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HomeMy WebLinkAbout3132 TIGER RUN CT; ; AS0701846/27/24,3:41 PM AS070184 Permit Data City of Carlsbad Sprinkler Permit Job Address: 3132 TIGER RUN CT Permit Type: SPRINK Parcel No: 2210140400 Lot #: 0 Reference No.: Permit No: AS070184 Status: ISSUED Applied 7/12/2007 Approved: 7/12/2007 Issued: 7/12/2007 PC #: Inspector: Project Title: GREYHAWK BUSINESS PARK THREE FIRE SPRINKLER INSPECTIONS @ $62/EA Applicant: Owner: PRO-TECH FIRE PROTECTION SYSTEMS PALOMAR MELROSE L L C CORP C/O ARNEL DEVELOPMENT SUITE G 949 S COAST DR #600 179 ROYMAR RD. COSTA MESA CA OCEANSIDE, CA 760-722-2455 Fees_($)J AddhI Fees jTo tal I Balance ($) _ 0 186 0 about:blarik 1/1 PRO-TECH FIRE PROTECTION APPROVED BMITT 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 CARLSBAD PA T1E HYDRAULIC CALCULATIONS REMOTE ARE #1 FOR GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I BUILDING G CARLSBAD CA DATE: June 28, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: EXTRA HAZARD DENSITY: 0.45 gpm/3000 sq. ft. AREA OF APPLICATION: 3021 sq. ft. COVERAGE PER SPRINKLER: 85 SQ. FT. NUMBER OF SPRINKLERS CALCULATED: 45 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 1839.1 gpm TOTAL WATER REQUIRED (including hose) : 2339.1 gpm FLOW AND PRESSURE (@ BOR): 1839.1 gpm @ 71.8 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 709152 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/28/2001C:\bWG\FIRE SPRINKLER\JOBS IN PROGRESS\PAIOMAR FORUM\SEFP\C,ALCS\BLDG. G\6-2 JOE TITLE: building g - .45 - WATER SUPPLY DATA SOURCE STATIC RESID. NODE PRESS. PRESS. @ TAG (PSI) (PSI) SRC 125.0 20.0 AGGREGATE FLOW ANALYSIS: FLOW AVAIL. TOTAL REQ'D PRESS. 8 DEMAND PRESS. (GPM) (PSI) (GPM) (PSI) 5390.0 102.6 2339.2 87.7 TOTAL FLOW AT SOURCE . 2339.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1839.2 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT2) (GPM/FT-2) Si 16.2 K=11.20 13.8 41.5 80.0 0.450 0.519 S2 16.2 K=11.20 13.5 41.1 80.0 0.450 0.514 S3 16.2 K=11.20 13.4 40.9 80.0 0.450 0.512 S4 16.2 K=11.20 12.8 40.0 80.0 0.450 0.500 S5 16.2 K=11.20 12.8 40.0 80.0 0.450 0.500 S6 16.2 K=11.20 12.8 40.1 80.0 0.450 0.501 S7 16.2 K=11.20 14.2 42.3 80.0 0.450 0.528 S8 16.2 K=11.20 14.5 42,7 80.0 0.450 0.533 S9 16.2 K=11.20 15.0 43.3 80.0 0.450 0.542 S1O 16.2 K=11.20 15.7 44.4 80.0 0.450 0.554 Sli 16.2 K=11.20 19.4 49.4 80.0 0.450 0.617 S12 17.0 K=11.20 12.2 39.1 80.0 0.450 0-.488 S13 17.0 K=11.20 11.7 38.4 80.0 0.450 0,479 - S14 17.0 K=11.20 11.5 37.9 80.0 0.450 0.474 S15 17.0 K=11.20 11.2 37.4 83.0 0.450 0.451 S16 17.0 K=11.20 11.1 37.3 83.0 0.450 0.450 S17 17.0 K=11.20 11.1 37.4 80.0 0.450 0.467 S18 17.0 K=11.20 11.2 37.4 80.0 0,450 0.468 S19 17.0 K=11.20 11.4 37.8 80.0 0.450 0.473 S20 17.0 K=11.20 11.6 38.2 800 0.450 0.477 S21 17.0 K=11.20 12.0 38.8 80.0 0.450 0.485 S22 17.0 K=11.20 12.6 39.7 80.0 0.450 0.497 S23 17.0 K=11.20 15.5 44.1 80.0 0.450 0.552 523A 17.0 K=11.20 17.3 46.5 80.0 0.450 0.582 S24 17.9 K=11.20 13.6 41.3 80.0 0,450 0.516 S25 17.9 K=11.20 13.4 41.0 80.0 0,450 0.512 S26 17.9 K=11.20 13.3 40.9 80.0 0.450 0.511 S27 17.9 K=11.20 13.3 40.9 85,0 0.450 0.481 S28 17.9 K=11.20 13.3 40.9 85.0 0.450 0.481 S29 17,9 K=11.20 13.4 41.0 80.0 0.450 0.513 S30 17.9 K=11.20 13.3 40.9 80.0 0.450 0.511 S31 17.9 K=11.20 14.3 42,3 80.0 0.450 0.529 S32 17.9 K=11.20 14.9 43.2 80.0 0.450 0.540 S33 17.9 K=11.20 19.6 49.6 80.0 0.450 0.620 S35 18.8 K=11.20 13.0 40.4 80.0 0.450 0.505 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOE TITLE: building g - .45 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT '2) (GPM/FT'2) S36 18.8 K=11.20 12.8 40.1 80.0 0.450 0.501 S37 18.8 K=11.20 12.7 40.0 80.0 0.450 0.500 S38 18.8 K=11.20 12.1 39.0 80.0 0.450 0.488 S39 18.8 K=11.20 12.7 40.0 80.0 0.450 0.500 S40 18.8 K=11.20 12.6 39.7 80.0 0.450 0,496 S41 18.8 K=11.20 13.3 40.8 80.0 0.450 0.510 S42 18.8 K=11.20 12.7 40.0 80.0 0.450 0.499 S43 18.8 K=11.20 12.8 40,0 80.0 0.450 0.500 S44 18.8 K=11.20 13.0 40.4 80.0 0.450 0.504 S45 18.8 K=11.20 13.4 41.0 80.0 0.450 0.512 S61 9.0 - - - - 28,8 --- S62 9.0 - - - - 30.6 --- S63 9.0 - - - - 32.0 --- S64 9.0 - - - - 33.0 --- S65 9.0 - - - - 28.8 --- S66 9.0 - - - - 29.8 --- S67 9.0 - - - - 31.0 --- S68 9.0 - - - - 32.1 - - - Ri 18.8 - - - - 56.8 --- R2 17.9 - - - - 57.1 --- R3 17.0 - - - - 56.0 --- R4 16.2 - - - - 56,7 --- R5 15.2 - - - - 59.2 --- R6 14.2 - - - - 59.9 --- R7 18.8 - - - - 14.0 --- R8 17.9 - - - - 14.5 --- R9 17.0 - - - - 13.8 - - - RiO 16.2 - - - - 15.0 - - - Ru 15.2 - - - - 20.7 --- P.12 14.2 - - - - 21.0 - - - M 17.2 - - - - 62.8 - - - Ml 16.8 - - - - 63.0 --- M2 15.9 - - - - 62.7 --- M3 15.0 - - - - 62.7 --- M3A 15.0 - - - - 62.8 --- M4 14.2 - - - - 62.9 --- M5 13.7 - - - - 63.1 --- M6 12.7 - - - - 63.5 --- M7 16.8 - - - - 16.1 --- M8 15.9 - - - - 16.5 --- M9 15.0 - - - - 16.9 --- M1O 14.2 - - - - 17.5 - - - Nil 13.7 - - - - 18.2 ---- M12 12.8 - - - - 18.7 --- L4 16.2 - - - - 13.3 --- L5 16.2 - - - - 13.3 --- L6 16.2 - - - - 13.4 --- Lu1 16.2 - - - - 20.3 --- L23 17.0 - - - - 16.4 --- L30 17.9 - - - - 13.7 --- L37 18.8 - - - - 12.7 --- L38 18.8 - - - - 12.7 --- L40 18.8 - - - - 13.1 --- L41 18.8 - - - - 15.4 --- L61 16.2 - - - - 25.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2E JOB TITLE: building g - .45 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FTA2) (GPM/FT-2) L62 16.2 - - - - 27.5 --- L63 16.2 ---- 28.9 --- L64 16.2 - - - - 29.9 ___ L65 16.2 - - - - 25.7 --- L66 16.2 - - - - 26.7 --- L67 16.2 - - - - 27,9 --- L68 16.2 - - - - 29.0 - - - TOR 17.2 - - - - 64.0 - - - BOR 1.0 - - -i - 71.8 - - - DI -3.0 - - - - 74.5 - - - U 6.0 ---- 86.5 - - - Ui 6.0 - - - - 87,4 - - - UG -3.0 - - - - 86.9 --- UG1 -3.0 - - - - 83.4 --- UG2 -3.0 - - - - 77.0 --- BF1 3.0 - - - - 79.9 --- 3F2 3.0 - - - - 75.9 --- HYD -3.0 HOSE STREAM 87.1 500.0 SRC 5.5 SOURCE 87.7 2339.