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3146 TIGER RUN CT; ; AS070182; Permit
6/20/24, 8:53 AM AS070182 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS070182 Job Address: 3146 TIGER RUN CT Permit Type: SPRINK Parcel No: 2210140400 Lot #: 0 Reference No.: 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 Applicant: - Owner: PRO-TECH FIRE PROTECTION SYSTEMS PALOMAR MELROSE L L C CORP C/O ARN.EL 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. about:blank L] PRO-TECH FIRE PROTECTION 82, 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 APPROVEVAYSUBMITTE HYDRAULIC CALCULATIONS CARLSBACFFIP4E DEPARTMENT REMOTE ARE #1 GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I CARLSBAD CA BUILDING I DATE: June 28, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: EXTRA HAZARD DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: 0.45 gpm/3000. sq. ft. 3055 sq. ft. 93 FT. IN EXTRA HAZARDS AREAS 35 sprinklers 1513.5 gpm TOTAL WATER REQUIRED(+outside hose): 2013.5 gpm FLOW AND PRESSURE (@ BOR): 1513.5 gpm 8 82.7 psi SPRINKLER ORIFICE SIZE: 3/4 inch NAME OF CONTRACTOR: PRO-TECH FIRE PROTECTION DESIGN/LAYOUT BY: SEFPF AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C16 HIC SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMR FORUM\SEFP\CALCS\BLDG. JOB TITLE: Grey Hawk Bldg. I .45 WATER SUPPLY DATA StJRCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 0 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 125.0 20.0 5390.0 108.0 2013.4 94.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 2013.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1513.4 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT A2) (GPM/FTA2) Si 20.0 K=11.20 14.0 41.9 93.0 0.450 0.451 S2 20.0 K=11.20 14.0 41.9 93.0 0.450 0.450 S3 20.0 K=11.20 14.0 41.9 93.0 0.450 0.450 S4 20.0 K=11.20 14.0 41.9 93.0 0.450 0.450 S5 20.0 K=11.20 14.1 42.1 93.0 0.450 0.452 S6 20.0 K=11.20 14.4 42.4 93.0 0.450 0.456 S7 20.0 . K=11.20 14.8 43.1 93.0 0.450 0.464 S8 20.0 K=11.20 15.6 44.2 93.0 .0.450 0.475 S8A 20.0 K=11.20 18.5 48.1 93.0 0.450 0.517 S9 20.0 K=11.20 14.0 41.9 93.0 0.450 0.451 S1O 20.0 K=11.20 14.0 41.9 93.0 0.450 0.451 Sii 20.0 K=11.20 14.0 41.9 93.0 0.450 0.451 S12 20.0 K=11.20 