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HomeMy WebLinkAbout2765 LOKER AVE WEST; ; AS000148; Permit5/2/25,3:28 PM AS000148 Permit Data City of Carlsbad Sprinkler Permit 2765 LOKER AV Job Address: WEST Permit Type: SPRINK Parcel No: 2090811800 Lot #: 0 Reference No.: PC #: Permit No: AS000148 Status: ISSUED Applied 9/27/2000 Approved: 10/30/2000 Issued: 10/30/2000 Inspector: Project Title: ASHWORTH, INC. Applicant: Owner: COBC PARCEL 18LLC CIO KEN SATTERLEE 4510 EXECUTIVE DR #5 SAN DIEGO CA Fees ($) Add'l Fees ($) Total ($) Balance ($) 700.75 0 700.75 0 about:blank 1/1 Lñ5OOO// CARLSBAD FIRE PROTECTION SERVICES Permit Submittal Form Check or fill in pertinent information for type of permit you are submitting. AS - A utoinatic Sprinklers Commercial Residential______________ Number of Heads per System: System #\ Heads 441 System # Heads_____ System # Heads System # Heads_____ System # Heads System # Heads Underground included for approval Underground included for reference only Total Fees FA - Fire Alarm 10 devices or less Over 10 devices # of devices FS -Fixed Systems (Circle One) Hood & Duct, Halon. Special Chemical Agent, Standpipe, Spray Booth, or Appliance. Total Fee -700 There may bee an additional fee of $50.00 per V2 hour for Failed Inspections h/a,217f Address of job site 21(, 4\JFt '.tE'sT Suite # Building Permit # CB iO 33( Contractor Information Consolidated Fireprotection, Inc. IName_________________________________________________ Address 6108 Avenida Encinas, Ste. A City, State, Zip Carlsbad, CA 92009 Kind of License and number C16 #641834 - Phone (760) 4319901 Certificate of Insurance on file with Fire Dept.? YorN Business License on filr with City? or Signature - Date SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: .10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) BOR 94.4 80.0 1500.0 93.8 259.0 64.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 259.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 259.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 10.0 K= 5.60 7.0 14.8 2 10.0 K= 5.60 7.6 15.4 3 10.0 K= 5.60 10.8 18.4 4 10.0 K= 5.60 13.8 20.8 5 10.0 K= 5.60 18.9 24.4 6 10.0 K= 5.60 16.8 22.9 7 10.0 K= 5.60 18.9 24.4 8 10.0 K= 5.60 27.1 29.1 9 10.0 K= 5.60 12.1 19.5 10 10.0 K= 5.60 13.7 20.7 11 10.0 K= 5.60 17.7 23.5 12 10.0 K= 5.60 19.8 24.9 22 11.0 - - - - 7.8 23 11.0 - - -- 11.1 24 11.0 14.9 25 110 - - - 19.7 26 11.0 17.6 27 11.0 - - - - 19.7 28 11.0 - --- 28.0 29 11.0 - - - - 12.3 30 11.0 - - - - 13.9 31 11.0 - - - - 18.1 32 11.0 - - - - 21.0 40 11.0 - - - - 27.2 41 11.0 - - - - 38.7 42 11.0 - - - - 47.8 43 11.0 - - - - 35.4 44 11.0 44.0 45 11.0 48.1 46 11.0 27.1 47 11.0 - - - - 40.3 48 11.0 48.9 49 11.0 ---- 51.1 50 30.0 - - - - 46.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) POC 30.0 - - - - 50.6 TOR 30.0 - - - - 51.0 BOR 0.5 SOURCE 64.0 259.