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3129 TIGER RUN CT; BLDG A; AS070209; Permit
11/10/2020 AS070209 Permit Data City of Carlsbad, Sprinkler Permit Job Address: 3129 TIGER RUN CT Permit Type: SPRINK .Parcel No: 2210140100 Lot #: 0 Reference No.: Permit No: AS070209 Status: ISSUED. Applied 8/1/2007 Approved: 8/1/2007 Issued: 8/1/2007 PC #: . . Inspector: Project Title: PALOMAR FORUM BLDG. A THREE FIRE SPRINKLER INSPECTIONS @ $62/EA Applicant: . Owner: PRO-TECH FIRE PROTECTION SYSTEMS PALOMAR MELROSE L L C CORP . . . C/O ARNEL DEVELOPMENT. SUITE G . 949 S COAST DR #600 179 ROYMAR RD. COSTA MESA CA OCEANSIDE, CA 760-722-2455 Fees ($) Add'I Fees ($) Total ($) Balance ($) 186 0 186 . .0 1/1 A&1—o 2ôc Contractor's Material and Test Certificate for Aboveground piping. PROCEDURE Upon completion of work Inspection and tests shall be made by the contracto?s representative and witnessed by an owner's representative. All defects-shall beLcorrected'and'systemleftln'servicé 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 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 NAME: Palomar Forum Building 'A 1DATE: L..crr—i PROPERTY ADDRESS: t3129TijuflCLCaflsb'idiCAf PLANS ACCEPTED. BY APPROVING AUTHORITIES (NAMES): Carlsbad Fire Dept. ADDRESS: 1635 Faraday Ave., Carlsbad, CA INSTALLATION CONFORMS TO ACCEPTED PLANS LJ YES U 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 OF CONTROL VALVES AND CARE AND. MAINTENANCE OF THIS NEW EQUIPMENT? YES 0 NO IF NO, EXPLAIN . HAVE COPIES OF THE FOLLOWING BEEN'LEFT ON THE PREMISES: 1J YES . NO SYSTEM COMPONENTS INSTRUCTIONS . . YES NO CARE AND MAINTENANCE INSTRUCTIONS . 21 y ' El NO NFPA25 . . . . YES NO LOCATION OF SYSTEM SUPPLIES BUILDINGS: . . SPRINKLERS MAKE MODEL YEAR OF MANUFACTURI ORIFICE SIZE QUANTITY TEMPERATURE RATING Tyco TY-FRL 322' 2007 . 1/2 . 48 212 Tyco fY-FRL 3221 2007. 1/2 161 165 Tyco TY-PRL 3221 2007 1/2 2 165 Tyco TY-FRL3121 2007 112 .9 212 PIPE AND FITTINGS Type of Pipe: Sch 40,Sch10,Dyna.Flow Dyna-Thread Type of Fitting: Grooved,Ci/DI Threaded__. ALARM VALVE OR FLOW INDICATOR ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION TYPE MODEL MIN SEC Flow Switch _MAKE . Electric. VSF.R _Potter • DRY PIPE OPERATING TEST ''._,. DRY VALVE . . Q.O.D, MAR MODEL SERIAL NO. .MAKE MODEL SEjIArNO. TIME TO TRIP" THROUGH TEST ' CONNECTION , "W&SER . PRE AIR PRESSURE 'TRIP POINT AIR PRESS TIMJ..TER -'EACHED. TEST OUTLET' ALARM OPERATED PROPERLY MIN I SEC PSI PSI ,-Pl MIN SEC YES NO Without , O.O.D. With Q.O.D. IF NO, EXPLAIN 0 PNEUMATIC DELECTPIC 0 HYDRAULIC PIPING SUPERVISED -.Lxs U NO I DETECTING MEDIA SUPER VIED-1J YES Lj NO DOES VALVE OPERATE FROM THE PItIALtP AND/OR REMOTE CONTROL SIGNS fl YES fl NO - DELUGE AND PREACTION IS THERE AN ACCESSIBLE FACILITY IN EACH.CIR TESTING IF NO, EXPLAIN VALVES DYES I)OEgAH-C1RCUIT OPERATE DOES. EACH ( RCUI MAXIMUM TIME TO MAKE MODEL ,3URVISION LOSS ALARM? OPERATE VALVE RELEASE? TE RELEASE YES NO YES NO N. SEC. PRESSURE REDUCING VALVE TEST LOXTIN •MAKE.&..._ SETTING STATIC PRESSURE RESIDUAL FrESS E & FLOOR MODEL __________ _____________________ ING) OUT "I OUTLET (PSI) FLOW (GPM TEST DESCRIPTION IYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psI (13.8 bars) for two hours or 50 pal (3.4 bars) above static 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 damage. All abovegroung piping leakage shall be stopped. PNEUMATIC: EstaIIsh 40 p51(2.7 bars) air pressure and measure drop which shall not exceed 1-1/2 psi (.01 bars) In 24 hours. Teat pressure tanks at normal water level 'and air pressure and measure air pressure drop which snail not exceed 1-1/2 psi (0.1-bars) In 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR ...._ HRS DRY PIPING PNEUMATICALLY TESTED DYES El NO EQUIPMENT OPERATES PROPERLY El YES 0 NO IF NO, STATE REASON N/A DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR TEST DERIVATIVES OF SODIUM SILICATE, BRINE, OR-OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? El YES 0 NO DRAIN • READING OF GAGE LOCATED NEAR WATER. RESIDUAL PRESSURE WITH VALVE IN TEST • TEST SUPPLY TEST CONNECTION: PSI CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD IN CONECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MAKE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 85B El YES 0 NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDER- GROUND SPRINKLER PIPING El YES 0 NO F POWDER-DRIVEN FASTENERS ARE USED IN CONCRETE, HAS REP- RESENTATIVE SAMPLE TESTING BEEN SATISFACTORILY COMPLETED? El YES 0 NO IF NO, EXPLAIN BLANK TESTING GASKETS NUMBER USED [LOCATIONS 0 NUMBER REMOVED WELDED PIPING EJ YES U NO IF YES DO YOU CERTIFY-AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY • WITH THE REQUIREMENTS OF AT LEAST AWS 010.9, LEVEL AR-3? El YES ONO WELDING DO YOU CERITIFY THAT THE WELDING WAS PREFORMED BY WELDERS QUALIFIED IN COMPLIANCE WITH THE REQUIREMENTS OF AT LEAST AWS D11 0.9, LEVEL AR-3? El YES 0 NO DO YOU CERITIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH.A DOCUMENTED QUALITY CONTROL PROCEDURE TO ENSURE 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 0 NO CUTOUTS DO YOU CERITIFY THE YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL (DISCS) CUTOUTS (DISCS)ARE RETRIEVED? El YES 0 NO HYDRAULIC DATA • NAMEPLATE NAME PLATE PROVIDED JIF El 0 NO NO, EXPLAIN DATE LE IN SERVICE WITH ALL CONTROL.VALVES OPEN: REMARKS NAME UI SIKINN..EN (.0N1NA1.iON j • PRO-TECH FIRE PROTECTION SYSTEM CORP. I TESTS WITNESSED BY SIGNATURES :c PROPERTY O)NEITGNED) TITLE DATE i 11 /6/2o7 1 M4 I4e4z4/ -'r r i ADDITIONAL EXPLANATION A 0 NOTES MOE PRO-TECH-FIRE PROTECTION— 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 HYDRAULIC CALCULATIONS BUILDING A REMOTE ARE C. FOR GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I BUILDING A CARLSBAD CA DATE: JULY 9, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: 0.1 gpm/1500 sq. ft. AREA OF APPLICATION: 1701 sq. ft. COVERAGE PER SPRINKLER: 225 SQ. FT. NUMBER OF SPRINKLERS CALCULATED: 18 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 425.3 gpm TOTAL WATER REQUIRED +(OUTSIDE hose): 525.5 gpm FLOW AND PRESSURE (@ BOR): 425.3 gpm @ 29.3 psi - - SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: PRO-TECH FIRE PROTECTION DESIGN/LAYOUT BY:PRO-TECH FIRE PROTECTION AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C16 HIC APPROVE D4 MITTED CARLSBAD FIRE SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\:SUBD JOB TITLE: BUILDING A .1 CALC WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 125.0 20.0 5390.0 121.0 925.3 35.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 925.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 425.3 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT-2) (GPM/FT-2) Si 22.0 - - - - 18.1 --- S2 22.0 - - - - 18.2 --- S3 22.0 - - - - 18.3 --- S4 22.0 - - - - 18.3 --- S5 22.0 - - - - 18.4 --- S6 22.0 - - - - 18.5 --- S7 22.0 - - - - 18.6 --- S8 22.0 - - - - 18.6 --- S9, 22.0 - - - - 18.7 --- SI0 22.0 - - - - 18.1 - - - Sli 22.0 - - - - 18.2 --- S12 22.0 18.2 --- S13 22.0 - - - - 18.3 --- -. S14 22.0 - - - - 18.4 --- S15 22.0 - - - - 18.5 --- S16 22.0 - - - - 18.5 --- S17 22.0 - --- 18.6 --- S18 22.0 - - - - 18.7 --- S19 22.0 - - - - 17.6 --- S20 22.0 - - - - 17.6 --- S21 22.0 - - - - 17.6 --- S22 22.0 - - - - 17.6 523 22.0 - - - - 17.6 --- S24 22.0 - - - - 20.0 --- S25 22.0 - - - - 20.0 --- S26 22.0 - - - - 20.0 --- S27 22.0 - - - - 20.0 --- S28 22.0 - - - - 18.1 S29 22.0 - - - - 18.2 ---- S30 22.0 - - - - 18.3 S31 22.0 - - - - 18.4. S32 22.0 - - - - 18.6 S33 22.0 - - - - i7.9 --- S34 22.0 - - - - 18.0 --- S35 22.0 - - - - 18.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .1 CALC NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT-2) (GPM/FT-2) S36 22.0 - - - - 18.3 --- S37 22.0 - - - - 18.4 --- 38 22.0 - - - - 18.5 --- S39 22.0 - - - - 17.7 - - - - S51. 10.0 K= 5.60o 17.9 23.7 225.0 0.100 0.105 S52 10.0 K= 5.600 17.8 23.6 225.0 0.100 0.105 S53 10.0 K= 5.600 17.7 23.6 225.0 0.100 0.105 S54 10.0 K= 5.600 17.7 23.6 225.0 0.100 0.105 S55 10.0 K= 5.600 17.8 23.6 225.0 0.100 0.105 S56 10.0 K= 5.60o 17.9 23.7 225.0 0.100 0.105 S57 9.0 K= 5.60. 16.3 22.6 225.0 0.100 0.100 S58 9.0 K= 5.60c 17.2 23.2 225.0 0.100 0.103 S59 9.0 K= 5.60. 16.1 22.5 225.0 0.100 0.100 S60 9.0 K= 5.60o 16.1 22.5 225.0 0.100 0.100 S61 9.0 K= 5.60. 17.2 23.2 2.25.0 0.100 0.103 S62 9.0 K= 5.609 16.2 22.6 225.0 0.100 0.100 S63 9.0 K= 5.60, 19.1 24.5 225.0 0.100 0.109 S64 9.0 K= 5.600 19.1 24.5 225.0 0.100 0.109 S65 9.0 K= 5.600 18.5 24.1 225.0 0.100 0.107 S66 9.0 K= 5.60. 19.4 24.7 225.0 0.100 0.110 S67 9.0 K= 5.606 19.4 24.7 225.0 0.100 0.110 S68 9.0 K= 5.600 19.1 24.5 225.0 0.100 0.109 25.4 10 71 20.0 10.0 - - - --- 72 10.0 -F1'- 17.8 - - - 73 10.0 - - - - 17.7 74 10.0 17.7 --- 75 10.0 - - - - 17.8 -- 76 10.0 - - - - 17.8 --- 77 10.0 - - - - 21.1 --- 78 10.0 - - - - 21.1 - - - - 79 10.0 - - - - 20.2 --- 80 10.0 - - - - 20.2 --- 81 10.0 - - - - 20.2 --- 82 10.0 - - - - 20.2 - - - Ml 10.0 - - - - 24.7 --- M2 10.0 - - - - 24.5 --- M3 10.0 - - - - .24.2 --- M4 10.0 - - - - 24.1 --- M5 10.0 - - - - 24.1 - - - Mit 10.0 - - - - 20.3 --- M12 10.0 - - - - 20.4 --- M13 10.0 - - - - 21.1 --- M14 10.0 - - - - 21.1 --- M14A 10.0 - - - - 21.2 --- M21 10.0 - - - - 24.8 --- M21A 10.0 - - - - 24.9 --- M22 10.0 - - - - 24.8 --- M23 10.0 - - - - 24.6 --- M31 20.0 - ---' 20.9 --- M32 20.0 - - - - 20.9 --- M33 20.0 - - - - 20.9 --- M34 20.0 - - - - 20.8 --- M35 20.0 - - - - 20.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBL' JOB TITLE: BUILDING.A .1 CALC NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) . (PSI) (GPM) (FT A2) (GPM/FT'2) M36 20.0 - --- 20.8 --- M37 20.0 - - - - 20.8 --- M41 20.0 - - - - 18.6 --- M42 20.0 - - - - 18.5 --- M43 .20.0 - - - - 18.5 --- M44 20.0 - - - - 18.5 --- M45 20.0 - - - - 18.3 --- M46 20.0 - - - - 18.1 --- M47 20.0 - - - - 18.0 --- M47A 20.0 - - - - 18.0 --- M51 20.0 - - - - 20.8 --- M52 20.0 - - - - 20.8 - - - - M53 20.0 - - - - 20.8 --- M54 20.0 - - - - 20.7 --- M54A 20.0 - -. -- 20.7 --- M55 20.0 - - - - 20.7 --- M56 20.0 - - - - 20.7 --- M57 20.0 - - - - 20.7 --- R31 22.0 - - - - 20.0 --- R32 22.0 - - - - 19.9 --- R33 22.0 - - - - 20.0 - - - BOR 1.0 - - - - 29.3 - - - DI -3.0 ---- 31.2 U -3.0 --.