14.1 42.0 93.0 0.450 0.452 S13 20.0 K=11.20 14.2 42.3 93.0 0.450 0.454 S14 20.0 K=11.20 14.6 42.8 93.0 0.450 0.460 S15 - 20.0 K=11.20 15.2 43.6 93.0 0.450 0.469 S16 20.0 K=11.20 16.1 44.9 93.0 0.450 0.483 S16A 20.0 K=11.20 17.3 46.6 93.0 0.450 0.501 S17 20.0 K=11.20 14.1 42.0 93.0 0.450 0.452 S18 20.0 K=11.20 14.1 42.0 93.0 0.450 0.452 S19 20.0 K=11.20 14.1 42.0 93.0 0.450 0.452 S20 20.0 K=11.20 14.1 42.1 93.0 0.450 0.453 S21 20.0 K=11.20 14.3 42.4 93.0 0.450 0.456 S22 20.0 K=11.20 14.7 43.0 93.0 0.450 0.462 S23 20.0 . K=11.20 15.3 43.9 93.0 0.450 0.472 S24 20.0 K=11.20 16.3 45.2 93.0 0.450 0.486 524A 20.0 K=11.20 17.6 47.0 93.0 0.450 0.505 S25 20.0 K=11.20 14.4 42.4 93.0 0.450 0.456 S26 20.0 K=11.20 14.4 42.4 93.0 0.450 0.456 S27 20.0 K=11.20 14.4 42.5 93.0 0.450 0.457 S28 20.0 K=11.20 14.5 42.7 93.0 0.450 0.459 S29 . 20.0 K=11.20 14.8 43.1 93.0 0.450 0.464 $30 20.0 K=11.20 15.3 43.9 93.0 0.450 0.472 S31 20.0 K=11.20 16.1 45.0 93.0 0.450 0.484 S32 20.0 K=11.20 17.3 46.6 93.0 0.450 0.501 I\6-2E n SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. I .45 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT.. (FT) (PSI) (GPM) (FT A2) (GPM/FT"2) Mi4 17.5 - - - - 16.2 --- M13 17.5 - - - - 16.1 --- M12 17.5 - - - - 15.9 - - - Mu 17.5 - - - - 15.8 - - - . M10 17.5 - - - - 15.7 --- M9 17.5 - - - - 15.7 ___ M8 17.5 - --- 73.4 --- M7 17.5 - - - - 73.4 --- M6 17.5 - - - - 73.4 --- M5 17.5 - - - - 73.5 --- M4 17.5 - - - - 73.8 --- M3 17.5 - - - - 74.1 - -.- Li 20.0 - - - - 19.0 --- L2 20.0 - - - - 20.5 - - - -. -- L3 20.0 ---- 22.0 - - - L4 20.0 - - - - 23.6 --- L5 20..0 - - - - 18.3 --- L6 20.0 - - - - 18.5 --- L7 20.0 - - - - 19.1 --- L8 20.0 - - -i- 19.9 --- L9 20.0 - - - - 21.6 .--- LiO 20.0 ---- 45.2 - - - Lii 20.0 - - - - 61.2 --- P1 8.9 - - - - 23.8 --- P2 8.9 - - - - 25.3 --- P3 8.9 - - - - 26.8 --- P4 8.9 - - - - 28.4 --- P5 8.9 - - - - 23.1 --- P6 8.9 - - - - 23.3 --- P7 8.9 - - - - 23.9 --- P8 8.9 - - - - 24.7 --- P9 8.9 - - - - 26.4 --- R2 20.0 ----- 16.7 - - - Ri 20.0 - - - - 16.6 --- R3 20.0 -. - - - 14.3 . --- R4 20.0 - - - - 14.4 --- R5 20.0 - -- - 14.4 --- R6 20.0 - - - - 14.5 --- R7 20.0 - - - - 70.3 --- R8 20.0 - - - - 69.9 --- R9 20.0 - - - - 67.2 - - - RiO 20.0 - - - - 66.7 - - - - - - - - - Rll 20.0 - - - - 66.7 --- Ri2 20.0 - - - - 67.7 - - - TOR 17.2 - - - - 75.2 --- BOR 2.0 - - - - 82.7 - - - DI -3.0 - - - - 85.8 --- UG2 -3.0 - - - - 90.2 --- BF2 3.0 - - - - 88.6 --- BF1 3.0 - - - - 92.6 - -- UGi -3.0 - - - - 95.5 - - - UG -3.0 ---- 96.5 - - - Ui . 