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 10/12/1999 . A:\ASH.SDF JOB TITLE: ashworth mezzanine PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUN. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 -14.8 1.049 PL 12.00 PF 1.3 1 10.0 5.6 7.0 14.8 5.5 150 FTG 2ET PE -0.4 2.2 11.0 0.0 7.8 0.0 0.049 TL 25.60 PV 0.2 Pipe: 2 -15.4 1.049 PL 2.00 PF 0.7 2 10.0 5.6 7.6 15.4 5.7 150 FTG ET PE -0.4 22 11.0 0.0 7.8 0.0 0.053 TL 12.58 PV 0.2 Pipe: 3 -18.4 1.049 PL 3.50 PF 0.7, 3 10.0 5.6 10.8 18.4 6.8 150 FTG 2E PE -0.4 23 11.0 0.0 11.1 0.0 0.074 TL 9.54 PV 0.3 Pipe: 4 -20.8 1.049 PL 10.00 PF 1.5 4 10.0 5.6 13.8 20.8 7.7 150 FTG 2E PE -0.4 (24 11.0 0.0 14.9 0.0 0.093 TL 16.04 PV 0.4 Pipe: 5 -24.4 1.049 PL 3.50 PF 1.2 5 10.0 5.6 18.9 24.4 9.0 150 FTG 2E PE -0.4 25 11.0 0.0 19.7 0.0 0.124 TL 9.54 PV 0.6 Pipe: 6 -22.9 1.049 PL 5.00 PF 1.2 6 10.0 5.6 16.8 22.9 8.5 150 FTG 2E PE -0.4 26 11.0 0.0 17.6 0.0 0.111 TL 11.04 PV 0.5 Pipe: 7 -24.4 1.049 PL 4.00 PF 1.2 7 10.0 5.6 18.9 24.4 9.0 150 FTG 2E PE -0.4 27 11.0 0.0 19.7 0.0 0.124 TL 10.04 PV 0.6 Pipe: 8 -29.1 1.049 PL 2.00 PF 1.4 8 10.0 5.6 27.1 29.1 10.8 150 FTG 2E PE -0.4 '28 11.0 0.0 28.0 0.0 0.173 TL 8.04 PV 0.8 Pipe: 9 -19.5 1.049 PL 2.00 PF 0.7 9 10.0 5.6 12.1 19.5 7.2 150 FTG 2E PE -0.4 29 11.0 0.0 12.3 0.0 0.082 TL 8.04 PV 0.4 Pipe: 10 -20.7 1.049 PL 1.00 PF 0.6 10 10.0 5.6 13.7 20.7 7.7 150 FTG 2E PE -0.4 30 11.0 0.0 13.9 0.0 0.092 TL 7.04 PV 0.4 Pipe: 11 -23.5 1.049 PL 1.50 PF 0.9 11 10.0 5.6 17.7 23.5 8.7 150 FTG 2E PE -0.4 31 11.0 0.0 18.1 0.0 0.116 TL 7.54 PV 0.5 Pipe: 12 -24.9 1.049 PL 6.50 PF 1.6 12 10.0 5.6 19.8 24.9 9.3 150 FTG 2E PE -0.4 32 11.0 0.0 21.0 0.0 0.130 TL 12.54 PV 0.6 Pipe: 13 -30.2 1.049 PL 10.00 PF 3.2 22 11.0 0.0 7.8 0.0 11.2 150 FTG T PE 0.0 23 11.0 0.0 11.1 0.0 0.185 TL 17.56 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUN. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 -48.7 1.049 PL 1.00 PF 3.8 23 11.0 0.0 11.1 0.0 18.1 150 FTG T PE 0.0 24 11.0 0.0 14.9 0.0 0.446 TL 8.56 PV 2.2 Pipe: 15 -69.5 1.380 PL 12.00 PF 4.8 24 11.0 0.0 14.9 0.0 14.9 150 FTG T PE 0.0 25 11.0 0.0 19.7 0.0 0.227 TL 21.07 PV 1.5 Pipe: 16 -93.9 1.380 PL 10.00 PF 7.5 25 11.0 0.0 19.7 0.0 20.1 150 FTG T PE 0.0 40 11.0 0.0 27.2 0.0 0.396 TL 19.07 PV 2.7 Pipe: 17 -93.9 1.380 PL 20.00 PF 11.5 40 11.0 0.0 27.2 0.0 20.1 150 FTG T PE 0.0 41 11.0 0.0 38.7 0.0 0.396 TL 29.07 PV 2.7 Pipe: 18 -93.9 1.380 PL 14.00 PF 9.1 41 11.0 0.0 38.7 0.0 20.1 150 FTG T PE 0.0 42 11.0 0.0 47.8 0.0 0.396 TL 23.07 PV 2.7 Pipe: 19 -22.9 1.049 PL 12.00 PF 2.2 26 11.0 0.0 17.6 0.0 8.5 150 FTG T PE 0.0 / 27 11.0 0.0 19.7 0.0 0.111 TL 19.56 PV 0.5 Pipe: 20 -47.3 1.049 PL 12.00 PF 8.3 27 11.0 0.0 19.7 0.0 17.6 150 FTG T PE 0.0 11.0 0.0 28.0 0.0 0.423 TL 19.56 PV 2.1 Pipe: 21 -76.4 1.380 PL 18.00 PF 7.3 28 11.0 0.0 28.0 0.0 16.4 150 FTG T PE 0.0 43 11.0 0.0 35.4 0.0 0.271 TL 27.07 PV 1.8 Pipe: 22 -76.4 1.380 PL 23.00 PF 8.7 43 11.0 0.0 35.4 0.0 16.4 150 FTG T PE 0.0 44 11.0 0.0 44.0 0.0 0.271 TL 32.07 PV 1.8 Pipe: 23 -76.4 1.380 PL 6.00 PF 4.1 44 11.0 0.0 44.0 0.0 16.4 150 FTG T PE 0.0 45 11.0 0.0 48.1 0.0 0.271 TL 15.07 PV 1.8 Pipe: 24 -19.5 1.049 PL 11.00 PF 1.5 29 11.0 0.0 12.3 0.0 7.2 150 FTG T PE 0.0 30 11.0 0.0 . 