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HomeMy WebLinkAbout6050 AVENIDA ENCINAS; ; AS120071; PermitUity ot uarlsbacl Sprinkler Permit Permit No: AS120071 6050 AVENIDA Job :Address: Status: APPROVED. ENCINAS Permit Type: SPRINK Applied 6/21/2012 Parcel No: 2110303200 Approved: 6/26/2012 Lot #: 0 Reference No.: . . Issued: 6/26/2012 PC #: . . Inspector: Project Title:. CALIBER COLLISION INSTALLATION OF FIRE SPRINKLERS IN NEW PAINT SPRAY BOOTHS Applicant: FIVE, STAR FIRE PROTECTION INC UNIT 1040 S CYPRESS ST LA HABRA, CA 714-441-1315 Owner: 0 AVEN IDA ENCINAS CARLSBAD L L C 8039 BALBOA. AVE SAN DIEGO CA Fees ($) Add'l Fees ($) Total ($) Balance ($) 262 0 0 262 0 Date: June 6, 2012 System No.: BOOTH Contract No.: I Drawing No.: FS-2 Calculated by: TERRY Ceiling Height: lift AV) AS SviiTTi) FIVE STAR FIRE HYDRAULIC DESIGN INFORMATION SHEET Name: CALIBER COLLISION CENTER Location: 6050 AVENIDA ENCINAS CARLSBAD, CA 92009 Building: EXISTING SPRINKLERED Contractor: FIVE STAR FIRE PROTECTION File Name: CALIBER CARLSBADI.the Construction: 0 Combustible J Noncombustible Occupancy: S-I AHJ: CARLSBAD FIRE DEPARTMENT SYSTEM DESIGN tEl NFPA 13: (J Light Hazard 0 Ordinary Hazard Group: tEl Extra Hazard Group: 2 Figure: Curve: O Other (Specify): Specific Rulling: Made By: Date: Area of Sprinkler Operation: ENTIRE sqft System Type: W Wet 0 Dry 0 Deluge J Pre-Action Density: .40 gpm/sqft Area per Sprinkler: 96 sqft SPRINKLER or NOZZLE Hose Allowance Inside: 100 gpm Make: VIKING Model: MICROMATIC Hose Allowance Outside: 400 gpm Size: 3/4 in K-factor: 8.0 Rack Sprinkler Allowance: gpm Temperature Rating: 155 OF CALCULATION SUMMARY Flow Required: 859.04 gpm Pressure Required: 61.71 psi At: BASE OF RISER "C" Factor Used: Overhead: 120 Underground: 100 WATER SUPPLY WATER FLOW TEST PUMP DATA Date: 540-12 Rated Capacity: Time: 8AM At: Static: 85 psi Elevation: Residual: 70 psi Flowing: 1040 gpm Elevation: ft Location: 6050 AVENIDA ENCINAS Source of Information: CARLSBAD WATER TANK OR RESERVOIR gpm Capacity: gals psi Elevation: ft ft WELL Proof Flow: gpm COMMODITY STORAGE Commodity: Class: Location: Storage Height: Area: Aisle Width: Storage Method: Solid Pile: % Palletized: % Rack: % RACK STORAGE Single Row Double Row O Multiple Row FLUE SPACING Longitudinal: Conventional Pallet Slave Pallet in Transverse: Automatic Storage 0 Encapsulated O Solid Shelving 0 Nonencapsulated Open CLEARANCE FROM TOP OF STORAGE TO CEILING in ft in Horizontal Barriers Provided: File: CALIBER CARLSBADI .the Page 1 o 3 Node Node Flow K-factor Elevation Pressure Diameter Length Fnc Loss Node Node Flow K-factor Elevation Pressure HWC Fittings Eqv Length Elev Loss Pipe Flow Velocity TtI Length Ttl FL 0 859.04 Source -4.00 61.71 6.340 12.000 0.006 1 0.00 -4.00 61.48 100 T 26.572 0.00 359.04 3.65 38.570 0.23 1 0.00 -4.00 61.48 6.340 7.000 0.006 2 0.00 3.00 58.33 100 E 12.400 3.03 359.04 3.65 19.400 0.12 2 0.00 3.00 58.33 6.340 6.000 0.006 3 0.00 3.00 55.19 100 E,2GV 17.715 0.00 359.04 3.65 23.710 3.14 The Flow Dependent Pressure Loss Device in this pipe accounts for 