11.0 - - - - 92.9 - - - U 11.0 - - - - 94.1 - - - HYD 11.0 HOSE STREAM 93.8 500.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2 JOB TITLE: Grey Hawk Bldg. I .45 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FTA2) (GPM/FTA2) SOURCE 13.5 SOURCE 94.2 2013.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. 1 .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: 1 140.5 4.310 PL 12.25 PF 0.1 M14 17.5 0.0 16.2 0.0 3.1 120 FTG ---- PE 0.0 M13 17.5 0.0 16.1 0.0 0.005 TL 12.25 PV. 0.1 Pipe: 2 287.1 4.310 PL 12.00 PF 0.2 M13 17.5 0.0 16.1 0.0 6.3 120 FTG ---- PE 0.0 M12 17.5 0.0 15.9 0.0 0.018 TL 12.00 PV 0.3 Pipe: 3 192.0 4.310 PL 11.00 PF 0.1 M12 17.5 0.0 15.9 0.0 4.2 120 FTG ---- PE 0.0 Mil 17.5 0.0 15,8 0.0 0.009 TL 11.00 PV 0.1 Pipe: 4 . 117.1 4.310 PL 11.00 PF 0..0 .Mll 17.5 0.0 15.8 0.0 2.6 120 FTG ---- PE 0.0 M10 17.5 0.0 15.7 0.0 0.004 TL 11.00 PV .0.0 Pipe: 5. . . . . 47.7 4.310 PL 11.00 PF 0.0 MiD. 17.5 .0.0 15.7 0.0 1.0 120 FTG ---- PE 0.0 M9 17.5 0.0 15.7 0.0 0.001 TL 11.00 PV 0.0 Pipe: 6 . -136.0 6.403 PL 12.25 PF 0..0 M8 17.5 0.0 73.4 0.0 1.4 120 FTG ---- PE 0.0 M7 17.5 0.0 73.4 0.0 0.001 TL 12.25 PV 0.0 Pipe: 7 . -287.1 6.403 PL 11.41 PF 0.0 M7 17.5 0.0 73.4 0.0 2.9 120 FTG ---- PE 0.0 M6 . .17.5 0.0 73.4 0.0 0.003 TL 11.41 PV 0.1 Pipe: 8 . -579.5 6.403 PL 9.75 PF 0.1 M6 17.5 0.0 73.4 0.0 5.8 120 FTG ---i- PE 0.0 M5 17.5 0.0 73.5 0.0 0.010 TL. 9.75 PV 0.2 Pipe: 9 -892.5 6.403 PL 9.75 PF 0.2 M5 . 17.5 0.0 73.5 0.0 8.9 120 FTG ---- PE 0.0 M4 17.5 0.0 73.8 0.0 0.022 TL 9.75 PV 0.5 Pipe: 10 -1212.6 6.403 PL 9.75 PF 0.4 M4 . 17.5 0.0 73.8 0.0 12.1 120 FTG ---- PE 0.0 M3 17.5 0.0 74.1 0.0 0.039 TL 9.75 PV 1.0 Pipe: 11 -140.5 2.203 PL 1.50 PF 1.6 M14 17.5 0.0 16.2 0.0 11.8 120 FTG T PE -1.1 Ri 20.0 0.0 16.6 0.0 0.129 TL 12.15 PV 0.9 • Pipe: 12 -140.5 2.203 PL 7.42 PF 2.3 Ri . 20.0 0.0 16.6 0.0 11.8 120 FTG T PE 0.0 Li 20.0 0..0 19.0 0.0 0.129 TL 18.07 PV 0.9 Pipe: 13 -140.5 2.203 PL 12.00 PF 1.6 Lb 20.0 0.0 19.0 0.0 11.8 120 FTG ---- PE 0.0 L2 20.0 0.0 20.5 0.0 0.129 TL 12.00 PV 0.9 Pipe:. 