv Gatvlv NPTee 4.220 18.00 36.00 11.00 39.00 22.00 4.00 36.00 6. 280 24.00 52.00 16.00 55.00 17.00 5.00 52.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv Bfyvlv Gatvlv NPTee 4.240 19.00 39.00 12.00 43.00 23.00 4.00 39.00 6.080 21.00 46.00 14.00 49.00 15.00 5.00 46.00 N NPTee 5.00 6.00 8.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC PAGE: F Diameter (in) 2.203 2.703 3.314 MATERIAL: DYNAFL HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 5.00 10.00 3.00 11.00 6.00 1.00 10.00 6.00 12.00 4.00 14.00 7.00 1.00 10.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 D 45ELL 1.80 2.20 2.60 N 0.00 0.00 0.00 .. • t • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/10/2001 C:\HASS73\05-1013D3RDREV.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 3RD FLR ROOF SSU ATTIC CALC WATER SUPPLY ANALYSIS G A u G E p .R E s s u R E ( p s i ) 1 112.0 84.0 2 56.0 28.0 0.0 Static: 130.50 psi Resid: 18.00 psi Flow: 4000.0 gpm 80,120<1600 2000 2400 2800 3200 FLOW (GPM) 3600 1 ~ 2 ~ 4000 LEGEND Available pressure 129.73 psi@ 269.8 Required pressure 66.41 psi@ 269.8 gpm gpm ACTION FIRE SYSTEMS CO.,INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR LA COSTA GLEN NORTH BLDG. D 7835 RUSH ROSE DR. CARLSBAD, CA. 92008 FILE NUMBER: 05-1013D2ND-REV3.SDF DATE: 9-23-05 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: 1420 sq. ft. (2ND FLR ROOF ATTIC) COVERAGE PER SPRINKLER: 130 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 17 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 331.9 gpm TOTAL WATER REQUIRED (including hose): 431.9 gpm FLOW AND PRESSURE(@ BOR): 331.9 gpm@ 111.4 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: ACTION FIRE SYSTEMS CO., INC. DESIGN/LAYOUT BY: JB AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: LIC. #388160 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4904076910) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC WATER SUPPLY DATA SOURCE NODE TAG SOURCE STATIC PRESS. (PSI) 130.5 RESID. FLOW PRESS.@ (PSI) (GPM) 18.0 4000.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE AVAIL. PRESS. (PSI) 128.7 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 25 34 34A 35 35A . 36 37 38 38A 39 39A 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 ELEVATION (FT) 19.8 19.5 19.0 19.5 19.0 19.5 18.8 19.5 19.0 19.5 19.0 19.5 18.8 22.8 22.8 22.8 22.8 22.8 22.8 20.6 23.3 24.5 24.5 25. 2 25.2 25.2 20.6 25. 9 27.3 27.3 27.3 27.3 20.6 23.8 NODE TYPE K= 5. 60 K= 5.60 K= 5. 60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5. 60 K= 5.60 K= 5.60 K= 5. 60 K= 5.60 K= 5.60 K= 5. 60 K= 5. 60 PRESSURE (PSI) 69.8 69.9 70.1 69.9 70.1 69.9 70.2 69.9 70.1 69.9 70.1 69.9 70.2 7.6 8.8 11.9 13.5 15.8 16.4 22.3 7.0 7.7 9.9 12.1 13.5 15.3 22.9 11.1 12.2 12.4 13.4 16.7 25.1 16.2 TOTAL @ DEMAND (GPM) REQ'D PRESS. (PSI) 431.9 116.6 431. 9 GPM 100.0 GPM 0.0 GPM 331. 9 GPM DISCHARGE (GPM) 15.5 16.6 19.3 20.6 22.3 14.8 15.5 17.6 19.5 20.6 18.7 19.6 19.7 20.5 22.