-- 37.9 - - - --.- - UG -3.0 - - - - 37.7 --- UG1 -3.0 - - - - 37.1 --- UG2 -3.0 HOSE STREAM 31.5 . 500.0 BF1 3.0 - - - - 34.3 --- BF2 3.0 - - - - 29.3 - - - HYD 1.0 - - - - 36.4 - - - SRC 3.5 SOURCE 35.7 925.3 Pipe: 3 BL 3.0 3.0 YG 4 3.0 2 -3.0 Pipe: 5 U -3.0 -3.0 Pipe: 6 -3.0 BO.k 1.0 f Pipe: 7 BR 1.0 10.0 Pipe: 8 5 10.0 0 20.0 j Pipe: 9 5/ 10.0 11 10.0 jPipe: 10 Ml 10.0 M 10.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 4ATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .1 CALC PIPE DATA PIPE TAG END ELEV. NOZ. NODES (FT) (K) Pipe: 1 3.5 Ao HXtD 1.0 'i Pipe: 1A Hb 1.0 4rG -3.0 Pipe: lB UJ -3.0 FG -3.0 Pipe: 1C U -3.0 YD 1.0 Pipe: 1D , tJG -3.0 G1 -3.0 Pipe: 2 UG -3.0 d BV1 3.0 Q(GPM) DIA(IN) LENGTH PRESS. PT DISC. VEL(FPS) HW(C) (FT) SUM. (PSI) (GPM) FL/FT (PSI) 925.3 7/-8 PL 20.00 PF 0.4 35.7 (N/A) 5.9 FTG TG PE 1.1 36.4 0.0 0.005 TL 74..Q0 __I L. PV 0.2 722.3 7.980 PL 75.00 PF 0.5 36.4 0.0 4.6 150 FTG TL PE 1.7 37.7 0.0 0.00 TL 144.00 PV 0.1 203.0 7 980 PL 795.00 PF 0.3 37.9 0.0 1.3 150 FTG 2L PE 0.0 37.7 0.0 0.000 dommow PV 0.0 -203.0 7.980. PL 575.00 PF 0.2 37.9 0.0 1.3 150 . FTG 2T PE -1.7 36.4 0.0 0.000 TL 675.00 PV 0.0 • 925.3 7.24 PL 30.00 PF 0.5 37.7 0.0 5.9 50 FTG TLG PE 0.0 37.1 0.0 .005' TL.103.00 PV 0.2 925.3 8 390 PL 6.00 PF 0.2 37.1 0.0 5.4 140 FTG E PE -2.6 34.3 0.0 0.005 TL 37.00PV.0.2 S RCE 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 FIXED PRESSURE LOSSDEVlk 0.0 34.3 0 olcon 0 .3 gpm 0.0 29.3 0.0 29.3 0 FTG ET PE 2.6 H .S. 31.5 TL PV 0.2 425.3 PL 228.00 PF 0.3 H.S. 31.5 500.0 2.7 0 FTG L PE 0.0. 0.0 31.2 0.0 0.001 TL 247.00 PV 0.1 390 PL 9.00 PF 0.1 0.0 31.2 )40 FTG 3E PE -1.7 0.0 0.0 0.001 TL 102.00 PV 0.0 doom 425.3 ~03 PL 8.75 PF 0.0. 0.0 29.._ 0.0 0 FTG ---- PE -3.9 0.0 25.4 0.0 0.006 TL 8.75 PV 0.1 244.7 03 PL 12.75 PF 0.1 0.0 25.4 0.0 2.4 JO 120 FTG T PE -4.3 0.0 20.9 0.0 0.002 TL 51.66 PV 0.0 180.6 4 3?0 PL 40..50 PF 0.7 0.0 25.4 0.0 4.0 I10 FTG 2ET PE 0.0 0.0 24.7 0.0 0.008 TL 88.30 PV 0.1 'o dMEMP 188.2 2 7 PL 2.42 PF 0.2 0.0 24.7 0.0 10.5 20 FTG ---- PE 0.0 0.0 24.5 0.0 0.082 TL 2.42 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBD JOB TITLE: BUILDING A .1 CALC 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) 121.9 2 7f PL 8.42 PF 0.3 0.0 24.5 0.0 6.8 120 FTG ---- PE 0.0 0.0 24.2 0.0 0.037 TL 2.PV 0.3 58.1 .1 "PL 8.00 PF 0.1 0.0 24.2 0.0 3.2 120 FTG ---- PE 0.0 0.0 24.1 0.0 0.009 TL IAOQfl PV 0.1 33.1 PL 8.50 PF 0.0 0.0 24.1 0.0 1.8 120 FTG ---- RE 0.0 0.0 24.1 0.0 0.003 TL 8.50 PV. 0.0 -75.5 2.fr3 PL 6.25 PF 0.1 0.0 20.3 0.0 4.2 120 FTG ---- PE 0.0 0.0 20.4 0.0 0.015 TL 6.25 PV 0.1 -148.2 2.7,QØ'"PL 13.92 PF 0.7 0.0 20.4 0.0 8.3 cT20 FTG ---- PE 0.0 0.0 21.1 0.0 0.053 TL 13.92 PV 0.5 -156.5 2.7Q"PL 1.50 PF 0.1 21.1 0.0 8.7 0 FTG ---- PE 0.0 21.2 0.0 0.058 TL 1.50 PV 0.5 50.1 2703 PL 6.33 PF 0.0 0.0 2.8 120 FTG ---- PE 0.0 0.0 0.007 TL 6.33 PV 0.1 -206.6 30.04 PL 10.00 PF 1.1 0.0 7.7 120 FTG T PE -4.3 0.0 0.036 TL 31.80 PV 0.4 38.1 2. 03 PL 3.67 PF 0.1 0.0 2.1 120 FTG T PE 0.0 0.0 0.004 TL eQr22.l PV 0.0 30. Aft 2.7'03 PL 9.25 PF 0.0 0.0 1.7 120' FTG ---- PE 0.0 0.0 0.003. TL. 9.25 PV 0.0 -38.1 2. 03 PL 11.50 PF 0.1 0.0 2.1 120 FTG T PE -4.3 0.0 0.004 TL 30.10 PV 0.0 30.5 2.7/3 PL 18.00 PF 0.2 0.0 1.7 FTG 3ET PE 0.0 0.0 '003 TL 54.60 PV 0.0 43.5 jI,3 PL 1.42 PF 0.0 0.0 0.4 120 FTG T PE 0.0 0.0 0.000 TL 40.33 PV 0.0 201.2 Ao PL 6.58 PF 0.1 0.0 2.0 FTG T PE 0.0. 0.0 .0.001 TL 45.49 PV 0.0 0.0 20.9 0.0 20.9 Pipe: 11 M2 10.0 M-30000' 10.0 'Pipe: 12 10.0 10.0 Pipe: 13 10.0 h5oe 10.0 ,Ppe: 14 10.0 10.0 Pie 15 10.0 10.0 Pipe: 16 ml 10.0 Mj4A 10.0 Pipe: 16A 10.0 10.0 Ml cipe: 16b 10.0 M4A .20.0 Pipe: 160 M2i4 10.0 10.0 Pipe: 17 M2 10.0 9 22 10.0 17A KA 10.0 54A 20.0 .0 .0 .0 IGi u.0 Pipe: 20 10J'20.0 L'2 20.0 Pipe: 18 42jV 10 10 Pipe: 19 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 4 21.2 21.1 21.2 18.0 24.9 24.8 24.8 24.8 24.9 20.7 0.0 24.8 0.0 24.6 0.0 20.9 0.0 20.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 jiATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .1 CALC 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: 21 160.4 6..40fl PL 11.00 PF 0.0 M2 20.0 0.0 20.9 0.0 1.6 c20 FTG ----. PE 0.0 20.0 0.0 20.9 0.0 0.001 TL 11.00 PV 0.0 /Pipe: 22 153.7 4.3 PL 8.50 PF 0.0 M33'/ 20.0 0.0 20.9 0.0 3.4 420 FTG ---- PE 0.0 M3/' 20.0 0.0 20.8 0.0 0.006 TL 8.50 PV 0.1 23 115.2 44PL 3.50 PF 0.0 20.0 0.0 20.8 0.0 2.5 '120 FTG ---- PE 0.0 M05 20.0 0.0 20.8 0.0 0.003 TL 3.50 PV 0.0 eipe: 24 77.2 44 ' PL 12.00 PF 0.0 M3 20.0 -0.0 20.8 0.0 1.7 . e/120 FTG ---- PE 0.0 M5 6 20.0 0.0 20.8 0.0 0.002 TL 12.00 PV 0.0 25 38.9 44'10 PL 12.00 PF 0.0 M3'6 20.0 0.0 20.8 0.0 0.9 V120 FTG ---- PE 0.0 20.0 0.0 20.8 0.0 0.000 TL 12.00 PV . 0.0 Pipe: 26 34.1 3.3t PL 8.00 PF 0.0 M7]. 20.0 0.0 18.6 0.0. 1.3 620 FTG ---- PE 0.0 (j42 20.0 0.0 18.5 0.0 0.001 TL 8.00 PV 0.0 Pipe: 27 67.8 3' PL 11.00 PF 0.1 M 4.27 20.0 0.0 18.5 0.0 2.5 "120 FTG ---- PE 0.0 43 20.0 0.0 18.5 0.0 0.005 TL 11.00 PV 0.0 ipe: 28 - 67.8 33)J1' PL 8.50 PF 0.0 M4 20.0 0.0 18.5 0.0 2.5 (/120 FTG ---- PE 0.0 20.0 0.0 18.5 0.0 0.005 TL 8.50 PV 0.0 P ' e: 29 101.1 34 PL 11.58 PF 0.1 M4 20.0 0.0 18.5 0.0 3.8 2'120 FTG ---- PE 0.0 M5 20.0 0.0 .18.3 0.0 0.010 TL 11.58 PV 0.1 Bipe: 30 135.1 X33 , 14 PL 11.83 PF 0.2 M45 20.0 0.0 18.3 0.0 5.0 0 FTG ---- PE 0.0 M6 20.0 0.0 18.1 0.0 0.016 TL 11.83 PV 0.2 - // 20.0 30A 170.3 PL 6.00 PF 0.2 20.0 0.0 18.1 0.0 6.3 120 FTG ---- PE 0.0 MA' 7AA 20.0 0.0 18.0 0.0 0.025 TL 6.00 PV 0.3 /'ipe: 30B -36.3 3 e~O ff PL 6.00 PF 0.0 M417( 20.0 0.0 18.0 0.0 1.3 . 20 FTG ---- PE 0.0 - 20.0 0.0 18.0 0.0 01 TL 6.00 PV 0.0 'Pipe: 31 9.4 PL 8.00 PF 0.0 M5. 20.0 0.0 20.8 0.0 0.3 0 FTG ---- PE 0.0 If52 20.0 0.0 20.8 0.0 0.000 TL 8.00 PV 0.0 jPipe: 32 16.5 3.3114 PL 13.75 PF 0.0 M57' .20.0 0.0. 20.8 0.0 0.6 //12o FTG 2E PE 0.0 M53 . 20.0 0.0 20.8 0.0 0.000 TL 27.75 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SU3I JOB TITLE: BUILDING A .1 CALC 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: 33 23.3 3.3,14 PL 8.58 PF 0.0 M37 20.0 0.0 20.8 0.0 0.9 %'20 FTG ---- PE 0.0 20.0 0.0 20.7 0.0 'O01 TL 8.58 PV 0.0 Pipe: 33A 38.1 3/3?4 PL 10.33 PF 0.1 M/I 20.0 0.0 20.7 0.0 1.4 7120 FTG T PE O.O g54A 20.0 0.0 20.7 0.0 0.002 TL PV 0.0 ,Pipe: 34 -9.7 3)%14 PL 3.42 PF 0.0 M5 20.0 0.0 20.7 0.0 0.4 óf120 FTG ---- PE 0.0 20.0 0.0 20.7 0.0 0.000 TL 3.42 PV 0.0 Pipe: 35 -5.6 3X14 PL 12.00 PF 0.0 M5/ 20.0 0.0 20.7 0.0 0.2 (/120 FTG ---- PE 0.0 M56 20.0 0.0 20.7 0.0 0.000 TL 12.00 PV 0.0 ? Pipe: 36 -2.6 ,314 PL 12.00 PF 0.0 20.0 0.0 20.7 0.0 0.1 '' 120 FTG ---- PE 0.0 17 20.0 0.0 20.7 0.0 0.000 TL 12.00 PV 0.0 , Pipe: 37 -7.6 2.203 PL 159.50 PF 0.1 M1// 10.0 0.0 24.7 0.0 0.6 c'I'20 FTG 7E2T PE 0.0 M:21 10.0 0.0 24.8 0.0 0.001 TL 215.80 PV 0.0 /Pipe: 38 -15.7 2•2453 PL 193.00 PF 0.5 10.0 0.0 24.1 0.0 1.3 '1'0 FTG 4E27 PE 0.0 10.0 0;0 24.6 0.0 cI.002 TL 2_-3A0 PV 0.0 4Pipe: 39 -14.7 2.2Q3 PL 211.34 PF 0.6 M5/J 10.0 0.0 24.1 0.0 1.2 r].'0 FTG 5E4T PE 0.0 M2/- 10.0 0.0 24.6 0.0 0.002 TL 278.94 PV 0.0 ,,. Pipe: 40 75.5 2.'03 PL 26.00 PF 2.3 Ml" 10.0 0.0 20.3 0.0 6.4 (7120 FTG 4ET PE 0.0 1 10.0 5.6 17.9 23.7 0.041 TL 56.65 PV 0.3 , Pipe: 41 51.7 ,'7203 PL 8.00 PF 0.2 S5X 10.0 5.6 17.9 23.7 4.4 120 FTG ---- PE 0.0 P2 10.0 5.6 17.8 23.6 0.020 TL 8.00 PV 0.1 ,q Pipe: 42 28.1 é.203 PL 8.00 PF 0.1 fi,.52 10.0 5.6 17.8 23.6 2.4 120 FTG ---- PE 0.0 10.0 5.6 17.7 23.6 0.007 TL 8.00 PV 0.0 j Pipe: 43 4.5 2,403 PL 8.00 PF 0.0 S5j 10.0 5.6 17.7 23.6 0.4 120 FTG ---- PE 0.0 10.0 5.6 17.7 23.6 0.000 TL 8.00 PV 0.0 Pipe: 44 -19.0 ?j.203 PL 8.00 PF 0.0 10.0 5.6 17.7 23.6 1.6 120 FTG ---- PE 0.0 10.0 5.6 17.8 23.6 0.003 TL 8.00 PV 0.0 , Pipe: 45 -42.6 20'3 PL 8.00 PF 0.1 S5b' 10.0 5.6 17.8 23.6 3.6 120 FTG ---- PE 0.0 S''6 10.0 5.6 17.9 23.7 0.014 TL 8.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG.. A\SUB JOB TITLE: BUILDING A .1 CALC 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) jPipe: Sj 46 10.0 (6 17.9 23.7 -66.3 5.6 2. 03 120 PL FTG 184.67 2ET PF PE 6.6 0.0 42 10.0 .0 24.5 0.0 0.032 TL 205.32 PV 0.2 Pipe: 47' 72.7 op 2. 03 PL 34.00 PF 2.5 J,2 10.0 0.0 20.4 0.0 6.1 120 FTG 4ET PE 0.0 10.0 0.0 17.9 0.0 .038 TL iiww PV 0.3 $ipe: 48 7R0 50.1 PL 5.92 PF 10.0 0.0 17.9 0. e 1 0.0 4.2 '120 FTG ---- PE 0.0 10.0 0.0 17.8 0.0 0.019 TL 5.92 PV 0.1 Pipe: 7 49 10.0 0.0 17.8 0.0 26.9 2.3 . 03 120 PL FTG 6.42 ---- PF PE 0.0 0.0 7' 10.0 0.0 17.7 0.0 0.006 TL 6.42 PV 0.0 pe 50 4.4 PL 8.75 PF 0.0 ~epi 10.0 0.0 17.7 0.0 0.4 120 FTG ---- PE 0.0 10.0 0.0 17.7 0.0 0.000 TL 8.75 PV 0.0 pe: 51 -18.1e 120 PL 7.42 PF 0.0 74 10.0 0.0 17.7 0.0 1.5 FTG ---- PE 0.0 75 10.0 0.0 17.8 0.0 0.003 TL 7.42 PV 0.0 1p 'pe: 52 -41.3 29 PL 6.08 PF 0.1 75 10.0 0.0 17.8 0.0 3.5 !20 FTG ---- PE 0.0 7 10.0 0.0 17.8 0.0 0.013 TL 6.08 PV 0.1 4 rPipe: 53 10.0 0.0 17.8 0.0 -63.8 5.4 2. 03 120 PL FTG 190.42 2ET PF PE 6.3 0.0 M'3 10.0 0.0 24.2 0.0 0.030 TL 211.07 PV 0.2 Pipe: 54 8.3 2.206V PL 37.67 PF 0.0 M13joV 10.0 0.0 21.1 0.0 0.7 FTG 2ET PE 0.0 10.0 0.0 21.1 0.0 0.001 TL 58.32 PV 0.0 ldr :tPipe: 55 -16.2 .203 PL PF 0.0 11.50 77 10.0 0.0 21.1 0.0 1.4 120 FTG ---- PE 0.0 7'8 10.0 0.0 21.1 0.0 0.002 TL 11.50 PV 0.0 Pipe: 56 -40.7 /1'203C PL 200.17 PF 3.0 8 10.0 0.0 21.1 0.0 3.4 FTG 4ET PE 0.0 M4 10.0 0.0 24.1 0.0 0.013 TL 230.82 PV 0.1 ipe: 57 10.0 0.0 21.1 0.0 50.1 4.2 e2-4203 120 PL FTG 26.17 2ET PF PE 0.9 0.0 iT 10.0 0.0 20.2 0.0 0.019 TL 46.82 PV 0.1 Pipe: 79 58 10.0 0.0 20.2 0.0 26.1 2.2 2 203 120 PL FTG 12.00 ---- PF PE 0.1 0.0 10.0 0.0 .20.2 0.0 0.006 TL L2.09, PV 0.0 80 o'p 59 10.0 0.0 20.2 0.0 1.4 0.1 .203 120 PL FTG 10.50 ---- PF PE 0.0 0.0 8 10.0 0.0 20.2 0.0 0.000 TL 10.50 PV 0.0 Pipe: 62 10.0 0.0 ç) 9.0 dw / Pipe: 63 72 10.0 0.0 58 9.0 5.6 oop Pipe: 64 73 10.0 0.0 59 9.0 5.6 oom 91 Pipe: 65 10.0 0.0 b6p 9.0 5.6 Pipe: 66 10.0 0.0 bs 9.0 5.6 Pipe: 67 10.0 0.0 4 62 9.0 5.6 quaw 68 7.7/Pipe: .,~ 10.0 0.0 9.0 5.6 Pipe: 69 78 10.0 0.0 S 4 9.0 5.6 Pipe: 70 79 10.0 0.0 20.'2 0.0 8.9 120 FTG 2ET PE 56'5 9.0 .618.5 24.1 0.183 TL 12.00 PV Pipe: 71 10.0 0.0 6 n6 9.0 5.6 dPipe: 72 0 81 10.0 0.0 20.2 0.0 9.2 9120 FTG T PE 5. symomb - Iddo 9.0 5.6 19.4 24.7 0.192 TL 6.00 PV Pipe: 73 82 10.0 0.0 S68 9.0 5.6 lmmww Pipe: 61 10.0 0.0 45 10.0 0.0 Pipe: 60 -23.3 PL 12.00 PF 20.2 0.0 2.0 120 FTG ---- PE 20.2 0.0 0.005 TL 12.00 PV IF -47.8 PL 188.00 PF 20.2 0.0 4.0 120 FTG 4ET PE 24.1 0.0 0.018 TL 218.65 PV 22.6 1 PL 3.50 PF 17.9 0.0 8.4 120 FTG 2ET PE 16.3 22.6 0.163 TL 12.50 PV 23.2 14lPL 1.00 PF 17.8 0.0 8.6 'i FTG T PE 17.2 23.2 O offl TL 462" Pv 22.5 . 