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Home My WebLink About2100 PALOMAR AIRPORT RD; 214; AS110172; Permit12/28/2020 AS110172 Permit Data City of Carlsbad Sprinkler Permit 2100 PALOMAR Job Address: AIRPORT RD Permit Type: SPRINK Parcel No: 2130201800 Lot #: 0 Reference No.: PC #: Permit No: AS110172 Status: APPROVED Applied 11/21/2011 Approved: 12/22/2011 Issued: 12/22/2011 Inspector: Project Title: SWAIN COLLINS AVIATION PROP. T.I. STE 214 Applicant: PACIFIC FIRE SYSTEMS, INC. 13142 NELSON LANE POWAY, CA 858-722-9865 Owner: COUNTY OF SAN DIEGO PUBLIC AGENCY Fees ($) Add'l Fees ($) Total ($) Balance ($) 262 0 262 0 1/1 Contractor's Material and Test Certificate for Aboveground Piping FILE COPY PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's 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 owner's 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 NAME SL-Al 1¼) C_O(v ) I DATE IZ_k-7/1i PROPERTY ADDRESS 2100 4po.-r tQA ACCEPTED BY APPROVING AUTHORITIES (NAMES) D I2 RESS PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS 0 YES El NO EQUIPMENT USED IS APPROVED YES 0 NO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 0 YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN U NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES Z YES SYSTEM COMPONENTS INSTRUCTIONS 9 YES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA 25 0 YES El NO El NO U NO 0 NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING ________________ f -F3 I vz, - 1 / S-S- 01( PIPE AND FITTINGS TYPE OF PIPE TYPE OF FITTINGS ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE I MODEL MIN SEC FLOW INDICATOR i\J MAKE MODEL I SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING TEST TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE POINT AIR PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY MIN WITH SEC PSI PSI PSI MIN I SEC YES I NO NJ/ O.O.D. W/O Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO ' fr MAKE I MODELI DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE I\J YES NO YES NO MIN SEC REDUCING WL,M I IJIN & FLOOR IvitiNt a, Ot 1 I ii' MODEL I A I It, t-'htbbIJht MIUU/kL VSUI-th LUW HA I It (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) PILE COPY \ ( ô (1 FILE COPY HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED 0-YES El NO EQUIPMENT OPERATES PROPERLY El YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? El YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 El YES []NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING El YES flNO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING El YES IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR3? El YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? El YES El NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? El YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? 'YES El NO HYDRAULIC DATA NAMEPLATE PROVIDED IF NO, EXPLAIN El YES NO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAME OF SPRINKER CONTRACTOR: SIGNATURES TESTS WITNESSED BY FR f1QERTY OWNER (SIGNED) TITLE DATE i1J V \ t/\ Lc- L F'bR TITLE DATE ADDITIONAL EXPLANATIONS AND NOTES: M ASIIOI-~~- Tfl •-r" 42 (I 4 JL Pacific Fire Systems 13142 Nelson Lane Poway, ca 92064 858-722-9865 Job Name : Swain Collins Building Location : 2100 Palomar Airport Road, Suite 214 System : Existing Contract Data File : proofcalc.WXF Pacific Fire Systems Page 1 Swain Collins Date 12/21/11 Hydraulic Design Information Sheet Name - Swain Collins Date - 12/21/11 Location - 2100 Palomar Airport Road, Suite 214 Building - System No. - Existing Contractor - Pacific Fire Systems, Inc. Contract No. - Calculated By - Pacific Fire Systems, Inc. Drawing No. - Construction: ( ) Combustible (x) Non-Combustible Ceiling Height - 91 -0" Occupancy - Light Hazard - Office S (x) NFPA 13 (x) Lt. Haz Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve S Other Area reduced for ceiling heights of 9 1 -0" T Specific Ruling Made By Date E M Area of Sprinkler Operation - 900 System Type Sprinkler/Nozzle Density - .1 (x) Wet Make Tyco D Area Per Sprinkler - 18'x18' ( ) Dry Model EC-8/ssp-qr E Elevation at Highest Outlet - 201 9" ( ) Deluge Size 3/4TT/1/2! S Hose Allowance - Inside - ( ) Preaction K-Factor 8.0/5.6 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.135/155 G Hose Allowance - Outside - 150 N Note PROOF CALC TO BASE OF RISER Calculation Flow Required - 407.877 Press Required - 29.787 Summary C-Factor Used: 120 Overhead Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - @ Press - R Residual Press - Elev. - Well Flow - Proof Flow S Elevation - U P Location - P L Source of Information Y C Commodity