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HomeMy WebLinkAbout7140 AVENIDA ENCINAS; ; AS080058City of Carlsbad Sprinkler Permit Permit No: AS080058 7140 AVENIDA Job Address: Status: ISSUED ENCINAS Permit Type: SPRINK Applied 4/7/2008 Parcel No: 2144302700 Approved: 4/17/2008 Lot #: 0 Reference No.: Issued: 4/17/2008 PC #: Inspector: Project Title: RALPH'S - EXPANSION TI FIRE SPRINKLER PLAN CHECK & INSPECTIONS Applicant: RICE FIRE PROTECTION 24300 VERA LANE 951-243-0137 Owner: RALPHS GROCERY CO 1100W ARTESIA BLVD COMPTON CA L Fees ($) Add'I Fees ($) Total ($) Balance ($) 130. 0 130 . 0 RICE FIRE PROTECTION /S0'A3'S1 24300 VERA LANE MORENO VALLEY,CA 92557 HYDRAULIC CALCULATIONS FOR RALPHS 175 CARLSBAD, CA. FILE NUMBER: CARLSBAD175 DATE: MAR 31, 2008 FILE COPY -DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY GRP. II DENSITY: .20 AREA OF APPLICATION: 1500 SQ. FT. (\ , COVERAGE PER SPRINKLER: VARIES MAX. sq. ft. NUMBER OF SPRINKLERS CALCULATED: 15 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 324.4 gpm TOTAL WATER REQUIRED (including hose): 574.4 gpm FLOW AND PRESSURE (@ BOR): 302.5 gpm @ 84.3 Psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: DESIGN/LAYOUT BY: CL AUTHORITY HAVING JURISDICTION:CITY OF CARLSBAD FIRE. WATER FLOW INFORMATION IS REDUCED BY 10 TO PROVIDE BUFFER. CONTRACTOR CERTIFICATION NUMBER: CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27031226 HRS SYSTEMS, INC. TUCKER, GA 30084 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 C:\HASS78\CARLSBAD17SPEND.SDF RESID. FLOW AVAIL. TOTAL REQ'D PRESS. @ PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) (GPM) (PSI) 90.0 1316.0 108.0 552.5 88.6; DATE: 3/31/2008 JOB TITLE: WATER SUPPLY DATA SOURCE STATIC NODE PRESS. TAG (PSI) SOURCE 112.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 552.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 302.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 24.0 - - - - 16.5 - - - 2 24.0 K= 5.60 16.5 22.8 3 24.0 - - - - 16.9 - - - 3A 24.0 K= 5.60 17.1 23.2 4 24.0 K= 5.60 16.0 22.4 4A 24.0 K= 5.60 15.3 21.9 5 24.0 - - - - 15.1 - - - 5A 24.0 K= 5.60 14.8 21.6 6 24.0 - - - - 15.5 - - - 6A 24.0 K= 5.60 14.2 21.1 7 24.0 - - - - 16.1 - - - 7A 24.0 K= 5.60 15.6 22.1 8 24.0 - - - - 17.4 - - - 9 24.0 - - - - 15.2 - - - 9A 24.0 K= 5.60 14.8 21.5 9B 24.0 K= 5.60 15.0 21.7 10 24.0 K= 5.60 16.5 22.8 11 24.0 - - - - 13.8 - - - hA 24.0 K= 5.60 12.8 20.1 12 24.0 K= 5.60 14.0 21.0 12A 24.0 K= 5.34 14.0 20.0 12B 24.0 K= 5.34 14.8 20.5 13 24.0 - - - - 17.1 - - - 14 24.0 - - - - 22.4 - - - 15 24.0 - - - - 22.4 - - - A 23.0 - - - - 24.6 - - - Al 24.0 - - - - 18.5 - - - B 23.0 - - - - 24.9 - - - B1 24.0 - - - - 19.0 - - - 302.