14 -140.5 2.203 PL 11.67 PF 1.5 L2 • 20.0 0.0 20.5 0.0 11.8 120 FTG ---- PE 0.0 L3 20.0 0.0 22.0 0.0 0.129 •.TL 11.67 PV 0.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE:• 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN FROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. I .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: 15 -140.5 2.203 PL 12.08 PF 1.6 L3 20.0 0.0 22.0 0.0 11.8 120 FTG ---- PE 0.0 L4 20.0 0.0 23.6 0.0 0.129 TL 12.08 PV 0.9 Pipe: 16 -140.5 2.203 PL 152.75 PF 21.6 L4 20.0 0.0 23.6 0.0 11.8 120 FTG TL PE 0.0 L10 20.0 0.0 45.2 0.0 0.129 TL 167.13 PV 0.9 Pipe: 17 -146.6 2.203 PL 7.42 PF 1.6 R2 20.0 0.0 16.7 0.0 12.3 120 FTG L PE 0.0 L5 20.0 0.0 18.3 0.0 0.140 TL 11.15 PV 1.0 Pipe: 18 -146.6 2.203 PL 1.67 PF 0.2 L5 20.0 0.0 18.3 0.0 12.3 120 FTG ---- FE 0.0 L6 20.0 0.0 18.5 0.0 0.140 TL 1.67 PV 1.0 Pipe: 19 -146.6 2.203 PL 4.25 PF 0.6 L6 20.0 0.0 18.5 0.0 12.3 120 FTG ---- PE 0.0 L7 20.0 0.0 19.1 0.0 0.140 TL 4.25 PV 1.0 Pipe: 20 -146.6 2.203 PL 6.08 PF 0.8 L7 20.0 0.0 19.1 0.0 12.3 120 FTG ---- PE 0.0 L8 20.0 0.0 19.9 0.0 0.140 TL 6.08 PV 1.0 Pipe: 21 -146.6 2.203 FL 11.67 PF 1.6 L8 20..0 0.0 19.9 0.0 12.3 120 FTG ---- PE 0.0 L9 20.0 0.0 21.6 0.0 0.140 TL 11.67 PV 1.0 Pipe: 22 -146.6 2.203 FL 154.00 PF 23.6 L9 20.0 0.0 21.6 0.0 12..3 120 FTG 4L PE 0.0 L10 20.0 0.0 45.2 0.0 0.140 TL 168.92 PV 1.0 Pipe: 23 -287.1 2.703 FL 64.00 PF 16.0 L10 20.0 0.0 45.2 0.0 16.1 120 FTG TL PE 0.0 Lii 20.0 0.0 61.2 0.0 0.179 TL 89.20 PV 1.7 Pipe: 24 -151.1 2.203 PL 48.58 PF 8.8 Lii 20.0 0.0 61.2 0.0 12.7 120 FTG T PE 0.0 R8 20.0 0.0 69.9 0.0 0.148 TL 59.23 PV 1.1 Pipe: 25 -136.0 2.203 PL 60.83 PF 9.2 Lii 20.0 0.0 61.2 0.0 11.4 120 FTG TL FE 0.0 R7 20.0 0.0 70.3 0.0 0.122 TL 75.21 PV 0.9 Pipe: 26 0.0 1.049 FL 12.67 PF 0.0 Li 20.0 0.0 19.0 0.0 0.0 120 FTG 2E2T FE 4.8 P1 8.9 0.0 23.8 0.0 0.000 TL 26.67 PV 0.0 Pipe: 27 0.0 1.049 FL 11.42 PF 0.0 L2 20.0 0.0 20.5 0.0 0.0 120 FTG E2T FE 4.8 P2 8.9 0.0 25.3 0.0 0.000 TL 23.42 PV 0.0 Pipe: 28 0.0 1.049 PL 11.42 PF 0.0 L3 20.0 0.0 22.0 0.0 0.0 120 FTG E2T PE 4.8 P3 8.9 0.0 26.8 0.0 0.000 TL 23.42 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. I .