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC NODE ANALYSIS DATA (cont.) NODE TAG 63 64 65 66 A Al A2 B C D E F TOR BOR DI UGl UG2 BFl BF2 SOURCE ELEVATION (FT) 23.8 23.8 20.6 20.6 9.8 9.8 9.8 19.8 29.8 29.8 19.8 9.8 9.8 0.5 -3.0 -3.0 -3.0 2.0 2.0 2.5 NODE TYPE K= 5. 60 K= 5. 60 SOURCE PRESSURE (PSI) 18.2 19.5 25.9 29.2 100.4 102.8 101.2 95.0 90.2 46.2 50.1 54.8 105 .4 111.4 113.3 115.6 118.7 113.5 116.5 116.6 DISCHARGE (GPM) 23.9 24.7 331.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC 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 0.0 1.101 PL 2.00 PF 0.0 34 19.5 0.0 69.9 0.0 0.0 150 FTG E PE 0.2 34A 19.0 0.0 70.1 0.0 0.000 TL 9.00 PV 0.0 Pipe: 2 0.0 1.101 PL 13.00 PF 0.0 35 19.5 0.0 69.9 0.0 0.0 150 FTG E PE 0.0 34 19.5 0.0 69.9 0.0 0.000 TL 20.00 PV 0.0 Pipe: 3 0.0 1.101 PL 2.00 PF 0.0 35 19.5 0.0 69.9 0.0 0.0 150 FTG ET PE 0.2 35A 19.0 0.0 70.1 0.0 0.000 TL 14.00 PV 0.0 Pipe: 4 0.0 1.394 PL 6. 50 PF 0.0 36 19.5 0.0 69.9 0.0 0.0 150 FTG E PE 0.0 35 19.5 0.0 69.9 0.0 0.000 TL 14. so PV 0.0 Pipe: 5 0.0 1.101 PL 0.75 PF 0.0 37 18.8 0.0 70.2 0.0 0.0 150 FTG E PE -0.3 36 19.S 0.0 69.9 0.0 0.000 TL 7.75 PV 0.0 Pipe: 6 0.0 1. 598 PL 15.50 PF 0.0 41 18.8 0.0 70.2 0.0 0.0 150 FTG ----PE 0.0 37 18.8 O.Q 70.2 0.0 0.000 TL 15.50 PV 0.0 Pipe: 7 0.0 1.101 PL 0. 50 PF 0.0 38 19.5 0.0 69.9 0.0 0.0 150 FTG E PE 0.2 38A 19.0 0.0 70.1 0.0 0.000 TL 7.50 PV 0.0 Pipe: 8 0.0 1.101 PL 13.00 PF 0.0 39 19.5 0.0 69.9 0.0 0.0 150 FTG ----PE 0.0 38 19.5 0.0 69.9 0.0 0.000 TL 13.00 PV 0.0 Pipe: 9 0.0 1.101 PL 0. 50 PF 0.0 39 19.5 0.0 69.9 0.0 0.0 150 FTG T PE 0.2 39A 19.0 0.0 70.1 0.0 0.000 TL 5.50 PV 0.0 Pipe: 10 0.0 1.101 PL 6.25 PF 0.0 40 19.5 0.0 69.9 0.0 0.0 150 FTG T PE 0.0 39 19.5 0.0 69.9 0.0 0.000 TL 11.25 PV 0.0 Pipe: 11 0.0 1.101 PL 0.75 PF 0.0 41 18.8 0.0 70.2 0.0 0.0 150 FTG T PE -0.3 40 19.5 0.0 69.9 0.0 0.000 TL 5.75 PV 0.0 Pipe: 12 0.0 1. 598 PL 21. 50 PF 0.0 25 19.8 0.0 69.8 0.0 0.0 150 FTG 6ET PE 0.4 41 18.8 0.0 70.2 0.0 0.000 TL 83.50 PV 0.0 Pipe: 13 15.5 1.049 PL 12.66 PF 1.2 43 22.8 5.6 8.8 16.6 5.7 120 FTG E PE 0.0 42 22.8 5.6 7.6 15.5 0.081 TL 14.66 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC 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: 14 32.1 1.049 PL 10.00 PF 3.1 44 22.8 5.6 11.9 19.3 11.9 120 FTG PE 0.0 43 22.8 5.6 8.8 16.6 0. 312 TL 10.00 PV 1.0 Pipe: 15 51.4 1.380 PL 8.00 PF 1.6 45 22.8 5.6 13.5 20.6 11.0 120 FTG PE 0.0 44 22.8 5.6 11.9 19.3 0.196 TL 8.00 PV 0.8 Pipe: 16 72.0 1.380 PL 2.00 PF 2.9 47 22.8 0.0 16.4 0.0 15.4 120 FTG T PE 0.0 45 22.8 5.6 13.5 20.6 0.366 TL 8.00 PV 1.6 Pipe: 17 22.3 1.380 PL 8.00 PF 0.6 47 22.8 0.0 16.4 0.0 4.8 120 FTG T PE 0.0 46 22.8 5.6 15.8 22.3 0.042 TL 14.00 PV 0.2 Pipe: 18 94.3 1.380 PL 2.20 PF 4.9 48 20.6 0.0 22.3 0.0 20.2 120 FTG T PE -1.0 47 22.8 0.0 16.4 0.0 0.603 TL 8.20 PV 2.8 Pipe: 19 94.3 2.203 PL 9. 