49 PL 3.50 PF 17.7 0.0 8.4 120 FTG 2ET PE 16.1 22.5 0.1.6-2 TL 12.50 PV 22.5 .-49 PL 3.50 PF 17.7 0.0 8.4 120 FTG 2ET PE 16.1 22.5 0.162 TL 12.50 PV -- 23.2 Y49 PL 1.00 PF 17.8 0.0 8.6 V120 FTG T PE 17.2 23.2 0.171 TL 6.00 PV 22.6 l.O2If PL 3.50 PF 17.8 0.0 8.4 .f'o FTG 2ET PE 16.2 22.6 0.163 TL 12.50 PV 24.5 1A9,9 PL 3.50 PF 21.1 0.0 9.1 #1120 FTG 2ET PE 19.1 24.5 0.189 TL 12.50 PV 24.5 PL 3.50 PF 21.1 0.0 9.1 0 49 9120 FTG 2ET PE 19.1 24.5 0.189 TL 12.50 PV 24.1 3.00 PF 24.5 PL 3.00 PF 1.5 20.2 0.0 9.1to oT 120 FTG T PE 0.4 19.1 24.5 0.189 TL 8.00 PV 0.6 24.7 äPL 1.00 PF 20.2 0.0 9.2 120 FTG T PE 19.4 24.7 0.192 TL 6.00 PV 24.7 PL 1.00 PF 1.0 -0.4 0.5 1.2 0.4 0.6 1.2 0.4 0.6 2.2 0.4 0.5 2.0 0.4 0.5- 2.4 0.4 0.6 2.4 0.4 0.6 2.0 0.4 0.5 2.0 0.4 0.5 3.8 0.0 0.1 2.0 0.4 0.5 1.0 0.4 0.5 0.1 0. 0 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBI JOB TITLE: BUILDING A .1 CALC 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) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 ,DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .1 CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NZ. PT DISC. •VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) 74 . 9.4 2 PL 127.50 PF 0.2 '120 M31/ 20.0 0.0 20.9 0.0 0.8 FTG 9E2T PE 0.0 20.0 0.0 20.8 0.0 PV .0.0 Pipe: M3'0 75 20.0 0.0 20.9 0.0 7.1 0.6 2/2'03 '120 PL 143.50 FTG 9E2T PF PE 0.1 0.0 20.0 0.0 20.8 0.0 0.001, TL 209.80 PV 0.0 P'ipe: M3e3/' 76 20.0 0.0 20.9 0.0 6.8 0.6 &(203 120 PL 162.75 FTG 9E2T PF PE 0.1 0.0 / M3 20.0 0.0 20.8 0.0 0.000 TL 229.05 PV 0.0 /PiPe: 77 5.1 2403 PL 180.00 PF 0.1 19,4' 20.0 0.0 20.8 0.0 0.0 0.4 //120 FTG 5E2T PE 0.0 0.0 ,54 20.0 0.0 20.7 Q000 TL ç 226.30 PV Pipe: 78 4.0 2.293 PL 187.0.0 PF 0.1 M3/ 20.0 0.0 20.8 0.0 0.3 41(20 FTG 9E5T PE 0.0 20.0 0.0 20.7 0.0 0.000 TL 285.25 PV 0.0 /7Pipe: 79 3.0 2.2-03' PL 211.00 PF 0.0 43'6 20.0 0.0 20.8 0.0 0.3 /,I0 FTG 9E4T PE 0.0 /j56 20.0 0.0 20.7 0.0 C0.000 TL 298.60 PV 0.0 /2Pipe: 263 80 2.6 "120 PL 237.00 PF 0.0 M3 20.0 0.0 20.8 0.0 0.2 FTG 9E4T PE 0.0 6 t '. 20.0 0.0 20.7 0.0 0.000 TL 6-0 PV 0.0 Pipe: 81 -34.1 2.4 ' PL 24.50 PF 0.4 MA'9 20.0 0.0 18.6 0.0 2.9 /120 FTG 2ET PE -0.9 22,0 0.0 18.1 0.0 0.009 TL PV 0.1 Pipe: 82 -34.1 2.233 PL 8.00 PF 0.1 S1' 22.0 0.0 18.]. 0.0 2.9 1:5 FTG ---- PE 0.0 22.0 0.0 18.2 0.0 0.009 TL 8.00 PV 0.1 Pipe: 83 . -34.1 23 PL 8.00 PF 0.1 527 22.0 0.0 18.2 0.0 2.9 <"120 FTG ---- PE 0.0 22.0 0.0 18.3 0.0 0.009 TL 8.00 PV 0.1 Pipe: 84 . -34.1 27203 PL 8.00 PF) 0.1 S37 22.0 0.0 .18.3 0.0 2.9 120 FTG ------ PE 0.0 (4 22.0 0.0 18.3 0.0 0.009 TL 8.00 '11 0.1 Pipe: 85 -34.1 ./2?203 PL 8.00 PF 0.1 22.0 0.0 18.3 0.0 2.9 " 120 FTG ---- PE 0.0 'S5 22.0 0.0 18.4 0.0 0.009 TL 8.00 PV 0.1 Pipe: 86 -34.1 21203 PL 8.00 PF 0.1 S-57 22.0 0.0 18.4 0.0 2.9 <' 120 FTG ---- PE 0.0 22.0 0.0 18.5 0.0 0.009 TL 8.00 PV 0.1 Pipe: 87 . -34.1 2203 PL 8.00 PF 0.1 S7 22.0 0.0 18.5 0.0 2.9 6"120 FTG ---- PE 0.0 . S'7 22.0 0.0 18.6. 0.0 0.009 TL 8.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUr JOB TITLE: BUILDING A .1 CALC 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) 7Pipe: 88 -34.1 2.f3 PL 8.00 PF 0.1 s/ 22.0 0.0 18.6 0.0 2.9 120 FTG ---- PE 0.0 48 22.0 0.0 18.6 0.0 0.009 TL 8.00 PV 0.1 /7Pipe: 89 -34.1 03 PL 8.00 PF 0.1 S8'/ 22.0 0.0 18.6 0.0 2.9 120 FTG ---- PE 0.0 22.0 0.0 18.7 0.0 0.009 TL 8.00 PV 0.1 Pipe: 90 -34.1 2 03 PL 130.33 PF 1.3 5'9/ 22.0 0.0 18.7 0.0 2.9 120 FTG L PE 0.0 _113 1 22.0 0.0 20.0 0.0 0.009 TL 134.06 PV 0.1 9Pipe: 90A 34.1 2.70,3 PL 1.66 PF 0.1 20.0 0.0 20.9 0.0 1.9 /c2O FTG TL PE -0.9 R31 22.0 0.0 20.0 0.0 0<003 TL 26.86 PV 0.0 Pipe: 91 . -33.7 2,-12,03 PL 24.50 PF 0.4 , 1LY42 20.0 0.0 18.5 0.0 2.8 t , 11120 FTG 2ET PE -0.9 (S10 22.0 0.0 18.1 0.0 0.009 TL 45.15 PV 0.1 /9 Pipe: 92 -33.7 2,.~Z03 PL 8.00 PF 0.1 (Sf10 22.0 0.0 18.1 0.0 2.8 (1120 FTG ---- PE 0.0 S11 22.0 0.0 18.2 0.0 0.009 TL 8.00 PV 0.1 /9 Pipe: 93 -33.7 2..-203 PL 8.00 PF 0.1 51.11 22.0 0.0 18.2 0.0 2.8 7120 FTG ---- PE 0.0 9/12 22.0 0.0 18.2 0.0 .0.009 TL 8.00 PV 0.1 Pipe: 94 -33.7 2,2'03 PL 8.00 PF 0.1 (5-12 22.0 0.0 18.2 0.0 2.8 (1120 FTG ---- PE 0.0 S13 22.0 0.0 18.3 0.0 0.009 TL 8.00 PV 0.1 /9 Pipe: 95 -33.7 2 '03 PL 8.00 PF 0.1 (S/13 22.0 0.0 18.3 0.0 2.8 V 120 FTG ---- PE 0.0 514 22.0 0.0 18.4 0.0 0.009 TL 8.00 PV 0.1 / Pipe: 96 -33.7 23 PL 8.00 PF 0.1 y14 22.0 0.0 18.4 0.0 2.8 (/120 FTG ---- PE 0.0 S15 22.0 0.0 18.5 0.0 0.009 TL 8.00 PV 0.1 / Pipe: 97 -33.7 2403 PL 8.00 PF 0.1 S15 22.0 0.0 18.5 0.0 2.8 &120 FTG ---- PE 0.0 S16 22.0 0.0 18.5 0.0 0.009 TL 8.00 PV 0.1 Pipe: sdr 22.0 98 -33.7 ~9~ PL 8.00 PF 0.1 0.0 18.5 0.0 2.8 120 FTG ---- PE 0.0 Sj17 22.0 0.0 18.6 0.0 0.009 TL 8.00 PV 0.1 Pipe: 99 -33.7 2'103 PL 8.00 PF 0.1 SP 22.0 0.0 18.6 0.0 2.8 &'120 FTG ---- PE 0.0 S18 U 22.0 0.0 18.7 0.0 0.00. // TL 8.00 PV 0.1 Pipe: 100 -33.7 2.4i3 PL 130.33 PF 1.2 Si/B/ 22.0 0.0 18.7 0.0 2.8 120 FTG L PE 0.0 R32 22.0 0.0 19.9 0.0 0.009 TL 134.06 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .1 CALC 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: 100A -33.7 PL 1.66 PF 0.1 R32 22.0 0.0 19.9 0.0 1.9 120 FTG TL PE 0.9 .2 20.0 0.0 20.9 0.0 0.003 TL 26.86 PV 0.0 P7ipe: 101 20.0 0.0 18.5 0.0 0.0 0.0 2.2032 120 PL FTG -I--- 24.50 2ET PF PE 0.0 -0.9 5" 22.0 0.0 17.6 0.0 0.000 TL offth PV 0.0 102 0.0 2"0' PL 8.00 PF 0.0 Sly Pipe: 22.0 0.0 17.6 0.0 0.0 120 FTG ---- PE 0.0 5 0 22.0 0.0 17.6 0.0 0.000 TL 8.00 PV 0.0 Pipe: 103 0.0 2.203 PL 8.00 PF 0.0 S2;0' 22.0 0.0 17.6 0.0 0.0 V120 FTG ---- PE 0.0 S21 22.0 0.0 17.6 0.0 0.000 TL 8.00 PV 0.0 Pipe: 104 0.0 2,1003 PL 8.00 PF 0.0 22.0 0.0 17.6 0.0 0.0 V'120 FTG ---- PE 0.0 S22 22:0 0.0 17.6 0.0 0.000 TL 8.00 PV 0.0 Pipe: 105 0.0 .203 PL 8.00 PF 0.0 S22 22.0 0.0 17.6 0.0 0.0 120 FTG ---- PE 0.0 43 22.0 0.0 17.6 0.0 0.000 TL 8.00 PV 0.0 Pipe: 106 0.0 2'03 PL 8.00 PF 0.0 S24 22.0 0.0 20.0 0.0 0.0 V120 FTG ---- PE 0.0 (5 22.0 0.0 20.0 0.0 0.000 TL 8.00 PV 0.0 Pipe: 107 0.0 PL 8.00 PF 0.0 S25 22.0 0.0 20.0 0.0 0.0 120 FTG ---- PE 0.0 (26 22.0 0.0 20.0 0.0 0.000 TL 8.00 PV 0.0 Pipe: 108 0.0 .203 PL 8.00 PF 0.0 52(6 22.0 0.0. 20.0 0.0 0.0 120 FTG ---- PE 0.0 22.0 0.0 20.0 0.0 000 TL 8.00 PV 0.0 0 ;?.03 .áPipe: 109 0.0 PL 130.66 PF 0.0 SjT' 22.0 0.0 20.0 0.0 0.0 120 FTG L TL ' PE 0.0 R 22.0 0.0 . 20.0 0.0 0.000 PV 0.0 Pipe: .A 109A 0.0 j20. 1 003 PL 1.66 PF 0.0 22.0 0.0 20.0 0.0 0.0 20 FTG TL PE 0.9 33 20.0 0.0 20.9 0.0 0.000 TL 4!6 PV 0.0 ipe: 110 -33.3 2 '03 PL 32.00 PF 0.5 MAI#20.0 0.0 18.5 0.0 2.8 120 FTG 2ET PE -0.9 28 22.0 0.0 18.1 0.0 0.009 TL 52.65 PV 0.1 Pipe: 111 -33.3 2. 03 PL 14.00 PF 0.1 22.0 0.0 18.1 0.0 2.8 120 FTG ---- PE 0.0 29 22.0 0.0 18.2 0.0 0.009 TL 14.00 PV 0.1 112 . -33.3 2.2.03 PL 14.00 PF 0.1 22.0 0.0 18.2 0.0 2.8 4t20 FTG ---- PE 0.0 22.0 0.0 18.3 0.0 0.009 TL 14.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PRbGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SU JOB TITLE: BUILDING A .1 CALC 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) -2'Pipe: 113 -33.3 2.2 PL 14.00 PF 0.1 S37 22.0 22.0 0.0 18.3 0.0 2.8 FTG ---- PE 0.0 0.0 18.4 0.0 0'009 TL 14.00 PV 0.1 114 -33.3 2.20,3' PL 14.00 PF 0.1 22.0 0.0 18.4 0.0 2.8 /i'20 FTG ---- PE 0.0 32 22.0 0.0 18.6 0.0 0.009 TL 14.00 PV 0.1 115 7pipe: -33.3 2.'203 PL 133.00 PF 1.4 S32 22.0 0.0 18.6 0.0 2.8 (S'120 FTG 2ET PE 0.9 03 4 20.0 0.0 20.8 0.0 0.009 TL PV 0.1 Pipe: -7 116 -34.0 -111 2..,23 PL 26.00 PF 0.4 /20.0 0.0 18.3 0.0 2.9 (/120 FTG 2ET PE -0.9 X13 22.0 0.0 17.9 0.0 0.009 TL 46.65 PV 0.1 Pipe: 117 -34.0 227 PL 14.00 PF 0.1 S37 22.0 0.0 17.9 0.0 2.9 ('/120 FTG ---- PE 0.0 22.0 0.0 18.0 0.0 0.009 TL 14.00 PV 0.1 e,34 /2 Pipe: 118 -34.0 24'03 PL 10.00 PF 0.1 S3j7 22.0 0.0 18.0 0.0 2.9 (/120 FTG ---- PE 0.0 S 22.0 0.0 18.1 0.0 0'.009 TL 10.00 PV 0.1 LI /-Pipe: 119 -34..0 2.29'3 PL 14.00 PF 0.1 S35,/ 22.0 0.0 18.1 0.0 2.9 //r'20 FTG ---- PE 0.0 22.0 0.0 18.3 0.0 O-'009 TL 14.00 PV 0.1 Pipe: S12) 120 22.0 0.0 18.3 .0.0 -34.0 2.9 2.fr'3 (120 PL 9.34 FTG ---- PF PE 0.1 0.0 7 22.0 0.0 18.4 0.0 0.009 TL 9.34 PV 0.1, Pipe: 121 -34.0 2.)03 PL 14.00 PF 0.1 S3.7, 22.0 0.0 18.4 0.0 2.9 C'i'0 FTG ---- PE 0.0 22.0 0.0 18.5 0.0 0.009 TL 14.00 PV 0.1 Pipe: 122 -34.0 2.203 PL' 134.00 PF 1.4 S38-2 22.0 0.0 18.5 0.0 2.9 120 FTG 2ET PE 0.9 20.0 0.0 20.8 0.0 0.009 TL 6i) PV 0.1 ,yPipe: 123 -35.3 ,,2,?03 PL 26.00 PF 0.5 M4,6" 20.0 0.0 18.1 0.0 3.0 "-' 120 FTG 2ET PE -0.9 fr 39 22.0 0.0 17.7 0.0 0.010 TL PV 0.1 ',7 Pipe: 124 -35.3 2,43 PL 195.50 PF 2.2 S9'9 22.0 0.0 17.7 0.0 3.0 (.7120 FTG 2ET PE 0.9 6136 20.0 0.0 20.8 0.0 0.010 TL 216.15 PV 0.1 1 ,.-, Pipe: 125 -36.3 2'203 PL 221.50 PF 2.8 M4/7 20.0 0.0 18.0 0.0 3.1 " 120 FTG 4E2T PE 0.0 M7 20.0 0.0 20.8 0.0 0.011 TL 262.80 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 PATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBI JOB TITLE: BUILDING A .1 CALC NOTES: Calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.103 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 10.5 ft/sec at pipe 10. 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 N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00. 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N D Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 45ELL 8.390 31.00 60.00 22.00 78.00 21.00 7.00 60.00 13.