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOSS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG. G\6-2E JOB TITLE: building g - .45 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 2339,2 7.980 PL 1.00 PF 0.0 SRC 5.5 SRCE 87,7 (N/A) 15.0 150 FTG ---- PE -0.2 Ui 6.0 0.0 87.4 0.0 0.029 TL 1.00 PV 1.5 Pipe: 2 1709.0 7,980 PL 205.00 PF 4.2 Ui 6.0 0.0 87.4 0.0 11.0 150 FTG T PE 3.9 HYD -3.0 H.S. 87.1 500.0 0.016 TL 255.00 PV 0.8 Pipe: 3 1209.0 7,980 PL 20.00 PF 0.2 HYD -3.0 H.S. 87.1 500.0 7.8 150 FTG ---- PE 0.0 UG -3.0 0.0 86.9 0.0 0.009 TL 20.00 PV 0.4 Pipe: 4 630.1 7.980 PL 360.00 PF 0.9 Ui 6.0 0.0 87,4 0.0 4.0 150 FTG ---- FE 0.0 U 6.0 0.0 86.5 0.0 0.003 TL 360.00 PV 0.1 Pipe: 5 630,1 7.980 PL1215.00 PF 3.4 U 6.0 0.0 86.5 0.0 4,0 150 FTG T3L PE 3.9 UG -3.0 0.0 86.9 0,0 0.003 TL1322.00 PV 0.1 Pipe: 5A 1839.1 7.980 PL 135.00 PF 3.6 UG -3.0 0.0 86.9 0,0 11.8 150 FTG TG PE 0.0 UG1 -3.0 0.0 83.4 0.0 0.019 TL 189.00 PV 0.9 Pipe: 6 1839.1 8.390 PL 6.00 PF 0.8 UG1 -3.0 0.0 83.4 0.0 10.7 140 FTG 2L PE -2.6 SF1 3.0 0.0 79.9 0.0 0.017 TL 50.00 PV 0.8 Pipe: 7 FIXED PRESSURE LOSS DEVICE SF1 3.0 0.0 79.9 0.0 4.0 psi, 1839.1 gpm SF2 3.0 0.0 75.9 0.0 Pipe: 8 1839,1 8.390 PL 6.00 PF 1.5 SF2 3.0 0.0 75.9 0.0 10.7 140 FTG TL PE 2.6 UG2 -3.0 0.0 77.0 0.0 0.017 TL 88.00 PV 0.8 Pipe: 9 1839,1 7.980 FL 135.00 PF 2.5 UG2 -3.0 0.0 77,0 0.0 11.8 150 FTG ---- PE 0.0 DI -3.0 0.0 74.5 0.0 0.019 TL 135.00 PV 0.9 Pipe: 10 1839.1 8.390 PL 12.00 PF 0.9 DI -3.0 0.0 74.5 0.0 10.7 140 FTG 2L PE -1.7 BOR 1.0 0.0 71.8 0.0 0.017 TL 56.00 PV 0,8 Pipe: 11 1839.1 8.249 PL 16.25 PF 0.7 3CR 1.0 0.0 71.8 0.0 11.0 120 FTG L FE -7.0 TOR 17.2 0.0 64.0 0.0 0.024 TL 30.71 PV 0.8 Pipe: 12 1839.1 8.249 PL 37.41 PF 1.3 TOR 17.2 0.0 64.0 0.0 11.0 120 FTG L FE 0,0 M 17.2 0.0 62.8 0.0 0.024 TL 51.87 PV 0.8 Pipe: 13 0.0 6.357 FL 4.00 PF 0.0 M 17.2 0.0 62.8 0.0 0.0 120 FTG L PE 0.2 Ml 16.8 0.0 63.0 0,0 0.000 TL 15.32 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/28/2001C:\DWG\FIRE SFRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOE TITLE: building g - .45 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: 14 1537,7 6.357 PL 10.00 PF 0.6 N 17.2 0.0 62.8 0.0 15.5 120 FTG ---- PE 0.6 M2 15.9 0.0 62.7 0.0 0.062 TL 10.00 PV 1.6 Pipe: 15 1250.4 6.357 PL 8.50 PF 0.4 M2 15.9 0.0 62.7 0.0 12.6 120 FTG ---- FE 0.4 M3A 15.0 0.0 62.8 0.0 0.042 TL 8.50 PV 1.1 Pipe: 16 1080.5 6.357 FL 1,50 PF 0.0 M3A 15.0 0.0 62.8 0.0 10.9 120 FTG ---- FE 0.0 M3 15.0 0.0 62,7 0.0 0.032 TL 1.50 PV 0.8 Pipe: 16A 759.8 6,357 PL 10.00 PF 0.2 M3 15.0 0.0 62.7 0.0 7.7 120 FTG ---- PE 0.4 M4 14.2 0.0 62.9 0.0 0.017 TL 10.00 PV 0.4 Pipe: 17 454.7 6.357 FL 10.00 PF 0.1 M4 14.2 0.0 62.9 0.0 4.6 120 FTG ---- PE 0.2 M5 13,7 0.0 63.1 0.0 0.007 TL 10.00 PV 0.1 Pipe: 18 221.2 6.357 PL 13.00 PF 0.0 M5 13.7 0.0 63.1 0.0 2.2 120 FTG ---- FE 0.4 M6 - 12.7 0.0 63.5 0.0 0.002 TL 13.00 PV 0.0 Pipe: 19 30.0 4.260 PL 10.00 PF 0.0 N7 16.8 0.0 16.1 0.0 0.7 120 FTG ---- FE 0.4 M8 15.9 0.0 16.5 0.0 0.000 TL 10.00 PV 0.0 Pipe: 20 -104.7 4.260 PL 10.00 FE' 0.0 M8 15.9 0.0 16.5 0.0 2.4 120 FTG ---- FE 0.4. M9 15.0 0.0 16'.9 0.0 .0.003 TL 10.00 PV 0.0 Pipe: 21 -294.1 4.260 PL 10.00 PF 0.2 M9 15.0 0.0 16.9 0.0 6.6 120 FTG ---- FE 0.4 mio 14.2 0.0 17.5 0.0 0.020 TL 10.00 PV 0.3 Pipe: 22 -454.7 4.260 PL 10.00 PF 0.5 M10 14.2 0.0 17.5 0.0 10.2 120 FTG ---- FE 0.2 Nil 13.7 0.0 18.2 0.0 0.046 TL 10.00 PV 0.7 Pipe: 23 -221.2 4,260 FL 12.00 PF 0.1 mil 13.7 0.0 18.2 0.0 5.0 120 FTG ---- FE 0.4 M12 12.8 0.0 18.7 0.0 0.012 TL 12.00 PV 0.2 Pipe: 24 301.4 2.703 FL 2.00 FE' 5.3 M 17.2 0.0 62.8 0.0 16.9 120 FTG TL FE -0.7 Rb 18.8 0.0 56.8 0.0 0.196 TL 26.87 PV 1.9 Pipe: 25 287.4 2.703 FL 2.00 PF 4,8 M2 15.9 0.0 62.7 0.0 16,1 120 FTG TL FE -0.9 R2 17,9 0.0 57.1 0.0 0.179 TL 26.87 PV 1.7 Pipe: 26 320.6 2.703 FL 2,00 PF 5.9 M3 15.0 0.0 62.7 0.0 17.9 120 FTG TL FE -0.9 R3 17.0 0.0 56.0 0.0 0.220 TL 26.87 PV 2.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 30E TITLE: building g - .45 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: 27 305.1 2.703 PL 2.00 PF 5.4 M4 14.2 0.0 62.9 0.0 17.1 120 FTG TL PE -0.9 R4 16.2 0.0 56.7 0.0 0.200 TL 26.87 PV 2.0 Pipe: 28 233.6 2.703 PL 1.50 PF 3.2 M5 13.7 0.0 63.1 0.0 13.1 120 FTG TL PE -0.6 R5 15.2 0.0 59.2 0.0 0.122 TL 26.37 PV 1.1 Pipe: 29 221.2 2.703 PL 1.60 PF 2.9 M6 12.7 0.0 63.5 0.0 12.4 120 FTG TL PE -0.7 R6 14.2 0.0 59.9 0.0 0.110 TL 26.47 PV 1.0 Pipe: 30 139.9 2.703 PL 2.00 PF 1.3 M7 16.8 0.0 16.1 0.0 7.8 120 FTG TL PE -0.9 R7 18.8 0.0 14.0 0.0 0.047 TL 26,87 PV 0.4 Pipe: 31 134.7 2.703 PL 2.00 PF 1.2 M8 15.9 0.0 16.5 0.0 7.5 120 FTG TL. FE -0.9 R8 17.9 0.0 14.5 0.0 0.044 TL 26.87 PV 0.4 Pipe: 32 189.5 2.703 PL 2.00 FE' 2.2 M9 15.0 0.0 16.9 0.0 10.6 120 FTG TL FE -0.9 R9 17.0 0.0 13.8 0.0 0.083 TL 26.87 PV 0.8. Pipe: 33 160.6 2.703 PL 2.00 FE' 1.6 M10 14.2 0.0 17.5 0.0 9.0 120 FTG TL FE -0.9 RiO 16.2 0.0 15.0 0.0. 0.061 TL 26.87 PV 0.5 Pipe: 34 -233.6 2.703 PL 1.50 FE' 3.2 Mil 13.7 0.0 18.2 0.0 13.1 120 FTG TL. PE -0.6 Rib 15.2 0.0 20.7 0.0 0.122 TL 26.37 PV 1.1 Pipe: 35 -221.2 2.703 PL 1.50 PF 2.9 M12 12.8 0.0 18.7 0.0 12.4 120 FTG TL PE -0.6 R12 14.2 0.0 21.0 0.0 0.110 TL 26.37 PV 1.0 Pipe: 36 301.4 2,703 PL 168.25 PF 41,5 Ri 18.8 0.0 56.8 0.0 16.9 120 FTG T4L PE 0.0 L41 18.8 0.0 15.4 0.0 0.196 TL 211.77 PV 1.9 Pipe: 37 155.1 2.703 FL 9.75 FE' 2.0 L41 18.8 0.0 15.4 0.0 8.7 120 FTG TL FE 0.0 S45 18.8 11.2 13.4 41.0 0.057 TL 34.62 PV 0.5 Pipe: 38 114.2 2.703 PL 12.00 PF 0.4 S45 18.8 11.2 13.4 41.0 6.4 120 FTG ---- FE 0.0 S44 18.8 11.2 13.0 40.4 0.032 TL 12.00 PV 0.3 Pipe: 39 73.8 2.703 FL 9.50 PF 0.2 S44 18.8 11.2 13.0 40.4 4.1 120 FTG L PE 0.0 S43 18.8 11.2 12.8 40.0 0.015 TL 15.72 PV 0.1 Pipe: 40 33.8 2.703 FL 7.25 PF 0.0 S43 18.8 11.2 12.8 40.0 1.9 120 FTG ---- PE 0.0 S42 18.8 11.2 12.7 40.0 0.003 TL 7.25 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOES IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2E JOE TITLE: building g - .45 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: 41 -6.1. 2.703 FL 4.50 PF 0.0 S42 18.8 11.2 12.7 40.0 0.3 120 FTG •---- PE 0.0 L37 18.8 0.0 12.7 0.0 0.000 TL 4.50 PV 0.0 Pipe: 42 146.3 2.703 FL 15.33 PF 2.1 L41 18.8 0.0 15.4 0.0 8.2 120 FTG TL PE 0.0 S41 18.8 11.2 13.3 40.8 0.051 TL 40.20 PV 0.5 Pipe: 43 105.5 2.703 PL 5.41 PF 0.2 S41 18.8 11,2 13.3 40.8 5.9 120 FTG ---- PE 0.0 L40 18.8 0.0 13.1 0.0 0.028 TL 5.41 PV 0.2 Pipe: 44 -39.7 1.610 PL 1.75 PF.