50 PF 0.6 55 20.6 0.0 22.9 0.0 7.9 120 FTG PE 0.0 48 20.6 0.0 22.3 0.0 0.062 TL 9.50 PV 0.4 Pipe: 20 14.8 1.049 PL 11.66 PF 1.2 50 24.5 5.6 7.7 15.5 5.5 120 FTG 2E PE 0.5 49 23.3 5.6 7.0 14.8 0.075 TL 15.66 PV 0.2 Pipe: 21 30.3 1.049 PL 8.00 PF 2.2 51 24.5 5.6 9.9 17.6 11.3 120 FTG PE 0.0 so 24.5 5.6 7.7 15.5 0.281 TL 8.00 PV 0.9 Pipe: 22 47.9 1.380 PL 8.41 PF 2.5 52 25. 2 5.6 12.1 19.5 10.3 120 FTG 2E PE 0.3 51 24.5 5.6 9.9 17.6 0.172 TL 14.41 PV 0.7 Pipe: 23 67.4 1. 380 PL 3.91 PF 3.2 54 25. 2 0.0 15.3 0.0 14.5 120 FTG T PE 0.0 52 25. 2 5.6 12.1 19.5 0.324 TL 9.91 PV 1.4 Pipe: 24 20.6 1.049 PL 7.91 PF 1.8 54 25. 2 0.0 15.3 0.0 7.6 120 FTG T PE 0.0 53 25 .2 5.6 13.5 20.6 0.137 TL 12.91 PV 0.4 Pipe: 25 88.0 1. 380 PL 4.60 PF 5.6 55 20.6 0.0 22.9 0.0 18.9 120 FTG T PE -2.0 54 25.2 0.0 15.3 0.0 0. 530 TL 10.60 PV 2.4 Pipe: 26 182.2 2.203 PL 10. 50 PF 2.2 61 20.6 0.0 25 .1 0.0 15.3 120 FTG PE 0.0 55 20.6 0.0 22.9 0.0 0.209 TL 10. 50 PV 1.6 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC 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: 27 18.7 1.049 PL 7.66 PF 1. 7 57 27.3 5.6 12.2 19.6 6.9 120 FTG ET PE 0.6 56 25 .9 5.6 11.1 18.7 0.115 TL 14.66 PV 0.3 Pipe: 28 38.2 1.049 PL 5.50 PF 4.5 60 27.3 0.0 16.7 0.0 14.2 120 FTG T PE 0.0 57 27. 3 5.6 12.2 19.6 0.432 TL 10.50 PV 1.4 Pipe: 29 19.7 1.049 PL 8.00 PF 1.0 59 27.3 5.6 13.4 20.5 7.3 120 FTG PE 0.0 58 27. 3 5.6 12.4 19.7 0.127 TL 8.00 PV 0.4 Pipe: 30 40.2 1.049 PL 2.00 PF 3.3 60 27.3 0.0 16.7 0.0 14.9 120 FTG T PE 0.0 59 27.3 5.6 13.4 20.5 0.474 TL 7.00 PV 1.5 Pipe: 31 78.5 1.380 PL 6.70 PF 5.5 61 20.6 0.0 25 .1 0.0 16.8 120 FTG T PE -2.9 60 27.3 0.0 16.7 0.0 0.429 TL 12.70 PV 1.9 Pipe: 32 260.7 2.203 PL 10.00 PF 4.1 66 20.6 0.0 29.2 0.0 21.9 120 FTG ----PE 0.0 61 20.6 0.0 25 .1 0.0 0.406 TL 10.00 PV 3.2 Pipe: 33 22.5 1.049 PL 8.66 PF 2.1 63 23.8 5.6 18.2 23.9 8.4 120 FTG 2E PE 0.0 62 23.8 5.6 16.2 22.5 0.162 TL 12.66 PV 0.5 Pipe: 34 46.4 1.380 PL 7.50 PF 1.2 64 23.8 5.6 19.5 24.7 10.0 120 FTG PE 0.0 63 23.8 5.6 18.2 23.9 0.163 TL 7.50 PV 0.7 Pipe: 35 71.1 1.380 PL 8.00 PF 5.0 65 20.6 0.0 25. 9 0.0 15.3 120 FTG T PE -1.4 64 23.8 5.6 19.5 24.7 0.358 TL 14.00 PV 1.6 Pipe: 36 71.1 1.380 PL 3.20 PF 3.3 66 20.6 0.0 29.2 0.0 15.3 120 FTG T PE 0.0 65 20.6 0.0 25. 9 0.0 0.358 TL 9.20 PV 1.6 Pipe: 37 331.9 -2. 703 PL 40.00 PF 20.6 E 19.8 0.0 50.1 0.0 18.6 120 FTG 2T6L PE -0.4 66 20.6 0.0 29.2 0.0 0.234 TL 88.00 PV 2.3 Pipe: 38 107.5 2.203 PL 292.50 PF 25.2 B 19.8 0.0 95 .0 0.0 9.0 120 FTG T6L PE 0.0 25 19.8 0.0 69.8 0.0 0.079 TL 320.50 PV 0.6 Pipe: 39 -107.5 2.203 PL 219.50 PF 19.6 E 19.8 0.0 50.1 0.0 9.0 120 FTG 3T PE 0.0 25 19.8 0.0 69.8 0.0 0.079 TL 249.50 PV 0.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC 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: 40 110.2 2.703 PL 10.00 PF 0.4 B 19.8 0.0 95 .0 0.0 6.2 120 FTG L PE -4.3 C 29.8 0.0 90.2 0.0 0.030 TL 14.00 PV 0.3 Pipe: 41 -110.2 2.703 PL 10.00 PF 0.4 E 19.8 0.0 50.1 0.0 6.2 120 FTG L PE -4.3 D 29.8 0.0 46.2 0.0 0.030 TL 14.00 PV 0.3 Pipe: 42 110.2 2.203 PL 512.00 PF 44.0 C 29.8 0.0 90.2 0.0 9.3 120 FTG T4L PE 0.0 D 29.8 0.0 46.2 0.0 0.082 