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 7.980 26.00 50.00 19.00 50.00 17.00 4.00 50.00 PAGE: F MATERIAL: DYNAFL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D F Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 45ELL FRLKL -------------------------------------------------------- FRLK45 FRLKT 2.203 5.00 10.65 .3.73 11.00 6.00 1.00 10.00 1.91 3.72 1.91 9.05 0.00 0.00 2.703 6.00 18.60 6.60 14.00 7.00 1.00 10.00 3.26 6.67 3.41 16.72 0.00 0.00 3.314 7.00 21.80 7.27 16.00 10.00 1.00 13.00 3.60 7.27 3.60 18.90 0.00 0.00 4.310 10.00 27.80 9.45 22.00 12.00 4.00 20.00 5.56 9.45 4.72 22.24 0.00 0.00 6.403 14.00 38.91 12.97 32.00 10.00 3.00 28.00 9.07 12.97 6.48 32.40 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUI JOB TITLE: BUILDING A .1 CALC WATER SUPPLY ANALYSIS Static: 125.00 psi Resid: 20.00 psi Flow: 5390.0 gpm LEGEND 1 Available pressure 120.97 psi @ 925.3 gpm 2 Required pressure 35.71 psi @ 925.3 gpm 12018002400 3000 3600 4200 4.800 5400 6000 FLOW (GPM) MoiZoC1 PRO-TECH FIRE PROTECTION 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 HYDRAULIC CALCULATIONS BUILDING A REMOTE ARE FOR GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I BUILDING A CARLSBAD CA DATE: JULY 4, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: EXTRA HAZARD DENSITY: 0.45 gpm/3000 sq. ft. AREA OF APPLICATION: 3066 sq. ft. COVERAGE PER SPRINKLER: 89 SQ. FT. NUMBER OF SPRINKLERS CALCULATED: 39 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 1599.6 gpm TOTAL WATER REQUIRED + (OUTSIDE hose) 2099.6 gpm FLOW AND PRESSURE (@ BOR): 1599.6 gpm @ 76.2 psi SPRINKLER ORIFICE SIZE: 3/4 inch NAME OF CONTRACTOR: PRO-TECH FIRE PROTECTION . DESIGN/LAYOUT BY:PRO-TECH FIRE PROTECTION AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C16 HIC lO ID ,443/ /O 12'i ,E430 'I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SU' JOB TITLE: BUILDING A .45 CALC WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 125.0 20.0 5390.0 106.7 2099.0 94.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 2099.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1599.0 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT '2) (GPM/FTA2) Si' 22.0 K=11.20 16.9 46.1 89.0 0.450 0.518 S20 22.0 K=11.20 16.0 44.8 89.0 0.450 0.503 S3° 22.0 K=11.20 15.6 44.2 89.0 0.450 0.497 S40 22.0 K=11.20 15.5 44.0 89.0 0.450 0.495 S50 22.0 K=11.20 15.5 44.0 89.0 0.450 0.495 S6b 22.0 K=11.20 15.6. 44.2 89.0 0.450 0.497 S7 22.0 K=11.20 16.0 44.8 89.0 0.450 0.504 S8 22.0 K=11.20 17.0 46.1 89.0 0.450 0.518 S9 22.0 K=11.20 18.6 48.3 89.0 0.450 0.543 sio 22.0 K=11.20 16.7 45.7 89.0 0.450 0.514 Sib- 22.0 K=11.20 15.7 44.4 89.0 0.450 0.498 S12 22.0 K=11.20 15.2 43.7 89.0 0.450 0.491 513 22.0 K=11.20 15.1 43.5 89.0 0.450 0.488 S14 22.0 K=11.20 15.1 .43.5 89.0 0.450 0.488 S15 22.0 K=11.20 15.1 43.6 89.0 0.450 0.490 S16 22.0 K=11.20 15.5 44.1 89.0 0.450 0.496. S17 22.0 K=11.20 16.3 45.3 89.0 0.450 0.509 S18 22.0 K=11.20 17.8 47.3 89.0 0.450 0.531 S19 22.0 K=11.20 15.4 44.0 89.0 0.450 0.494 S20 22.0 K=11.20 14.0 42.0 89.0 0.450 0.472 S21 22.0 K=11.20 13.3 40.8 89.0 0.450 0.458 S22 22.0 K=11.20 12.9 40.2 89.0 0.450 0.452 S23 22.0 K=11.20 12.8 40.0 89.0 0.450 0.450 S24 22.0 K=11.20 20.2 50.3 89.0 0.450 0.565 S25 22.0 K=11.20 20.3 50.5 89.0 0.450 0.568 S26 22.0 K=11.20 20.9 51.2 89.0 0.450 0.575 S27 22.0 K=11.20 22.1 52.6 89.0 0.450 0.592 S28 22.0 K= 5.60 29.4 30.4 225.0 0.100 0.135 S29 22.0 K= 5.60 29.6 30.4 225.0 0.100 0.135 S30 22.0 K= 5.60 30.1 30.7 225.0 0.100 0.136 S31 22.0 K= 5.60 31.0 31.2 225.0 0.100 0.139 S32 22.0 K= 5.60 32.7 32.0 225.0 0.100 0.142 S33 22.0 K= 5.60 31.6 31.5 225.0 0.100 0.140 S34 22.0 K= 5.60 31.6 31.5 225.0 0.100 0.140 S35 22.0 K= 5.60 31.7 31.5 225.0 0.100 0.140 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 4pATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB1 JOB TITLE: BUILDING A .45 CALC NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT "2) (GPM/FTA2) S36 22.0 K= 5.60 32.0 31.7 225.0 0.100 0.141 S37 22.0 K= 5.60 32.6 . 32.0 225.0 0.100 0.142 38 22.0 K=. 5.60 34.1 32.7 225.0 0.100 0.145 S39 22.0 K= 5.60 37.5 34.3 225.0 0.100 0.152 S51 10.0 - - - - 50.6 --- S52 10.0 - - - - 51.2 --- S53 10.0 - - - - 51.7 --- S54 10.0 - - - - 52.3 --- S55 10.0 - - - - 52.8 --- S56 10.0 - --- 53.4 --- S57 9.0 - - - - 51..0 --- S58 9.0 - - - - 51.4 --- S59 9.0 - - - - 51.8 --- S60 9.0 - - - - 52.4 S61 9.0 - --- .52.8 --- S62 9.0 - -.-- 53.2 --- S63 9.0 - - - - 49.6 --- S64 9.0 - --- 50.4 --- S65 9.0 - - - - 48.8 - - -. S66 9.0 - - - - 49.6 --- S67 - 9.0 - - - - 50.2 --- S68 9.0 - - - - 51.0 --- 5 10.0 - - - - 71.8 10 20.0 - - - - 65.6 --- 71 10.0 ---- 50.6 72 10.0 - - - - 51.0 --- 73 . 10.0 - - - - 51.4 --- 74 10.0 - - - - 51.9 --- 75 10.0 - - - - 52.4 --- 76 10.0 - - - - 52.8 --- 77 10.0 __ 49.2 __- 78 10.0 - - - - 50.0 --- 79 10.0 - - - - 48.3 --- 80 10.0 - --- 49.1 --- 81 10.0 - - - - 49.8 --- 82 10.0 - - - - 50.6 - - - Ml 10.0 - - - - 68.3 . - - -. M2 10.0 - - - - 67.6 --- M3 10.0 ---- 66.0 --- M4 10.0 - - - - 65.3 --- M5 10.0 - - - - 65.2 - - - Mu 10.0 - - - - 46.7 --- M12 10.0 - - - - 46.5 --- M13 10.0 - ---. 45.3 --- M14 10.0 - - - - 45.2 --- M14A 10.0 - - - - 45.0 --- M21 10.0 - - - - 65.3. --- M21A 10.0 - - - - 65.2 --- M22 10.0 - - - - 65.3 --- M23 10.0 - --- 65.3 --- M31 20.0 - - - - 65.1 --- M32 20.0 - - - - 60.5 --- M33 20.0 - - - - 60.4 --- M34 20.0 - - - - 59.9 --- M35 20.0 - - - - 59.9 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUI JOB TITLE: BUILDING A .45 CALC NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FTA2) (GPM/FTA2) M36 20.0 - - - - 59.7 --- M37 20.0 ---- 59.7 --- M41 20.0 - - - - 26.9 --- M42 20.0 - - - - 27.1 --- M43 20.0 - - - - 28.2 --- M44 20.0 - - - - 30.2 --- M45 20.0 - - - - 32.8 --- M46 20.0 - - - - 35.8 --- M47 20.0 - - - - 37.0 --- M47A 20.0 - - - - 37.0 --- M51 20.0 - - - - 60.7 --- M52 20.0 - - - - 60.7 - - _ M53 20.0 - - - - 60.7 --- M54 20.0 - - - - 60.7 --- M54A 20.0 - - - - 60.7 --- M55 20.0 - - - - 60.6 --- M56 20.0 - - - - 60.6 --- M57 20.0 - - - - 60.6 --- R31 22.0 - - - - 61.1 --- R32 22.0 - - - - 56.8 --- R33 22.0 - - - - 56.9 ___ BOR 1.0 - - - - 76.2 - - - DI -3.0 - - - - 79.3 - - - U -3.0 - - - - 94.5 - - - UG -3.0 - - - - 93.3 --- UG1 -3.0 - - - - 90.8 ---, --------- UG2 -3.0 HOSE STREAM 82.9 500.0j BF1 3.0 - - - - 87.4 --- BF2 3.0 - - - - 82.4 - - - HYD 1.0 - - - - 937 ___ SRC 3.5 SOURCE 94.4 2099.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBt' JOB TITLE: BUILDING A .45 CALC 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 2099.0 7.9 0 PL 20.00 PF 1.8 3.5 SRCE 94.4 (N/A) 13.5 50 FTG TG PE 1.1 H D 1.0 0.0 93.7 0.0 0.024 TL 74.00 -a- PV 1.2 ipe: 1A 1638.6 7.980 PL 75.00 PF 2.2 H 1.0 0.0 93.7 0.0 10.5 FTG TL PE 1.7 -3.0 0.0 93.3 0.0 "is TL 1&O PV 0.7 Pipe: lB 460.4 7. PL 795.00 PF 1.2 -3.0 0.0 94.5 0.0 3.0 50 FTG 2L PE 0.0 e-G -3.0 0.0 93.3 0.0 0.001 TL 83.00 PV 0.1 Pipe: 1C -460.4 . 80 PL 575.00 PF 1.0 U JtD -3.0 1.0 0.0 0.0 94.5 93.7 0.0 0.0 3.0 150 0.001 FTG 2T TL6 .0 PE PV -1.7 0.1 Pipe: 1D 2099.0 80 PL. 30.00 PF 2.5 UG G -3.0 -3.0 0.0 0.0 93.3 90.8 0.0 . 0.0 13.5 150 0.024 FTG TLG TL 103.00 PE PV 0.0 1.2 Pipe: 2 2099.0 0 0! P sow PL 6.00 PF 0.8 ?le -3.0 0.0 90.8 0.0 12.2 140 FTG E PE -2.6 3.0 0.0 87.4 0.0 0.021 TL 37.00 PV 1.0 ipe: 3 FIXED PRESSURE LOSS DEVICE 3.0 0.0 87.4 0.0 dlokwpwo Si 2099.0 gpm 2 30 0.0 82.4 0.0 Pipe: .4 2099.0 80 PL 6.00 PF 2.1 BF2 3.0 0.0 82.4 0.0 12.2 ;~ 0 FTG ET PE 2.6 UG2 -3.0 H.S. 82.9 500.0 21 0.04 TL 97.00 PV 1.0 Pipe: 5 1599.0 70 PL 228.00 PF 3.6 UG2 -3.0 H.S. 82.9 500.0 10.3 T50 FTG L PE 0.0 DI -3.0 0.0 79.3 0.0 0.015 TL 247.00 PV 0.7 Pipe: 6 1599.0 PL 9.00 PF 1.3 DI -3.0 0.0 79.3 0.0 9.3 140 FTG 3E PE -1.7 1.0 0.0 0.0 0.013 TL 102.00 PV 0.6 Pipe: 7 6 4TQ3 PL 8.75 PF 0.6 IR 1.0 0.0 7. 0. 15.9 120 FTG ---- PE -3.9 5 10.0 0.0 71.8 0.0 . 0.064 TL 8.75 PV 1.7 Pipe: 8 1167.3 6 4r03 PL 12.75 PF 1.9 10.0 0.0 71.8 'aJ 5 0.0 11-.6 W120 FTG T PE -4.3 20.0 0.0 65.6 0.0 0.036 TL 51.66 PV 0.9 Pipe: 9 431.6 4A i0 PL 40.50 PF 3.5 5/ 10.0 0.0 71.8 0.0 9.5 V20 FTG 2ET PE 0.0 ol 10.0 0.0 68.3 0.0 0.039 TL 88.30 PV 0.6 J Pipe: 10 389.3 23 PL 2.42 PF 0.8 MJ' . 10.0 0.0 68.3 0.0 21.8 120 FTG ---- PE 0.0 10.0 0.0 67.6 0.0 0.314 TL 2.42 PV 3.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS. Page 5 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUI*I' JOB TITLE: BUILDING A .45 CALC 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: 11 289.2 03 PL 8.42 PF 1.5 102 10.0 0.0 67.6 0.0 16.2 120 FTG ---- PE 0.0 M3 10.0 0.0 66.0 0.0 0.181 TL 8.42 PV 1.8 J Pipe: 12 194.0 2 703 PL 8.00 PF 0.7 3 10.0 0.0 66.0 0.0 10.8 '12O FTG ---- PE 0.0 M4 10.0 0.0 65.3 0.0 0.087 TL 8.00 PV 0.8 J Pipe: 13 91.4 21O3 PL 8.50 PF 0.2 10.0 0.0 65.3 0.0 5.1 12O FTG ---- PE 0.0 "M5 10.0 0.0 65.2 0.0 0.022 TL 8.50 PV 0.2 J Pipe: 14 100.1 3&03 PL 6.25 PF 0.2 11 10.0 0.0 46.7 0.0 5.6 '120 FTG ---- PE 0.0 'I12 10.0 0.0 46.5 0.0 0.026 TL 6.25 PV 0.2 j Pipe: 15 195.3 703 PL 13.92 PF 1.2 M 0p 10.0 0.0 46.5 010 10.9 120 FTG ---- PE 0.0 3 10.0 0.0 45.3 0.0 0.088 TL 13.92 PV 0.8 Pipe: 16 . . 293.4 203 PL 1.50 PF 0.3 M]J 10.0 0.0 45.3 0.0 16.4 120 FTG ---- PE 0.0 T4A 10.0 0.0 45.0 0.0 .186 TL 1.50 PV 1.8 Pipe: 16A -98.1 2&03 PL 6.33 PF 0.2 Ml'LA 10.0 0.0 45.0 0.0 5.5 120 FTG ---- PE 0.0 M41 10.0 0.0 45.2 0.0 0.025 TL 6.33 PV 0.2 ' ipe: 16b . 391.6 PL 10.00 PF 3.7 M1 10.0 0.0 45.0 0.0 14.6 '0 FTG T PE -4.3 LWA 20.0 0.0 - 37.0 0.0 0.118 TL 31.80 PV 1.4 160 -40.1 2.79PL 3.67 PF 0.1 10.0 0.0 65.2 0.0 2.2 I FTG T PE 0.0 M24 10.0 0.0 65.3 0.0 0.005 TL 22.27 PV 0.0 ,Pipe: 17 . 2.3 2.7PL 9.25 PF 0.0 10.0 0.0 65.3 0.0 0.1 1W FTG ---- PE 0.0 10.0, 0.0 65.3 0.0 0.000 TL 9.25 PV 0.0 Lpe 17A 40.1 2. PL 11.50 PF-- 0.1 M2j 10.0 0.0 65.2 0.0 2.2 1O, FTG T PE -4.3 MTiA . 20.0 0.0 60.7 0.0 0.005 TL 30.10 PV . 0.0 4ipe: 18 2.3 PL 18.00 PF 0.0 10.0 0.0 65.3 0.0 0.1 W FTG 3ET PE 0.0 10.0 0.0 65.3 0.0 0.00 TL 54.60 PV 0.0 Pipe: 19 282.5 .310 1.42. PF 0.5 10 20.0 0.0 65.6 0.0 6.2 FTG T PE 0.0 M3]. 20.0 0.0 65.1 0..0 0.018 TL 29.22 PV 0.3 Pipe: 20 884.8 4.310 6.58 PF 5.1 10 20.0 0.0 65.6 0.0 19.5 F T PE 0.0 M32 20.0 0.0 60.5 0.0 0. A8 T- 34.38 PV 2.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .45 CALC 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) j Pipe: 21 677.5 PL 11.00 PF 0.1 M 20.0 0.0 60.5 0.0 6.8 20 FTG ---- PE 0.0 03 20.0 0.0 60.4 0.0 0.013 TL 11.00 PV 0.3 Ppe: 22 484.7 A 210 PL 8.50 PF 0.4 M33 20.0 0.0 60.4 0.0 10.7 olow,20 FTG ---- PE 0.0 I. 4 20.0 0.0 59.9 0.0 0.049 TL 8.50 PV 0.8 Pipe: 23 339.5 4O PL 3.50 PF 0.1 20.0 0.0 59.9 0.0 7.5 120 FTG ---- PE 0.0 /M!5 20.0 0.0 59.9 0.0 0.025 TL 3.50 PV 0.4 Pipe: 24 198.8 4110 PL 12.00 PF 0.1 M) 20.0 0.0 59.9 0.0 4.4 120 FTG ---- PE 0.0 6 20.0 0.0 59.7 0.0 0.009 TL 12.00 PV 0.1 tipe: 25 95.3 j10 PL 12.00 PF 0.0 M31r 20.0 0.0 59.7 0.0 2.1 "120 FTG ---- PE 0.0 20.0 0.0 59.7 0.0 0.002 TL 12.00 PV 0.0 26 -178.4 . 