- 0.6 S40 18.8 11.2 12.6 39.7 6.3 120 FTG T FE 0.0 L40 18.8 0.0 13.1 0.0 0.057 TL 9.75 PV 0.3 - Pipe: 45 65.7 2.703 FL 8.47 PF 0.4 L40 18.8 0.0 13.1 0.0 3.7 120 FTG 4L FE 0,0 S39 18.8 11.2 12.7 40.0 0.012 TL 33.34 PV 0.1 Pipe: 46 25.8 2.703 FL 10.41 PF 0.0, S39 18.8 11.2 12.7 40.0 1.4 120 FTG L FE 0.0 L38 18.8 0.0 12.7 0.0 0.002 TL 16,63 PV 0.0 Pipe: 47 -39.0 1.610 FL 2.08 PF 0.6 S38 18.8 11.2 12.1 39.0 6.2 120 FTG T FE 0.0 L38 18.8 0.0 12.7 0.0 0.056 TL 10.08 PV 0.3 Pipe: 48 -13.3 2.703 FL 22.75 PF 0.0 L38 18.8 0.0 12.7 0.0 0.7 120 ' FTG L FE 0.0 L37 18.8 0.0 12.7 0.0 0.001 TL 28.97 PV 0.0- Pipe: 49 -19.4 2.703 FL 1.75 PF 0.0 L37 18.8 0.0 12.7 0.0 1.1 120 FTG 7.0 FE 0.0 S37 18.8 11.2 12.7 40.0 0.001 TL 8.75 PV 0.0 Pipe: 50 -59.4 ' 2.703 PL 8.00 PF 0.1 S37 18.8 11.2 12.7 40.0 3.3 120 FTG ---- FE 0.0' S36 18.8 11.2 12.8 40.1 0.010 TL, 8.00 PV 0.1 Pipe: 51 ' -99.5 2.703 FL 8.00 PP 0.2 S36 18.8 11.2 12.8 40.1 5.6 120 FTG ---- FE 0.0 S35 18.8 11.2 13.0 40.4 0.025 TL 8.00 PV 0.2 Pipe: 52 -139.9 2.703 FL 1.58 PP 1.0 S35 18.8 11.2 13.0 40.4 7.8 120 FTG T FE 0.0 R7 18.8 0.0 14.0 0.0 0.047 TL 20.23 PV. 0.4 Pipe: 53 287.4 2.703 FL 165.25 PF .37.4 R2 17.9 0.0 57.1 0.0 16.1 120 FTG T4L FE 0,0 S33 17,9 11.2 19.6 49.6 0.179 TL 208.77 PV 1.7 Pipe: 54 237.8 2.703 FL 12.50 PP 4.7 S33 17.9 11.2 19.6 49.6 13.3 120 FTG 4L FE 0.0 S32 17.9 11.2 14,9 43.2 ' 0.126 TL 37.37 PV 1.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOES IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 'JOB TITLE: building g - .45 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: 55 194.5 2.703 FL 7.00 PF 0.6 S32 17.9 11.2 14.9 43.2 10.9 120 FTG ---- PE 0.0 S31 17.9 11.2 14.3 42.3 0.087 TL 7.00 PV 0.8 Pipe: 56 152.2 2.703 PL 5.33 PF 0.6 S31 17.9 11.2 14.3 42.3 8.5 120 FTG L FE 0.0 L30 17.9 0.0 13.7 0.0 0.055 TL 11.55 PV 0.5 Pipe: 57 111.3 2.703 FL 7.08 PF 0.2 L30 17.9 0.0 13.7 0.0 6.2 120 FTG ---- PE 0.0 S29 17.9 11.2 13.4 41.0 0.031 TL 7.08 PV 0.3 Pipe: 58 70.2 2.703 PL 6.66 PF 0.1 S29 17.9 11.2 13.4 41.0 3.9 120 FTG ---- FE 0.0 S28 17.9 11.2 13.3 40.9 0.013 TL 6.66 PV 0.1 Pipe: 59 29.3 2.703 FL 8.91 PF 0.0 S28 17.9 11.2 13.3 40.9 1.6 120 FTG ---- FE 0.0 S27 17.9 11.2 13.3 40.9 0.003 TL 8.91 FV 0.0 Pipe: 60 -11.6 2.703 PL 8.41 PF 0.0 S27 17.9 11.2 13.3 40.9 0.6 120 FTG ---- PE 0.0 S26 17,9 11.2 13.3 40.9 0.000 TL 8.41 PV 0.0 Pipe: 61 -52.4 2.703 PL 8.00 PF 0.1 S26 17.9 11.2 13.3 40.9 2.9 120 FTG ---- PE 0.0 S25 17.9 11.2 13.4 41.0 0.008 TL 8.00 FV 0.1 Pipe: 62 -93.4 2.703 P.L 8.00 PF 0.2 S25 17.9 11.2 13.4 41.0 5.2 120 FTG ---- PE 0.0 S24 17.9 11.2 13.6 41.3 0.022 TL 8.00 PV 0.2 Pipe: 63 -134.7 2.703 FL 1.58 PF 0.9 S24 17.9 11.2 13.6 41.3 7.5 120 FTG T FE 0.0 R8 17.9 0.0 14.5 0.0 0.044 TL 20.23 PV 0.4 Pipe: 64 320.6 2.703 FL 157.50 PF 38.7 R3 17.0 0.0 56.0 0.0 17.9 120 FTG T PE 0.0 523A 17.0 11.2 17.3 46.5 0.220 TL 176.15 PV 2.2 Pipe: 65 274.1 2.703 FL 5.41 PF 0.9 S23A 17.0 11.2 17.3 46.5 15.3 120 FTG ---- FE 0.0 L23 17.0 0.0 16.4 0.0 0.164 TL 5.41 PV 1.6 Pipe: 66 -44.1 1.610 FL 4.25 PF 0.9 S23 17.0 11.2 15.5 44.1 7.0 120 FTG T PE 0.0 L23 17.0 0,0 16.4 0.0 0.070 TL 12.25 PV 0.3 Pipe: 67 230.0 2.703 FL 7,08 PF 3.8 L23 17.0 0.0 16,4 0.0 12.9 120 FTG 4L FE 0.0 S22 17.0 11.2 12.6 39.7 0.119 TL 31.95 PV 1.1 Pipe: 68 190.2 2.703 FL 7.00 PF 0.6 S22 17.0 11.2 12.6 39.7 10.6 120 FTG ---- FE 0.0 S21 17.0 11.2 12.0 38.8 0.084 TL 7.00 PV 0.8. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALCMAR FRUM\SEFP\CALCS\BLDG. G\6-2E JOB TITLE: building g - .45 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: 69 151.4 2.703 PL 7.00 PF 0.4 S21 17.0 11.2 12.0 38.8 8.5 120 FTG ---- PE 0.0 S20 17.0 11.2 11.6 38.2 0.055 TL 7.00 PV 0.5 Pipe: 70 113.2 2.703 PL 6.58 PF 0.2 S20 17.0 11.2 11.6 38.2 6.3 120 FTG ---- FE 0.0 S19 17.0 11.2 11.4 37.8 0.032 TL 6.58 PV 0.3 Pipe: 71 75.4 2.703 PL 10.75 PF 0.3 S19 17.0 11.2 11.4 37.8 4.2 120 FTG L PH 0.0 S18 17.0 11,2 11.2 37,4 0.015 TL 16.97 PV 0.1 Pipe: 72 . 38.0. 2.703 FL 8.08 PF 0.0 S18 17.0 11.2 11.2 37.4 2.1 120 FTG ---- PH 0.0 S17 17.0 11.2 11.1 37.4 0.004 TL 8.08 PV 0.0 Pipe: 73 0.6 2.703 FL 7.66 PF 0.0 S17 17.0 11.2 11.1 37.4 ' 0.0 120 FTG 2L FE 0.0 S16 17.0 11.2 11.1 37.3 0.000 TL 20.09 PV 0.0 Pipe: 74 -36.7 2.703 PL 8.91 PF 0.0 S16 17.0 11.2 11.1 37.3 2.1, 120 FTG ---- FE 0.0 S15 17.0 11.2 11.2 37.4 0.004 TL 8.91 PV 0.0 Pipe: 75 -74.1 2.703 PL 9.41 PF 0.3 S15 17.0 11.2 11.2 37.4 4.1 120 FTG 2L PE 0.0 S14 17.0 11.2 11.5 37.9 0.015 TL 21.84 PV 0.1 Pipe: 76 . -112.1 2.703 PL 8.00 FE' 0.3 S14 17.0 11,2 11.5 37.9 6.3 120 FTG ---- FE 0.0 S13 17.0 11:2 11'.7 38.4 0.031 TL 8.00 PV, 0.3 Pipe: 77 -150.4 2.703 PL 8.00 FE' 0.4 S13 17,0 11.2 11.7 38.4 8,4 120 FTG ---- FE 0.0 S12 17.0 11.2 12.2 39.1 0.054 TL 8.00 PV 0.5 Pipe: 78 -189.5 2.703 FL 1,58 PF 1.7 S12 17.0 11.2 12.2 39.1 10.6 120 FTG T FE 0.0 R9 17.0 0.0 13.8 0.0 0.083 TL 20.23 PV 0.8 Pipe: 79 305.1 2.703 FL 162.91 PP 36.4 R4 16.2 0.0 56.7 0.0 17.1 120 FTG' T FE 0.0 Lii 16.2 0.0 20.3 0.0 0.200 TL 181.56 PV 2.0 Pipe: 80 -49.4 1.610 FL 2.25 PF 0.9 Sli 16.2 11.2 19.4 49.4 7.8 120 FTG T FE 0.0 Lii 16,2 0.0 20.3 0.0 0.086 TL 10.25 PV 0.4 Pipe: 81 255.8 2,703 FL 7.08 PP 4.6 Lii 16.2 0.0 20.3 0.0 14.3 120 FTG 4L FE 0.0 sio 16.2 11.2 15.7 44.4 0.145 TL 31.95 PV 1.4 Pipe: 82 211.4 2,703 FL 7.00 PF 0.7 sio 16.2 11.2 15.7 44.4 11.8 120 FTG ---- FE 0.0 S9 16.2 11.2 15.0 43.3 0.102 T'L 7.00 PV 0.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG. G\6-2 'JOB TITLE: building g - .45 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: 83 168.1 2.703 PL 7.00 PF 0,5 S9 16.2 11.2 15.0 43.3 9.4 120 FTG ---- PE 0.0 S8 16.2 11.2 14.5 42.7 0.066 TL 7.00 PV 0.6 Pipe: 84 125.4 2.703 FL 7.00 PF 0.3 S8 16.2 11.2 14.5 42.7 7.0 120 FTG ---- PE 0.0 S7 16.2 11.2 14.2 42.3 0.039 TL 7.00 PV 0.3 Pipe: 85 83.2 2.703 PL 42.08 PF 0.9 S7 16.2 11.2 14.2 42.3 4,6 120 FTG L PE 0.0 L6 16.2 0.0 13.4 0.0 0.018 TL 48.30 PV 0,1 Pipe: 86 -40,1 1.610 PL 1,41 PF 0.6 S6 16.2 11.2 12,8 40.1 6.3 120 FTG T FE 0.0 L6 16.2 0.0 13.4 0.0 0.058 TL 9.41 PV 0.3 Pipe: 87 43.1 2.703 FL 7.15 PF 0.0 L6 16.2 0.0 13.4 0.0 2.4 120 FTG ---- PE 0.0 L5 16.2 0.0 13.3 0.0 0.005 TL 7.15 PV 0.0 Pipe:88 -40.0 1.610 FL 1.41 PF 0.5 S5 16.2 11.2 12.8 40.0 6.3 120 FTG T PE 0.0 L5 16.2 0.0 13,3 0.0 0.058 TL 9.41 PV 0.3 Pipe: 89 3.0 2.703 PL 6.00 PF 0.0 L5 16.2 0.0 13.3 0.0 0.2 120 FTG ---- FE 0.0 L4 16.2 0.0 13.3 0.0 0.000 TL 6.00 PV 0.0 Pipe: 90 -40.0 1.610 PL 1.41 PF 0.5 S4 16.2 11.2 12.8 40.0 6.3 120 FTG T PE 0.0 L4 16.2 0.0 13.3 0.0 0.058 TL 9.41 PV 0.3 Pipe: 91 -37.0 2.703 PL 7.16 PF 0,0 L4 16.2 0.0 13.3 0.0 2.1 120 FTG ---- FE 0.0 S3 16.2 11.2 13.4 40.9 0.004 TL 7,16 PV 0.0 Pipe: 92 -77.9 2.703 FL 8.00 PF 0.1 S3 16.2 11.2 13.4 40.9 4.4 120 FTG ---- PE 0.0 52 16.2 11.2 13.5 41.1 0.016 TL 8.00 PV 0.1 Pipe: 93 -119.0 2.703 FL 8.00 PF 0.3 S2 16.2 11.2 13.5 41.1 6.7 120 FTG ---- PE 0.0 Si 16.2 11.2 13.8 41.5 0.035 TL 8.00 PV 0.3 Pipe: 94 -160.6 2.703 FL 1.58 PF 1.2 Si 16.2 11.2 13,8 41.5 9.0 120 FTG T FE 0.0 RiO 16.2 0.0 15.0 0.0 0.061 TL 20.23 PV 0.5 Pipe: 95 233.6 2.703 PL 211.00 PF 28.8 R5 15.2 0.0 59.2 0.0 13.1 120 FTG TL PE -0.4 L64 16.2 0.0 29.9 0.0 0.122 TL 235.87 PV 1.1 Pipe: 96 233.6 2.703 FL 8.92 PF 1.1 L64 16.2 0.0 29.9 0.0 13.1 120 FTG ---- FE 0.0 L63 16.2 0.0 28.9 0.0 0.122 TL 8.92 PV 1.