Loading...
HomeMy WebLinkAbout6185 PASEO DEL NORTE; ; AS000026; Permit10/31/25, 1:27 PM AS000026 Pennit Data Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: Fees($) 426.25 about blank City of Carlsbad Sprinkler Permit Permit No: AS000026 6185 PASEO DEL Status: NORTE SPRINK Applied Approved: 0 Issued: Inspector: CARLSBAD CORP PLAZA Owner: Add'I Fees ($) 0 Total($) 426.25 ISSUED 3/6/2000 Balance($) 0 1/1 FEB-25-99 THU 16:17 CARLSBAD-FIRE DEPT FAX NO. 7609290255-.......,.... .. L:l..l.,l'Jla'U .a,· I a 'lllf ,_,. ..,_.a,a. .... a. ........__........_,._ Fire-Protect-i&n--System AppU~a-tiolL Permit Information A. Check or fili in pertinent information for type of permit you are submitting. AS -Autommw Sprinklers Commercial£ Residential __ _ Number of heads per system System # _\ _ Heads --r2::> System # _ System#-Heads_ System_# __ System # Heads System # _ Underground included for approval Underground included for reference only FA -Fire Alarm T---en_ -de.vie-es or less Over 10 devices # of devices __ Heads--.- Heads _ Heads Total Fees To.ta! Fees FS -FixedSystems -Circle One Hoodand.DuctJ Halon .. Speciai Chemical Agent, Standpipe, Spray Booth, or Appliance- Total Fees There may be an nddition:.11 charge of $50.00 per 1/2 hour for foiled inspections. B. Address of job site 0\f>S ~ :t;:,e:L.~te # __ Bldg Permit# C. Contractor Information Nainc L-\ f12§\le;Z:R fi.\:21c, l?f?oT. lj::f::... • Address 'Zcp\.'.7 ::Dil'::"\R..£ L4::)~ A?. ~ 'e, City. Stale ~'2:,\~ cA-::rz.~ Kind of License and Number ~ Phone 7(¢ ~ -r::Fl:J Certilicalc of lrrsurnnt:L'--0»-file wilh Fir1: Dept? ©,r N Business License on lilc wilh Cily? ~ N P. 02 Fe-es LIFEGUARD FIRE PROTECTION, INC. 2613 TEMPLE HEIGHTS DR. STE: B, OCEANSIDE, CA 92056 (760) 806-9997 • FAX (760) 806-4813 Hydraulic Design Information Sheet Name: NETCENTRIC TENANT IMPROVEMENT Location: 6185 PASEO DEL NORTE, CARLSBAD Date: 3-2-00 Building: EXISTING System No. Contractor: LIFEGUARD FIRE PROTECTION, INC. Contract No. Calculated By: RAB Drawing No. 1 OF I -==---------==--------------------Construction: D Combustible tzl Non-Combustible Ceiling Height IO Ft. ------ SYSTEM DESIGN tzl NFPA 13: tzl Light Hazard Ordinary Hazard Group D 1 □ 2 □ 3 D Extra Hazard 0 NFPA231 0 NFPA 231C: Figure: Curve: D Other (Specify) □Specific Ruling Made By Date Area of Sprinkler Operation 1500 SQ. FT. System TyQe Density .10 ~ Wet □ Dry D Deluge D Pre-Action Area Per Sprinkler 225 SQ. FT. MAX. SQrinkler or Nozzle Hose Allowance GPM: Inside 0 Make GEM Model A Hose Allowance GPM: Outside 100 Size ½" K-factor: 5.6 Rack