14 PL 8.00 PF 0.2 114 20.0 0.0 26.9 0.0 6.6 0 , 120 FTG ---- PE 0.0 aff 20.0 0.0 27.1 0.0 0.028 TL 8.00 PV 0.3 Pipe: 27 -361.7 3.314 PL 11.00 PF 1.1 M42 20.0 0.0 27.1 0.0 13.5 120 0FTG ---- PE 0.0 20.0 0.0 28.2 0.0 0.102 TL 11.00 PV 1.2 Pipe: 28 -568.7 !L4 PL 8.50 PF 2.0 20.0 0.0 28.2 0.0 21.2 120 FTG ---- PE 0.0 j;oof 20.0 0.0 30.2 0.0 0.235 TL 8.50 PV 3.0 Pipe: 29 -559.4 214 PL 11.58 PF 2.6 M44 20.0 0.0 30.2 0.0 20.8 120 FTG ---- PE 0.0 M45 20.0 0.0 32.8 0.0 0.228 TL 11.58 PV 2.9 Pipe: 30 -591.9 PL 11.83 PF 3.0 M45 20.0 0.0 32.8 0.0 22.0 #oPPwl20 FTG ---- PE 0.0 M4 20.0 0.0 35.8 0.0 0.253 TL 11.83 PV 3.3 Pipe: 30A -504.5 434 PL 6.00 PF 1.1 M46 20.0 0.0 35.8 0.0 18.8 fr 120 FTG ---- PE 0.0 M4 20.0 0.0 37.0 0.0 0. .188 TL 6.00 PV 2.4 Pipe: 30B -113.0 Ø14 PL 6.00 PF 0.1 M47A 20.0 0.0 37.0 0.0 4.2 00 120 FTG ---- PE 0.0 20.0 0.0 37.0 0.0 0.012 TL 6.00 PV 0.1 Pipe: 31 54.4 3314 PL 8.00 PF 0.0 M51 20.0 0.0 60.7 0.0 2.0 "120 FTG ---- PE 0.0 20.0 0.0 60.7 0.0 0.003 TL 8.00 PV 0.0 Pipe: 32 44.0 3.314 PL 13.75 PF 0.1 M52 20.0 0.0 60.7 0.0 1.6 120 FTG 2E PE 0.0 M53 20.0 0.0 60.7 0.0 0.002 TL 27.75 PV 0.0 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER SYSTEM SPRINKLER\JOBS HYDRAULIC ANALYSIS IN PROGRESS\PALOMAR Page 7 FORUM\SEFP\CALCS\BLDG. A\SU JOB TITLE: BUILDING A .45 CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) T (PSI) t Pipe: 33 20.0 0.0 60.7 0.0 32.2 1.2 r.314 120 PL FTG 8.58 ---- PF PE 0.0 0.0 M54 20.0 0.0 60.7 0.0 0.001 TL 8.58 PV 0.0 Pipe: 33A -46.1 14 PL 10.33 PF 0.1 54 20.0 0.0 60.7 0.0 1.5 120 FTG T PE 0.0 M54A 20.0 0.0 60.7 0.0 0.002 TL 32.13 PV 0.0 Pipe: 34 53.4 14 /-211,20 PL 3.42 PF 0.0 20.0 0.0 60.7 0.0 2.0 FTG ---- PE 0.0 55 20.0 0.0 60.6 0.0 0.003 TL 3.42 PV 0.0 Pipe: 35 35.9 1.3/3 14 PL 12.00 PF 0.0 M5 20.0 0.0 60.6 0.0 20 FTG ---- PE 0.0 M6 20.0 0.0 60.6 0.0 0.001 TL 12.00 PV 0.0 Pipe: 36 17.7 .314 PL 12.00 PF 0.0 M56 20.0 0.0 60.6 0.0 0.7 V 120 FTG ---- PE 0.0 M5 20.0 0.0 60.6 0.0 0.000 TL 12.00 PV 0.0 Pipe: 37 42.3 2.g3PL 159.50 PF 3.0 Ml g;,21r 10.0 0.0 68.3 0.0 3.6 r2 0 FTG 7E2T PE 0.0 10.0 0.0 65.3 0.0 0.014 TL 215.80 PV 0.1 Pipe: 38 4.5 PL 193.00 PF 0.1 M4 10.0 0.0 65.3 0.0 0.4 .20 FTG 4E2T PE 0.0 lvi. 10.0 0.0 65.3 0.0 0.000 TL 234.30 PV 0.0 Pipe: 39 -6.8 03 PL 211.34 PF 0.1 MS 10.0 0.0 65.2 0.0 0.6 '120 FTG 5E4T PE 0.0 jd?3 10.0 0.0 65.3 0.0 0.000 TL 278.94 PV 0.0 Pipe: 40 -100.1 03 PL 26.00 PF 3.9 M 10.0 0.0 46.7 0.0 8.4 120 FTG 4ET PE 0.0 OT 10.0 0.0 50.6 0.0 0.069 TL 56.65 PV 0.5 Pipe: 41 -100.1 PL 8.00 PF 0.6 10.0 0.0 50.6 0.0 8.4 120 FTG ---- PE 0.0 10.0 0.0 51.2 0.0 0.069 TL 8.00 PV 0.5 Pipe: 42 0.0 51.2 -100.1 0.0 8.4 23 '120 PL FTG 8.00 ---- PF PE 0.6 0.0 ?5 P 10.0 10.0 0.0 51.7 0.0 0.069 TL 8.00 PV 0.5 Pipe: 43 -100.1 PL 8.00 PF 0.6 S53 10.0 0.0 51.7 0.0 8.4 jjf3 ].20 FTG ---- PE 0.0 S 10.0 0.0 52.3 0.0 0.069 TL 8.00 PV 0.5 Pipe: 44 10.0 0.0 52.3 -100.1 0.0 8.4 2.203 120 PL FTG 8.00 ---- PF PE 0.6 0.0 10.0 0.0 52.8 0.0 0.069 TL 8.00 PV 0.5 Pipe: 45 -100.1 2.03 PL 8.00 PF 0.6 10.0 0.0 52.8 0.0 8.4 20 FTG ---- PE 0.0 wS55 10.0 0.0 53.4 0.0 0.069 TL 8.00 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 'iDATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .45 CALC 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) /-2 pe: 46 -100.1 .203 PL 184.67 PF 14.2 10.0 0.0 53.4 0.0 8.4 120 FTG 2ET PE 0.0 10.0 0.0 67.6 0.0 0.069 TL 205.32 PV 0.5 I Pipe: 47 -95.1 PL 34.00 PF 4.1 Ml T 10.0 0.0 46.5 0.0 8.0 20 FTG 4ET PE 0.0 10.0 0.0 50.6 0.0 0.063 TL 64.65 PV 0.4 1 . Pipe: 48 -95.1 2.203 PL 5.92 PF 0.4 ji. 10.0 0.0 50.6 0.0 8.0 '120 FTG ---- PE 0.0 10.0 0.0 51.0 0.0 .063 TL 5.92 PV 0.4 / Pipe: 49 -95.1 2.203 PL 6.42 PF 0.4 10.0 0.0 51.0 0.0 8.0 120 FTG ---- PE 0.0 73 10.0 0.0 51.4 0.0 0.063 TL 6.42 PV 0.4 Pipe: 50 -95.1 2.203 PL 8.75 PF 0.5 10.0 0.0 51.4 0.0 8.0 120 FTG ---- PE 0.0 4 10.0 0.0 51.9 0.0 0.063 TL 8.75 PV 0.4 d Pipe: 51 -95.1 2.203 PL 7.42 PF 0.5 10.0 0.0 51.9 0.0 8.0 120 FTG ---- PE 0.0 10.0 0.0 52.4 0.0 0.063 TL 7.42 PV 0.4 Pipe: 52 -95.1 /2.203 PL 6.08 PF 0.4 10.0 0.0 52.4 0.0 8.0 120 FTG ---- PE 0.0 IT6 10.0 0.0 52.8 0.0 0.063 TL 6.08 PV 0.4 J Pipe: 53 -95.1 2.203 PL 190.42 PF 13.3 10.0 0.0 52.8 0.0 8.0 120 FTG 2ET PE 0.0 10.0 0.0 66.0 0.0 0.063. TL 211.07 PV 0.4 J Pipe: 54 -98.2 2.203 PL 37.67 PF 3.9 10.0 0.0 45.3 0.0 8.3 120 FTG 2ET PE 0.0 ' 7 10.0 0.0 49.2 0.0 /0 . 067 TL 58.32 PV 0.5 dMftmr Pipe: 55 -98.2 203 PL 11.50 PF 0.8 10.0 0.0 49.2 0.0 8.3 120 FTG ---- PE 0.0 78 10.0 0.0 50.0 0.0 0.067 TL 11.50 PV 0.5 Pipe: 56 -98.2 1.120 203 PL 200.17 PF 15.4 7 10.0 0.0 50.0 0.0 8.3 FTG 4ET PE 0.0 M4 10.0 0.0 65.3 0.0 0.067 TL 230.82 PV 0.5 Pipe: 57 -98.1 1.203 PL 26.17 PF 3.1 M2cr 10.0, 0.0 45.2 0.0 8.3 V 120 FTG 2ET PE 0.0 10.0 0.0 48.3 0.0 0.067 TL 46.82 PV 0.5 I Ammoloo j. Pipe: 58 -98.1 (203 PL 12.00 PF 0.8 7 10.0 0.0 48.3 0.0 8.3 120 FTG ---- PE 0.0 80 10.0 0.0 49.1 0.0 0.067 TL jjV0400. PV 0.5 Pipe: 59 -98.1 2.203 PL 10.50 PF 0.7 80 10.0 0.0 49.1 0.0 8.3 120 FTG ---- PE 0.0 10.0 0.0 49.8 0.0 ".067 TL jill ia PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUtb JOB TITLE: BUILDING A .45 CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 60 -98.1 FL 12.00 PF 0.8 81 10.0 0.0 49.8. 0.0 8.3 120 FTG ---- PE 0.0 82 10.0 0.0 50.6 0.0 0.067 TL 12.00 PV 0.5 Pipe: 61 . -98.1 2 03 PL 188.00 PF 14.5 10.0 0.0 50.6 0.0 8.3 120 FTG 4ET PE 0.0 M5 10.0 0.0 65.2 0.0 0.067 TL 0.5 Pipe: 62 0.0 .049 FL 3.50 PF 0.0 7 10.0 0.0 50.6 0.0 0.0 120 FTG 2ET PE 0.4 57 9.0 0.0 51.0 0.0 0.000 TL 12.50 .PV 0.0 Pipe: 63 0.0 1.049 PL 1.00 PF 0.0 10.0 0.0 51.0 0.0 0.0 120 FTG T FE 0.4 58 9.0 0.0 51.4 0.0 .000 TL 6.00 PV 0.0 Pipe: 64 0.0 1.049 PL 3.50 PF 0.0 710 10.0 0.0 51.4 0.0 0.0 120 FTG 2ET PE 0.4 9 9.0 0.0 51.8 0.0 0.000 TL 12.50 PV 0.0 Pipe: 65 0.0 1.049 PL 3.50 PF 0.0 74 10.0 0.0 51.9 0.0 0.0 120 FTG 2ET PE 0.4 S60 9.0 0.0 52.4 0.0 .000 TL 12.50 PV 0.0 / Pipe: 66 0.0 1.049 FL 1.00 PF 0.0 15 10.0 0.0 52.4 0.0 0.0 120 FTG T PE. 0.4 561 9.0 0.0 52.8 0.0 0.000 TL 6.00 PV 0.0 Pipe: 67 0.0 .049 FL 3.50 PF 0.0 J62 10.0 0.0 52.8 0.0 0.0 120 FTG 2ET FE 0.4 9.0 0.0 53.2 0.0 0.000 TL 12.50 PV 0.0 Pipe: 68 0.0 1.049 FL 3.50 PF 0.0 7 10.0 0.0 49.2 0.0 0.0 ( 120 FTG 2ET FE 0.4 3 9.0 0.0 49.6 0.6 0.000 TL 12.50 pv 0.0 Pipe: 69 0.0 1.049 FL 3.50 PF 0.0 78 10.0 0.0 50.0 0.0 0.0 120 FTG 2ET FE 0.4 1 S6 9.0 0.0 50.4 0.0 /.000 TL 1.Q1 PV 0.0 Pipe: 70 0.0 1.049 PL 3.00 PF 0.0 9 10.0 0.0 48.3 0.0 0.0 120 FTG 2ET FE 0.4 S65 9.0 0.0 48.8 0.0 0 000 TL 12.00 PV 0.0 Pipe: 71 0.0 .049 FL 1.00 PF 0.0 8' 10.0 0.0 49.1 0.0 0.0 120 FTG T FE 0.4 S66 9.0 0.0 49.6 0.0 0.000 TL 6.00 PV 0.0 j Pipe: 72 0.0 /120 049 FL 1.00 PF 0.0 10.0 0.0 49.8 0.0 0.0 FTG T FE 0.4 67 9.0 0.0 50.2 0.0 0.000 TL 6.00 PV 0.0 Pipe: 73 0.0 1j049 FL 3.00 PF 0.0 82 10.0 0.0 50.6 0.0 0.0 120 FTG T PE 0.4 9.0 0.0 51.0 0.0 0.000 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 PATE: 6/16/2001C:\DWG\FIRE' SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBI' JOB TITLE: BUILDING A .45 CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEVi NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 74 . 54.4 e2.203 PL 127.50 PF 4.3 20.0 - 0.0 65.1 0.0 4.6 120 FTG 9E2T PE 0.0 Y51/4 20.0 0.0 60.7 0.0 6'.022 TL 193.80 PV 0.1 Pipe: 75 -10.4 2.203 PL 143.50 PF 0.2 20.0 0.0 60.5 0.0 0.9 . 120 FTG 9E2T PE 0.0 M52 20.0 0.0 60.7 0.0 .001 TL 209.80 PV 0.0 Pipe: 76 -11.8 2.203 PL5 PF 0.3 63 20.0 0.0 60.4 0.0 1.0 120 FTG 9E2T PE 0.0 M53 20.0 0.0 60.7 0.0 .001 TL 229.05 PV 0.0 I Pipe: 77 -18.8 2.203 PL 1rr PF 0.7 20.0 0.0 59.9 0.0 1.6 120 FTG 5E2T PE 0.0 M54 20.0 0.0 60.7 0.0 0 003 TL 226.30PV 0.0 J Pipe: 78 -17.6 /2.203 PL 187.00 PF 0.8 1%15 20.0 0.0 59.9 0.0 1.5 120 FTG 9E5T PE 0.0 M55 20.0 0.0 60.6 0.0 0.003 TL 285.25 PV 0.0 Pipe: 79 -18.2 .203 PL 211.00 PF 0.9 M' 20.0 0.0 59.7 0.0 1.5 120 FTG 9E4T PE 0.0 Ivf'6 20.0 0.0 60.6 0.0 0.003 TL 298.60 PV 0.0 Pipe: 80 -17.7 2,j003 PL 237.00 PF 0.9 .3 20.0 0.0 59.7 0.0 1.5 #F120 FTG 9E4T PE 0.0 1657 20.0 0.0 60.6 0.0 0.003 TL 324.60 PV 0.0 ' Pipe: 81 178.4 2.203 PL 24.50 PF 9.1 20.0 0.0 26.9 0.0 15.0 120 FTG 2ET PE -0.9 1 22.0 11.2 16.9 46.1 0.201 TL 4PV 1.5 Pipe: 82 132.4 2.203 PL 8.00 PF 0.9 - 22.0 11.2 16.9 46.1 11.1 i0 FTG ---- PE 0.0 S/ 22.0 11.2 16.0 44.8 .116 TL 8.00 PV 0.8 Pipe: 83 87.6 PL 8.00 PF 0.4 22.0 11.2 16.0 44.8 7.4 e 22 0 FTG ---- PE 0.0 22.0 11.2 15.6 44.2 4 TL 8.00 PV 0.4 Pipe: 84 43.4 2.203 PL 8.00 PF 0.1 22.0 11.2 15.6 44.2 3.7 20 FTG ---- PE 0.0 /S4 22.0 11-.2 15.5 44.0 .015 TL 8.00 PV 0.1 Pipe: 85 -0.7 2.93 PL 8.00 PF 0.0 22.0 11.2 15.5 44.0 0.1 #?20 FTG ---- PE 0.0 22.0 11.2 - 15.5 44.0 0.000 TL 8.00 PV 0.0 4MM Pipe: 86 -44.7 2.203 PL 8.00 PF 0.1 22.0 11.2 15.5 44.0 3.8 20 FTG ---- PE 0.0 eS6 22.0 11.2 15.6 44.2 . 0:016 TL 8.00 PV 0.1 Pipe: 87 -88.9 2.203 PL 8.00 PF 0.4 S6 22.0 11.2 15.6 44.2 7.5 660 FTG ---- PE 0.0 22.0 11.2 16.0 44.8 .055 TL 8.00 PV 0.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SU1? JOB TITLE: BUILDING A .45 CALC PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NOD (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 88 -133.7 2 0 3 PL 8.00 PF 0.9 47 22.0 11.2 16.0 44.8 11.3 FTG ---- PE 0.0 22.0 11.2 17.0 46.1 0.120 18 TL 8.00 PV 0.9 4P Pipe: 89 -179.8 2A203 PL 8.00 PF 1.6 ts,9 22.0 11.2 17.0 46.1 15.1 120 FTG ---- PE 0.0 22.0 11.2 V 18.6 48.3 0.204 TL 8.00 PV 1.5 Pipe: 90 -228.1 2A203 PL 130.33 PF 42.5 9 22.0 11.2 18.6 48.3 19.2 20 FTG L PE 0.0 ;31 31 22.0 0.0 61.1 .0.0 0 317 TL 134.06 PV 2.5 , Pipe: 90A 228.1 2.703 PL 1.66 PF 3.1 20.0 0.0 5.1 • 0.0 12.8 120 FTG TL PE -0.9 R31 22.0 0.0 1.1 .0.0 0 117 TL 26.86 PV 1.]