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOE TITLE: building g - .45 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: 97 233.6 2.703 PL 10.75 PF 1.3 L63 16.2 0.0 28.9 0.0 13.1 120 FTG ---- PE 0.0 L62 16.2 0.0 27.5 0.0 0.122 TL 10.75 PV 1.1 Pipe: 98 233.6 2.703 PL 15.00 PF 1.8 L62 16.2 0.0 27.5 0.0 13.1 120 FTG ---- PE 0.0 L61 16.2 0.0 25,7 0.0 0.122 TL 15.00 PV 1.1 Pipe: 99 233.6 2.703 PL 44.16 PF 5.4 L61 16.2 0.0 25.7 0.0 13.1 120 FTG ---- PE 0.4 Rll 15.2 0.0 20.7 0.0 0.122 TL 44.16 PV 1.1 Pipe: 100 221.2 2.703 PL 235.00 PF 30.1 R6 14.2 0.0 59.9 0.0 12.4 120 FTG T3L PE -0.8 L68 16.2 0.0 29.0 0.0 0.110 TL 272.30 PV 1.0 Pipe: 101 221.2 2.703 PL 9,83 PF 1.1 L68 16.2 0.0 29.0 0.0 12.4 120 FTG ---- PE 0.0 L67 16.2 0.0 27.9 0.0 0.110 TL 9.83 PV 1.0 Pipe: 102 221.2 2.703 PL 10.75 PF 1.2 L67 16.2 0,0 27.9 0.0 12.4 120 FTG ---- PE 0.0 L66 16.2 0.0 26.7 0.0 0.110 TL 10.75 PV 1.0 Pipe: 103 221.2 2.703 FL 9.25 PF 1.0 L66 16.2 0.0 26.7 0.0 12.4 120 FTG ---- FE 0.0 L65 16.2 0.0 25.7 0.0 0.110 TL 9.25 PV 1,0 Pipe: 104 221.2 2.703 FL 49.92 PF 5.5 L65 16.2 0.0 25.7 0.0 12.4 120 FTG ---- FE 0.8 R12 14.2 0.0 21.0 0.0 0.110 TL 49.92 PV 1,0 Pipe: 105 0.0 1.049 PL 9.67 PF 0.0 L61 16.2 0.0 25.7 0.0 0.0 120 FTG 2T2L FE 3.1 S61 9.0 0.0 28.8 0.0 0.000 TL 23.67 PV 0.0 Pipe: 106 0.0 1.049 FL 8.67 FE' 0.0 L62 16.2 0.0 27.5 0.0 0.0 120 FTG 2T2L FE 3.1 S62 9.0 0.0 30.6 0.0 0.000 TL 22.67 PV 0,0 Pipe: 107 0.0 1,049 FL 9.75 FE' 0.0 L63 16.2 0.0 28.9 0.0 0.0 120 FTG 2T2L FE 3.1 S63 9.0 0.0 32.0 0.0 0,000 TL 23.75 PV 0.0 Pipe: 108 0.0 1.049 FL 8.75 PF 0.0 L64 16.2 0.0 29,9 0.0 0.0 120 FTG 2T2L FE 3.1 S64 9.0 0.0 33.0 0.0 0.000 TL 22.75 PV 0.0 Pipe: 109 0.0 1.049 FL 7.33 FE' 0.0 L65 16.2 0.0 25.7 0.0 0.0 120 FTG TL FE 3.1 S65 9.0 0.0 28.8 0.0 0.000 TL 14.33 PV 0.0 Pipe: 110 0.0 1,049 FL 11.00 PF 0.0 L66 16.2 0.0 26.7 0.0 0.0 120 FTG 2T2L FE 3.1 S66 9.0 0.0 29.8 0.0 0.000 TL 25.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG. G\6-2 'JOE TITLE: building g - .45 PIPE TAG Q(GEM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 111 0.0 1.049 PL 10.67 PF 0.0 L67 16.2 0.0 27.9 0,0 0.0 120 FIG 2T2L PE 3.1 S67 9.0 0.0 31.0 0.0 0.000 TL 24.67 PV 0.0 Pipe: 112 0.0 1.049 PL 8.67 PF 0.0 L68 16.2 0.0 29.0 0.0 0.0 120 FIG 212L PE 3.1 S68 9.0 0.0 32.1 0.0 0.000 TL 22.67 PV 0,0 Pipe: 113 40.9 2.703 PL 22.00 PF 0.3 L30 17.9 0.0 13.7 0.0 2,3 120 FTG 2TL PE 0.0 S30 17.9 11.2 13.3 40.9 0.005 TL 65.52 PV 0.0 Pipe: xpress 169.9 2.227 PL 227.33 PF 45.9 M3A 15.0 0.0 62.8 0.0 14.0 120 FIG E2T PE -0.8 M7 16.8 0.0 16.1 0.0 0.174 TL 263.27 PV 1.3 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 0.153 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 17.9 ft/sec at pipe 26. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv EfyVlv GatVlv AlmChk DPVlv NPTee 2.227 7.19 14.38 4.31 15.82 8.63 1.44 14.38 14.38 14.38 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15,54 18.65 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 26.33 6.357 17.60 37.72 11.32 40.23 12.57 3.77 35.21 23.89 37.72 8.249 20.02 38.92 14.46 50.04 13,35 4.45 38.92 30.03 38.92 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .45 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D 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 1.610 4.00 8.00 2.00 9.00 6.00 1,00 10.00 10.00 8.00 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 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 'JOB TITLE: building g - .45 WATER SUPPLY ANALYSIS Static: 125.00 psi Resid: 20.00 psi Flow: 5390.0 gpm 140.0 LEGEND 1 Available pressure 112.0 102.59 psi 8 2339. gpm G A U G E 84.0 P R E S S U R E 56.0 1 2 Required pressure 87.65 psi @ 2339.2 gpm 28.0 -14.7 I 1 I 12C180C2400 3000 3600 4200 4800 5400 6000 FLOW (GPM) Supply Flow Curve C PALOMAR FORUM BUILDING G.45 Test Date: 6/28/2007 Static Hydrant: NE INTERSECTION OF K STREET AND 13 1/2 STREET. Design GPM: 2339 GPM Flow Hydrant: NEW CONNECTION OF FIRE SERVICE BACKFLOW PREVENTER Design PSI: 71.8 PSI Ps 125.0 PSI Test Static Pressure Reading Available Pressure at Design GPM: 102.6 PSI Pr 20.0 PSI Test Residual Pressure Reading PSI Headroom: 30.80 PSI 30% GPMr 5390 GPM Test Flow at Residual Pressure GPM Headroom: 1393 GPM 60% Flow Test Summary Curve QA1B5 120 100 Ira 80 —• —Psi IDesian Point 60 40- 0 0 500 1000 1500 2000 2500 3000 3500 4000 Flow GPM REMOTE AREA 1 Printed 6/28/2007 PRO-TECH FIRE PROTECT4PROVED ZJWITTED 179 ROYMAR ROAD SUITE G /v OCEANSIDE, CA 92054 dE CARLSBAD Fl PARTMENT HYDRAULIC CALCULATIONS REMOTE ARE ASo-foi 94- FOR GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I BUILDING CARLSBAD CA DATE: June 28, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: 0.10 gpm/1500 sq. ft. 1045 sq. ft. 225 SQ. FT. 8 sprinklers 182.2 gpm TOTAL WATER REQUIRED (including hose): 282.2gpm FLOW AND PRESSURE (@ BOR): 182.2 gprn @ 25 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 709152 - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/28/2001C:\DWG\FIRE'5PRINKLER\JOES IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG. G\6-2 JOE TITLE: building g• WATER SUPPLY DATA. SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 125.0 20.0 5390.0 124.6 282.1 27.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 282.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 182.1 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT"2) (GPM/FT-2) 51 16.2 - - - - 17.8 --- S2 16.2 - --- 17.8 --- S3 16,2 - - - - 17.9 --- S4 16,2 - - - - 17.9 --- S5 16.2 - - - - 17.9 --- S6 16.2 - - - - 17.9 --- S7 16.2 - - - - 18.0 --- S8 16.2 - - - - 18.0 --- S9 16.2 - ---. 