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HomeMy WebLinkAbout5901 PRIESTLY DR; ; AS080096; Permit12/6/24, 7:41 AM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: AS080096 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS080096 5901 PRIESTLY DR Status: ISSUED SPRINK Applied 6/20/2008 2120610300 Approved: 6/26/2008 0 Issued: 6/26/2008 Inspector: LEUCADIA EQUITIES Tl FIRE SPRINKLER PLAN CHECK & INSPECTIONS Owner: SENTRY FIRE PROTECTION MULLER CENTERPOINT LLC THE MULLER COMPANY 318 STATE PL ESCONDIDO, CA 760-747-7447 about blank Fees($) 130 Add'I Fees ($) 0 23521 PASEO DE VALENCIA#200 LAGUNA HILLS CA Total($) 130 Balance($) 0 1/1 SENTRY FIRE PROTECTION CO. 318 STATE STREET ESCONDIDO, CA 92029 612721 HYDRAULIC CALCULATIONS FOR CENTERPOINT PLAZA CARLSBAD RESEARCH CENTER CARLSBAD, CALIFORNIA 3RD FLOOR TENANT ADDITION DATE: JUL 9, 2008 5 SPRINKLERS IN HALLWAY REMOTE AREA -DESIGN DATA- FlLBcopy OCCUPANCY CLASSIFICATION: Light Hazard (Offices) DENSITY: .10 gpm per sq. ft. AREA OF APPLICATION: 5 Heads in Hallway COVERAGE PER SPRINKLER: Varies NUMBER OF SPRINKLERS CALCULATED: 5 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 77.9 gpm TOTAL WATER REQUIRED (including hose): 177.9 gpm FLOW & PRESSURE (at base of riser) 77.9 gpm@ 32.6 psi (at node BOR) SPRINKLER ORIFICE SIZE: 1/2" K= 5. 60 NAME OF CONTRACTOR: SENTRY FIRE PROTECTION, CO. DESIGN/LAYOUT BY: TT ... ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECI<MAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD, CA 3RD FL.10 5 HDS IN HALL WATER SUPPLY DATA SOURCE NODE TAG CITY STATIC PRESS. (PSI) 105.0 RES ID. FLOW PRESS. @ {PSI) (GPM) 100.0 1500.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER ijOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG Al Bl Cl D1 El Fl Gl Hl Il Jl Kl Ll Ml A B C D E 3RD 2ND 1ST GARAGE TOR BOR DI-PVC DCKl DCK2 UGl CITY ELEVATION (FT) 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 39.5 38.4 38,4 38.4 38.4 38.4 38.4 25.0 11.3 11.3 11.3 0.0 0.0 0.0 0.0 0.0 o.o NODE TYPE K= 5.60 K= 5.60 K= 5,60 K= 5.60 K= 5.60 HOSE STREAM SOURCE AVAIL. TOTAL REQ'D @ DEMAND PRESS. 177. 9 GPM 0.0 GPM 100.0 GPM 77. 9 GPM PRESSURE (PSI) 7.0 11.5 7.4 11.6 7.5 12.1 8.6 14.1 8.3 14.1 14. 8 14. 8 14. 8 15.3 15.4 15.5 15.4 15.6 15.6 21.5 27.5 27.6 27.6 32.6 32.6 32.6 44.6 44.6 44.6 (Gl?M) 177. DISCHARGE (GPM) 14.8 15.2 15.3 16.4 16.1 100.0 177 .9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECKMAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD; CA 3RD FL.10 5 HOS IN HALL 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 -16.1 1.049 PL 55.00 PF 5.8 Il 39.5 5.6 8.3 16.1 6.0 120 FTG E2T PE 0.0 Jl 39.5 0.0 14.l o.o 0.087 TL 67.00 PV Pipe: 2 -16.1 1.408 PL 19.00 PF 0.7 Jl 39.5 0.0 14.1 0.0 3.3 120 FTG 2T PE 0.0 Ml 39.5 0.0 14.8 0.0 0.021 TL 32.23 PV Pipe: 3 -16.4 1.049 PL 51.00 PF 5.4 Gl 39.5 5.6 8.6 16.4 6.1 120 FTG 2ET PE 0.0 Hl 39.5 0.0 14.1 o.o 0.091 TL 60.00 PV Pipe: 4 -16.4 1.408 PL 19.00 PF 0.7 Hl 39.5 0.0 14.1 0.0 3.4 120 FTG 2T PE 0.0 Ll 39.5 0.0 14.8 0.0 0.022 TL 32.23 PV Pipe: 5 -15.3 1. 