3.00 psi of the total friction loss. 3 0.00 3.00 55.19 6.340 7.000 0.006 4 0.00 -4.00 58.11 100 E 12.400 -3.03 359.04 3.65 19.400 0.12 4 0.00 -4.00 58.11 6.340 138.000 0.006 5 0.00 -4.00 57.14 100 2E 24.801 0.00 359.04 3.65 162.800 0.97 5 0.00 -4.00 57.14 6.340 4.000 0.006 6 0.00 0.00 55.31 100 E 12.400 1.73 359.04 3.65 16.400 0.10 6 0.00 0.00 55.31 4.260 16.000 0.030 7 0.00 16.00 47.90 120 0.000 6.93 359.04 8.08 16.000 0.47 7 0.00 16.00 47.90 3.260 118.000 0.109 8 0.00 16.00 32.00 120 3E 28.223 0.00 359.04 13.80 146.220 15.90 8 0.00 16.00 32.00 4.260 6.000 0.030 9 0.00 16.00 31.05 120 T 26.334 0.00 35904 6.08 32.330 0.96 9 0.00 16.00 31.05 4.260 13.000 0.030 10 0.00 4.00 35.48 120 E 13.167 -5.20 359.04 8.08 26.170 0.77 10 0.00 4.00 35.48 4.260 2.000 0.030 11 0.00 4.00 34.56 120 E,BV 28.968 0.00 359.04 8.08 30.970 0.91 11 0.00 4.00 34.56 3.260 7.000 0.109 12 0.00 11.00 29.74 120 E 9.408 3.03 359.04 13.80 16.410 1.78 06/19/12 "THE" Sorinkler Proaram 2001 File: CALIBER CARLSBADI .the Page 2 of 3 Node Node Flow K-factor Elevation Pressure Diameter Length Fnc Loss Node Node Flow K-factor Elevation Pressure HWC Fittings Eqv Length Elev Loss Pipe Flow Velocity TtI Length Ttl FL 12 0.00 11.00 29.74 3.260 6.000 0.109 13 0.00 11.00 28.07 120 E 9.408 0.00 359.04 13.80 15.410 1.68 13 0.00 11.00 28.07 3.260 10.000 0.038 14 0.00 11.00 27.69 120 0.000 0.00 203.02 7.80 10.000 0.38 14 0.00 11.00 27.69 3.260 2.000 0.023 15 0.00 11.00 27.64 120 0.000 0.00 154.86 5.95 2.000 0.05 13 0.00 11.00 28.07 1.682 2.500 0.164 16 0.00 11.00 26.04 120 T 9.900 0.00 78.48 11.33 12.400 2.03 16 0.00 11.00 26.04 1.442 8.000 0.097 17 0.00 11.00 25.26 120 0.000 0.00 39.46 7.75 8.000 0.78 13 0.00 11.00 28.07 1.682 5.500 0.160 18 0.00 11.00 25.60 120 T 9.900 0.00 77.54 11.20 15.400 2.47 18 0.00 11.00 25.60 1.097 11.000 0.358 19 0.00 11.00 21.67 120 0.000 0.00 38.85 13.19 11.000 3.93 15 0.00 11.00 27.64 1.682 2.500 0.161 20 0.00 11.00 25.64 120 T 9.900 0.00 77.88 11.25 12.400 2.00 20 0.00 11.00 25.64 1.442 8.000 0.096 21 0.00 11.00 24.88 120 0.000 0.00 39.16 7.69 8.000 0.77 15 0.00 11.00 27.64 1.682 5.500 0.158 22 0.00 11.00 25.21 120 T 9.900 0.00 76.98 11.11 15.400 2.43 22 0.00 11.00 25.21 1.097 11.000 0.353 23 0.00 11.00 21.33 120 0.000 0.00 38.58 13.10 11.000 3.88 14 0.00 11.00 27.69 1.097 15.000 0.532 24 0.00 16.00 11.59 120 T,2E 11.191 2.17 48.16 16.35 26.190 13.93 06/19/12 "THE" Sorinkler Proaram 2001 File: CALIBER CARLSBADI .the Page 3 of 3 Node Node Flow K-factor Elevation Pressure Diameter Length Fric Loss Node Node Flow K-factor Elevation Pressure HWC Fittings Eqv Length Elev Loss Pipe Flow Velocity Ttl Length Ttl FL 16 0.00 11.00 26.04 1.049 0.500 0.448 25 39.02 8.00 10.50 23.79 120 T 5.000 -0.22 39.02 14.48 5.500 2.46 17 0.00 11.00 25.26 1.049 0.500 0.457 26 39.46 8.00 10.50 24.33 120 E 2.000 -0.22 39.46 14.65 2.500 1.14 18 0.00 11.00 25.60 1.049 0.500 0.441 27 38.69 8.00 10.50 23.39 120 T 5.000 -0.22 38.69 14.36 5.500 2.43 19 0.00 11.00 21.67 1.049 0.500 0.445 28 38.85 8.00 4.00 23.59 120 E 2.000 -3.03 38.85 14.42 2.500 1.11 20 0.00 11.00 25.64 1.049 