. Pipe: 91 183.3 2.203 PL 24.50 PF 9.5 M42 20.0 0.0 27.1 0.0 15.4 120 FTG 2ET PE -0.9 10 22.0 11.2 16.7 45.7 0.211 TL 45.15 PV 1.6 -I-- 1120 Pipe: 92 137.6 203 PL 8.00 PF 1.0 10 22.0 11.2 16.7 45.7 11.6 FTG ---- PE 0.0 Sil 22.0 11.2 15.7 44.4 0.124 TL 8.00 PV 0.9 Pipe: 93 93.2 2,.203 PL 8.00 PF 0.5 22.0 11.2 15.7 44.4 7.8 120 FTG ---- PE 0.0 (2 22.0 11.2 15.2 43.7 .060 TL 8.00 PV 0.4 yl Pipe: 94 49.5 2.203 PL 8.00 PF 0.2 22.0 11.2 15.2 43.7 4.2 '120 FTG ---- PE 0.0 22.0 11.2 15.1 43.5 0 019 TL 8.00 PV 0.1.. Pipe: 95 6.1 2.203 PL 8.00 PF 0.0 S3 22.0 11.2 15.1 43.5 0.5 120 FTG ---- PE 0.0 4 22.0 11.2 15.1 43.5 0.000 TL 8.00 PV 0.0 dommp Pipe: 96 -37.4 .203 PL 8.00 PF 0.1 S14 22.0 11.2 15.1 43.5 3.1 1 •-.,120 FTG ---- PE 0.0 S15 22.0 11.2 15.1 43.61 0.011 TL 8.00 PV 0.1 -I- I Pipe: 97 -81.0 203 PL 8.00 PF 0.4 22.0 11.2 15.1 43.6 6.8 120 FTG ---- PE 0.0 16 22.0 11.2 15.5 44.1 0.047 TL 8.00 PV 0.3 dwow /203 Pipe: 98 -125.1 PL 8.00 PF 0.8 Si 22.0 11.2 15.5 44.1 10.5 120 FTG ---- PE 0.0 S17 22.0 11.2 16.3 45.3 0.104 TL 8.00 PV 0.7 AS Pipe: 99, -170.410- .185 203 PL 8.00 PF 1.5 0 S7' 22.0 11.2 16.3 45.3 14.3120 FTG ---- PE 0.0 fl8 22.0 11.2 17.8 47.3 TL 8.00 PV , 1.4. Al Pipe: 100 -217.7 2.03 PL 130.33 PF 38.9 Sle 22.0 11.2 17.8 47.3 18.3 20 FTG L PE 0.0 Rl~l 22.0 0.0 56.8 0.0 .290 TL 134.06 PV 2.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 'b)ATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUBL' JOB TITLE: BUILDING A .45 CALC 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) jPipe: 100A -217.; 2 P 1.66. PF 2.9 R3' 22.0 0.0 56.8 0.0 12.2 20 FTG .TL PE 0.9 i42 20.0 0.0 60.5 0.0 - .107 TL 26 86 PV 1.0 - pe: 101 207.0 2 03 PL 24.50 PF 11.9 M43 20.0 0.0 28.2 0.0 17.4 .•120 FTG 2ET PE -0.9 S 9 22.0 11.2 15.4 44.0 0.265 TL 45-1-5w PV 2.0 Pipe: 102 163.0 2.203 PL 8.00 PF 1.4 S19 22.0 11.2 15.4 44.0 13.7 20 FTG ---- PE 0.0 s,09 0 22.0 11.2 14.0 42.0 0.170 TL 8.00 PV 1.3 Pipe: 103 121.0 2.203 PL 8.00 PF 0.8 S20 22.0 11.2 14.0 42.0 10.2 120 FTG ---- PE 0.0 S-I. 22.0 11.2 13.3 40.8 0.098 TL 8.00 PV 0.7 Pipe: 104 80.3 24203 PL 8.00 PF 0.4 S21 22.0 11.2 13.3 40.8 6.8 "120 FTG ---- PE 0.0 S22 22.0 11.2 12.9 40.2 0.046 TL 8.00 PV 0.3 Pipe: 105 40.0 240203 PL 8.00 PF 0.1 V S22 .22.0 11.2 12.9 40.2 3.4 f 120 FTG ---- PE 0.0 22.0 11.2 12.8 40.0 0.013 TL 8.00 PV 0.1 Wo U Pipe: 106 -50.3 2e.03 PL 8.00 PF 0.2 Y5 2 22.0 11.2 20.2 50.3 4.2 120. FTG ---- PE 0.0 22.0 11.2 20..3 50.5 0.019 TL 8.00 PV 0.1 A - Pipe: 107 . -100.8 p203 PL 8.00 PF 0.6 S25A 22.0 11.2 20.3 50.5 8.5 120 FTG ---- PE 0.0 22.0 11.2 20.9 51.2 0.070 TL 8.00 PV 0.5 Pipe: 108 -152.0 /22/03 PL 8.00 PF 1.2 220 11.2 20.9 51.2 12.820 FTG ---- PE 0.0 V22.0 11.2 22.1 52.6 0.150 TL 8.00 PV 1.1 Pipe: 109 -204.7 2. 03 PL 130.66 PF 34.8 S2 22.0 11.2 22.1 52.6 17.2 120 FTG L PE 0.0 22.0 56.9 0.0 0.259 wWo 2.0 Pipe: 109A -204.7 2 703 PL 1.66 PF 2.6 Ri 22.0 0.0 56.9 0.0 11.4 120 FTG TL PE 0.9 M83 20.0 0.0 60.4 0.0 0.096 TL jjg8PV 0.9 V Pipe: 110 -9.3 203 PL 32.00 PF 0.0 M49 20.0 .0 30.2 0.0 0.8 p120 FTG 2ET PE -0.9 SZ'8 22.0 5.6 29.4 30.4 0.'001 TL 52.65 PV 0.0 V ). Pipe: 111 -39.7 J.203 PL 14.00 PF 0.2 22.0 5.6 29.4 30.4 3.3 120 FTG ---- PE 0.0 W9, 22.0 5.6 29.6 30.4 0.012 TL 14.00 PV 0.1 Pipe: 112 •' -70.1 2.203 PL 14.00 PF 0.5 S29 22.0 5.6 29.6 30.4 5.9 120 FTG ---- PE 0.0 io 22.0 30.1 30.7 0.036 TL 14.00 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUlb JOB TITLE: BUILDING A .45 CALC 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) 4 Pipe: 113 -100.8 e-120 203 PL 14.00 PF 1.0 S3'9' 22.0 5.6 30.1 30.7 8.5 FTG ---- PE 0.0 s14ã 22.0 5.6 31.0 31.2 0.070 TL 14.00 PV 0.5 Un //Pipe: 114 -132.0 /.203 PL 14.00 PF 1.6 S34" 22.0 5.6 31.0 31.2 11.1 (J 120 FTG ---- PE 0.0 S42 22.0 5.6 32.7 32.0 0.115 TL 14.00 PV 0.8 V 4 Pipe: 115 -164.0 2t'.203 PL 133.00 PF 26.4 S3/ 22.0 5.6 32.7 32.0 13.8 1/120 FTG 2ET PE 0.9 T 1 20.0 0.0 59.9 0.0 1p1.1172 TL 153.65 PV 1.3 ___ Pipe: 116 32.6 2.203 PL 26.00 PF 0.4 M45 20.0 0.0 32.8 0.0 2.7 120 FTG 2ET PE -0.9 e 22.0 5.6 31.6 31.5 0.009 TL 46.65 PV 0.1 Pipe: 117 1.1 j2.203 PL 14.00 PF 0.0 22.0 5.6 31.6 31.5 0.1 1(120 FTG ---- PE 0.0 S4 22.0 5.6 31.6 31.5 0.000 TL 14.00 PV 0.0 Pipe: 118 -30.4 2.203 PL 10.00 PF 0.1 S3,,4' 22.0 5.6 31.6 31.5 2.6 120 FTG ---- PE 0.0 4r35 22.0 5.6 31.7 31.5 ~2.203 0.008 TL 10.00 PV 0.0 Pipe: 119 -61.9 PL 14.00 PF 0.4 S45 22.0 5.6 31.7 31.5 5.2 120 FTG ---- PE 0.0 22.0 5.6 32.0 31.7 ñ•028 TL 14.00 PV 0.2 e PiPe: 120 -93.6 2.203 PL 9.34 PF 0.6 22.0 5.6 32.0 31.7 7.9 120 FTG ---- PE 0.0 22.0 5.6 32.6 32.0 0.061 TL 9.34 PV 0.4 6 .203/2Pipe: 121 -125.6 PL 14.00 PF 1.5 S3i/' 22.0 5.6 32.6 32.0 10.6 120 FTG ---- PE 0.0 22.0 4.1 32.7 0. lOS TL 14.00 PV 0.8 /epipe: 122 -158.3 p.203 PL 134.00 PF 24.9 S38/ 22.0 5.6 34.1 32.7 13.3 120 FTG 2ET PE 0.9 M3'5, 20.0 0.0 59.9 0.0.. 0.161 TL 15_4...6.5 PV 1.2 C",, //Pipe: 123 -87.4 e203 PL 26.00 PF 2.5 M4G/ 20.0 0.0 35.8 0.0 7.4 120 FTG 2ET PE -0.9 22.0 5.637.5 343 0.054 TL 4'V 0.4 //Pipe 22.0 124 -121.7 2.203 PL 195.50 PF 21.4 S 5.6 37.5 34.3 10.2 0 120 FTG 2ET PE 0.9 76 20.0 0.0 59 7 0.0 0.099 0.7 Pipe: 125 -113.0 2203 PL 221.50 PF 22.7 M47 20.0 0.0 37.0 0.0 9.5 //120 FTG 4E2T PE 0.0 'M37 20.0 0.0 59.7 0.0 4/086 TL 262.80 PV 0.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUB JOB TITLE: BUILDING A .45 CALC NOTES: Calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084. 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 0.052 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 22.0 ft/sec at pipe 30. 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 N Ell Tee LngEii ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N D Ell Tee LngEli ChkVlv BfyVlv GatVlv NPTee 45ELL 8.390 31.00 60.00 22.00 78.00 21.00 7.00 60.00 13.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Fèét (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 7.980 26.00. 50.00 19.00 50.00 17.00 4.00 50.00 PAGE: F MATERIAL: DYNAFL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D F Eli Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 45ELL FRLKL FP.LK45 FRLKT -------------------------------------------------------- 2.203 5.00 10.65 3.73 11.00 6.00 1.00 10.00 1.91 3.72 1.91 9.05 0.00 0.00 2.703 6.00 18.60 6.60 14.00 7.00 1.00 10.00 3.26 6.67 3.41 16.72 0.00 0.00 . 3.314 7.00 21.80 7.27 16.00 10.00 1.00 13.00 3.60 7.27 3.60 18.90 0.00 0.00 4.310 10.00 27.80 9.45 22.00 12.00 4.00 20.00 5.56 9.45 4.72 22.24 0.00 0.00 6.403 14.00 38.91 12.97 32.00 10.00 3.00 28.00 9.07 12.97 6.48 32.40 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\SUI JOB TITLE: BUILDING A .45 CALC WATER SUPPLY ANALYSIS Static: 125.00 psi Resid: 20.00 psi Flow: 5390.0 gpm LEGEND 1 Available pressure 106.66 psi @ 2099.0 gpm 2 Required pressure 94.43 psi @ 2099.0 gpm -14.71 I I I 1 I I 12C180C24003000 3600 4200 4800 5400 6000 FLOW (GPM) PRO-TECH FIRE PROTECTION 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 HYDRAULIC CALCULATIONS REMOTE ARE #1 FOR GREY HAWK BUSINESS PART&, LOT 801 NATIONAL S. 1,2,8 PHASE I BUILDING A CARLSBAD CA DATE: MAY 17, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: EXTRA HAZARD DENSITY:. 0.45 gpm/3000 sq. ft. AREA OF APPLICATION: . 3066 sq. ft. COVERAGE PER SPRINKLER: 88 SQ. FT. NUMBER OF SPRINKLERS CALCULATED: 39spr1nk1ers TOTAL SPRINKLER WATER FLOW REQUIRED: 1488 gpm TOTAL WATER REQUIRED (including hose): 1988 gpm FLOW AND PRESSURE (@ BOR): . 1488gpm @ 77 psi SPRINKLER ORIFICE SIZE: 3/4 inch NAME OF CONTRACTOR: PRO-TECH FIRE PROTECTION DESIGN/LAYOUT BY:PRO-TECH FIRE PROTECTION AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C16 HIC APPROV9 SUBMITTEL CARLS) E_ PARTMENT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1. DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLII( JOB TITLE: BUILDING A WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 109.0 104.0 1500.0 100.6 1988.6 91.8 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1988.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1488.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) Si 22.0 K=11.20 14.7 42.9 S2 . 22.0 K=11.20 13.9 41.7 S3 22.0 K=11.20 13.5 41.1 S4 22.0 K=11.20 13.4 41.0 S5 22.0 K=11.20 13.4 41.0 S6 22.0 K=11.20 13.5 41.1 S7 22.0 K=11.20 13.9 41.7 S8 22.0 K=11.20 14.7 43.0 S9 22.0 K=11.20 16.1 45.0 sio 22.0 K=11.20 14.4 42.6 Sib 22.0 K=11.20 13.6. 41.3 S12 22.0 K=11.20 13.2 40.6 S13 22.0 K=11.20 13.0 40.4 S14 22.0 K=11.20 13.0 40.4 S15 22.0 K=11.20 13.1 40.5 S16 22.0 K=11.20 13.4 41.0 S17 22.0 K=11.20 14.2 42.2 S18 22.0 K=11.20 15.5 44.0 S19 22.0 K=11.20 13.3 40.9 S20 22.0 K=11.20 12.1 39.0 S21 22.0 K=11.20 11.4 37.9 S22 22.0 K=11.20 11.1 37.3 S23 22.0 K=11.20 11.0 37.2 S24 22.0 K=11.20 17.4 46.7 S25 22.0 K=11.20 17.5 46.9 S26 22.0 K=11.20 18.0 47.5 S27 22.0 K=11.20 19.0 48.9 S28 22.0 K= 5.60 25.6 28.3 S29 22.0 K= 5.60 25.7 28.4 S30 22.0 K= 5.60 26.2 28.7 S31 22.0 K= 5.60 27.2 29.2 S32 22.0 K= 5.60 28.7 30.0 S33 22.0 K= 5.60 27.5 29.4 S34 22.0 K= 5.60 27.5 29.4 S35 22.0 K=5.60 27.6 29.4 S36 22.0 K= 5.60 28.0 29.6. S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) S37 22.0 K= 5.60 28.5 29.9 S38 22.0 K= 5.60 29.9 30.6 39 22.0 K= 5.60 32.7 32.0 S51 10.0 - - - - 47.0 - - - S52 10.0 - - - - 47.5 S53 10.0 - - - - 47.9 - - - S54 10.0 - - - - 48.3 S55 10.0 - - - - 48.8 S56 10.0 - - - - 49.2 S57 9.0 - - - - 47.4 - - - S58 9.0 - - - - 47.7 - - - S59 9.0 - - - - 48.1 S60 9.0 - --- 48.5 S61 9.0 - - - - 48.9 S62 9.0 - - - - 49.2 - - - S63 9.0 - - - - 46.2 - - - S64 9.0 - - - - 46.8 - - - S65 9.0 ---- 45.5 S66 9.0 - - - - 46.1 S67 9.0 - - - - 46.7 - - - S68 9.0 - - - - 47.3 - - - 5 10.0 - - - - 69.4 10 20.0 - - - - 60.0 - - - 71 10.0 - - - - 47.0 - - - 72 10.0 - - - - 47.3 - - - 73 10.0 - - - - 47.6 - - - 74 10.0 - - - - 48.1 75 10.0 - - - - 48.4 76 10.0 - - - - 48.7 77 10.0 - - - - 45.7 - - - 78 10.0 - - - - 46.3 - - - 79 10.0 - - - - 45.0 - - - 80 10.0 - - - - 45.7 81 10.0 - - - - 46.2 - - - 82 10.0 - - - - 46.9 Ml 10.0 - - - - 61.3 - - - M2 10.0 - - - - 60.8 - - - M3 10.0 - --- 59.6 M4 10.0 - - - - 59.1 - - - M5 10.0 - - - - 59.0 Mil 10.0 - - - - 43.4 M12 10.0 - - - - 43.3 - - - M13 10.0 - - - - 42.3 M14 10.0 - - - - 42.2 M14A 10.0 ---- 42.1 M21 10.0 - - - - 59.2 M21A 0.0 - - - - 63.5 - - - M22 10.0 - - - - 59.2 M23 10.0 - - - - 59.2 M31 20.0 - - - - 59.5 M32 20.0 - - - - 55.2 M33 20.0 - - - - 54.4 M34 20.0 - - - - 54.0 - - - M35 20.0 - - - - 53.9 M36 20.0 - - - - 53.8 M37 20.0 - - - - 53.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BL1C JOB TITLE: BUILDING A NODE ANALYSIS DATA (cont.) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) M41 20.0 - - - - 23.4 --- M42 20.0 - - - - 23.6 M43 20.0 - - - - 24.6 M44 20.0 - - - - 26.3 - - - M45 20.0 - - - - 28.6 - - - M46 20.0 - - - - 31.2 M47 20.0 - - - - 32.2 - - - M47A 20.0 - - - - 32.1 - - - M51 20.0 - - - - 55.0 --- M52 20.0 - - - - 54.9 - - - M53 20.0 - - - - 54.8 M54 20.0 - - - - 54.8 M54A 20.0 - - - - 54.8 M55 20.0 - - - - 54.8 M56 20.0 - - - - 54.7 M57 20.0 -.--- 54.7. BOR 1.0 - - - - 77.0 - - - DI -3.0 - - - - 79.9 UG1 -3.0 - - - - 90.6 - - - UG2 -3.0 HOSE STREAM 83.0 500.0 BF1 3.0 - - - - 87.3 - - - BF2 3.0 - - - - 82.3 SRC 0.0 SOURCE 91.8 1988.6 A SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A 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 1988.6 7.980 PL 34.00 PF 2.5 RC 0.0 SRCE 91.8 (N/A) 12.8 150 FTG ETG PE 1.3 UG1 -3.0 0.0 90.6 0.0 0.022 TL 114.00 PV 1.1 Pipe: 2 1988.6 8.390 PL 6.00 PF 0.7 UG1 -3.0 0.0 90.6 0.0 11.5 140 FTG E PE -2.6 BF1 3.0 0.0 87.3 . 0.0 0.019 TL 37.00 PV 0.9 Pipe: 3 FIXED PRESSURE LOSS DEVICE BF1 3.0 0.0 87.3 0.0 5.0 psi, 1988.6 gpm BF2 3.0 0.0 82.3 0.0 Pipe: 4 1988.6 8.390 PL 6.00 PF 1.9 BF2 3.0 0.0 82.3 0.0 11.5 140 FTG ET PE 2.6 UG2 -3.0 H.S. 83.0 500.0 0.019 TL 97.00 PV 0.9 Pipe: 5 1488.6 7.980 PL 228.00 PF 3.2 UG2 -3.0 H.S. 83.0 500.0 9.5 150 FTG L PE 0.0 DI -3.0 0.0 79.9 0.0 0.013 TL 247.00 PV 0.6 Pipe: 6 1488.6 8.390 PL 9.00 PF 1.2 DI -3.0 0.0 79.9 0.0 8.6 140 FTG 3E FE -1.7 BOR 1.0 0.0 77.0 0.0 0.011 TL 102.00 PV 0.5 Pipe: 7 1488.6 .4.310 PL 9.50 PF 3.7 BOR 1.0 0.0 77.0 0.0 32.7 120 FTG ---- . PE -3.9 5. 10.0 0.0 69.4 0.0 0.388 TL 9.50 PV 7.2 Pipe: 8 1121.4 4.31.0 PL 12.00 PF 5.0 5 10.0 0.0 69.4 0.0 24.7 120 FTG E PE -4.3 10 20.0 0.0 60.0 0.0 0.229 TL 22.00 PV 4.1 Pipe: 9 367.2 3.314 PL 41.00 PF 8.0 5 10.0 0.0 69.4 0.0 13.7 120 FTG 2ET PE 0.0 Ml 10.0 0.0 61.3 0.0 0.105 TL 76.80 PV 1.3 Pipe: 10 333.6 2.703 PL 2.50 PF 0.6 Ml 10.0 0.0 61.3 0.0 18.7 120 FTG ---- PE 0.0 M2 10.0 0.0 60.8 0.0 0.236 TL 2.50 PV 2.3 Pipe: 11 245.6 2.703 FL 8.50 PF 1.1 M2 10.0 0.0 60.8 0.0 13.7 120 FTG ---- PE 0.0 M3 10.0 0.0 59.6 0.0 Ô.134 TL 8.50 PV 1.3 Pipe: 12 161.5 2.703 PL 8.00 PF 0.5 M3 10.0 0.0 59.6 0.0 9.0 120 FTG ---- PE 0.0 M4 10.0 0.0 59.1 0.0 0.062 TL 8.00 PV 0.5 Pipe: 13 78.9 2.703 FL 8.50 PF 0.1 M4 10.0 0.0 59.1 0.0 4.4 120 FTG- ---- FE 0.0 M5 10.0 0.0 59.0 0.0 0.016 TL 8.50 PV 0.1 Pipe: 14 88.1 2.703 PL 6.25 PF 0.1 Mil 10.0 0.0 43.4 0.0 4.9 120 FTG ---- PE 0.0 M12 10.0 0.0 43.3 0.0 0.020 TL 6.25 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLI?( JOB TITLE: BUILDING A 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: 15 172.1 2.703 PL 13.92 PF 1.0 M12 10.0 0.0 43.3 0.0 9.6 120 FTG ---- PE 0.0 M13 10.0 0.0 42.3 0.0 0.069 TL 13.92 PV 0.6 Pipe: 16 258.9 2.703 PL 1.50 PF 0.2 M13 10.0 0.0 42.3 0.0 14.5 120 FTG ----- PE 0.0 M14A 10.0 0.0 42.1 0.0 0.148 TL 1.50 PV 1.4 Pipe: 16A -86.8 2.703 PL 6.33 PF 0.1 M14A 10.0 0.0 42.1 0.0 4.9 120 FTG ---- PE 0.0 M14 10.0 0.0 42.2 0.0 0.020 TL 6.33 PV 0.2 Pipe: 16b 345.7 3.314 PL 16.83 PF 5.7 M14A 10.0 0.0 42.1 0.0 12.9 120 FTG 2T PE -4.3 M47A 20.0 0.0 32.1 0.0 0.094 TL 60.43 PV 1.1 Pipe: 160 -21.5 2.703 PL 3.67 PF 0.0 M21A 0.0 0.0 63.5 0.0 1.2 120 FTG T PE -4.3 M21 10.0 0.0 59.2 0.0 0.001 TL 22.27 PV 0.0 Pipe: 17 12.0 2.703 PL 9.25 PF 0.0 M21 10.0 0.0 59.2 0.0 0.7 120 FTG ---- PE 0.0 M22 10.0 0.0 59.2 0.0 0.001 TL 9.25 PV 0.0 Pipe: 17A 21.5 2.703 PL 11.50 PF 0.0 M21A 0.0 0.0 63.5 0.0 1.2 120 FTG T PE -8.7 M54A. 20.0 0.0 54.8 0.0 0.001 TL 30.10 PV 0.0 Pipe: 18 12.0 2.703 PL 18.00 PF 0.0 M22 10.0 0.0 59.2 0.0 0.7 120 FTG 3ET PE 0.0 M23 10.0 0.0 59.2 0.0 0.001 TL 54.60 PV 0.0 Pipe: 19 268.8 4.310 PL 1.42 PF 0.5 10 20.0 0.0 60.0 0.0 5.9 120 FTG T PE 0.0 M31 20.0 0.0 59.5 0.0 0.016 TL 29.22 PV 0.2 Pipe: 20 852.6 4.310 PL 6.58 PF 4.8 10 20.0 0.0 60.0 0.0 18.7 120 FTG T PE 0.0 M32 20.0 0.0 55.2 0.0 0.138 TL 34.38 PV 2.4 Pipe: 21 637.1 4.310 PL 11.00 PF 0.9 M32 20.0 0.0 55.2 0.0 14.0 120 FTG ---- PE 0.0 M33 20.0 0.0 54.4 0.0 0.081 TL 11.00 PV 1.3 Pipe: 22 461.6 4.310 PL 8.50 PF 0.4 M33 20.0 0.0 54.4 0.0 10.2 120 FTG ---- PE 0.0. M34 20.0 0.0 54.0 0.0 0.044 TL 8.50 PV 0.7 Pipe: 23 324.4 4.310 PL 3.50 PF 0.1 M34 .20.0 0.0 54.0 0.0 7.1 120 FTG ---- PE 0.0 M35 20.0 0.0 53.9 0.0 0.023 TL 3.50 PV 0.3 Pipe: 24 190.7 4.310 PL 12.00 PF 0.1 M35 20.0 0.0 53.9 0.0 4.2 120 FTG ---- PE 0.0 M36 20.0 0.0 53.8 0.0 0.009 TL 12.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLDC JOB TITLE: BUILDING A 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 91.7 4.310 PL 12.00 PF 0.0 M36 20.0 0.0 53.8 0.0 2.0 120 FTG ---- PE 0.0 M37 20.0 0.0 53.8 0.0 0.002 TL 12.00 PV 0.0 Pipe: 26 -165.7 3.314 PL 8.00 PF 0.2 M41 20.0 0.0 23.4 0.0 6.2 120 FTG ---- PE 0.0 M42 20.0 0.0 23.6 0.0 0.024 TL 8.00 PV 0.3 Pipe: 27 -335.9 3.314 PL 11.00 PF 1.0 M42 20.0 0.0 23.6 0.0 12.5 120 FTG ---- PE 0.0 M43 20.0 0.0 24.6 0.0 0.089 TL 11.00 PV 1.1 Pipe: 28 -528.2 3.314 PL 8.50 PF 1.7 M43 20.0 0.0 24.6 0.0 19.6 120 FTG ---- PE 0.0 M44 20.0 0.0 26.3 0.0 0.205 TL 8.50 PV 2.6 Pipe: 29 -515.5 3.314 PL 11.58 PF 2.3 M44 20.0 0.0 26.3 0.0 19.2 120 FTG ---- PE 0.0 M45 20.0. 0.0 28.6 0.0 0.196 TL 11.58 PV 2.5 Pipe: 30 -541.7 3.314 PL 11.83 PF . 2.5 M45 20.0 0.0 28.6 0.0 20.1 120 FTG ---- PE 0.0 M46 20.0 0.0 31.2 0.0 0.215 TL 11.83 PV 2.7 Pipe: 30A -455.7 3.314 PL 6.00 PF 0.9 M46 20.0 0.0 31.2 0.0 17.0 120 FTG ---- PE 0.0 M47A 20.0 0.0 32.1 0.0 0.156 TL 6.00 PV 1.9 Pipe: 30B -110.1 3.314 PL 6.00 PF 0.1 M47A 20.0 0.0 32.1 0.0 4.-1 1.20 FTG ---- PE 0.0 M47 20.0 0.0 32.2 0.0 0.011 TL 6.00 PV 0.1 Pipe: 31 56.0 3.314 PL 8.00 PF. 0.0 M51 20.0 0.0 55.0 0.0 2.1 120 FTG ---- PE 0.0 M52 20.0 0.0 54.9 0.0 0.003 TL 8.00 PV 0.0 Pipe: 32 68.7 3.314 PL 13.75 PF 0.1 M52 20.0 0.0 54.9 0.0 2.6 120 FTG 2E PE 0.0 M53 20.0 0.0 54.8 0.0 0.005 TL 27.75 PV 0.0 Pipe: 33 54.2 3.314 PL 8.58 PF 0.0 M53 20.0 0.0 54.8 0.0 2.0 120 FTG ---- PE 0.0 M54 20.0 0.0 54.8 0.0 0.003 TL 8.58 PV 0.0 Pipe: 33A -21.5 3.314 PL 10.33 PF 0.0 M54 20.0 0.0 54.8 0.0 0.8 120 FTG T PE 0.0 M54A 20.0 0.0 54.8 0.0 0.001 TL 32.13 PV 0.0 Pipe: 34 55.7 3.314 PL 3.42 PF 0.0 M54 20.0 0.0 54.8 0.0 2.1 120 FTG ---- PE 0.0 M55 20.0 0.0 54.8 0.0 0.003 TL 3.42 PV 0.0 Pipe: 35 37.3 3.314 PL 12.00 PF 0.0 M55 20.0 0.0 54.8 0.0 1.4 120 FTG ---- PE 0.0 M56 20.0 0.0 54.7 0.0 0.002 TL 12.00 PV 0.0 r SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A 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: 36 18.3 3.314 PL 12.00 PF 0.0 M56 20.0 0.0 54.7 0.0 0.7 120 FTG ---- PE 0.0 M57 20.0 0.0 54.7 0.0 0.000 TL 12.00 PV 0.0 Pipe: 37 33.6 2.203 PL 159.50 PF 2.1 Ml 10.0 0.0 61.3 0.0 2.8 120 FTG 7E2T PE 0.0 M21 10.0 0.0 59.2 0.0 0.009 TL 234.51 PV 0.1 Pipe: 38 -4.2 2.203 PL 193.00 PF 0.0 M4 10.0 0.0 59.1 0.0 0.4 120 FTG 4E2T PE 0.0 M23 10.0 0.0 59.2 0.0 0.000 TL 247.55 PV 0.0 Pipe: 39 . -7.9 2.203 PL 211.34 PF 0.2 MS 10.0 0.0 59.0 0.0 0.7 120 FTG 5E4T PE 0.0 M23 10.0 0.0 59.2 0.0 0.001 TL 299.99 PV 0.0 Pipe: 40 -88.1 2.203 PL 26.00 PF 3.6 Mil 10.0 0.0 43.4 0.0 7.4 120 FTG 4ET PE 0.0 S51 10.0 0.0 47.0 0.0 0.054 TL 66.92 PV 0.4 Pipe: 41 -88.1 2.203 PL 8.00 PF 0.4 S51 10.0 0.0 47.0 0.0 7.4 120 FTG ---- PE 0.0 S52 10.0 0.0 47.5 0.0 0.054 TL 8.00 PV 0.4 Pipe: 42 -88.1. 2.203 PL 8.00 PF 0.4 S52 10.0 0.0 47.5 0.0 7.4 120 FTG ---- PE 0.0 S53 10.0 0.0 47.9 0.0 0.054 TL 8.00 PV 0.4 Pipe: 43 -88.1 2.203 PL 8.00 PF 0.4 S53 10.0 0.0 47.9 0.0 7.4 120 FTG ---- PE 0.0 S54 10.0 0.0 48.3 0.0 0.054 TL 8.00 PV 0.4 Pipe: 44 -88.1 2.203 PL 8.00 PF 0.4 S54 10.0 0.0 48.3 0.0 7.4 120 FTG ---- PE 0.0 S55 10.0 0.0 48.8 0.0 0.054 TL 8.00 PV 0.4 Pipe: 45 -88.1 2.203 PL 8.00 PF 0.4 S55 10.0 0.0 48.8 0.0 7.4 120 FTG ---- PE 0.0 S56 10.0 0.0 49.2 0.0 0.054 TL 8.00 PV 0.4 Pipe: 46 -88.1 2.203 PL 184.67 PF 11.5 S56 10.0 0.0 49.2 0.0 7.4 120 FTG 2ET PE 0.0 M2 10.0 0.0 60.8 0.0 0.054 TL 211.95 PV 0.4 Pipe: 47 -84.1 2.203 PL 34.00 PF 3.7 M12 10.0 0.0 43.3 0.0 7.1 120 FTG 4ET PE 0.0 71 10.0 0.0 47.0 0.0 0.050 TL 74.92 PV 0.3 Pipe: 48 -84.1 2.203 PL 5.92 PF 0.3 71 10.0 0.0 47.0 0.0 7.1 120 FTG ---- PE 0.0 72 10.0 0.0 47.3 0.0 0.050 TL 5.92 PV 0.3 Pipe: 49 -84.1 2.203 PL 6.42 PF 0.3 72 10.0 0.0 47.3 0.0 7.1 120 FTG ---- PE 0.0 73 10.0 0.0 47.6 0.0 0.050 TL 6.42 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( TOB TITLE: BUILDING A 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: 50 -84.1 2.203 PL 8.75 PF 0.4 73 10.0 0.0 47.6 0.0 7.1 120 FTG ---- PE 0.0 74 10.0 0.0 48.1 0.0 0.050 TL 8.75 PV 0.3 Pipe: 51 =84.1 2.203 PL 7.42 PF 0.4 74 10.0 0.0 48.1 0.0 7.1 120 FTG ---- PE 0.0 75 10.0 0.0 48.4 0.0 0.050 TL 7.42 PV 0.3 Pipe: 52 -84.1 2.203 PL 6.08 PF 0.3 75 10.0 0.0 48.4 0.0 7.1 120 FTG ---- PE 0.0 76 10.0 0.0 48.7 0.0 0.050 TL 6.08 PV 0.3 Pipe: 53 -84.1 2.203 PL 190.42 PF 10.9 76 10.0 0.0 48.7 0.0 7.1 120 FTG 2ET PE 0.0 M3 10.0 0.0 59.6 0.0 0.050 TL 217.70 PV 0.3 Pipe: 54 -86.8 2.203 PL 37.67 PF 3.4 M13 10.0 0.0 42.3 0.0 7.3 120 FTG 2ET PE 0.0 77 10.0 0.0 45.7 0.0 0.053 TL 64.95 PV 0.4 Pipe: 55 -86.8 2.203 PL 11.50 PF 0.6 77 10.0 0.0 45.7 0.0 7.3 120 FTG ---- PE 0.0 78 10.0 0.0 46.3 0.0 0.053 TL 11.50 PV 0.4 Pipe: 56 -86.8 2.203 PL 200.17 PF 12.8 78 10.0 0.0 46.3 0.0 7.3 120 FTG 4ET PE 0.0 M4 10.0 0.0 59.1 0.0 0.053 TL 241.09 PV 0.4 Pipe: 57 -86.8 2.203 PL 26.17 PF 2.8 M14 10.0 0.0 42.2 0.0 7.3 120 FTG 2ET PE 0.0 79 10.0 0.0 45.0 0.0 0:053 TL 53.45 PV 0.4 Pipe: 58 -86.8 2.203 PL 12.00 PF 0.6 79 10.0 0.0 45.0 0.0 7.3 120 FTG ---- PE 0.0 80 10.0 0.0 45.7 0.0 0.053 TL 12.00 PV 0.4 Pipe: 59 -86.8 2.203 PL 10.50 PF 0.6 80 10.0 0.0 45.7 0.0 7.3 120 FTG ---- PE 0.0 81 10.0 0.0 46.2 0.0 0.053 TL 10.50 PV 0.4 Pipe: 60 -86.8 2.203 PL 12.00 PF 06 81 10.0 0.0 46.2 0.0 7.3 120 FTG ---- PE 0.0 82 10.0 0.0 46.9 0.0 0.053 TL 12.00 PV 0.4 Pipe: 61 -86.8 2.203 PL 188.00 PF 12.1 82 10.0 0.0 46.9 0.0 7.3 120 FTG 4ET PE 0.0 M5 10.0 0.0 59.0 0.0 0.053 TL 228.92 PV 0.4 Pipe: 62 0.0 1.049 PL 3.50 PF 0.0 71 10.0 0.0 47.0 0.0 0.0 120 FTG 2ET PE 0.4 557 9.0 0.0 47.4 0.0 0.000 TL 12.50 PV 0.0 Pipe: 63 0.0 1.049 PL 1.00 PF 0.0 72 10.0 0.0 47.3 0.0 0.0 120 FTG T PE 0.4 S58 9.0 0.0 47.7 0.0 0.000 TL 6.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BL(. JOB TITLE: BUILDING A 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: 64 0.0 1.049 PL 3.50 PF 0.0 73. 