Class Location O Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M Single Row ) Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mult. Row ( ) Open Shelf O C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G E Horizontal Barriers Provided: VVdLI OUFJFJIY L,UIVt IL#) Pacific Fire Systems Page 2 Swain Collins Date 12/21/11 Demand: Dl - Elevation : -0.433 D2 - System Flow : 257.877 stem Pressure : 29.787 D2 - SrDemand Hose Adj City) ________ Hose ) : 150 D3 - System Demand : 407.877 Safety Margin 02 ____ ______ _______ 30 - 28 26 i11____ p24 R22 E2° S 18 S 16 u 14 R 12 E 10 50D1100 150 200 250 300 350 400 450 FLOW( N"1.85) Comouter Proarams by Hvdratec Inc. Route 111 Windham NH. USA 03087 riuii iy utu OUItlllIdI Pacific Fire Systems Page 3 Swain Collins Date 12/21/11 Fitting Legend Abbrev. Name 1/2 % 1 1½ 11/2 2 21/2 3 31/2 4 5 6 8 10 12 14 16 18 20 24 B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0 E 90StandardElbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 Fsp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow T 90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Units Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Comouter Proarams by Hvdratec Inc. Route 111 Windham N.H. USA 03087 Pressure / Flow Summary - STANDARD Pacific Fire Systems Page 4 Swain Collins Date 12/21/11 Node No. Elevation K-Fact Pt Actual Pn Flow Actual Density Area Press Req. Hi 20.75 5.6 65.61 na 45.36 0.1 30 7.0 H2 H3 20.75 20.75 5.6 8 66.38 36.9 na na 45.63 48.59 0.1 1.0 204 1 1-7 H4 20.75 8 40.08 na 50.65 1.0 1 1-7 H5 20.75 5.6 38.31 na 34.66 0.1 166 7.0 H6 20.75 8 17.0 na 32.98 1.0 1 17.0 1 21.75 78.21 na 2 21.75 72.13 na 3 21.75 49.34 na 4 21.75 48.88 na 5 21.75 42.25 na 10 21.75 29.64 na 6 21.75 19.81 na 12 21.75 20.9 na ii 21.0 21.69 na 13 21.0 21.57 na 15 21.0 20.91 na 16 21.0 19.83 na TOR 0.0 28.85 na BOR 0.0 29.79 na 150.0 The maximum velocity is 4959 and it occurs in the pipe between nodes 1 and 2 Final Calculations - Hazen-Williams Pacific Fire Systems Page 5 Swain Collins Date 12/21/11 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn Hi 45.36 1.08 2E 4.61 15.000 65.613 K Factor = 5.60 to 120 iT 5.762 10.372 -0.433 1 45.36 0.5138 0.0 25.372 13.035 Vel= 15.89 0.0 45.36 78.215 K Factor = 5.13 H2 45.63 1.08 1 E 2.305 3.830 66.381 K Factor = 5.60 to 120 1 5.762 8.067 -0.433 2 45.63 0.5193 0.0 11.897 6.178 Vel= 15.98 0.0 45.63 72.126 K Factor = 5.37 H3 48.59 1.08 1E 2.305 14.000 36.896 K Factor = 8.00 to 120 iT 5.762 8.067 -0.433 3 48.59 0.5835 0.0 22.067 12.877 Vel= 17.02 0.0 48.59 49.340 KFactor= 6.92 H4 50.65 1.08 1 E 2.305 6.580 40.085 K Factor = 8.00 to 120 iT 5.762 8.067 -0.433 4 50.65 0.6300 0.0 14.647 9.227 Vet = 17.74 0.0 50.65 48.879 K Factor = 7.24 H5 34.66 1.08 1 2.305 5.920 38.310 K Factor =5.60 to 120 1 5.762 8.067 -0.433 5 34.66 0.3124 0.0 13.987 4.369 Vel= 12.14 0.0 34.66 42.246 KFactor= 5.33 H6 32.98 1.08 1 E 2.305 3.330 17.000 K Factor = 8.00 to 120 iT 5.762 8.067 -0.433 6 32.98 0.2849 0.0 11.397 3.247 Vel= 11.55 0.0 32.98 19.814 K Factor = 7.41 1 -362.52 1.728 0.0 2.500 78.215 to 120 0.0 0.0 0.0 2 -362.52 -2.4356 0.0 2.500 -6.089 Vel = 49.59 2 45.63 1.728 0.0 12.000 72.126 to 120 0.0 0.0 0.0 3 -316.89 -1.8988 0.0 12.000 -22.786 Vel = 43.35 3 48.59 1.728 0.0 0.330 49.340 to 120 0.0 0.0 0.0 4 -268.3 -1.3970 0.0 0.330 -0.461 Vel = 36.70 4 50.65 1.728 0.0 7.000 48.879 to 120 0.0 0.0 0.0 5 -217.65 -0.9476 0.0 7.000 -6.633 Vet = 29.78 Final Calculations - Standard Pacific Fire Systems Page 6 Swain Collins Date 12/21/11 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 5 34.67 1.728 0.0 18.330 42.246 to 120 0.0 0.0 0.0 10 -182.98 -0.6875 0.0 18.330 -12.602 Vel = 25.03 10 0.0 1.728 iT 11.29 0.750 29.644 to 120 0.0 11.290 0.325 11 -182.98 -0.6875 0.0 12.040 -8.278 Vel= 25.03 0.0 -182.98 21.691 K Factor = -39.29 6 32.98 1.728 0.0 37.500 19.814 to 120 0.0 0.0 0.0 12 32.98 0.0289 0.0 37.500 1.084 Vel = 4.51 12 0.0 1.728 iT 11.29 0.750 20.898 to 120 0.0 11.290 0.325 13 32.98 0.0288 0.0 12.040 0.347 Vel = 4.51 0.0 32.98 21.570 K Factor = 7.10 Ii -182.98 4.31 0.0 15.000 21.691 to 120 0.0 0.0 0.0 13 -182.98 -0.0081 0.0 15.000 -0.121 Vel = 4.02 13 32.98 4.31 2E 27.874 90.500 21.570 to 120 0.0 27.874 0.0 15 -150.0 -0.0056 0.0 118.374 -0.657 Vel = 3.30 15 0.0 4.31 2E 27.874 168.000 20.913 to 120 0.0 27.874 0.0 16 -150.0 -0.0056 0.0 195.874 -1.088 Vel = 3.30 16 0.0 6.357 3E 52.808 29.000 19.825 to 120 0.0 52.808 9.095 TOR -150.0 -0.0008 0.0 81.808 -0.068 Vel = 1.52 TOR 0.0 6.357 1 12.573 10.000 28.852 to 120 iFsp 0.0 67.896 1.000 * Fixed loss = 1 BOR -150.0 -0.0008 1E 17.603 77.896 -0.065 Vel = 1.52 1 37.72 150.00 Qa= 150.00 0.0 29.787 K Factor =0