TL 534.00 PV 0.6 Pipe: 43 217.6 2.703 PL 10.00 PF 1.1 A 9.8 0.0 100.4 0.0 12.2 120 FTG ----PE -4.3 B 19.8 0.0 95 .0 0.0 0.107 TL 10.00 PV 1.0 Pipe: 44 114.2 2.703 PL 10.00 PF 0.3 F 9.8 0.0 54.8 0.0 6.4 120 FTG ----PE -4.3 E 19.8 0.0 50.1 0.0 0.033 TL 10.00 PV 0.3 Pipe: 45 114.2 2.203 PL 501.00 PF 46.4 A2 9.8 0.0 101.2 0.0 9.6 120 FTG 2T2L PE 0.0 F 9.8 0.0 54.8 0.0 0.088 TL 527.00 PV 0.6 Pipe: 46 114.2 2.203 PL 8.50 PF 1.6 Al 9.8 0.0 102.8 0.0 9.6 120 FTG T PE 0.0 A2 9.8 0.0 101.2 0.0 0.088 TL 18.50 PV 0.6 Pipe: 47 217.6 2.703 PL 7.00 PF 2.5 Al 9.8 0.0 102.8 0.0 12.2 120 FTG TL PE 0.0 A 9.8 0.0 100.4 0.0 0.107 TL 23.00 PV 1.0 Pipe: 48 331.9 3.314 PL 20.00 PF 2.6 TOR 9.8 0.0 105 .4 0.0 12.3 120 FTG 2L PE 0.0 Al 9.8 0.0 102.8 0.0 0.087 TL 30.00 PV 1.0 Pipe: 49 331.9 3.314 PL 12.75 PF 2.0 BOR 0.5 0.0 111.4 0.0 12.3 120 FTG 2L PE -4.0 TOR 9.8 0.0 105.4 0.0 0.087 TL 22.75 PV 1.0 Pipe: 50 331.9 4.220 PL 9.00 PF 0.4 DI -3.0 0.0 113.3 0.0 7.6 140 FTG L PE -1.5 BOR 0.5 0.0 111.4 0.0 0.020 TL 20.00 PV 0.4 Pipe: 51 331.9 4.240 PL 108.00 PF 2.3 UGl -3.0 0.0 115.6 0.0 7.5 150 FTG 2L PE 0.0 DI -3.0 0.0 113.3 0.0 0.017 TL 132.00 PV 0.4 Pipe: 52 331.9 6.280 PL 5.00 PF 0.1 BFl 2.0 0.0 113.5 0.0 3.4 140 FTG L PE 2.2 UGl -3.0 0.0 115.6 0.0 0.003 TL 21.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Ff) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 FIXED PRESSURE LOSS DEVICE BF2 2.0 0.0 116.5 0.0 3.0 psi, 331.9 gpm BFl 2.0 0.0 113.5 0.0 Pipe: 54 331.9 6.280 PL 5.00 PF 0.1 UG2 -3.0 0.0 118.7 0.0 3.4 140 FTG L PE -2.2 BF2 2.0 0.0 116.5 0.0 0.003 TL 21.00 PV 0.1 Pipe: 55 331.9 6.080 PL 16.00 PF 0.2 SOURCE 2.5 SRCE 116.6 (N/A) 3.7 150 FTG TLG PE 2.4 UG2 -3.0 0.0 118.7 0.0 0.003 TL 81.00 PV 0.1 NOTES: (1) calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (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 0.136 gpm. (3) velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 21.9 ft/sec at pipe 32. (4) 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 Ell Tee LngEll chkvlv Bfyvlv Gatvlv Almchk DPVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll Chkvlv Bfyvlv Gatvlv NPTee 4.220 18.00 36.00 11.00 39.00 22.00 4.00 36.00 6.280 24.00 52.00 16.00 55.00 17.00 5.00 52.00 N NPTee 5.00 6.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC PAGE: E Diameter (in) 4.240 6.080 PAGE: F Diameter (in) 2.203 2.703 3.314 PAGE: I oiame·ter (in) 1.101 1.394 1. 598 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 19.00 39.00 12.00 43.00 23.00 4.00 39.00 21.00 46.00 14.00 49.00 15.00 5.00 46.00 MATERIAL: DYNAFL HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 5.00 10.00 3.00 11.00 6.00 1.00 10.00 6.00 12.00 4.00 14.00 7.00 1.00 10.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 MATERIAL: CPVC HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGTEE CHKVAV BTRVAV GATE COUP 7.00 5.00 1.00 1.50 1. 50 1. 50 1.00 8.00 6.00 1.00 2.00 2.00 2.00 1.00 9.00 8.00 1.00 2.00 2.00 2.00 1.00 D 45ELL 1.80 2.20 2.60 D 45ELL 1.00 2.00 2.00 N 0.00 0.00 0.00 N 0.