13.9 0.0 0.082 TL 18.56 PV 0.4 Pipe: 25 -40.2 1.049 PL 6.00 PF 4.2 30 11.0 0.0 13.9 0.0 14.9 150 FTG T PE 0.0 31 11.0 0.0 18.1 0.0 0.313 TL 13.56 PV 1.5 Pipe: 26 -63.7 1.380 PL 6.00 PF 2.9 31 11.0 0.0 18.1 0.0 13.7 150 FTG T PE 0.0 32 11.0 0.0 21.0 0.0 0.193 TL 15.07 PV 1.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -88.7 1.380 PL 8.00 PF 6.1 32 11.0 0.0 21.0 0.0 19.0 150 FTG T PE 0.0 46 11.0 0.0 27.1 0.0 0.356 TL 17.07 PV 2.4 Pipe: 28 -88.7 1.380 PL 28.00 PF 13.2 46 11.0 0.0 27.1 0.0 19.0 150 FTG T PE 0.0 47 11.0 0.0 40.3 0.0 0.356 TL 37.07 PV 2.4 Pipe: 29 -88.7 1.380 PL 15.00 PF 8.6, 47 11.0 0.0 40.3 0.0 19.0 150 FTG T PE 0.0 48 11.0 0.0 48.9 0.0 0.356 TL 24.07 PV 2.4 Pipe: 30 -93.9 2.635 PL 16.00 PF 0.3 (42 11.0 0.0 47.8 0.0 5.5 150 FTG --- PE 0.0 45 11.0 0.0 48.1 0.0 0.017 TL 16.00 PV 0.2 Pipe: 31 -170.3 2.635 PL 15.00 PF 0.8 45 11.0 0.0 48.1 0.0 10.0 150 FTG ---- PE 0.0 48 11.0 0.0 48.9 0.0 0.051 TL 15.00 PV 0.7 Pipe: 32 -259.0 2.635 PL 8.00 PF 2.3 48 11.0 0.0 48.9 0.0 15.2 150 FTG E PE 0.0 49 11.0 0.0 51.1 0.0 0.111 TL 20.45 PV 1.6 Pipe: 33 -259.0 2.635 PL 16.00 PF 3.2 49 11.0 0.0 51.1 0.0 15.2 150 FTG E PE -8.2 50 30.0 0.0 46.1 0.0 0.111 TL 28.45 PV 1.6 Pipe: 34 -259.0 2.635 PL 16.00 PF 4.5 50 30.0 0.0 46.1 0.0 15.2 150 FTG T PE 0.0 POC 30.0 0.0 50.6 0.0 0.111 TL 40.89 PV 1.6 Pipe: 35 _2591.0 6.357 PL 144.00 PF 0.4 POC 30.0 0.0 50.6 0.0 2.6 150 FTG 4E PE 0.0 TC~R 30.0 0.0 51.0 0.0 0.002 TL 250.40 PV 0.0 Pipe: 36 -259.0 6.357 PL 29.50 PF 0.2 TOR 30.0 0.0 51.0 0.0 2.6 150 FTG TC PE 12.8 BO R 0.5 SRCE 64.0 (N/A) 0.002 TL 147.30 PV 0.0 NOTES: Calculations were performed by the HASS 6.4.0 computer program under license no. 126F611 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been balanced to provide an average - imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.109 gpm. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 20.1 ft/sec at pipe 17. 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 N NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 - 10.00r 6.00 PAGE: * 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 DPV1v N NPTee 2.635 8.24 16.47 5.49 19.22 9.61 1.37 13.73 13.73 16.47 / 6.357 17.60 37.72 11.32 40.23 12.57 3.77 35.21 23.89 37.72 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 10/12/1999 A:\ASH.SDF JOB TITLE: ashworth mezzanine WATER SUPPLY CURVE 96+ \\\\\ \\\\\\ 88+ \\\\\ \\\\\\ \\\\\ \\\)(c - 80+ * -80.0 psi @ 1500 gpm Flow Test Point 72+ S 56+ U R E 48+ ( P S I 40+ ) I 11 16+ LEGEND 'I X = Required Water Supply 63.98 psi @ 259.0 gpm 8+ 0 = Available Water Supply I of 93.84 psi @ 259.0 gpm 0++-+—+—+--+--+ -+------1----- 1- -r 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)