Sprinkler Allowance NA Temperature Rating 155 DEG. CALCULATION SUMMARY GPM Required _25_3_._13 ______ _ PSI Required 70.42 At Base of Riser ---------"C" Factor Used: 0 v er head 120 Under ound 150 WATER SUPPLY Water Flow Test Pump Data Tank or Reservoir Date& Time Rated Capacity Capacity Static PSI 120 At PSI Elevation Residual PSI 80 Elevation GPM Flowing 2915 Well Elevation Proof Flow GPM Location SITE Source of Information SHELL DRAWINGS COMMODITY STORAGE Commodity OFFICE Class Location Storage Height Area Aisle Width Storage Method: Solid Piled % Palletized %Rack Rack D Single Row D Conventional Pallet D Automatic Storage D Encapsulated D DoubleRow D Slave Pallet 0 Solid Shelving D Non-Encapsulated D Multiple Row D Open Flue Spacing In Inches Clearance From Top of Storage to Ceiling Longitudinal Transverse Ft. In. Horizontal Barriers Provided NETCENTRIC Tl PROOF CALC. .10/1500 250 24 23 22 21 200 19 18 17 16 15 14 13 12 11 10 0 0 0 0 0 0 0 0 0 0 0 0 0 0 9 0 8i!t 7 0 0 n_ .:. r,°' -C ... '-_./ ,.._..,, 6 5 4 3 2 1 ~ o, - 0 350 700 1050 1400 1750 System Demand .. Sprinkler Demand 73.88 PSI @ 253.13 Additional rlows o.oo Hose at Source 100.00 Total Demand 73.88 PSI@ 353.13 2100 GPM GPM GPM GPM 2450 Water Flow (GPM) Sigma Dynamics Corporation 7700 Supply/ Demand Graph I Margin f--- Pressure 33.40 PSI f---rlow 2478.68 GPM --·---s - N 1.85 2800 3150 3500 Water Supply .. Static 108.00 PSI Residual 72.00 PSI @ 2915.00 GPM Elevation 0.00 PSI SUBMITTAL SERIAL N0:4144HY1 NETCERTRIC TI PROOF CALC .. 10/1500 FLOW TEST RESULTS water Supply STATIC 108.00 PSI RESIDUAL 72.00 PSI @ 2915.00 GPM CITY PRESSURE AVAILABLE AT 353.l SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K-FACTOR -------- 100 20.95 14.83 5.60 101 20.51 14.83 5.60 102 20.42 14.83 5.60 103 20.44 14.83 5.60 104 20.69 14.83 5.60 105 21.52 14.83 5.60 106 18.92 14.83 5.60 107 18.86 14.83 5.60 108 24.47 21.00 5.60 109 24.12 21.00 5.60 110 21.00 21.00 5.60 111 21.22 21.00 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY FROM 5 TO 12 GPM 107.27 PSI PRESSURE -------- 13.99 13.41 13.30 13.32 13.65 14.77 11.42 11.35 19.10 18.56 14.06 14.36 253.13 GPM 100.00 GPM 353.13 GPM 73.88 PSI 0.00 PSI 23.00 FPS 03-02-2000 PAGE 1 SUBMITTAL SERIAL N0:4144HY1 03-02-2000 PAGE 2 NETCENTRIC TI PROOF CALC. .10/1500 Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From TO GPM IN Devices Ft PSI/Ft PSI 32 110 1.080 L 14.00 C=120 PT 14.06 (110) Q 21.00 F=T/E F 8.10 PE -0.87 AO T 22.10 0.1236 PF 2.73 PT 15.92 ( 32) ------------------33 111 1.080 L 14.00 C=l20 PT 14.36 (111) Q 21.22 F=T/E F 8.10 