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: 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 1.408 PL 10.00 PF 0.0 1 24.0 0.0 16.5 0.0 0.0 120 FTG ---- PE 0.0 2 24.0 5.E 16.5 22.8 0.000 TL 10.00 PV Pipe: 2 -22.8 1.408 PL 10.00 PP 0.4 2 24.0 5.E 16.5 22.8 4.7 120 FTG ---- PE 0.0 3 24.0 0.0 16.9 0.0 0.039 TL 10.00 PV Pipe: 3 -22.8 1.408 PL 4.75 PF 0.2 3 24.0 0.0 16.9 0.0 4.7 120 FTG ---- PE 0.0 3A 24.0 5.E 17.1 23.2 0.039 TL 4.75 PV Pipe: 4 -45.9 1.408 PL 2.66 PF 1.3 3A 24.0 5.6 17.1 23.2 9.5 120 FTG T PE 0.0 Al 24.0 0.0 18.5 0.0 0.145 TL 9.28 PV Pipe: 5 -21.6 1.408 PL 4.66 PF 0.2 5 24.0 0.0 15.1 0.0 4.4 120 FTG ---- PE 0.0 4A 24.0 5.6 15.3 21.9 0.036 TL 4.66 PV Pipe: 6 -43.5 1.408 PL 5.33 PF 0.7 4A 24.0 5.6 15.3 21.9 9.0 120 FTG ---- PE 0.0 4 24.0 5.6 16.0 22.4 0.130 TL 5.33 PV Pipe: 7 -21.6 1.408 PL 7.50 PF 0.3 5A 24.0 5.6 14.8 21.6 4.4 120 FTG ---- PE 0.0 5 24.0 0.0 15.1 0.0 0.036 TL 7.50 PV Pipe: 8 -65.8 1.408 PL 2.25 PF 2.5 4 24.0 5.6 16.0 22.4 13.6 120 FTG T PE 0.0 Al 24.0 0.0 18.5 0.0 0.281 TL 8.87 PV Pipe: 9 -21.1 1.080 PL 4.66 PF 1.3 6A 24.0 5.6 14.2 21.1 7.4 120 FTG T PE 0.0 6 24.0 0.0 15.5 0.0 0.124 TL 10.42 PV Pipe: 10 -21.1 1.408 PL 4.66 PF 0.2 6 24.0 0.0 15.5 0.0 4.3 120 FTG ---- PE 0.0 7A 24.0 5.6 15.6 22.1 0.034 TL 4.66 PV Pipe: 10A -43.2 1.408 PL 3.66 PF 0.5 7A 24.0 5.6 15.6 22.1 8.9 120 FTG ---- PE 0.0 7 24.0 0.0 16.1 0.0 0.129 TL 3.66 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/31/2008 C:\HASS78\CARLSBAD17SPEND.SDF JOB TITLE: 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: 11 -43.2 1.408 PL 10.00 PF 1.3 7 24.0 0.0 16.1 0.0 8.9 120 FTG ---- PE 0.0 8 24.0 0.0 17.4 0.0 0.129 TL 10.00 PV Pipe: 12 -43.2 1.408 PL 6.00 PF 1.6 8 24.0 0.0 17.4 0.0 8.9 120 FTG T PE 0.0 B1 24.0 0.0 19.0 0.0 0.129 TL 12.62 PV Pipe: 13 -21.5 1.408 PL 5.66 PF 0.2 9A 24.0 5.6 14.8 21.5 4.4 120 FTG ---- PE 0.0 9B 24.0 5.6 15.0 21.7 0.036 TL 5.66 PV Pipe: 14 -43.2 1.408 PL 1.83 PF 0.2 9B 24.0 5.6 15.0 21.7 8.9 120 FTG ---- PE 0.0 9 24.0 0.0 15.2 0.0 0.129 TL 1.83 PV Pipe: 15 -43.2 1.408 PL 10.00 PF 1.3 9 24.0 0.0 15.2 0.0 8.9 120 FTG ---- PE 0.0 10 24.0 5.6 16.5 22.8 0.129 TL 10.00 PV Pipe: 16 -66.0 1.408 PL 2.25 PF 2.5 10 24.0 5.6 16.5 22.8 13.6 120 FTG T PE 0.0 Bi 24.0 0.0 19.0 0.0 0.282 TL 8.87 PV Pipe: 17 -20.1 1.080 PL 2.50 PF 0.9 hA 24.0 5.6 12.8 20.1 7.0 120 FTG T PE 0.0 11 24.0 0.0 13.8 0.0 0.114 TL 8.26 PV Pipe: 18 -20.1 1.408 PL 8.25 PF 0.3 11 24.0 0.0 13.8 0.0 4.1 120 FTG ---- PE 0.0 12A 24.0 5.3 14.0 20.0 0.031 TL 8.25 PV Pipe: 18A 21.0 1.408 PL 0.50 PF 0.0 12A 24.0 5.3 14.0 20.0 4.3 120 FTG ---- PE 0.0 12 24.0 5.6 14.0 21.0 0.034 TL 0.50 PV Pipe: 18B -61.0 1.408 PL 3.00 PF 0.7 12A 24.0 5.3 14.0 20.0 12.6 120 FTG ---- PE 0.0 12B 24.0 5.3 14.8 20.5 0.244 TL 3.00 PV Pipe: 19 -81.5 1.408 PL 5.66 PF 2.4 12B 24.0 5.3 14.8 20.5 16.8 120 FTG ---- PE 0.0 13 24.0 0.0 17.1 0.0 0.418 TL 5.66 PV Pipe: 20 -81.5 1.408 PL 6.00 PF 5.3 13 24.0 0.0 17.1 0.0 16.8 120 FTG T PE 0.0 Cl 24.0 0.0 22.4 0.0 0.418 TL 12.62 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: 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: 