049 PL 48.25 PF 4.6 El 39.5 5.6 7.5 15.3 5.7 120 FTG 2ET PE 0.0 Fl 39.5 0.0 12.1 o.o 0.080 TL 57.25 PV Pipe: 6 -15.2 1.049 PL 47.00 PF 4.2 Cl 39.5 5.6 7.4 15.2 5.6 120 FTG ET PE 0.0 D1 39.5 0.0 11.6 0.0 0.078 TL 54.00 PV Pipe: 7 -14.8 1.049 PL 51.25 PF 4.5 Al 39.5 5.6 7.0 14.8 5.5 120 FTG 2ET PE 0.0 Bl 39.5 0.0 11.5 0.0 0.075 TL 60.25 PV Pipe: 8 -14.8 1.408 PL 6.00 PF 0.1 Bl 39.5 0.0 11.5 0.0 3.1 120 FTG PE 0.0 D1 39.5 0.0 11. 6 0.0 0.018 TL 6.00 PV Pipe: 9 -30.0 1.408 PL 7.00 PF 0.5 D1 39.5 0.0 11.6 0.0 6.2 120 FTG PE o.o Fl 39.5 0.0 12.1 0.0 0.066 TL 7.00 PV Pipe: 10 -45.4 1.408 PL 6.00 PF 2.7 Fl 39.5 0.0 12.1 o.o 9.4 120 FTG 2T PE o.o Kl 39.5 0.0 14.8 0.0 0.141 TL 19.23 PV Pipe: 11 9.2 1. 639 PL 12.00 PF 0.0 Kl 39.5 o.o 14.8 0.0 1.4 120 FTG PE 0.0 Ll 39.5 0.0 14.8 0.0 0.004 TL 12.00 PV Pipe: 12 -7.3 3.314 PL 12.00 PF 0.0 Ll 39.5 0.0 14.8 o.o 0.3 120 FTG PE 0.0 Ml 39.5 o.o 14.8 a.a 0.000 TL 12.00 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECKMAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD, CA 3RD FL.10 5 HDS IN HALL 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 -23.4 3.314 PL 150 .17 PF 0.1 Ml 39.5 0.0 14.8 0.0 0.9 120 FTG T PE 0.5 A 38.4 o.o 15.3 0.0 0.001 TL 172. 01 PV Pipe: 14 -23.4 3.314 PL 48.75 PF 0.0 A 38.4 0.0 15.3 0.0 0.9 120 FTG T PE 0.0 B 38.4 0.0 15.4 0.0 0.001 TL 70.59 PV Pipe: 15 -23.4 3.314 PL 168.00 PF 0.1 B 38.4 0.0 15.4 o.o 0.9 120 FTG T PE 0.0 C 38.4 0.0 15.5 0.0 0.001 TL 189.84 PV Pipe: 16 -54.6 3.314 PL 6.00 PF 0.1 Kl 39.5 0.0 14.8 0.0 2.0 120 FTG T PE 0.5 D 38.4 0.0 15.4 0.0 0.003 TL 27.84 PV Pipe: 17 -54.6 3.314 PL 48.75 PF 0.1 D 38.4 0.0 15.4 0.0 2.0 120 FTG PE 0.0 C 38.4 o.o 15.5 0.0 0.003 TL 48.75 PV Pipe: 18 -77 .9 4.310 PL 34.08 PF 0.1 C 38.4 0.0 15.5 o.o 1. 7 120 FTG T PE 0.0 E 38.4 0.0 15.6 0.0 0.002 TL 61.95 PV Pipe: 19 -77 .9 4.310 PL 6.17 PF 0.0 E 38.4 0.0 15.6 0.0 1. 7 120 FTG L PE 0.0 3RD 38.4 0.0 15.6 0.0 0.002 TL 14.53 PV Pipe: 20 -77.9 4.310 PL 18.54 PF 0.1 3RD 38.4 0.0 15.6 0.0 1. 7 120 FTG TL PE 5.8 2ND 25.0 0.0 21.5 0.0 0.002 TL 54.78 PV Pipe: 21 -77.9 4.310 PL 15.17 PF 0.1 2ND 25.0 0.0 21.5 a.a 1.7 120 FTG TL PE 5.9 1ST 11.3 0.0 27.5 0.0 0.002 TL 51.41 PV Pipe: 22 -77.9 4.310 PL 34.00 PF 0.1 1ST 11.3 0.0 27.5 0.0 1.7 120 FTG PE o.o GARAGE 11.3 0.0 27.6 0.0 0.002 TL 34.00 PV Pipe: 23 -77.9 4.310 PL 1. 50 PF 0.0 GARAGE 11.3 0.0 27.6 0.0 1. 7 120 FTG L PE 0.0 TOR 11.3 0.0 27.6 0.0 0.002 TL 9.86 PV Pipe: 24 -77.9 4.310 PL 17 .49 PF 0.1 TOR 11.3 o.o 27.6 o.o 1. 7 120 FTG 3LG PE 4.9 BOR 0.0 0.0 32.6 o.o 0.002 TL 45.36 PV ... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECKMAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD, CA 3RD FL.IO 5 HDS IN HALL 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: 25 -77.9 8.390 PL 6.00 PF 0.0 BOR 0.0 0.0 32.6 0.0 0.5 140 FTG PE o.o DI-PVC 0.0 0.0 32.6 o.o 0.000 TL 6.00 PV Pipe: 26 -77.9 7.670 PL 224.00 PF 0.0 DI-PVC 0.0 0.0 32.6 0.0 0.5 150 FTG 3L PE 0.0 DCKl 0.0 0.0 32.6 0.0 0.000 TL 352.00 PV Pipe: RPDEVICE FIXED PRESSURE LOSS DEVICE DCK2 0.0 0.0 44.6 0.0 12.0 psi, 77.9 gpm DCKl 0.0 0.0 32.6 0.0 Pipe: UGl -77.9 9.400 PL 90.00 PF a.a DCK2 0.0 0.0 44.6 0.0 0.4 150 FTG T2LG PE 0.0 UGl o.o H.S. 44.6 100.0 0.000 TL 307.93 PV Pipe: TO-CITY -177.9 9.400 PL 70.00 PF o.o UGl 0.0 H.S. 44.6 100.0 0.8 150 FTG TG PE 0.0 CITY 0.0 SRCE 44.6 (N/A} 0.000 TL 200.76 PV NOTES: (1) Calculations were performed by the HASS 7.6 computer program under license no. 3808132110 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 0.023 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 9.4 ft/sec at pipe 10. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP ..,. . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECKMAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD, CA 3RD FL.10 5 HDS IN HALL PAGE: * Diameter (in) 1.408 1.639 3.314 4.310 7. 670 9.400 PAGE: A Diameter (in) 1.049 PAGE: D Diameter (in) 8.390 MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv 3.31 6.62 2.21 7. 72 6.62 1.10 11.03 11.03 4.36 8.73 2.18 9.82 6.54 1.09 10.91 10.91 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 13.94 27.87 8.36 30.66 16. 72 2.79 27.87 27.87 43.92 94.12 28.24 100.40 31.37 9.41 87.85 87.85 39.94 77.66 28.84 99.84 26.63 8.88 68.78 68.78 MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv V VicCp 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.00 MATERIAL: DIRON HWC: 140 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 31.00 60.00 22.00 78.00 21.00 7.00 60.00 N NPTee 6.62 8.73 21. 84 27.87 94.12 77.66 N NPTee 5.00 WATER SUPPLY ANALYSIS 120.0 -----.--.----------------Static: 105.00 psi Resid: 100.DO psi Flow: 1500.0 gpm'---~ LEGEND Available pressure 1 ® 104.90 psi@ 177.9 gpm 1 ~ Required pressure ,1---------------------------<>---~z-~®~----'44, 64 psi @ 177. 9 gpm cf O O • 0 ~ A. Source Supply curve A B. System Demand Curve----1 u G E so.a _ p R E s s 60. 0 _ u R E 40.0 _ p s i 20.0 _ 0.0 B -14. 7 I I ' 400 600 ' I I I I 8D0 1000 1200 I 1400 FLOW (GPM) I 1600 I 1800 2000 ~~ b:l~ t':I 8 •• H 8 ...J t'-1 ..... t>':l'-0 . . ..... N no t':I 0 lz: OJ 1--'J t>':I :;ti ;g H ~ --.. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 7/9/2008 C:\HASS77\FILES\SENTRY\BECRMAN-TENANT\BECK-3AR.SDF JOB TITLE: CENTERPOINT PLAZA, CARLSBAD, CA 3RD FL.10 5 HOS IN HALL WATER SUPPLY CURVE 108+ *0\\\\\\\\\\\ I \\\\\\\\\\\\\ I \\\\\\\\\\\\ 99+ * <-100.0 psi@ 1500 gpm I Flow Test Point I I 90+ I I I 81+ I I I p 72+ R I E I s I s 63+ U I R I E I p s 54+ I I I I 45+X l I I I 36+ I I I 27+ I I 18+ LEGEND l I X = Required Water Supply I 44.64 psi@ 177.9 gpm 9+ I O = Available Water Supply I 104.90 psi@ 177.9 gpm I .. .. .. " n " " " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)