0.500 0.442 29 38.72 8.00 10.50 23.43 120 T 5.000 -0.22 38.72 14.37 5.500 2.43 21 0.00 11.00 24.88 1.049 0.500 0.451 30 39.16 8.00 10.50 23.96 120 E 2.000 -0.22 39.16 14.54 2.500 1.13 22 0.00 11.00 25.21 1.049 0.500 0.435 31 38.39 8.00 10.50 23.04 120 T 5.000 -0.22 38.39 14.25 5.500 2.39 23 0.00 11.00 21.33 1.049 0.500 0.439 32 38.58 8.00 4.00 23.26 120 E 2.000 -3.03 38.58 14.32 2.500 1.10 24 0.00 16.00 11.59 1.049 1.500 0.199 33 25.17 8.00 16.00 9.90 120 T,E 7.000 0.00 25.17 9.34 8.500 1.69 24 0.00 16.00 11.59 1.049 5.500 0.168 34 22.99 8.00 20.00 8.26 120 2E 4.000 1.73 22.99 8.53 9.500 1.60 Units Legend Flow = gpm Velocity = ft/sec Fnc Loss = psi/ft Elevation = feet Length, Elev Loss, Pressure = psi Eqv Length, Ttl FL = psi Diameter = inches TO Length = feet 06/19/12 "THE" Sorinkler Proaram 2001 File: CALIBER CARLSBADI .the Page 1 of 3 Nozzle Flow Pipe Fittings Pipe Friction Type & in Size & Eqiv. Loss Req. Reference Location gpm inches Devices Length psi/ft psi Notes I q 0.00 6.340 Igth 12.000 Pt 61.48 to Q 359.04 100 T fig 26.572 0.006 Pf 0.23 0 Source tot 38.570 Pe 0.00 2 q 0.00 6.340 Igth 7.000 Pt 58.33 to Q 359.04 100 E ftg 12.400 0.006 Pf 0.12 1 tot 19.400 Pe 3.03 3 q 0.00 6.340 Igth 6.000 Pt 55.19 FDPLD = to Q 359.04 100 E,2GV ftg 17.715 0.006 Pf 3.14 3.00 2 FDPLD tot 23.710 Pe 0.00 4 q 0.00 6.340 Igth 7.000 Pt 58.11 to Q 359.04 100 E ftg 12.400 0.006 Pf 0.12 3 tot 19.400 Pe -3.03 5 q 0.00 6.340 Igth 138.000 Pt 57.14 to Q 359.04 100 2E fig 24.801 0.006 Pf 0.97 4 tot 162.800 Pe 0.00 6 q 0.00 6.340 Igth 4.000 Pt 55.31 to Q 359.04 100 E fig 12.400 0.006 Pf 0.10 5 tot 16.400 Pe 1.73 7 q 0.00 4.260 Igth 16.000 Pt 47.90 to Q 359.04 120 fig 0.000 0.030 Pf 0.47 6 tot 16.000 Pe 6.93 8 q 0.00 3.260 Igth 118.000 Pt 32.00 to Q 359.04 120 3E fig 28.223 0.109 Pf 15.90 7 tot 146.220 Pe 0.00 9 q 0.00 4.260 Igth 6.000 Pt 31.05 to Q 359.04 120 T ftg 26.334 0.030 Pf 0.96 8 tot 32.330 Pe 0.00 10 q 0.00 4.260 Igth 13.000 Pt 35.48 to Q 359.04 120 E fig 13.167 0.030 Pf 0.77 9 tot 26.170 Pe -5.20 11 q 0.00 4.260 Igth 2.000 Pt 34.56 to Q 359.04 120 E,BV fig 28.968 0.030 Pf 0.91 10 tot 30.970 Pe 0.00 12 q 0.00 3.260 Igth 7.000 Pt 29.74 to Q 359.04 120 E fig 9.408 0.109 Pf 1.78 11 tot 16.410 Pe 3.03 06/19/12 "THE" Sorinkler Proaram 2001 File: CALIBER CARLSBAD1 .the Page 2 of 3 Reference Nozzle Type & Location Flow in gpm Pipe Fittings Size & inches Devices Pipe Eqiv. Length Friction Loss psi/ft Req. psi Notes 13 q 0.00 3.260 Igth 6.000 Pt 28.07 to Q 359.04 120 E ftg 9.408 0.109 Pf 1.68 12 tot 15.410 Pe 0.00 14 q 0.00 3.260 Igth 10.000 Pt 27.69 to Q 203.02 120 ftg 0.000 0.038 Pf 0.38 13 tot 10.000 Pe 0.00 15 q 0.00 3.260 Igth 2.000 Pt 27.64 to Q 154.86 120 ftg 0.000 0.023 Pf 0.05 14 tot 2.000 Pe 0.00 16 q 0.00 1.682 Igth 2.500 Pt 26.04 to Q 78.48 120 T ftg 9.900 0.164 Pf 2.03 13 tot 12.400 Pe 0.00 17 q 0.00 1.442 Igth 8.000 Pt 25.26 to Q 39.46 120 ftg 0.000 0.097 Pf 0.78 16 tot 8.000 Pe 0.00 18 q 0.00 1.682 Igth 5.500 Pt 25.60 to Q 77.54 120 T ftg 9.900 0.160 Pf 2.47 13 tot 15.400 Pe 0.00 19 q 0.00 1.097 Igth 11.000 Pt 21.67 to Q 38.85 120 ftg 