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: 29 0.0 1.049 PL 12.33 PF 0.0 L4 20.0 0.0 23.6 0.0 0.0 120 FTG 2E2T PE 4.8 P4 8.9 0.0 28.4 0.0 .0.000 TL 26.33 PV 0.0 .Pipe:.30 0.0 1.049 PL 12.75 PF 0.0 L5 20.0 0.0 18.3 0.0 0.0 120 FTG E2T PE 4.8 P5 8.9 0.0 23.1 0.0 0.000 TL 24.75 PV 0.0 Pipe: 31 . 0.0 1.049 PL 16.25 PF 0.0 L6 20.0 0.0 18.5 0.0 0.0 120 FTG 2ET PE 4.8 P6 8.9 0.0 23.3 0.0 0.000 TL 25.25 PV 0.0 Pipe: 32 0.0 1.049 PL 12.42 PF 0.0 L7 20.0 0.0 19.1 0.0 0.0 120 FTG 2ET PE 4.8 P7 8.9 0.0 23.9 0.0 0.000 TL 21.42 PV 0.0 Pipe: 33 - 0.0 1.049 PL 11.33 PF 0.0 L8 20.0 0.0.. 19.9 0.0 0..0 120 FTG E2T PE 4.8 P8 8.9 0.0 24.7 0.0 . 0.000 TL 23.33 PV 0.0 Pipe: 34 0.0 1.049 PL 11.33 . PF 0.0 L9 20.0 . 0.0 21.6 0.0 0.0 120 FTG E2T PE 4.8 P9 8.9 0.0 26.4 0.0 0.000 -TL 23.33 .pj 0.0 Pipe: 35 -136.0 2.203 PL 2.17 PF 2.0 R7 20.0 0.0 70.3 0.0 11.4 120 FTG TL PE 1.1 M8 17.5 0.0 73.4 0.0 0.122 TL 16.55 PV 0.9 Pipe: 36 . -146.6 2.203 PL 1.50 PF 1.7 M13 . 17.5 0.0 16.1 0.0 12.3.. 120 FTG T PE -1.1 R2 20.0 0.9 16.7 0.0 0.140 TL 12.15 PV 1.0 Pipe: 38 -151.1 2.203 . PL 2.00 PF 2.4 R8 20.0 0.0 69.9 0.0 12.7 120 FTG TL PE. 1.1 M7 17.5 0.0 73.4 0.0 0.148 TL 16.38 PV 1.1 Pipe: 39 95.1 2.703 PL 2.17 PF 0.5 M12 17.5 0.0 15.9 0.0 5.3 120 FTG T PE -1.1 R3 20.0 0.0 14.3 0.0 0.023 TL 20.77 PV 0.2 Pipe: 40 95.1 2.703 PL 5.50 PF 0.3 R3 20.0 0.0 14.3 0.0 5.3 120 FTG L PE 0.0 Si 20.0 11.2 14.0 41.9 0.023 TL 12.10 PV 0.2 Pipe: 41 53.1 2.703 PL 8.00 PF 0.1 Si 20.0 11.2 14.0 41.9 3.0 120 FTG ---- PE 0.0 S2 20.0 11.2 14.0 41.9 0.008 TL 8.00 PV 0.1 Pipe: 42 11.3 2.703 PL 8.00 PF 0.0 S2 20.0 11.2 14.0 41.9 0.6 120 FTG ---- PE 0.0 S3 20.0 11.2 14.0 41.9 0.000 TL 8.00 PV 0.0 Pipe: 43 -30.6 2.703 PL 8.00 PF 0.0 S3 20.0 11.2 14.0 41.9 1.7 .120 FTG ---- PE 0.0 S4 20.0 11.2 14.0 41.9 0.003 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. I .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: 44 -72.5 2.793 PL 8.00 PF 0.1 S4 20.0 11.2 14.0 41.9 4.1 120 FTG ---- PE 0.0 S5 20.0 11.2 14.1 42.1 0.014 TL 8.00 PV 0.1 Pipe: 45 -114.5 2.703 PL 8.00 PF 0.3 S5 20.0 11.2 14.1 42.1 6.4 120 FTG ---- PE 0.0 S6 20.0 11.2 14.4 42.4 0.033 TL 8.00 PV 0.3 Pipe: 46 -157.0 2.703 PL 8.00 PF 0.5 S6 20.0 11.2 14.4 42.4 8.8 120 FTG ---- PE 0.0 S7 . 