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV3SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR ROOF SSU ATTIC CALC WATER SUPPLY ANALYSIS Static: 130.50 psi Resid: 18.00 psi Flow: 4000.0 gpm G A u G E 140.0 ,..........------------------~ P 84.0 R E s s u R E ( p s 1 ) 56.0 ~ 28.0 _ 0.0 _ -14 . 7 ._________.l______.l _ __.__ _ _.___ _ _.___ _ __._ __ ..____----1.. __ ____, 1 ~ 2 ~ 80·120(1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) LEGEND Available pressure 128.67 psi@ 431.9 Required pressure 116.61 psi@ 431.9 gpr gpr ACTION FIRE SYSTEMS CO.,INC. 9185 HARNESS STREET SPRING VALLEY, CA. 91977-3948 HYDRAULIC CALCULATIONS FOR LA COSTA GLEN NORTH BLDG. D 7835 RUSH ROSE DR. CARLSBAD, CA. 92008 FILE NUMBER: 05-1013D2ND-REV2.SDF DATE: 9-23-05 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHTY HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: DWELLING UNIT (2ND FLOOR) COVERAGE PER SPRINKLER: 324 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 134.6 gpm TOTAL WATER REQUIRED (including hose): 234.6 gpm FLOW AND PRESSURE(@ BOR): 134.6 gpm@ 105.8 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: ACTION FIRE SYSTEMS CO., INC. DESIGN/LAYOUT BY: JB AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: LIC. #388160 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4904076910) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC WATER SUPPLY DATA SOURCE NODE TAG SOURCE STATIC PRESS. (PSI) 130.5 RESID. PRESS.@ (PSI) 18.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE FLOW (GPM) 4000.0 AVAIL. PRESS. (PSI) 129.9 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 25 34 34A 35 35A 36 37 38 38A 39 39A 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 ELEVATION (FT) 19.8 19.5 19.0 19.5 19.0 19.5 18.8 19.5 19.0 19.5 19.0 19.5 18.8 22.8 22.8 22.8 22.8 22.8 22.8 20.6 23.3 24.5 24.5 25.2 25.2 25.2 20.6 25. 9 27.3 27.3 27.3 27.3 20.6 23.8 NODE TYPE K= 5. 50 K= 5. 50 K= 5. 50 K= 5. 50 PRESSURE (PSI) 84.1 36.0 34.7 39.3 37.0 47.6 51.5 39.1 37.7 41.4 40.4 48.9 53.1 90.3 90.3 90.3 90.3 90.3 90.3 91.3 90.1 89.6 89.6 89.3 89.3 89.3 91. 3 89.0 88.4 88.4 88.4 88.4 91.3 89.9 TOTAL @ DEMAND (GPM) REQ'D PRESS. (PSI) 234.6 108.5 234.6 GPM 100.0 GPM 0.0 GPM 134.6 GPM DISCHARGE (GPM) 32.4 33.5 33.8 34.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 63 23.8 89.9 --- 64 23.8 89.9 --- 65 20.6 ----91. 3 --- 66 20.6 91.3 --- A 9.8 100.4 --- Al 9.8 ----101.0 --- A2 9.8 ----100.8 --- B 19.8 95.8 --- C 29.8 91.4 --- D 29.8 87.3 --- E 19.8 ----91.6 --- F 9.8 96.0 --- TOR 9.8 ----101. 5 --- BOR 0.5 105.8 --- DI -3.0 107.4 --- UGl -3.0 107.9 --- UG2 -3.0 110.9 --- BFl 2.0 ----105.7 --- BF2 2.0 ----108.7 --- SOURCE 2.5 SOURCE 108.5 134.