18.0 - sio 16.2 - - - - 18.0 - - - Sil 16.2 - - - - 18.0 --- 512 17.0 ''---- 17,5 --- S13 17.0 - - - - 17.5 --- S14 17.0 - - - - 17.5 --- S15 17.0 - - - - 17.5 --- S16 17.0 - - - - 17.6 --- S17 17,0 - - - - 17.6 --- S18 17.0 - - - - 17.6 --- S19 17.0 - - - - 17.6 --- S20 17.0 - - - - 17.6 --- S21 17.0 - - - - 17.6 --- S22 17.0 - - - - 17.6 --- S23 17.0 - - - - 17.7 --- 523A 17.0 - - - - 17.7 --- S24 17.9 - - - - 17.1 --- S25 17.9 - - - - 17.1 --- S26 17.9 - - - - 17.1 --- S27 17.9 - - - - 17.1 --- S28 17.9 - - - - 17.2 --- S29 17.9 - - - - 17.2 --- 530 17.9 - - - - 17.2 --- S31 17.9 - - - - 17.2 --- S32 17.9 - - - - 17.2 --- S33 17.9 - - - - 17.3 --- S35 18.8 - - - - 16.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 30E TITLE: building g - .1 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT"2) (GPM/FT'2) S36 18.8 - - - - 16.7 --- S37 18.8 - - - - 16.7 --- S38 18.8 - - - - 16.8 --- S39 18.8 - - - - 16.8 --- S40 18.8 - - - - 16.8 --- S41 18.8 - - - - 16.8 --- S42 18.8 - - - - 16.8 --- S43 18.8 - --- 16.8 --- S44 18.8 - - - - 16.8 --- S45 18.8 - - - - 16.8 --- 561 9.0 K= 5.60 16.4 22.7 225,0 0.100 0.101 S62 9.0 K= 5.60 16.5 22.8 225.0 0.100 0.101 S63 9.0 K= 5.60 16.4 22.7 225.0 0.100 0.101 S64 9.0 K= 5.60 16.5 22.8 225.0 0.100 0.101 S65 9.0 K= 5.60 17.7 23.6 225.0 0.100 0.105 S66 9.0 K= 5.60 16.1 22.5 225.0 0.100 0.100 S67 9.0 K= 5.60 16.2 22.5 225.0 0.100 0.100 S68 9.0 K= 5.60 16.5 22.7 225.0 0.100 0.101 Ri 18.8 - - - - 17.2 --- R2 17.9 - - - - 17.6 --- R3 17.0 - - - - 18.0 --- R4 16.2 - - - - 18.3 --- R5 15.2 - - - - 18.7 --- R6 14.2 - - - - 19.1 --- R7 18.8 - - - - 16.7 --- R8 17.9 - - - - 17.1 --- R9 17.0 - - - - 17.5 - - - RiO 16.2 - - - - 17.8 - - - Ru 15.2 - - - - 18.0 --- Ri2 14.2 - - - - 18,3 - - - M 17.2 - - - - 17.9 - - - Mi 16.8 - - - - 18.1 --- M2 15.9 - - - - 18.5 --- M3 15.0 - - - - 18.9 --- M3A 15.0 - - - - 18.9 --- M4 14.2 - - - - 19.2 --- M5 13.7 - - - - 19.4 --- M6 12.7 - - - - 19.9 --- M7 16.8 - - - - 17.5 --- M8 15.9 - - - - 17.9 --- M9 15.0 - - - - 18.3 - - - Mb 14.2 - - - - 18.6 - - - Mu 13.7 - - - - 18.8 --- M12 12.8 - - - - 19.2 --- L4 16.2 - - - - 17.9 --- L5 16.2 - - - - 17.9 --- L6 16.2 - - - - 17.9 - - - Lii 16.2 - - - - 18.0 --- L23 17.0 - - - - 17.7 --- L30 17.9 - - - - 17.2 --- L37 18.8 - - - - 16.8 --- L38 18.8 - - - - 16.8 --- L40 18.8 - - - - 16.8 --- L4i 18.8 - - - - 16.8 --- L6i 16.2 - - - - 17.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOES IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT '2) (GPM/FT"2) L62 16,2 - --- 17.2 --- L63 16.2 - - - - 17.2 --- L64 16.2 - - - - 17.2 --- L65 16.2 - - - - 17.1 --- L66 16.2 - - - - 17.1 --- L67 16.2 - - - - 17.1 --- L68 16.2 - - - - 17.1 - - - TOR 17.2 - - - - 17.9 - - - BOR 1.0 - - - - 25.0 --- DI -3.0 - - - - 26.7 - - - U 6.0 - --- 27.0 - - - Ui 6.0 - - - - 27.0 - - - UG -3.0 - - - - 30.8 --- UG1 -3.0 - - - - 30.8 --- UG2 -3.0 - - -- 26.8 --- BF1 3.0 - - - - 28.2 --- BF2 3.0 - - - - 24.2 - - - HYD -3.0 HOSE STREAM 30.8 100.0 SRC 5.5 SOURCE 27.2 282.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 J05 TITLE: building g - .1 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: 1 282.1 7.980 PL 1.00 PF 0.0 SRC 5.5 SRCE 27.2 (N/A) 1.8 150 FTG ---- PE -0.2 Ui 6.0 0.0 27.0 0.0 0.001 TL 1.00 PV 0.0 Pipe: 2 206.7 7.980 PL 205.00 PF 0.1 Ui 6.0 0.0 27.0 0.0 1.3 150 FTG T PE 3.9 HYD -3.0 H.S. 30.8 100.0 0.000 TL 255.00 PV 0,0 Pipe: 3 106.7 7.980 EL 20.00 PF 0.0 HYD -3.0 H.S. 30.8 100.0 0.7 150 FTG ---- PE 0.0 UG -3.0 0.0 30.8 0.0 0.000 TL 20.00 PV 0.0 Pipe: 4 75.5 7.980 PL 360.00 FE' 0.0 Ui 6.0 0.0 27.0 0.0 0.5 150 FTG ---- PE 0.0 U 6.0 0.0 27.0 0.0 0.000 TL 360.00 PV 0.0 Pipe: 5 75.5 7.980 PL1215,00 PF 0.1 U 6.0 0.0 27.0 0.0 0.5 150 FTG T3L PE 3.9 UG -3.0 0.0 30.8 0.0 0.000 TL1322.00 PV 0.0 Pipe: 5A 182.2 7.980 PL 135.00 PF 0.0 UG -3.0 0.0 30.8 0.0 1.2 150 FTG TG PE 0.0 UG1 -3.0 0.0 30.8 0.0 0.000 TL 189.00 PV 0.0 Pipe: 6 182.2 8.390 EL 6.00 PF 0,0 UG1 -3.0 0.0 30.8 0.0 1.1 140 FTG 2L PE -2.6 SF1 3.0 0.0 28.2 0.0 0.000 TL 50.00 PV 0.0 Pipe: 7 FIXED PRESSURE LOSS DEVICE SF1 3.0 0.0 28.2 0.0 4.0 psi, 182.2 gpm SF2 3.0 0.0 24.2 0.0 Pipe: 8 182.2 8.390 FL 6.00 PF 0.0 SF2 3.0 0.0 24.2 0.0 1.1 140 FTG TL PE 2.6 UG2 -3.0 0.0 26.8 0.0 0.000 TL 88.00 PV 0.0 Pipe: 9 182.2 7.980 PL 135.00 PF 0.0 UG2 -3.0 0.0 26.8 0.0 1.2 150 FTG ---- PE 0.0 DI -3.0 0.0 26.7 0.0 0.000 TL 135.00 PV 0.0 Pipe: 10 182.2 8.390 PL 12.00 PF 0.0 DI -3.0 0.0 26.7 0.0 1.1 140 FTG 2L PE -1.7 BOR 1.0 0.0 25.0 0.0 0.000 TL 56.00 PV 0.0 Pipe: 11 182.2 8.249 PL 16.25 FE' 0.0 BOR 1.0 0.0 25.0 0.0 1.1 120 FTG L PE -7.0 TOR 17.2 0.0 17.9 0.0 0.000 TL 30.71 PV 0.0 Pipe: 12 165.9 8.249 PL 37.41 FE' 0.0 TOR 17.2 0.0 17.9 0.0 1.0 120 FTG L FE 0.0 N 17.2 0.0 17.9 0.0 0.000 TL 51.87 PV 0.0 Pipe: 13 0.0 6.357 FL 4.00 PF 0.0 N 17.2 0.0 17.9 0.0 0.0 120 FTG L PE 0.2 Ml 16.8 0.0 18.1 0.0 0.000 TL 15.32 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 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: 14 142.4 6.357 FL 10.00 PF 0.0 M 17,2 0.0 17.9 0.0 1.4 120 FTG ---- FE 0.6 M2 15.9 0.0 18,5 0.0 0.001 TL 10.00 PV 0.0 Pipe: 15 120.7 6.357 PL 8.50 PF 0.0 M2 15.9 0.0 18.5 0.0 1.2 120 FTG ---- PE 0.4 M3A 15.0 0.0 18.9 0.0 0.001 TL 8.50 PV 0.0 Pipe: 16 120.7 6.357 PL 1,50 PF 0.0 M3A 15.0 0.0 18.9 0.0 1.2 120 FTG ---- FE 0,0 M3 15.0 0.0 18.9 0.0 0.001 TL 1.50 PV 0,0 Pipe: 16A 99.3 6.357 PL 10.00 PF 0.0 M3 15.0 0.0 18.9 0.0 1.0 120 FTG ---- FE 0.4 M4 14.2 0.0 19.2 0.0 0.000 TL 10,00 PV 0.0 Pipe: 1.7 77.3 6,357 PL 10.00 PF 0.0 M4 14.2 0.0 19.2 0.0 0.8 120 FTG ---- PE 0.2 M5 13.7 0.0 19.4 0.0 0.000 TL 10.00 PV 0.0 Pipe: 18 38.0 6.357 PL 13.00 PF 0.0 MS 13.7 0.0 19.4 0.0 0.4 120 FTG ---- PE 0.4 M6 12,7 0.0 19.9 0.0 0.000 TL 13.00 PV 0.0 Pipe: 19 39.7 4.260 FL 10.00 PF 0.0 M7 16.8 0.0 17.5 0.0 0.9 120 FTG ---- FE 0.4 M8 15.9 0.0 17.9 0.0 0.001 TL 10.00 PV 0.0 Pipe: 20 61.5 4.260 PL 10.00 PF 0.0 M8 15.9 0.0 17.9 0.0 1.4 120 FTG ---- PE 0.4 M9 15.0 0.0 18.3 0.0 - 0.001 TL 10.00 PV 0.0 Pipe: 21 82.9 4.260 PL 10.00 PF 0.0 M9 15.0 0.0 18.3 0.0 1.9 120 FTG ---- FE 0.4 mlo 14.2 0.0 18.6 0.0 0.002 TL 10.00 PV .0.0 Pipe: 22 104.8 4.260 FL 10.00 PF 0.0 M10 14.2 0.0 18.6 0.0 2.4 120 FTG ---- FE 0.2 Mil 13.7 0.0 18.8 0.0 0.003 TL 10.00 PV 0.0 Pipe: 23 53.3 4.260 FL 12.00 PF 0.0 Mil 13.7 0.0 18.8 0.0 1.2 120 FTG ---- PE 0.4 M12 12.8 0.0 19.2 0.0 0.001 TL 12.00 