21 0.0 1.408 PL 10.00 PF 0.0 14 24.0 0.0 22.4 0.0 0.0 120 FTG ---- PE 0.0 15 24.0 0.0 22.4 0.0 0.000 TL 10.00 PV Pipe: 22 0.0 1.408 PL 2.25 PF 0.0 15 24.0 0.0 22.4 0.0 0.0 120 FTG T PE 0.0 Cl 24.0 0.0 22.4 0.0 0.000 TL 8.87 PV Pipe: 23 -111.8 1.408 PL 1.00 PF 5.7 Al 24.0 0.0 18.5 0.0 23.0 120 FTG T PE 0.4 A 23.0 0.0 24.6 0.0 0.749 TL 7.62 PV Pipe: 24 -109.2 1.408 PL 1.00 PF 5.5 Bl 24.0 0.0 19.0 0.0 22.5 120 FTG T PE 0.4 B 23.0 0.0 24.9 0.0 0.717 TL 7.62 PV Pipe: 25 -81.5 1.408 PL 1.00 PF 3.2 Cl 24.0 0.0 22.4 0.0 16.8 120 FTG T PE 0.4 C 23.0 0.0 26.0 0.0 0.418 TL 7.62 PV Pipe: 26 -111.8 2.703 PL 10.00 PF 0.3 A 23.0 0.0 24.6 0.0 6.2 120 FTG ---- PE 0.0 B 23.0 0.0 24.9 0.0 0.031 TL 10.00 PV Pipe: 27 -221.0 2.703 PL 10.00 PF 1.1 B 23.0 0.0 24.9 0.0 12.4 120 FTG ---- PE 0.0 C 23.0 0.0 26.0 0.0 0.110 TL 10.00 PV Pipe: 28 -302.5 2.703 PL 155.00 PF 32.4 C 23.0 0.0 26.0 0.0 16.9 120 FTG E PE 0.0 E 23.0 0.0 58.4 0.0 0.197 TL 164.33 PV Pipe: 29 -302.5 3.314 PL 185.00 PF 15.9 E 23.0 0.0 58.4 0.0 11.3 120 FTG ET PE 0.0 TOR 23.0 0.0 74.3 0.0 0.073 TL 217.03 PV Pipe: 30 -302.5 6.403 PL 23.00 PF 0.1 TOR 23.0 0.0 74.3 0.0 3.0 120 FTG ---- PE 10.0 BOR 0.0 0.0 84.3 0.0 0.003 TL 23.00 PV Pipe: 31 -302.5 6.220 PL 50.00 PF 0.2 BOR 0.0 0.0 84.3 0.0 3.2 150 FTG E PE 0.0 DC1 0.0 0.0 84.5 0.0 0.002 TL 73.92 PV Pipes 32 FIXED PRESSURE LOSS DEVICE DC2 0.0 0.0 88.5 0.0 4.0 psi, 302.5 gpm DCl 0.0 0.0 84.5 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: 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: 33 -302.5 6.220 PL 15.00 PF 0.1 DC2 0.0 0.0 88.5 0.0 3.2 150 FTG T PE 0.0 SOURCE 0.0 SRCE 88.6 (N/A) 0.002 TL 66.26 PV NOTES (HASS): Calculations were performed by the HASS 7.9 computer program under license no. 27031226 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.103 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 23.0 ft/sec at pipe 23. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) B T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 1.408 3.31 6.62 2.21 7.72 6.62 1.10 11.03 11.03 6.62 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 21.84 6.220 15.83 33.92 10.18 36.18 11.31 3.39 31.66 31.66 33.92 6.403 18.23 39.07 11.72 41.67 13.02 3.91 36.46 36.46 39.07 NOTES (USER): 0 0 ¼0 H 0 0 co 0 '.0 0 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: N 0 0 0 0 0 0 0 H 0 0 0 0 0 0 0 ('.1 0 a) '.0 H d a)U) 0 •,i [1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 3/31/2008 C:\HASS78\CARLSBAD175PEND.SDF JOB TITLE: WATER SUPPLY CURVE 120+ 110+ \\\ I o\\\ \\\\ I \\\ 100+ \\\ I \\\\ I \\\ I \\\ 90+ * <-90.0 psi @ 1316 gpm I X Flow Test Point P 80+ RI E I SI S 70+ UI RI El 60+ si 150+ ) I 40+ 30+ 20+ LEGEND It X = Required Water Supply 1 88.62 psi @ 552.5 gpm 1 10+ I 0 = Available Water Supply I 107.98 psi ® 552.5 gpm II 0++_+_ - -+- - - -+ -----+ ------+ --------+ --------+ ---------+ -----------+