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC 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 32.4 1.101 PL 2.00 PF 1.5 34 19.5 0.0 36.0 0.0 10.9 150 FTG E PE 0.2 34A 19.0 5.5 34.7 32 .4 0.166 TL 9.00 PV 0.8 Pipe: 2 32.4 1.101 PL 13.00 PF 3.3 35 19.5 0.0 39.3 0.0 10.9 150 FTG E PE 0.0 34 19.5 0.0 36.0 0.0 0.166 TL 20.00 PV 0.8 Pipe: 3 33.5 1.101 PL 2.00 PF 2.5 35 19.5 0.0 39.3 0.0 11.3 150 FTG ET PE 0.2 35A 19.0 5.5 37.0 33.5 0.176 TL 14.00 PV 0.9 Pipe: 4 65.9 1.101 PL 6. 50 PF 8.3 36 19.5 0.0 47.6 0.0 22.2 150 FTG E PE 0.0 35 19.5 0.0 39.3 0.0 0.617 TL 13.50 PV 3.3 Pipe: 5 65.9 1.101 PL 0.75 PF 3.5 37 18.8 0.0 51.5 0.0 22.2 150 FTG T PE -0.3 36 19.5 0.0 47.6 0.0 0.617 TL 5.75 PV 3.3 Pipe: 6 65.9 1. 598 PL 15.50 PF 1.6 41 18.8 0.0 53.1 0.0 10.5 150 FTG ----PE 0.0 37 18.8 0.0 51.5 0.0 0.101 TL 15.50 PV 0.7 Pipe: 7 33.8 1.101 PL 1. 50 PF 1.5 38 19.5 0.0 39.1 0.0 11.4 150 FTG E PE 0.2 38A 19.0 5.5 37.7 33.8 0.180 TL 8.50 PV 0.9 Pipe: 8 33.8 1.101 PL 13.00 PF 2.3 39 19.5 0.0 41.4 0.0 11.4 150 FTG ----PE 0.0 38 19.5 0.0 39.1 0.0 0.180 TL 13.00 PV 0.9 Pipe: 9 34.9 1.101 PL 1. SO· PF 1.2 39 19.5 0.0 41.4 0.0 11.8 150 FTG T PE 0.2 39A 19.0 5.5 40.4 34.9 0.191 TL 6. 50 PV 0.9 Pipe: 10 68.7 1.101 PL 6.25 PF 7.5 40 19.5 0.0 48.9 0.0 23.2 150 FTG T PE 0.0 39 19.5 0.0 41.4 0.0 0.668 TL 11.25 PV 3.6 Pipe: 11 68.7 1.101 PL 0.75 PF 3.8 41 18.8 0.0 53.1 0.0 23.2 150 FTG T PE -0.3 40 19.5 0.0 48.9 0.0 0.668 TL 5.75 PV 3.6 Pipe: 12 134.6 1. 598 PL 21. 50 PF 31. 5 25 19.8 0.0 84.1 0.0 21. 5 150 FTG 6ET PE 0.4 41 18.8 0.0 53.1 0.0 0.377 TL 83.50 PY 3.1 Pipe: 13 0.0 1.049 PL 12.66 PF 0.0 43 22.8 0.0 90.3 0.0 0.0 120 FTG E PE 0.0 42 22.8 0.0 90.3 0.0 0.000 TL 14.66 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC 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: 14 0.0 1.049 PL 10.00 PF 0.0 44 22.8 0.0 90.3 0.0 0.0 120 FTG ----PE 0.0 43 22.8 0.0 90.3 0.0 0.000 TL 10.00 PV 0.0 Pipe: 15 0.0 1.380 PL 8.00 PF 0.0 45 22.8 0.0 90.3 0.0 0.0 120 FTG PE 0.0 44 22.8 0.0 90.3 0.0 0.000 TL 8.00 PV 0.0 Pipe: 16 0.0 1.380 PL 2.00 PF 0.0 47 22.8 0.0 90.3 0.0 0.0 120 FTG T PE 0.0 45 22.8 0.0 90.3 0.0 0.000 TL 8.00 PV 0.0 Pipe: 17 0.0 1.380 PL 8.00 PF 0.0 47 22.8 0.0 90.3 0.0 0.0 120 FTG T PE 0.0 46 22.8 0.0 90.3 0.0 0.000 TL 14.00 PV 0.0 Pipe: 18 0.0 1.380 PL 2.20 PF 0.0 48 20.6 0.0 91. 3 0.0 0.0 120 FTG T PE -1.0 47 22.8 0.0 90.3 0.0 0.000 TL 8.20 PV 0.0 Pipe: 19 0.0 2.203 PL 9. 50 PF 0.0 55 20.6 0.0 91. 3 0.0 0.0 120 FTG PE 0.0 48 20.6 0.0 91.3 0.0 0.000 TL 9.50 PV 0.0 Pipe: 20 0.0 1.049 PL 11.66 PF 0.0 50 24.5 0.0 89.6 0.0 0.0 120 FTG 2E PE 0.5 49 23.3 0.0 90.1 0.0 0.000 TL 15.66 PV 0.0 Pipe: 21 0.0 1.049 PL 8.00 PF 0.0 51 24.5 0.0 89.6 0.0 0.0 120 FTG PE 0.0 50 24.5 0.0 89.6 0.0 0.000 TL 8.00 PV 0.0 Pipe: 22 0.0 1.380 PL 8.41 PF 0.0 52 25 .2 0.0 89.3 0.0 0.0 120 FTG 2E PE 0.3 51 24.5 0.0 89.6 0.0 0.000 TL 14.41 PV 0.0 Pipe: 23 0.0 1.380 PL 3.91 PF 0.0 54 25.2 0.0 89.3 0.0 0.0 120 FTG T PE 0.0 52 25.2 0.0 89.3 0.0 0.000 TL 9.91 PV 0.0 Pipe: 24 0.0 1.049 PL 7.91 PF 0.0 54 25 .2 0.0 89.3 0.0 0.0 120 FTG T PE 0.0 53 25 .2 0.0 89.3 0.0 0.000 TL 12.91 PV 0.0 Pipe: 25 0.0 1.380 PL 4.60 PF 0.0 55 20.6 0.0 91. 3 0.0 0.0 120 FTG T PE -2.0 54 25.2 0.0 89.3 0.0 0.000 TL 10.60 PV 0.0 Pipe: 26 0.0 2.203 PL 10. 