PE -0.87 AO T 22.10 0.1260 PF 2.78 PT 16.27 ( 33) ------------------41 109 1.080 L 4.00 C=l20 PT 18.56 (109) Q 24.12 F=T/E F 8.10 PE -0.87 AO T 12.10 0.1597 PF 1.93 PT 19.62 ( 41) ------------------40 108 1.080 L 4.00 C=120 PT 19.10 (108) Q 24.47 F=T/E F 8.10 PE -0.87 AO T 12.10 0.1640 PF 1.98 PT 20.21 ( 40) ------------------39 107 1.080 L 3.00 C=l20 PT 11.35 (107) Q 18.86 F=T/E F 8.10 PE -0.87 AO T 11.10 0.1013 PF 1.12 PT 11.60 ( 39) ------------------ 39 106 1.080 L 8.00 C=l20 PT 11.42 (106) Q 18.92 F=E F 2.30 PE -0.87 AO T 10.30 0.1019 PF 1.05 31 39DQ 18.86 1.080 L 6.00 C=l20 PT 11.60 ( 39) Q 37.79 F=T F 5.80 PE o.oo AO T 11.80 0.3664 PF 4.32 PT 15.92 ( 31) ------------------30 105 1.080 L 14.00 C=l20 PT 14.77 (105) Q 21.52 F=T,E F 8.10 PE -0.87 AO T 22.10 0.1293 PF 2.86 PT 16.76 ( 30) ------------------38 104 1.080 L 5.00 C=l20 PT 13.65 (104) Q 20.69 F=T,E F 8.10 PE -0.87 AO T 13.10 0.1202 PF 1.57 PT 14.35 ( 38) ------------------37 103 1.080 L 5.00 C=120 PT 13.32 (103) Q 20.44 F=T,E F 8.10 PE -0.87 AO T 13.10 0.1175 PF 1.54 PT 13.99 ( 37) SUBMITTAL SERIAL NO:4144BY1 03-02-2000 PAGE 3 NETCENTRIC TI PROOF CALC. .10/1500 Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length LOSS summary From To GPM IN Devices Ft PSI/Ft PSI ------------------36 102 1.080 L 5.00 C=l20 PT 13.30 (102) Q 20.42 F=T,E F 8.10 PE -0.87 AO T 13.10 0.1174 PF 1.54 PT 13.97 ( 36) ------------------35 101 1.080 L 5.00 C=120 PT 13.41 (101) Q 20.51 F=T,E F 8.10 PE -0.87 AO T 13.10 0.1183 PF 1.55 PT 14.09 ( 35) ------------------34 100 1.080 L 5.00 C=120 PT 13.99 (100) Q 20.95 F=T,E F 8.10 PE -0.87 AO T 13.10 0.1230 PF 1.61 PT 14.73 ( 34) ------------------37 36 1.536 L 11.00 C=l20 PT 13.97 ( 36) Q 5.61 F=O F o.oo PE 0.00 BL T 11.00 0.0019 PF 0.02 38 37DQ 20.44 1.536 L 11.00 C=120 PT 13.99 ( 37) Q 26.05 F=O F o.oo PE 0.00 BL T 11.00 0.0331 PF 0.36 24 38DQ 20.69 1.536 L 24.00 C=120 PT 14.35 ( 38) Q 46.74 F=O/T F 8.90 PE 0.00 BL T 32.90 0.0977 PF 3.21 23 24 1.728 L 20.00 C=l20 PT 17.56 ( 24) Q 46.74 F=O F 0.00 PE 0.00 CMI T 20.00 0.0550 PF 1.10 22 23DQ 42.75 1.728 L 5.00 C=120 PT 18.66 ( 23) Q 89.4:8 F=O F 0.00 PE o.oo CMl T s.oo 0.1830 PF 0.91 41 22DQ -85.04 1.536 L 24.00 C=120 PT 19.57 ( 22) Q 4.44 F=O/T F 8.90 PE o.oo BL T 32.90 0.0013 PF 0.04 40 41DQ 24.12 1.536 L 15.00 C=l20 PT 19.61 ( 41) Q 28.57 F=O F o.oo PE 0.00 BL T 15.00 0.0393 PF 0.59 12 40DQ 24.47 1.536 L 182.00 C=l20 PT 20.20 ( 40) Q 53.04 F=T,EE F 10.67 PE o.oo BL T 192.67 0.1234 PF 23.78 PT 43.98 ( 12) SUBMITTAL SERIAL NO:4144HY1 03-02-2000 PAGE 4 NETCENTRIC TI PROOF CALC. .10/1500 Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To GPM IN Devices Ft PSI/Ft PSI ------------------32 31 1.536 L 12.00 C=l20 PT 15.93 ( 31) Q 0.53 F=O F 0.00 PE 0.00 BL T 12.00 0.0000 PF o.oo 33 32DQ 21.00 1.536 L 15.00 C=120 PT 15.93 ( 32) Q 21.53 F=O F o.oo PE o.oo BL T 15.00 0.0233 PF 0.35 23 33DQ 21.22 1.536 L 20.00 C=120 PT 16.28 ( 33) Q 42.75 F=O/T F 8.90 PE o.oo BL T 28.90 0.0828 PF 2.39 PT 18.67 ( 23) ------------------30 31 1.536 L 13.00 C=120 PT 15.93 ( 31) Q 37.26 F=O F o.oo PE o.oo BL T 13.00 0.0642 PF 0.83 13 30DQ 21.52 1.536 L 162.00 C=120 PT 16.76 ( 30) Q 58.78 F=T,EE F 10.67 PE 0.00 BL T 172.67 0.1493 PF 25.78 PT 42.54 ( 13) ------------------35 36 1,536 L 11.00 C=120 PT 13.97 ( 36) Q 14.81 F=O F o.oo PE o.oo BL T 11.00 0.0117 PF 0.13 34 35DQ 20.51 1.536 L 11.00 C=120 PT 14.10 ( 35) Q 35.32 F=O F o.oo PE 0.00 BL T 11.00 0.0582 PF 0.64 14 34DQ 20.95 1.536 L 180.00 C=l20 PT 14.74 ( 34) Q 56.27 F=T,EE F 10.67 PE 0.00 BL T 190.67 0.1377 PF 26.26 13 14 1.728 L 20.00 C=l20 PT 41.00 ( 14) Q 56.27 F=O F 0.00 PE o.oo CMl T 20.00 0.0776 PF 1.55 12 13DQ 58.78 1.728 L 5.00 C=l20 PT 42.55 ( 13) Q 115.05 F=O F 0.00 PE o.oo CMl T 5.00 0.2914 PF 1.46 5 l2DQ 53.04 1.728 L 2.00 C=l20 PT 44.01 ( 12) Q 168.09 F=O F o.oo PE o.oo CMl T 2.00 0.5876 PF 1.18 PT 45.19 ( 5) SUBMITTAL SERIAL NO:4144HY1 03-02-2000 PAGE 5 NETCENTRIC TI PROOF CALC. .10/1500 Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length LOSS Swmnary From To GPM IN Devices Ft PSI/Ft PSI ------------------21 22 1. 728 L 15.00 C=120 PT 19.58 ( 22) Q 85.04 F=0 F o.oo PE o.oo CMl T 15.00 0.1666 PF 2.50 11 21DQ -42.95 1.536 L 226.00 C=l20 PT 22.08 ( 21) Q 42.09 F=T,4E,EE/T F 33.97 PE o.oo BL T 259.97 0.0805 PF 20.93 PT 43.01 ( 11) ------------------20 21 1.728 L 20.00 C=120 PT 22.08 ( 21) Q 42.95 F=0 F o.oo PE 0.00 CMl T 20.00 0.0471 PF 0.94 10 20 1.536 L 194.00 C=120 PT 23.02 ( 20) Q 42.95 F=T,4E,EE/T F 33.97 PE o.oo BL T 227.97 0.0835 PF 19.04 11 10 1. 728 L 20.00 C=120 PT 42.06 ( 10) Q 42.95 F=O F 0.00 PE 0.00 CMl T 20.00 0.0471 PF 0.94 s llDQ 42.09 1.728 L 13.00 C=120 PT 43.00 ( 11) Q 85.04 F=O F 0.00 PE 0.00 CMl T 13.00 0.1666 PF 2.17 3 5DQ 168.09 2.203 L 17.00 C=l20 PT 45.17 ( 5) Q 253.13 F=T/T F 23.20 PE o.oo FM T 40.20 0.3840 PF 15.44 2 3 2.203 L 12.00 C=l20 PT 60.61 ( 3) Q 253.13 F=O F o.oo PE 5.20 FR T 12.00 0.3840 PF 4.61 1 2 4.310 L 85.00 C=l50 PT 70.42 ( 2) Q 253.13 F=lE F 28.44 PE o.oo UN T 113.44 0.0097 PF 1.10 0 1 5.914 L 40.00 C=lSO PT 71.52 ( 1) Q 253.13 F=2T,DCA/2E F 135.58 PE 0.00 UN T 175.58 0.0021 PF 0.37 AMES DOUBLE DETECTOR CHECK VALVE 2.00 PT 73.89 ( 0)