PV 0.0 Pipe: 24 23.4 2.703 FL 2.00 PF 0.0 M 17.2 0.0 17.9 0.0 1.3 120 FTG TL FE -0.7 Ri 18.8 0.0 17.2 0.0 0.002 TL 26.87 PV 0.0 Pipe: 25 21.7 2.703 FL 2.00 PF 0.0 M2 .15.9 0.0 18.5 0.0 1.2 120 FTG TL FE -0.9 R2 17.9 0.0 17.6 0.0 0.002 TL 26.87 PV 0.0 Pipe: 26 21.4 2.703 FL 2.00 PF 0.0 M3 15.0 0.0 18.9 0.0 1.2 120 FTG TL PE -0.9 R3 17.0 0.0 18.0 0.0 0.001 TL 26.87 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOES IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG. G\6-2 JOE TITLE: building g - .1 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: 27 21.9 2.703 PL 2.00 PF 0.0 M4 14.2 0.0 19.2 0.0 1.2 120 FTG TL FE -0.9 R4 16.2 0.0 18.3 0.0 0.002 TL 26.87 PV 0.0 Pipe: 28 .39.4 2.703 FL 1.50 FE' 0.1 M5 13.7 0.0 19.4 0.0 2.2 120 FTG TL PE -0,6 R5 15.2 0.0 18.7 0.0 0.005 TL 26.37 PV 0.0 Pipe: 29 38.0 2.703 PL 1.60 FE' 0.1 M6 12.7 0.0 19.9 0.0 2.1 120 FTG TL PE -0.7 R6 14.2 0.0 19.1 0.0 0.004 TL 26.47 PV 0.0 Pipe: 30 -23.4 2.703 PL .2.00 PF 0.0 M7 16.8 0.0 17.5 0.0 1.3 120 FTG TL FE -0.9 R7 18.8 0.0 16.7 0.0 0.002 TL 26.87 PV 0.0 Pipe: 31 -21.7 2.703 PL 2.00 FE' 0.0 M8 15.9 0.0 17.9 0.0 1.2 120 FTG TL FE -0.9 R8 17.9 0.0 17.1 0.0 0.002 TL 26.87 PV 0.0 Pipe: 32 -21.4 2.703 FL 2.00 PF 0.0 M9 15.0 0.0 18.3 0.0 1.2 120 FTG TL PE -0.9 R9 17.0 0.0 17.5 0.0 0.001 TL 26.87 PV 0.0 Pipe: 33 -21.9 2.703 PL 2.00 PF 0.0 M10 14.2 0.0 18.6 0.0 1.2 120 FTG TL PE -0.9 RiO 16.2 0.0 17.8 0.0 0.002 TL 26.87 PV 0.0 Pipe: 34 51.5 2.703 FL 1.50 PF 0.2 Mil 13.7 0.0 18.8 0.0 2.9 120 FTG TL PE -0.6 Mi 15.2 0.0 18.0 0.0 0.007 TL 26.37 PV 0.1 Pipe: 35 53.3 2,703 PL 1.50 FE' 0.2 M12 12.8 0.0 19.2 0.0 3.0 120 FTG TL FE -0.6 R12 14.2 0.0 18.3 0.0 0.008 TL 26.37 PV 0.1 Pipe: 36 23.4 2.703 PL 168.25 FE' 0.4 Ri 18.8 0.0 17.2 0.0 1.3 120 FTG T4L FE 0.0 L41 18.8 0.0 16.8 0.0 0.002 TL 211.77 PV 0.0 Pipe: 37 13.4 2.703 FL 9.75 PF 0.0 L41 18.8 0.0 16.8 0.0 0.7 120 FTG TL FE 0.0 S45 18.8 0.0 16.8 0.0 0.001 TL 34.62 PV 0.0 Pipe: 38 13.4 2.703 PL 12.00 PF 0.0 S45 18.8 0.0 16.8 0.0 0.7 120 FTG ---- FE 0.0 S44 18.8 0.0 16.8 0.0 0.001 TL 12.00 PV 0.0 Pipe: 39 13.4 2.703 PL 9.50 FE' 0.0 S44 18.8 0.0 16.8 0.0 0.7 120 FTG L FE 0.0 S43 18.8 0.0 16.8 0.0 0.001 TL 15.72 PV 0.0 Pipe: 40 13.4 2.703 FL 7.25 PF 0.0 S43 18.8 0.0 16.8 0.0 0.7 120 FTG ---- FE 0.0 S42 18.8 0.0 16.8 0.0 0.001 TL 7.25 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS INPROGRESS\PALOMAR FORUM\SEFP\CALCS\ELDG, G\6-2 JOE TITLE: building g - .1 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: 41 13.4 2.703 PL 4.50 PF 0.0 S42 18.8 0.0 16.8 0.0 0,7 120 FTG ---- PE 0.0 L37 18.8 0.0 16.8 0.0 0.001 TL 4.50 PV 0.0 Pipe: 42 10.1 2.703 PL 15.33 PF 0.0 L41 18.8 0.0 16.8 0.0 0.6 120 FTG TL PE 0.0 S41 18.8 0.0 16.8 0.0 0.000 TL 40.20, PV 0.0 Pipe: 43 10.1 2.703 PL 5.41 PF 0.0 S41 18.8 0.0 16.8 0,0 0.6 120 FTG ---- PE 0.0 L40 18.8 0.0 16.8 0.0 0.000 TL 5.41 PV 0.0 Pipe: 44 0.0 1.610 PL 1.75 'PF 0.0 S40 18.8 0.0 16.8 0.0 0.0 120 FTG T PE 0.0 L40 18.8 0.0 16.8 0.0 0.000 TL 9.75 PV 0.0 Pipe: 45 10.1 2.703 PL 8.47 PF 0.0 L40 18.8 0.0 16.8 0.0 0.6 120 FTG 4L PE 0,0 S39 18.8 0.0 16.8 0.0 0.000 TL 33.34 PV 0.0 Pipe: 46 10.1 2.703 PL 10.41 PF 0.0 S39 18.8 0.0 16.8 0.0 0.6 120 FTG L FE 0.0 L38 18.8 0.0 16.8 0.0 0.000 TL 16.63 PV 0.0 Pipe: 47 0.0 1.610 PL 2.08 PF 0.0 S38 18.8 0.0 16.8 0.0 0.0 120 FTG T PE 0.0 L38 18.8 0.0 16.8 0.0 0.000 TL 10.08 PV 0.0 Pipe: 48 10.1 2,703 FL 22.75 PF 0.0 L38 18.8 0.0 16.8 0.0 0.6 120 FTG L FE 0.0 L37 18.8 0.0 16.8 0.0 0.000 TL 28.97 PV .0.0 Pipe: 49 23.4 2.703 FL 1.75 PF 0.0 L37 18.8 0.0 16.8 0.0 1.3 120 FTG 7.0 PE 0.0 S37 18.8 0.0 16.7 0.0 0.002 TL 8.75 PV 0.0 Pipe: 50 23.4 2.703 FL 8.00 PF 0.0 S37 18.8 0.0 16.7 0.0 1.3 120 FTG ---- PE 0.0 S36 18.8 0.0 16.7 0.0 0.002 TL 8.00 PV 0.0 Pipe: 51 23.4 2.703 PL 8.00 PF 0.0 S36 18.8 0.0 16.7 0.0 1.3 120 FTG ---- FE 0.0 535 18.8 0.0 16.7 0.0 0.002 TL 8.00 PV 0.0 Pipe: 52 23.4 2.703 FL 1.58 PF 0.0 S35 18.8 0.0 16.7 0.0 1.3 120 FTG T FE 0.0 R7 18.8 0.0 16.7 0.0 0,002 TL 20.23 PV 0.0 Pipe: 53 21.7 2.703 PL 165.25 PF 0.3 R2 17.9 0.0 17.6 0.0 1.2 120 FTG T4L PE 0,0 S33 17.9 0.0 17.3 0.0 0.002 TL 208.77 PV 0.0 Pipe: 54 21.7 2.703 PL 12,50 PF 0.1 S33 17,9 0.0 17.3 0.0 1.2 120 FTG 4L PE 0.0 S32 17.9 0.0 17.2 0.0 0.002 TL 37.37 PV 0.0 L SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 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: 55 21.7 2.703 PL 7.00 FE' 0.0 S32 17.9 0.0 17.2 0.0 1.2 120 FTG ---- PE 0.0 S31 17.9 0.0 17.2 0.0 0.002 TL 7.00 PV 0.0 Pipe: 56 21.7 2,703 FL 5.33 PF 0.0 S31 17,9 0.0 17.2 0.0 1.2 120 FTG L FE 0.0 L30 17,9 0.0 17.2 0.0 0.002 TL 11.55 PV 0.0 Pipe: 57 21,7 2.703 PL 7.08 FE' 0.0 L30 17.9 0.0 17.2 0.0 1.2 120 FTG ---- PE 0.0 S29 17.9 0.0 17.2 0.0 0.002 TL 7.08 PV 00 Pipe: 58 21,7 2.703 PL 6.66 PF 0,0 S29 17.9 0.0 17.2 0,0 1.2 120 FTG ---- PE 0.0 S28 17.9 0.0 17.2 0.0 0.002 TL 6.66 PV 0.0 Pipe: 59 21.7 2.703 PL 8.91 PF 0.0 S28 17,9 0.0 17.2 0.0 1.2 120 FTG ---- PE 0.0 S27 17.9 0.0 17.1 0.0 0.002 TL 8.91 PV 0.0 Pipe: 60 21.7 2.703 PL 8.41 PF 0.0 S27 17.9 0.0 17.1 0.0 1.2 120 FTG ---- PE 0.0 S26 17.9 0.0 17.1 0.0 0.002 TL 8.41 PV 0.0 Pipe: 61 21.7 2.703 PL 8.00 PF 0.0 S26. 17.9 0.0 17.1 0.0 1.2 120 FTG ---- PE 0.0 S25 17.9 0,0 17.1 0.0 0.002 TL 8.00 PV 0,0 Pipe: 62 21.7 2.703 FL 8.00 PF 0.0 S25 17.9 0.0 17.1 0.0 1.2 120 FTG ---- FE 0.0 S24 17.9 0.0 17.1 0.0 0.002 TL 8.00 PV 0.0 Pipe: 63 21.7 2.703 PL 1.58 PF 0.0 S24 17,9 0.0 17.1 0.0 1.2 120 FTG T FE 0.0 R8 17.9 0.0 17.1 0.0 0.002 TL 20.23 PV 0.0 Pipe: 64 21.4 2.703 FL 157.50 PF 0.3 R3 17.0 0.0 18.0 0.0 1.2 120 FTG T PE 0.0 S23A 17.0 0.0 17.7 0.0 0.001 TL 176.15 PV 0.0 Pipe: 65 21.4 2.703 PL 5.41 PF 0.0 523A 17,0 0.0 17.7 0.0 1.2 120 FTG ---- PE 0.0 L23 17.0 0.0 17.7 0.0 0.001 TL 5.41 PV 0.0 Pipe: 66 0.0 1.610 PL 4.25, FE' 0.0 S23 17.0 0.0 17.7 0.0 0.0 120 FTG T PE 0.0 L23 17.0 0.0 17.7 0.0 0.000 TL 12.25 PV 0.0 Pipe: 67 21.4 2.703 PL 7.08 FE' 0.0 L23 17.0 0.0 17,7 0.0 1.2 120 FTG 4L FE 0.0 S22 17.0 0.0 17.6 0.0 0.001 TL 31.95 PV 0.0 Pipe: 68 21.4 2.703 FL 7.00 PF 0.0 S22 17.0 0.0 17.6 0.0 1.2 120 FTG ---- PE 0.0 S21 17.0 0.0 17,6 0.0 0.001 TL 7.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 . 