20.0 11.2 14.8 43.1 0.059 TL 8.00 PV 0.5 Pipe: 47 -200.1 2.703 PL 8.00 PF O.7 S7 20.0 11.2 14.8 43.1 11.2 120 FTG ---- PE 0.0 S8 20.0 11.2 15.6 44.2 0.092 TL .8.00 PV 0.8 Pipe: 48 -244.3 2.703 PL 8.67 PF 2.9 S8 20.0 11.2 15.6 44..2 13.7 120 FTG 2L PE 0.0 58A 20.0 11.2 18.5 48.1 0.133 TL 21.87 PV 1.3 Pipe: 49 -292.4 2.703 PL 205.00 PF 48.7 S8A 20.0 11.2 18.5 48.1 16.3 120 FTG T6L PE 0.0 R9 20.0 0.0 67.2 0.0 0.185 TL 263.20 PV 1.8 Pipe: 50 . -292.4 2.703 PL 2.67 PF 5.2 R9 20.0 0.0 67.2 0.0 16.3 120 FTG TL PE 1.1 M6 17.5 . 0.0 73.4 0.0 0.185 TL 27.87 PV 1.8 Pipe: 51 75.0 2.703 PL 2.17 PF 0.3 Mil 17.5 0.0 15.8 0.0 4.2 120 FTG T PE -1.1 R4 20.0 0.0 14.4 0.0 0.015 TL 20.77 PV 0.1 Pipe: 52 75.0 2.703 PL 5.50 PF 0.4 R4 20.0 0.0 14.4 0.0 4.2 120 FIG T . PE 0.0 S9 20.0 11.2 14.0 41.9 0.015 TL 24.10 PV 0.1 Pipe: 53 - 33.0 2.703 PL 8.00 PF 0.0 S9 20.0 11.2 14.0 41.9 1.8 120 FTG ---- PE 0.0 Slo 20.0 11.2 14.0 41.9 0.003 TL 8.00 PV 0.0 Pipe: 54 . -8.9 2.703 PL 8.00 PF 0.0 Slo 20.0 11.2 14.0 41.9 0.5 120 FTG ---- PE 0.0 S11 20.0 11.2 14.0 41.9 0.000 TL 8.00 PV 0.0 Pipe: 55 -50.8 2.703 PL 8.00 PF 0.1 511 20.0 11.2 14.0 41.9 2.8 120 FTG ---- PE 0.0 S12 20.0 11.2 14.1 42.0 0.007 TL 8.00 PV 0.1 Pipe: 56 -92.8 2.703 FL 8.00 PF 0.2 S12 20.0 11.2 14.1 42.0 5.2 120 FTG ---- FE 0.0 S13 20.0 11.2 14.2 42.3 0.022 TL 8.00 PV 0.2 Pipe: 57 -135.0 2.703 PL 8.00 FE' 0.4 S13 20.0 11.2 14.2 42.3 7.6 120 FTG ---- PE 0.0 S14 20.0 11.2 14.6 42.8 0.044 TL 8.00 PV 0.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E OB TITLE: Grey Hawk Bldg. I .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: 58 -177.8 2.703 PL 8.00 PF 0.6 S14 20.0 11.2 14.6 42.8 9.9 120 FTG ---- PE 0.0 S15 20.0 11.2 15.2 43.6 0.074 TL 8.00 PV 0.7 Pipe: 59 -221.5 2.703 PL 8.00 PF 0.9 S15 20.0 11.2 15.2 43.6 12.4 1.20 FTG ---- PE 0.0 S16 20.0 11.2 16.1 44.9 0.111 TL 8.00 PV 1.0 Pipe: 60 -266.4 2.703 PL 8.00 PF 1.2 S16 20.0 11.2 16.1 44.9 14.9 120 FTG ---- PE 0.0 S16A 20.0 11.2 17.3 46.6 0.156 TL 8.00 PV 1.5 Pipe: 61 -313.0 2.703 PL 183.67 PF 49.4 S16A 20.0 11.2 17.3 46.6 17.5 120 FTG T5L PE 0.0 RiO 20.0 0.0 66.7 0.0 0.210 TL 235.27 PV 2.1 Pipe: 62 -313.0 2.703 PL 2.16 PF 5.7 RiO 20.0 0.0 66.7 0.0 17.5 120 FTG TL PE 1.1 M5 17.5 0.0 73.5 0.0 0.210 TL 27.36 PV 2.1 Pipe: 63 69.4 2.703 PL 2.16 PF 0.3 M10 17.5 0.0 15.7 0.0 3.9 120 FTG T PE -1.1 R5 20.0 0.0 14.4 0.0 0.013 TL 20.76 PV 0.1 Pipe: 64 69.4 2.703 PL 5.50 PF 0.3 R5 20.0 0.0 14.4 0.0 3.9 120 FTG T PE 0.0 S17 20.0 11.2 14.1. 