50 PF 0.0 61 20.6 0.0 91. 3 0.0 0.0 120 FTG ----PE 0.0 55 20.6 0.0 91. 3 0.0 0.000 TL 10.50 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC 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: 27 0.0 1.049 PL 7.66 PF 0.0 57 27.3 0.0 88.4 0.0 0.0 120 FTG ET PE 0.6 56 25.9 0.0 89.0 0.0 0.000 TL 14.66 PV 0.0 Pipe: 28 0.0 1.049 PL 5.50 PF 0.0 60 27.3 0.0 88.4 0.0 0.0 120 FTG T PE 0.0 57 27.3 0.0 88.4 0.0 0.000 TL 10. 50 PV 0.0 Pipe: 29 0.0 1.049 PL 8.00 PF 0.0 59 27.3 0.0 88.4 0.0 0.0 120 FTG PE 0.0 58 27.3 0.0 88.4 0.0 0.000 TL 8.00 PV 0.0 Pipe: 30 0.0 1.049 PL 2.00 PF 0.0 60 27.3 0.0 88.4 0.0 0.0 120 FTG T PE 0.0 59 27.3 0.0 88.4 0.0 0.000 TL 7.00 PV 0.0 Pipe: 31 0.0 1.380 PL 6.70 PF 0.0 61 20.6 0.0 91.3 0.0 0.0 120 FTG T PE -2.9 60 27.3 0.0 88.4 0.0 0.000 TL 12.70 PV 0.0 Pipe: 32 0.0 2.203 PL 10.00 PF 0.0 66 20.6 0.0 91.3 0.0 0.0 120 FTG PE 0.0 61 20.6 0.0 91.3 0.0 0.000 TL 10.00 PV 0.0 Pipe: 33 0.0 1.049 PL 8.66 PF 0.0 63 23.8 0.0 89.9 0.0 0.0 120 FTG 2E PE 0.0 62 23.8 0.0 89.9 0.0 0.000 TL 12.66 PV 0.0 Pipe: 34 0.0 1.380 PL 7.50 PF 0.0 64 23.8 0.0 89.9 0.0 0.0 120 FTG PE 0.0 63 23.8 0.0 89.9 0.0 0.000 TL 7.50 PV 0.0 Pipe: 35 0.0 1.380 PL 8.00 PF 0.0 65 20.6 0.0 91.3 0.0 0.0 120 FTG T PE -1.4 64 23.8 0.0 89.9 0.0 0.000 TL 14.00 PV 0.0 Pipe: 36 0.0 1.380 PL 3.20 PF 0.0 66 20.6 0.0 91. 3 0.0 0.0 120 FTG T PE 0.0 65 20.6 0.0 91.3 0.0 0.000 TL 9.20 PV 0.0 Pipe: 37 0.0 2.703 PL 40.00 PF 0.0 E 19.8 0.0 91.6 0.0 0.0 120 FTG 2T6L PE -0.4 66 20.6 0.0 91.3 0.0 0.000 TL 88.00 PV 0.0 Pipe: 38 70.7 2.203 PL 292.50 PF 11.6 B 19.8 0.0 95.8 0.0 6.0 120 FTG T6L PE 0.0 25 19.8 0.0 84.1 0.0 0.036 TL 320.50 PV 0.2 Pipe: 39 63.9 2.203 PL 219.50 PF 7.5 E 19.8 0.0 91.6 0.0 5.4 120 FTG 3T PE 0.0 25 19.8 0.0 84.1 0.0 0.030 TL 249.50 PV 0.2 DATE: 8/10/2001 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC 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: 40 30.4 2.703 PL 10.00 PF 0.0 B 19.8 0.0 95. 8 0.0 1.7 120 FTG L PE -4.3 C 29.8 0.0 91.4 0.0 0.003 TL 14.00 PV 0.0 Pipe: 41 -30.4 2.703 PL 10.00 PF 0.0 E 19.8 0.0 91.6 0.0 1. 7 120 FTG L PE -4.3 D 29.8 0.0 87.3 0.0 0.003 TL 14.00 PV 0.0 Pipe: 42 30.4 2.203 PL 512.00 PF 4.1 C 29.8 0.0 91.4 0.0 2.6 120 FTG T4L PE 0.0 D 29.8 0.0 87.3 0.0 0.008 TL 534.00 PV 0.0 Pipe: 43 101.1 2.703 PL 10.00 PF 0.3 A 9.8 0.0 100.4 0.0 5.7 120 FTG PE -4.3 B 19.8 0.0 95.8 0.0 0.026 TL 10.00 PV 0.2 Pipe: 44 33.5 2.703 PL 10.00 PF 0.0 F 9.8 0.0 96.0 0.0 1.9 120 FTG ----PE -4.3 E 19.8 0.0 91.6 0.0 0.003 TL 10.00 PV 0.0 Pipe: 45 33.5 2.203 PL 501.00 PF 4.8 A2 9.8 0.0 100.8 0.0 2.8 120 FTG 2T2L PE 0.0 F 9.8 0.0 96.0 0.0 0.009 TL 527.00 PV 0.1 Pipe: 46 33.5 2.203 PL 8.50 PF 0.2 Al 9.8 0.0 101.0 0.0 2.8 120 FTG T PE 0.0 A2 9.8 0.0 100.8 0.0 0.009 TL 18.50 PV 0.1 Pipe: 47 101.1 2.703 PL 7.00 PF 0.6 Al 9.8 0.0 101.0 0.0 5.7 120 FTG TL PE 0.0 A 9.8 0.0 100.4 0.0 0.026 TL 23.00 PV 0.2 Pipe: 48 134.6 3.314 PL 20.00 PF 0.5 TOR 9.8 0.0 101. 