10.0 0.0 47.6 0.0 0.0 120 FTG 2ET PE 0.4 S59 9.0 0.0 48.1 0.0 0.000 TL 12.50 PV 0.0 Pipe: 65 0.0 1.049 PL 3.50 PF 0.0, 74 10.0 0.0 48.1 0.0 0.0 120 FTG 2ET PE 0.4 S60 9.0 0.0 48.5 0.0 0.000 TL 12.50 PV 0.0 Pipe: 66 0.0 1.049 PL 1.00 PF 0.0 75 10.0 0.0 48.4 0.0 0.0 120 FTG T PE 0.4 S61 9.0 0.0 48.9 0.0 0.000 TL 6.00 PV 0.0 Pipe: 67 . 0.0 1.049 PL 3.50 PF 0.0 76 10.0 0.0 48.7 0.0 0.0 120 FTG 2ET PE 0.4 S62 .9.0 0.0 49.2 0.0 0.000 TL 12.50 PV 0.0 Pipe: 68 0.0 1.049 PL 3.50 PF 0.0. 77 10.0 0.0 45.7 0.0 0.0 120 FTG 2ET PE 0.4 S63 9.0 0.0 46.2 0.0 0.000 TL 12.50 PV 0.0 Pipe: 69 0.0 1.049 PL 3.50 PF 0.0 78 10.0 0.0 46.3 0.0 0.0 120 FTG 2ET PE 0.4 S64 9.0 0.0 46.8 0.0 . 0.000 TL 12.50 PV 0.0 Pipe: 70 0.0 1.049 PL 3.00 PF 0.0 79 10.0 0.0 45.0 0.0 0.0 120 FTG 2ET PE 0.4 S65 9.0 0.0 45.5 0.0 0.000 TL 12.00 PV 0.0 Pipe: 71 0.0 1.049 PL 1.00 PF 0.0 80 10.0 0.0 45.7 0.0 0.0 120 FTG T PE 0.4 S66 9.0 0.0 46.1 0.0 0.000 TL 6.00 PV 0.0 . . . Pipe: 72 0.0 1.049 PL 1.00 PF 0.0 81 10.0 0.0 46.2 0.0 0.0 120 FTG T PE 0.4 S67 9.0 0.0 46.7 0.0 0.000 TL 6.00 PV 0.0 Pipe: 73 0.0 1.049 PL 3.00 PF 0.0 82 10.0 .0.0 46.9 0.0 0.0 120 FTG T PE 0.4 S68 9.0 0.0 47.3 0.0 0.000 TL 8.00 PV 0.0 Pipe: 74 56.0 2.203 PL 127.50 PF 4.6 M31 20.0 0.0 59.5 0.0 4.7 120 FTG 9E2T PE 0.0 M51. 20.0 0.0 55.0 0.0 0.024 TL 193.80 PV 0.1 Pipe: 75 12.7 2.203 PL 143.50 PF 0..3 M32 20.0 0.0 55.2 0.0 1.1 120 FTG 9E2T PE 0.0 M52 20.0 0.0 54.9 0.0. 0.002 TL 209.80 PV 0.0 Pipe: 76 -14.5 2.203 PL 162.75 PF 0.4 M33 20.0 0.0 54.4 0.0 1.2 120 FTG 9E2T PE 0.0 M53 20.0 0.0 54.8 0.0 0.002 TL 229.05 PV 0.0 Pipe: 77 -20.0 2.203 PL 180.00 PF 0.8 M34 20.0 0.0 54.0 0.0 1.7 120 FTG 5E2T PE 0.0 M54 20.0 0.0 54.8 0.0 0.004 TL 226.30 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A 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: 78 -18.5 2.203 PL 187.00 PF 0.9 M35 20.0 0.0 53.9 0.0 1.6 120 FTG 9E5T PE 0.0 M55 20.0 0.0 54.8 0.0 0.003 TL 285.25 PV 0.0 Pipe: 79 -19.0 2.203 PL 211.00 PF 0.9 M36 20.0 0.0 53.8 0.0 1.6 120 FTG 9E4T PE 0.0 M56 20.0 0.0 54.7 0.0 0.003 TL 298.60 PV 0.0 Pipe: 80 -18.3 2.203 PL 237.00 PF 1.0 M37 20.0 0.0 53.8 0.0 1.5 120 FTG 9E4T PE 0.0 M57 20.0 0.0 54.7 0.0 - 0.003 TL 324.60 PV 0.0 -Pipe: 81 165.7 2.203 PL 24.50 PF 7.9 M41 20.0 0.0 23.4 0.0 13.9 120 FTG 2ET PE -0.9 Si 22.0 11.2 14.7 42.9 0.175 TL 45.15 PV 1.3 Pipe: 82 122.8 2.203 PL 8.00 PF 0.8 Si 22.0 11.2 14.7 42.9 10.3 120 FTG ---- PE 0.0 S2 22.0 11.2 13.9 41.7 0.101 TL 8.00 PV 0.7 Pipe: 83 . 81.1 2.203 PL 8.00 PF 0.4 S2 22.0 11.2 13.9 41.7 6.8 120 FTG ---- PE 0.0 S3 22.0 11.2 13.5 41.1 0.047 TL 8.00 PV 0.3 Pipe: 84 40.0 2.203 PL 8.00 PF 0.1 S3 22.0 11.2 13.5 41.1 3.4 120 FTG ---- PE 0.0 S4 22.0 11.2 13.4 41.0 0.013 TL 8.00 PV 0.1 Pipe: 85 -1.0 2.203 PL 8.00 PF 0.0 S4 22.0 11.2 13.4 41.0 0.1 120 FTG ---- PE 0.0 S5 22.0 11.2 13.4 41.0 0.000 TL 8.00 PV 0.0. Pipe: 86 -42.0 2.203 PL 8.00 PF 0.1 S5 - 22.0 11.2 13.4 41.0 3.5 120 FTG ---- PE 0.0 S6 22.0 11.2 13.5. 41.1 0.014 TL 8.00 PV 0.1 Pipe: 87 -83.1 2.203 PL 8.00 PF 0.4 S6 22.0 11.2 13.5 41.1 7.0 120 FTG ---- PE 0.0 S7 22.0 11.2 13.9 41.7 0.049 TL 8.00 PV 0.3 Pipe: 88 -124.8 2.203 PL 8.00 PF 0.8 S7 22.0 11.2 13.9 41.7 10.5 120 FTG ---- PE 0.0 S8 22.0 11.2 14.7 43.0 0.104 TL 8.00 PV 0.7 Pipe: 89 -167.8 2.203 PL 8.00 PF 1.4 S8 22.0 11.2 14.7 43.0 14.1 120 FTG ---- PE 0.0 S9 22.0 11.2 16.1 45.0 0.179 TL 8.00 PV 1.3 Pipe: 90 -212.8 2.203 PL 132.00 PF 42.5 S9 22.0 11.2 16.1 45.0 17.9 120 FTG 2ET PE 0.9 M31 20.0 0.0 59.5 0.0 0.278 TL 152.65 PV 2.2 Pipe: 91 170.2 2.203. PL 24.50 PF 8.3 M42 20.0 0.0 23.6 0.0 14.3 120 FTG 2ET PE -0.9 S1O 22.0 11.2 14.4 42.6 0.184 TL 45.15 PV 1.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLDC JOB TITLE: BUILDING A 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: 92 . 127.7 2.203 PL 8.00 PF 0.9 Slo 22.0 11.2 14.4 42.6 10.7 120 FTG ---- PE 0.0 s11 22.0 11.2 13.6 .41.3 0.108 TL 8.00 PV 0.8 Pipe: 93 86.4 2.203 FL 8.00 PF 0.4 Sil 22.0 11.2 13.6 41.3 7.3 120 FTG ---- PE 0.0 S12 22.0 11.2 13.2 40.6 0.053 TL 8.00 PV 0.4 Pipe: 94 45.8 2.203 PL 8.00 PF 0.1 S12 22.0 11.2 13.2 40.6 3.9 120 FTG ---- PE 0.0 S13 22.0 11.2 13.0 40.4 0.016 TL 8.00 PV 0.1 Pipe: 95 5.3 2.203 PL 8.00 PF 0.0 S13 22.0 11.2 13.0 40.4 0.4 120 FTG ---- PE 0.0 S14 22.0 11.2 13.0 40.4 0.000 TL 8.00 PV 0.0 Pipe: 96 . -35.1 2.203 PL 8.00 PF 0.1 S14 22.0 11.2 13.0 40.4 3.0 120 FTG ---- PE 0.0 S15 22.0 11.2 13.1 40.5 0.010 TL 8.00 PV 0.1 Pipe: 97 -75..6 2.203 PL 8.00 PF 0.3 S15 . 22.0 11.2 13.1 40.5 6.4 120 FTG ---- PE 0.0 S16 22.0 11.2 13.4 41.0 0.041 TL. 8.00 PV 0.3 Pipe: 98 -116.7 2.203 PL 8.00 PF. 0.7 S16 22.0 11.2 13.4 41.0 9.8 120 FTG ---- PE 0.0 S17 22.0 11.2 14.2 42.2 0.092 TL 8.00 PV 0.6 Pipe: 99 -158.8 2.203 PL 8.00 PF 1.3 S17 . 22.0 11.2 14.2 42.2 13.4 120 FTG ---- PE 0.0. S18 22.0 11.2 15.5 44.0 0.162 TL 8.00 PV 1.2 Pipe: 100 -202.9 2.203 PL 132.00 PF 38.9 S18 22.0 11.2 15.5 44.0 17.1 120 FTG 2ET FE 0.9 M32 20.0 0.0 55.2 0.0 0.255 TL.152.65 PV 2.0 Pipe: 101 192.3 2.203 PL 24.50 PF 10.4 M43 20.0 0.0 24.6 0.0 16.2 120 FTG 2ET PE -0.9 S19 22.0 11.2 13.3 40.9 0.231 TL 45.15 PV 1.8 Pipe: 102 151.4 2.203 PL 8.00 PF 1.2 S19 22.0 11.2 13.3 40.9 12.7 120 FTG ---- PE 0.0 S20 22.0 11.2 12.1 39.0 0.148 TL 8.00 PV 1.1 Pipe: 103 112.4 2.203 PL 8.00 PF 0.7 S20 22.0 11.2 12.1 39.0 9.5 120 FTG ---- FE 0.0 S21 22.0 11.2 11.4 37.9 0.086 TL 8.00 PV 0.6 Pipe: 104 74.5 2.203 PL 8.00 PF 0.3 S21 22.0 11.2 11.4 37.9 6.3 120 FTG ---- PE 0.0 S22 22.0 11.2 11.1 37.3 0.040 TL 8.00 PV 0.3 Pipe: 105 37.2 2.203 PL 8.00 PF 0.1 S22 22.0 11.2 11.1 37.3 3.1 120 FTG ---- PE 0.0 S23 22.0 11.2 11.0 37.2 0.011 TL 8.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page -12 pATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A 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: 106 -46.7 2.203 PL 8.00 PF 0.1 S24 22.0 11.2 17.4 46.7 3.9 120 FTG ---- PE 0.0 S25 22.0 11.2 17.5 46.9 0.017 TL 8.00 PV 0.1 Pipe: 107 -93.6 2.203 PL 8.00 PF 0.5 S25 22.0 11.2 17.5 46.9 7.9 120 FTG ---- . PE 0.0 S26 22.0 11.2 18.0 47.5 0.061 TL 8.00 PV 0.4 Pipe: 108 -141.1 2.203 PL 8.00 PF 1.0 S26 22.0 11.2 18.0 47.5 11.9 120 FTG ---- PE 0.0 S27 22.0 11.2 19.0 489 0.130 TL 8.00 PV 0.9 Pipe: 109 . -189.9 2.203 PL 132.00 PF 34.5 S27 22.0 11.2 19.0 48.9 16.0 120 FTG 2ET PE 0.9 M33 20.0 0.0 54.4 0.0 0.226 TL 152.65 PV 1.7 Pipe: 110 -12.6 2.203 PL 32.00 PF 0.1 M44 20.0 0.0 26.3 0.0 1.1 120 FTG 2ET PE -0.9 S28 22.0 5.6 25.6 28.3 0.002 . TL 52.65 PV 0.0 Pipe: 111 -41.0 2.203 PL 14.00 PF 0.2 S28 22.0 5.6 25.6 28.3 3.4 120 FTG ---- PE 0.0 S29 22.0 5.6 25.7 28.4 0.013 TL 14.00 PV 0.1 Pipe: 112 -69.4 2.203 PL 14.00 PF 0.5 S29 22.0 5.6 25.7 28.4 5.8 120 FTG ---- PE 0.0 S30 22.0 5.6 26.2 28.7 0.035 TL 14.00 PV 0.2 Pipe: 113 -98.1 2.203 PL 14.00 PF 0.9 S30 22.0 5.6 26.2 28.7 8.3 120 FTG ---- PE 0.0 S31 22.0 5.6 27.2 29.2 0.066 TL 14.00 PV 0.5 Pipe: 114 -127.2 2.203 PL .14.00 PF 1.5 S31 22.0 5.6 27.2 29.2 10.7 120 FTG ---- PE 0.0 S32 22.0 5.6 28.7 30.0 0.108 TL 14.00 PV 0.8 Pipe: 115 -157.2 2.203 PL 133.00 PF 24.4 S32 22.0 5.6 28.7 30.0 13.2 120 FTG 2ET PE 0.9 M34 20.0 0.0 54.0 0.0 0.159 TL 153.65 PV 1.2 Pipe: 116 26.2 2.203 PL 26.00 PF 0.3 M45 20.0 0.0 28.6 0.0 2.2 120 FTG 2ET PE -0.9 S33 22.0 5.6 27.5 29.4 0.006 TL 46.65 PV 0.0 Pipe: 117 . -3.2 2.203 PL 14.00 PF 0.0 S33 22.0 5.6 27.5 29.4 0.3 120 FTG ---- PE 0.0 S34 22.0 5.6 27.5 29.4 0.000 TL 14.00 PV 0.0 Pipe: 118 -32.6 2.203 PL 10.00 PF 0.1 S34 22.0 5.6 27.5 29.4 2.7 120 FTG ---- PE 0.0 S35 22.0 5.6 27.6 29.4 0.009 TL 10.00 PV 0.1 Pipe: 119 -62.0 2.203 PL 14.00 PF 0.4 S35 22.0 5.6 27.6 29.4 5.2 120 FTG ---- PE 0.0 S36 22.0 5.6 28.0 29.6 0.028 TL 14.00 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( JOB TITLE: BUILDING A 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: 120 -91.6 2.203 PL 9.34 PF 0.5 S36 22.0 5.6 28.0 29.6. 7.7 120 FTG ---- PE 0.0 S37 22.0 5.6 28.5 29.9 0.059 TL 9.34 PV 0.4 Pipe: 121 -121.5 2.203 PL 14.00 PF 1.4 S37 22.0 5.6 28.5 29.9 10.2 120 FTG ---- PE 0.0 S38 22.0 5.6 29.9 30.6 0.099 TL 14.00 PV. 0.7 Pipe: 122 -152.1 2.203 PL 134.00 PF 23.1 S38 22.0 5.6 29.9 30.6 12.8 120 FTG 2ET PE 0.9 M35 20.0 0.0 53.9 0.0 0.150 TL 154.65 PV 1.1 Pipe: 123 -85.9 2.203 PL 26.00 PF •2.4 M46 20.0 0.0 31.2 0.0 7.2 120 FTG 2ET PE -0.9 S39 22.0 5.6 32.7 32.0 0.052 TL 46.65 PV 0.4 Pipe: 124 -118:0 2.203 PL 195.50 PF 20.2 S39 22.0 5.6 32.7 32.0 9.9 120 FTG 2ET PE 0.9 M36 20.0 0.0 53.8 0.0 0.094 TL 216.15 PV 0.7 Pipe: 125 -110.1 .2.203 PL 221.50 PF 21.6 M47 20.0 0.0 32.2 0.0 9.3 120 FTG 4E2T PE 0.0 M37 20.0 0.0 53.8 0.0 0.082 TL 262.80 PV 0.6 NOTES: Calculations were performed by the HASS 7.3 computer program under license no. 4904076910 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.089 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 32.7 ft/sec at pipe 7. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BLD( 'JOB TITLE: BUILDING A PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee .2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 13.64 13.64 PAGE: A MATERIAL: S40 HWC: 120 - Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEil ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N D Eli Tee LngEil ChkVlv BfyVlv GatVlv NPTee 45ELL 8.390 31.00 60.00 22.00 78.00 21.00 7.00 60.00 13.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEil ChkVlv BfyVlv GatVlv NPTee 7.980 26.00 50.00 19.00 50.00 17.00 4.00 50.00 PAGE: F MATERIAL: DYNAFL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D F Eli Tee LNGELL CHKVLV BFYVLV GATVLV ALMCHK 45ELL FRLKL -------------------------------------------------------- FRLK45 FRLKT 2.203 5.00 10.65 3.73 11.00 6.00 1.00 10.00 1.91 3.72 1.91 9.05 0.00 0.00. 2.703 6.00 18.60 6.60 14.00 7.00 1.00 10.00 3.26 6.67 3.41 16.72 0.00 0.00 3.314 7.00 21.80 7.27 16.00 10.00 1.00 13.00 3.60 7.27 3.60 18.90 0.00 0.00 4.310 10.00 27.80 9.45 22.00 12.00 4.00 20.00 5.56 9.45 4.72 22.24 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. A\BL( JOB TITLE: BUILDING A WATER SUPPLY ANALYSIS Static.: 109.00 psi Resid: 104.00 psi Flow: 1500.0 gpm LEGEND 1 Available pressure 100.58 psi @ 1988.6 gpm 2J 2 Required pressure 91.79 psi @ 1988.6 gpm 400600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)