0.000 0.358 Pf 3.93 18 tot 11.000 Pe 0.00 20 q 0.00 1.682 Igth 2.500 Pt 25.64 to Q 77.88 120 T ftg 9.900 0.161 Pf 2.00 15 tot 12.400 Pe 0.00 21 q 0.00 1.442 Igth 8.000 Pt 24.88 to Q 39.16 120 ftg 0.000 0.096 Pf 0.77 20 tot 8.000 Pe 0.00 22 q 0.00 1.682 Igth 5.500 Pt 25.21 to Q 76.98 120 T ftg 9.900 0.158 Pf 2.43 15 tot 15.400 Pe 0.00 23 q 0.00 1.097 Igth 11.000 Pt 21.33 to Q 38.58 120 ftg 0.000 0.353 Pf 3.88 22 tot 11.000 Pe 0.00 24 q 0.00 1.097 Igth 15.000 Pt 11.59 to Q 48.16 120 T,2E ftg 11.191 0.532 Pf 13.93 14 tot 26.190 Pe 2.17 06/19/12 "THE" Sonnkler Proaram 2001 File: CALIBER CARLSBAD1 .the Page 3 of 3 Nozzle Flow Pipe Fittings Pipe Friction Type & in Size & Eqiv. Loss Req. Reference Location gpm inches Devices Length psi/ft psi Notes 25 8.00 q 39.02 1.049 Igth 0.500 Pt 23.79 to Q 39.02 120 T ftg 5.000 0.448 Pf 2.46 16 tot 5.500 Pe -0.22 26 8.00 q 39.46 1.049 Igth 0.500 Pt 24.33 to Q 39.46 120 E ftg 2.000 0.457 Pf 1.14 17 tot 2.500 Pe -0.22 27 8.00 q 38.69 1.049 Igth 0.500 Pt 23.39 to Q 38.69 120 T ftg 5.000 0.441 Pt 2.43 18 tot 5.500 Pe -0.22 28 8.00 q 38.85 1.049 Igth 0.500 Pt 23.59 to Q 38.85 120 E ftg 2.000 0.445 Pt 1.11 19 tot 2.500 Pe -3.03 29 8.00 q 38.72 1.049 Igth 0.500 Pt 23.43 to Q 38.72 120 1 ftg 5.000 0.442 Pt 2.43 20 tot 5.500 Pe -0.22 30 8.00 q 39.16 1.049 Igth 0.500 Pt 23.96 to Q 39.16 120 E ftg 2.000 0.451 Pf 1.13 21 tot 2.500 Pe -0.22 31 8.00 q 38.39 1.049 Igth 0.500 Pt 23.04 to Q 38.39 120 T ftg 5.000 0.435 Pf 2.39 22 tot 5.500 Pe -0.22 32 8.00 q 38.58 1.049 Igth 0.500 Pt 23.26 to Q 38.58 120 E ftg 2.000 0.439 Pf 1.10 23 tot 2.500 Pe -3.03 33 8.00 q 25.17 1.049 Igth 1.500 Pt 9.90 to Q 25.17 120 T,E ftg 7.000 0.199 Pf 1.69 24 tot 8.500 Pe 0.00 34 8.00 q 22.99 1.049 Igth 5.500 Pt 8.26 to Q 22.99 120 2E ftg 4.000 0.168 Pf 1.60 24 tot 9.500 Pe 1.7.3 Qt 859.04 Pt 61.71 06/19/12 "THE" Sorinkler Proaram 2001 Water Supply vs. Sprinkler Demand 100 90 80 70 1040 @ 70 35962 w/500HSA 60 50 40 30 20 10 0 0 200 300 400 500 600 700 800 900 1000 Flow (gpm) File: CALIBER CARLSBAD1 .the Page 1 of I Hydraulic Summary WATER SUPPLY INFORMATION: Static (psi): 85.00 Residual (psi): 70.00 @ (gpm): 1,040.00 Hose (gpm): 500.00 System req. (gpm): 859.04 @ (psi): 61.71 Supply available: 74.47 psi Safety margin: 12.76 psi Maximum velocity in the system is: Continuity at all nodes satisfied to: Pipe Type Legend Dl = Ductile Iron Class 51 10 = Schedule 10 40 = Schedule 40 NOTES: 16.35 ft/sec in the pipe between Nodes: 14 and 24 0.01 gpm Fitting Type Legend T = Tee (flow turned 90 degrees E = 90 degree standard elbow GV = Gate valve BV = Butterfly valve 06/19/12 "THE" Sonnkler Prooram 2001 Carlsbad Municipal Water District Potable Water Discharge Event Report Date: - 30 - 2-012-. - Location: _QO A\ILM 1\fQNThS __ Reason for Discharge Event: Type of Event. . initial Dewatering Water Mains _iLk Estimated Discharge Flow: tQ12 GPM Note: Includes flow testing and flushing 06 Dewatering Water Mains N Start Time _I Unscheduled Water Discharge N (k End Time Clear flow path of debris, surface contaminants and/or hazardous materials. Do not