5 0.0 5.0 120 FTG 2L PE 0.0 Al 9.8 0.0 101.0 0.0 0.016 TL 30.00 PV 0.2 Pipe: 49 134.6 3.314 PL 12.75 PF 0.4 BOR 0. 5 0.0 105.8 0.0 5.0 120 FTG 2L PE -4.0 TOR 9.8 0.0 101. 5 0.0 0.016 TL 22.75 PV 0.2 Pipe: 50 134.6 4.220 PL 9.00 PF 0.1 DI -3.0 0.0 107.4 0.0 3.1 140 FTG L PE -1.5 BOR 0.5 0.0 105 .8 0.0 0.004 TL 20.00 PV 0.1 Pipe: 51 134.6 4.240 PL 108.00 PF 0.4 UGl -3.0 0.0 107.9 0.0 3.1 150 FTG 2L PE 0.0 DI -3.0 0.0 107.4 0.0 0.003 TL 132.00 PV 0.1 Pipe: 52 134.6 6.280 PL 5.00 PF 0.0 BFl 2.0 0.0 105. 7 0.0 1.4 140 FTG L PE 2.2 UGl -3.0 0.0 107.9 0.0 0.001 TL 21.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC 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: 53 FIXED PRESSURE LOSS DEVICE BF2 2.0 0.0 108.7 0.0 3.0 psi, 134.6 gpm BFl 2.0 0.0 105.7 0.0 Pipe: 54 134.6 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 110.9 0.0 1.4 140 FTG L PE -2.2 BF2 2.0 0.0 108.7 0.0 0.001 TL 21.00 PV 0.0 Pipe: 55 134.6 6.080 PL 16.00 PF 0.0 SOURCE 2.5 SRCE 108.5 (N/A) 1.5 150 FTG TLG PE 2.4 UG2 -3.0 0.0 110.9 0.0 0.001 TL 81.00 PV 0.0 NOTES: (1) calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS systems, Inc. 4792 Lavista Road Tucker, GA 30084 (2) The system has been calcula·ted to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.107 gpm. (3) velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 23.2 ft/sec at pipe 10. (4) 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 Ell Tee LngEll Chkvlv Bfyvlv GatVlv Almchk DPVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll chkvlv Bfyvlv Gatvlv NPTee 4.220 18.00 36.00 11.00 39.00 22.00 4.00 36.00 6. 280 24.00 52.00 16.00 55.00 17.00 5.00 52.00 N NPTee 5.00 6.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC PAGE: E Diameter (in) 4.240 6.080 PAGE: F Diameter (in) 2.203 2.703 3.314 PAGE: I Diameter (in) 1.101 1.598 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll Chkvlv Bfyvlv Gatvlv NPTee 19.00 39.00 12.00 43.00 23.00 4.00 39.00 21.00 46.00 14.00 49.00 15.00 5.00 46.00 MATERIAL: DYNAFL HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 5.00 10.00 3.00 11.00 6.00 1.00 10.00 6.00 12.00 4.00 14.00 7.00 1.00 10.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 MATERIAL: CPVC HWC: 150 Equivalent Fitting Lengths in Feet D 45ELL 1.80 2.20 2.60 E T L C B G A D· Ell Tee LNGTEE CHKVAV BTRVAV GATE COUP 45ELL 7.00 5.00 1.00 1.50 1.50 1.50 1.00 1.00 9.00 8.00 1.00 2.00 2.00 2.00 1.00 2.00 N 0.00 0.00 0.00 N 0.00 0.00 ,J • • • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/10/2001 C:\HASS73\05-1013D2ND-REV2SDF.SDF JOB TITLE: LA COSTA GLEN NORTH BLDG D 2ND FLR 4 HD PEND UNIT CALC WATER SUPPLY ANALYSIS G A u G E Static: 130.50 psi Resid: 18.00 psi Flow: 4000.0 gpm 140. 0 ,.------------------------, 112. ~ _ ~ P 84. 0 _ R E s s u R E ( p s l ) 56.0 _ 28.0 _ 0.0 _ -14 . 7 ~---'---------'---------'---------'---------'--------'----------'-------' 80·120(1600 2000 2400 2800 3200 FLOW (GPM) 3600 4000 LEGEND Available pressure 129.91 psi@ 234.6 gp Required pressure 108.54 psi@ 234.6 gp