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: 69 21.4 2.703 FL 7.00 PF 0.0 S21 17.0 0.0 17.6 0.0 1.2 120 FTG ---- PE 0.0 S20 17.0 0.0 17.6 0.0 0.001 TL 7.00 PV 0.0 Pipe: 70 21.4 2.703 FL 6.58 PF 0.0 S20 17.0 0.0 17.6 0.0 1.2 120 FTG ---- PE 0.0 S19 17.0 0.0 17.6 0.0 0.001 TL 6.58 PV 0.0 Pipe: 71 21.4 2.703 PL 10.75 PF 0.0 S19 17.0 0.0. 17.6 0.0 1.2 120 FTG L PE 0.0 S18 17.0 0.0 17.6 0.0 0.001 TL 16.97 PV 0.0 Pipe: 72 21.4 2.703 PL 8.08 PF 0.0 S18 17.0 0.0 17.6 0.0 1.2 120 FTG ---- PE 0.0 S17 17.0 0.0 17.6 0.0 0.001 TL 8.08 PV 0.0 Pipe: 73 . 21.4 2.703 PL 7,66 PF 0.0 S17 17.0 0.0 17.6 0.0 1.2 120 FTG 2L FE 0.0 S16 17.0 0.0 .17.6 0.0 0.001 TL 20.09 PV 0.0 Pipe: 74 . 21.4 2.703 FL 8.91 PF 0.0 S16 17.0 0.0 17.6 0.0 1.2 120 FTG ---- FE 0.0 S15 17.0 0.0 17.5 0.0 0.001 TL 8.91 PV 0.0 Pipe: 75 21.4 2.703 PL 9.41 PF 0.0 S15 17.0 0,0 17.5 0.0 1.2 120 FTG 2L PE 0.0 S14 17,0 0.0 17.5 0.0 0.001 TL 21.84 PV 0.0 Pipe: 76 21.4 2.703 PL 8.00 PF 0.0 514 17.0 0.0 17.5 0.0 1.2 120 FTG ---- FE 0.0 S13 17.0 0.0 17.5 0.0 - 0.001 TL 8.00 FV 0.0' Pipe: 77 21.4 2.703 FL 8.00 PF 0.0 S13 17.0 0.0 17.5 0.0 1.2 120 FTG ---- PE 0.0 S12 17.0 0.0 17.5 0.0 0.001 TL 8.00 PV 0.0 Pipe: 78 21.4 2.703 FL 1.58 FE' 0.0 S12 17.0 0.0 17.5 0.0 1.2 120 FTG T FE 0.0 R9 17.0 0.0 17.5 0.0 0.001 TL 20.23 PV 0.0 Pipe: 79 21.9 2.703 FL 162.91 PF 0.3- R4 16.2 0.0 18.3 0.0 1.2 120 FTG T FE 0.0 Lii . 16.2 0.0 18.0 0.0 0.002 TL 181.56 PV 0.0 Pipe: 80 0.0 1.610 FL 2.25 PF 0.0 Sil 16.2 0.0 18.0 0.0 0.0 120 FTG T PE. 0.0 Lii 16.2 0.0 18.0 0.0 0.000 TL 10.25 PV 0.0 Pipe: 81 21.9 2.703 FL 7.08 PF 0.0 Lii 16.2 0.0 18.0 0.0 1.2 120 FTG 4L FE 0,0 Slo 16.2 0.0 18.0 0.0 0.002 TL 31,95 PV 0.0 Pipe: 82 21.9 2.703 FL 7.00 PF 0.0 Slo 16.2 0.0 18.0 0.0 1.2 120 FTG ---- FE 0.0 S9 16.2 0.0 18.0 0.0. 0.002 TL 7,00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOS IN PROGRESS\FALOMAR FORUM\SEFF\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 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: 83 21.9 2.703 PL 7.00 PF 0.0 S9 16.2 0.0 18.0 0.0 1.2 120 FTG ---- PE 0.0 58 16.2 0.0 18.0 0.0 0.002 TL 7.00 PV 0.0 Pipe: 84 21.9 2.703 FL 7.00 PF 0.0 S8 16,2 0.0 18.0 0.0 1.2 120 FTG ---- PE 0.0 S7 16.2 0.0 18.0 0.0 0.002 TL 7.00 PV 0.0 Pipe: 85 21.9 2.703 PL 42.08 PF 0.1 S7 16.2 0.0 18.0 0.0 1.2 120 FTG L FE 0.0 L6 16.2 0.0 17.9 0.0 0.002 TL 48.30 PV 0.0 Pipe: 86 0.0 1.610 FL 1.41 PF 0.0 S6 16.2 0.0 17.9 0.0 0.0 120 FTG T PE 0.0 L6 16.2 0.0 17.9 0.0 0.000 TL 9.41 PV 0.0 Pipe: 87 21.9 2.703 FL 7.15 PF 0.0 L6 16.2 0.0 17.9 0.0 1.2 120 FTG ---- PE 0.0 L5 16.2 0.0 17.9 0.0 0.002 TL 7.15 PV 0.0 Pipe: 88 0.0 1.610 FL 1,41 PF 0.0 S5 16.2 0.0 17.9 0.0 0.0 120 FTG T FE 0.0 L5 16.2 0.0 17.9 0.0 0.000 TL 9.41 PV 0.0 Pipe: 89 21.9 2.703 PL 6.00 PF 0.0 L5 16.2 0.0 17.9 0.0 1.2 120 FTG ---- FE 0.0 L4 16.2 0.0 17.9 0.0 0.002 TL 6.00 PV 0.0 Pipe: 90 0.0 1.610 PL 1.41 PF 0.0 S4 16.2 0.0 17.9 0.0 0.0 120 FTG T FE 0.0 L4 16.2 0.0 17.9 0.0 0.000 TL 9.41 PV 0.0 Pipe: 91 21.9 2.703 FL 7.16 PF 0.0 L4 16,2 0.0 17.9 0.0 1.2 120 FTG ---- FE 0.0 53 16.2 0.0 17.9 0.0 0.002 TL 7.16 PV 0.0 Pipe: 92 21.9 2.703 FL 8.00 PF 0.0 S3 16.2 0.0 17.9 0.0 1.2 120 FTG ---- FE 0.0 S2 16.2 0.0 17.8 0.0 0.002 TL 8.00 PV 0.0 Pipe: 93 21.9 2.703 FL 8.00 PF 0.0 S2 16.2 0.0 17.8 0.0 1.2 120 FTG ---- PE 0.0 Si 16.2 0.0 17.8 0.0 0.002 TL 8.00 PV 0.0 Pipe: 94 21.9 2.703 FL 1.58 PF 0.0 Si 16.2 0.0 17.8 0.0 1.2 120 FTG T FE 0.0 RiO 16.2 0.0 17.8 0.0 0.002 TL 20.23 PV 0.0 Pipe: 95 39.4 2.703 FL 211.00 PF 1.1 R5 15.2 0.0 18.7 0.0 2.2 120 FTG TL FE -0.4 L64 16.2 0.0 17.2 0.0 0.005 TL 235.87 PV 0.0 Pipe: 96 16.6 2.703 FL 8.92 PF 0.0 L64 16,2 0.0 17.2 0.0 0.9 120 FTG ---- FE 0.0 L63 16.2 0.0 17.2 0.0 0.001 TL 8.92 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/28/2001C:\DWG\FIRE SFRINKLER\JOES IN FROGRESS\FALOMAR FORUM\SEFF\CALCS\BLDG. G\6-2 JOE TITLE: building g - .1 FIFE 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: 97 -6.1 2.703 PL 10.75 PF 0.0 L63 16.2 0.0 17.2 0.0 0.3 120 FTG ---- PE 0.0 L62 16.2 0.0 17.2 0.0 0.000 TL 10,75 PV 0.0 Pipe: 98 -28.8 2.703 PL 15.00 PF 0.0 L62 16.2 0.0 17.2 0.0. 1.6 120 FTG ---- PE 0.0 L61 16.2 0.0 17.2 0.0 0.003 TL 15.00 FV 0.0 Pipe: 99 -51.5 2.703 FL 44.16 PF 0.3 L61 16.2 0.0 17.2 0.0 2.9 120 FTG ---- PE 0.4 Rll 15.2 0.0 18.0 0.0 ' 0.007 TL 44.16 PV 0.1 Pipe: 100 38.0 2.703 PL 235.00 PF 1.2 R6 14.2 0.0 19.1 0.0 2.1 120 FTG T3L FE -0.8 L68 16.2 0.0 17.1 0.0 0.004 TL 272.30 PV 0.0 Pipe: 101 15.3 2.703 FL 9.83 PF 0.0 L68 16.2 0.0 17.1 0.0 0.9 120 FTG ---- FE 0.0 L67 16,2 0.0 17.1 0.0 0.001 TL 9.83 PV 0.0 Pipe: 102 -7.3 2.703 FL 10.75 PF 0..0 L67 16.2 0.0 '17.1 0.0 0.4 120 FTG ---- FE 0.0 L66 16.2 0.0 17,1 0.0 0.000 TL 10.75 PV 0.0 Pipe: 103 -29,8 2.703 FL 9.25 PF 0.0 L66 16.2 0.0 17.1 0.0 1.7 120 FTG ---- FE 0.0 L65 . 16.2 0.0 17.1 0.0 0.003 TL 9,25 PV 0.0 Pipe: 104 -53.3 2.703 FL 49.92 PF 0.4 L65 16.2 0.0 17.1 0.0 3.0 120 FTG ---- FE 0.8 R12 14.2 0.0 18,3 0.0 0.008 TL 49.92 PV 0,1 Pipe: 105 22.7 1.049 FL 9.67 PF 3.9 L61 16.2 0.0 17.2 0.0 8.4 120 FTG 2T2L PE 3.1 S61 9.0 5.6 16.4 22.7 0.164 TL 23.67 PV 0.5 Pipe: 106 22.8 1.049 FL 8.67 PF 3.7 L62 16.2 0.0 17.2 0.0 8.4 120 FTG 2T2L FE 3.1 S62 9.0 5.6 16.5 22.8 0.165 TL 22.67 PV 0.5 Pipe: 107 . 22,7 1.049 FL 9.75 PF 3.9 L63 16.2 0.0 17.2 0.0 '8.4 120 FTG 2T2L PE 3.1 S63 9.0 5.6 16.4 22.7 0.164 TL 23.75 PV 0.5 Pipe:' 108 22.8 1.049 FL 8.75 PF 3.8 L64 16.2 0.0 17.2 0.0 8.4 120 FTG 2T2L FE 3.1 S64 9.0 5.6 16.5. 22.8 0.165 TL 22.75 PV 0.5 Pipe: 109 23.6 1.049 FL 7.33 PF 2.5 L65 16.2 0.0 17.1 0.0 8.7 120 FTG TL FE 3.1 S65 9.0 5.6 17.7 23.6 0.176 TL 14.33 PV 0.5 Pipe: 110 22.5 1.049 FL 11.00 PF 4.0 L66 16.2 0.0 17.1 0.0 8.4 120 FTG 2T2L FE 3.1 S66 9.0 5.6 16.1 22.5 0.162 TL 25.00 PV 0.5. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 "JOB TITLE: building g - .1 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: 111 22.5 1.049 PL 10.67 PF 4.0 L67 16.2 0.0 17.1 0.0 8.4 120 FTG 2T2L PE 3.1 S67 9.0 5.6 16.2 22.5 0.162 TL 24.67 PV 0.5 Pipe: 112 22.7 1.049 PL 8.67 PF 3.7 L68 16,2 0.0 17.1 0.0 8.4 120 FTG 2T2L PE 3.1 S68 9.0 5.6 16.5 22.7 0.165 TL 22.67 PV .0.5 Pipe: 113 0.0 2.703 PL 22.00 PF 0.0 L30 17.9 0.0 17.2 0.0 0.0 120 FTG 2TL PE 0.0 S30 17.9 0.0 17.2 0.0 0.000 TL 65.52 PV 0.0 Pipe: Xpress 16.3 2.227 PL 227.33 PF 0.6 TOR 17.2 0.0 17.9 0.0 1.3 120 FTG E2T PE 0.2 M7 16.8 0.0 17.5 0.0 0.002 TL 263.27 PV 0.0 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 0.106 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 8.7 ft/sec at pipe 109. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyVlv GatViv AimChk DPVlv NPTee 2.227 7.19 14.38 4.31 15.82 8.63 1.44 14.38 14.38 14.38 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 26.33 6.357 17,60 37.72 11.32 40.23 12.57 3.77 35.21 23.89 37.72 8,249 20.02 38.92 14.46 50.04 13.35 4.45 38.92 30.03 38.92 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 JOB TITLE: building g - .1 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyViv GatViv AimChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 1.610 4.00 8.00 2.00. 9.00 6.00 1.00 10.00 10.00 8.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N D Eli Tee LngEii ChkVlv BfyViv GatViv 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 LngEli ChkVlv BfyVlv GatViv NPTee 7.980 26.00 50.00 19.00 50.00 17.00 4.00 50.00 G A U G E 2 Required pressure 27.24 psi @ 282.1 gpm P R E S S U R E 84.0 1w,1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 6/28/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. G\6-2 'JOB TITLE: building g - .1 WATER SUPPLY ANALYSIS Static: 125.00 psi Resid: 20.00 psi Flow: 5390.0 gpm 140.0 LEGEND 1 Available pressure 124.55 psi 8 282.1 gpm p 5 i 28 .(2 -14.71 1 1 I 12018002400 3000 3600 4200 4800 5400 6000 FLOW (GPM) Supply Flow Curve C PALOMAR FORUM BUILDING GA Test pate: 6/28/2007 Static Hydrant: NE INTERSECTION OF K STREET AND 13 1/2 STREET. Design GPM: 182 GPM Flow Hydrant: NEW CONNECTION OF FIRE SERVICE BACKFLOW PREVENTER Design PSI: 25.0 PSI Ps 125.0 PSI Test Static Pressure Reading Available Pressure at Design GPM: 124.6 PSI Pr 20.0 PSI Test Residual Pressure Reading PSI Headroom : 99.60 PSI 80% GPMr 5390 GPM Test Flow at Residual Pressure GPM Headroom: 5068 GPM 2781% Flow Test Summary Curve QA1B5 140 120 100 80 -.-- PSI Design Point 'I 60 40 20 0+ 0 500 1000 1500 2000 2500 3000 3500 4000 Flow GPM REMOTE AREA 2 Printed 6/28/2007 -ME Contractor's Material and Test Certificate for Aboveground piping PROCEDURE Upon completion of work inspection and tests shall be made by the contractors representative and witnessed by an owners representative. All defects shall be corrected and system left in service before contractors personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners and contractor. It Is understood the owners representatives 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 G IDATEt.,,1 ?S' PROPERTY ADDRESS: 3132 tiger Run Court, Carlsbad, CA PLANS ACCEPTED BY APPROVING AUTHORITIES-(NAMES): Carlsbad Fire Dept. ADDRESS: 1635 Faraday Ave., Carlsbad, CA INSTALLATION CONFORMS TO ACCEPTED PLANS [j YES Li NO EQUIPMENT USED IS APPROVED P1 YES []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? El YES []NO IF NO, EXPLAIN HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES: ' Li YES NO SYSTEM COMPONENTS INSTRUCTIONS EvES NO CARE AND MAINTENANCE INSTRUCTIONS El YES El NO NFPA25 EYES NO LOCATION OF SYSTEM SUPPLIES BUILDINGS: SPRINKLERS MAKE MODEL YEAR OF MANUFACTURI ORIFICE SIZE QUANTITY TEMPERATURE RATING Tyco TY-FRL 5811 2007 3/4 150 212 Tyco TY-FRL 3221 2007 1/2 116 165 Tyco TY-FRL 3221 2007 1/2 6 165 Tyco TY-FRL 3121 2007 1/2 79 212 PIPE AND FITTINGS Type of Pipe: Sch 40, Sch 10, 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 MAKE . MODEL MIN SEC Flow Switch Potter Electric VSF-R DRY PIPE OPERATING TEST _I DRY VALVE Q.O.D. MK MODEL SERIAL NO. MAKE MODEL SE3INO. TIME TO TRIP THROUGH TEST CONNECTION TER PRESR&. AIR PRESSURE TRIP POINT AIR PRESS ' TIMJ.WAIER EACHED TEST OUTLET ALARM OPERATED PROPERLY MIN SEC PSI —PSI -PSI MIN ISEC YES NO Without Q.O.D. With D.O.D. EXPLAIN 77 El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED -L,LYjS U NO DETECTING MEDIA SUPERVID—fl YES Li NO DOES VALVE OPERATE FROM THE MRALIJP AND/OR REMOTE CONTROL STEINS Ti YES Ti NO DELUGE AND PREACTION IS THERE AN ACCESSIBLE FACILITY IN EACH ClR TESTING IF NO, EXPLAIN VALVES El YES DOES CUlT OPERATE DOES EACH CIRCUIT-----MAXIMUM TIME TO MAKE MODEL ERVISION LOSS ALARM? OPERATE VALVE RELEASE? RATE RELEASE YES NO YES NO MIN. SEC• PRESSURE REDUCING LOATION SETTING STATIC PRESSURE RESIDUAL PRESS E & FLOOR MODEL WING) VALVE TEST - OUTL I OUTLET (PSI) FLOW (GPM) TEST DESCRIPTION HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.8 bars) for two hours or 50 pat (3.4 bars) above static pressure in excess of 150 pal (10.2 bars) for two flours. Differential dry-pipe valve clappers shall be left open during test to prevent damage. All abovegroung piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop which shall not exceed 1-1/2 psi (01 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 1-1/2 psi (0.1 bars) in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT .200 PSI FOR 2_ HRS DRY PIPING PNEUMATICALLY TESTED El YES El NO EQUIPMENT OPERATES PROPERLY El YES El 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? EYES NO DRAIN READING OF GAGE LOCATED NEAR WATER. RESIDUAL PRESSURE WITH VALVE IN TEST TEST SUPPLY TEST CONNECTION: PSI I CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD IN CONECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MAKE TO SPRINKLR PIPING. VERIFIED BY COPY OF THE U FORM NO. 85B El YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDER- GROUND SPRINKLER PIPING El YES 0 NO IF POWDER-DRIVEN FASTENERS ARE USED IN CONCRETE, HAS REP- IF NO, EXPLAIN RESENTATIVE SAMPLE TESTING BEEN SATISFACTORILY COMPLETED? El YES 0. NO BLANK TESTING GASKETS NUMBER USED 0 LOCATIONS NUMBER REMOVED WELDED PIPING . LiJ YES Li NO IF YES... 00 YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS DI0.9, LEVEL AR-3? El YES El NO DO YOU CERITIFY THAT THE WELDING WAS PREFORMED BY WELDERS QUALIFIED IN WELDING COMPLIANCE WITH THE REQUIREMENTS OF AT LEAST AWS DI0.9, LEVEL AR-3? El YES El 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 El NO CUTOUTS DO YOU CERITIFY THE YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL (DISCS) CUTOUTS (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC DATA NAMEPLATE NAME PLATE PROVIDED EYES ON( IF NO, EXPLAIN EFt DATE L IN SERVICE WITH ALL CONTROL VALVES OPEN: REMARKS t NAME Ut- Z:iFKINKLi=K '.UN I RAG I UK PRO-TECH FIRE PROTECTION SYSTEM CORP. ii TESTS WITNESSED BY SIGNATURES F PROPER R (SI?NED TITLE OAT OR\PRI fR GNED) TITLE c_i o-J Zo 7 ADDITIONAL EXPLANATION AND NOTES