remove native vegetation. Pre-Dechlorination Residual: Post-Dechlorination Residual: (Less than 0,1 mg/L) PH within limits of 6.0 and 9.0 j Erosion control, i.e. sandbags, silt fencing, hay bales, gravel bags, decreasing the velocity of discharged water. A— Upon completion of dewatering, ensure that the flow path is free of all temporary erosion prevention materials. N/A Upon completion of dewatering, ensure that any sediments or silted areas are cleared. Water Sampling Performed by: Comments: Submitted by: Reviewed by: (Name & Date) (Name & Date) Flow Test Record Test Hydrant Location Hydrant ID No. Size Main Static ............. SS Residual........... Pressure Drop.. _________(PDI 1).....K factor for PDI 1 Flow Hydrant(s) Hydrant I location Hydrant 2 location Hydrant 3 location Hydrant 1 Pitot PSI GPM: Size of Orifice__________ Hydrant 2 Pitot PSI GPM: Size of Orifice__________ Hydrant 3 Pitot PSI GPM: Size of Orifice.__________ Total:_______ (Qi) Calculated test and flow data - 0 x PD2 k =Q2 PDI*k StaticS.................... Desired Residual.......20 Pressure Drop (PD 2).. K factor PD 2: ______ x divided by equals GPM at 20 psi residual Q PD2k PD1k Q2 Comments: Test conducted for: Conducted by: Date: Time: OCT 19 2012 CARLSBAD Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the contractors representative and witnessed by the property owner or their authorIzed sgent. All defects shell be corrected and system left In service before contractors personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It Is understood the owners representatIve's signature In no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. Property '° CôXc . joate. iO'Iq-iZ. Property address 19050 Rv€i 4AS Accepted by approving authorities (names) Address f (i36• Plans. Installation conforms to accepted plans 'yes QNo Equipment used Is approved No ,Yss Has person in charge of fire equipment been instructed as Yes ONO to location of control valves and care and maintenance of this new equipment? If no, explain Instructions -. Have copies of the following been left on the premises? Yes CJ No 1, System components instructions . . Yes ( No Care and maintenance Instructions Yee EkNo . NFPA 25 Yes (JNo Location of . Supplies buildingssystem Year of 1 Orifice - Temperature . . .. ------- _..Model,_—L.._.__maflUfaCtUt&. .......f. ._.aiz_......ouantity... rating Sprinklers Pipeand fittings Typeofpipe.S(..4 Sol Type of Alarm Valve Or Indicator . Alarm device Maxirmnii time to operate through test connection Type Make Model Secondsflow _Minutes - - P4 Dry pipe operating test Dry valve . 0. Q. D. Make Model Serial no. - Make Model j Serial no. Time to trip through teat connecfloria,b . Water pressure Air pressure Ttip point air pressure Time water reached lest o.nleta,b Alarm operated property . Minuteaf .. Secondaf pSi psi - psi Minutes Seconds Yes No It no explain 02006 National Fire Protection Association 5Measured from time Inspectors test connection is opened b NFPA 13 only requires the 60-second limitation in specific sections NFPA 13(p. I of 3) S I f S 9