42.0 0.013 TL 24.10 PV 0.1 Pipe: 65 27.4 2.703 PL 8.00 PF 0.0 517 20.0 11.2 14.1 42.0 1.5 120 FTG ---- PE 0.0 S18 20.0 11.2 14.1 42.0 0.002 TL 8.00 PV 0.0 Pipe: 66 -14.6 2.703 PL 8.00 PF 0.0 518 20.0 11.2 14.1 42.0 0.8 120 FTG ---- PE 0.0 S19 20.0 11.2 14.1 42.0 0.001 TL 8.00 PV 0.0 Pipe: 67 -56.6 2.703 PL 8.00 PF 0.1 S19 20.0 11.2 14.1 42.0 3.2 120 FTG ---- PE 0.0 S20 20.0 11.2 14.1 42.1 0.009 TL 8.00 PV 0.1 Pipe: 68 -98..7 2.703 PL 8.00 PF 0.2 S20 20.0 11.2 14.1 42.1 5.5 120 FTG ---- PE 0.0 S21 20.0 11.2 14.3 42.4 0.025 TL 8.00 PV 0.2 Pipe: 69 -141.1 2.703 PL 8.00 PF 0.4 S21 20.0 11.2 14.3 42.4 7.9 120 FTG ---- PE 0.0 S22 20.0 11.2 14.7 43.0 0.048 TL 8.00 PV 0.4 Pipe: 70 -184.1 2.703 PL 8.00 PF 0.6 S22 20.0 11.2 14.7 43.0 10.3 120 FTG ---- PE 0.0 S23 20.0 11.2 15.3 43.9 . 0.079 TL 8.00 PV 0.7 Pipe: 71 -228.0 2.703 PL 8.00 PF 0.9 S23 20.0 11.2 15.3 43.9 12.7 120 FTG ---- PE 0.0 S24 20.0 11.2 16.3 45.2 0.117 TL 8.00 PV 1.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E JOB TITLE: Grey Hawk Bldg. I .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: 72 -273.2 2.703 PL 8.00 PF 1.3 S24 20.0 11.2 16.3 45.2 15.3 120 FTG ---- PE 0.0 S24A 20.0 11.2 17.6 47.0 0.163 TL 8.00 PV 1.6 Pipe: 73 -320.1 2.703 PL 166.00 PF 49.1 S24A 20.0 11.2 17.6 47.0 17.9 120 FTG T6L PE 0.0 ..Rll 20.0 0.0 66.7 0.0 0.219 TL 224.20 PV 2.2 Pipe: 74 -320.1 2.703 PL 2.16 PF 6.0 Rll 20.0 0.0 66.7 0.0 17.9 120 FTG TL PE 1.1 M4 17.5 0.0 73.8 0.0 0.219 TL 27.36 PV 2.2 Pipe: 75 47.7 2.703 PL 2.16 PF 0.1 M9 17.5 0.0 15.7 0.0 2.7 120 FTG .T PE -1.1 R6 20.0 0.0 14.5 0.0 0.006 TL 20.76 PV 0.0 Pipe: 76 47.7 2.703 PL 5.50 PF 0.2 R6 20.0 0.0 14.5 0.0 2.7 120 FTG T PE 0.0 S25 20.0 11.2 14.4 42.4 0.006 TL 24.10 PV 0.0 Pipe: 77 5.3 2.703 PL 8.00 PF 0.0 S25 20.0 11.2 14.4 42.4 0.3 120 FTG ---- PE 0.0 S26 20.0 11.2 14.4 42.4 0.000 TL 8.00 PV 0.0 Pipe: 78 -37.2 2.703 PL 8.00 PF 0.0 S26 20.0 11.2 14.4 42.4 2.1 120 FTG ---- PE 0.0 S27 20.0 11.2 14.4 42.5 0.004 TL 8.00 PV 0.0 Pipe: 79 -79.7 2.703 PL 8.00 PF 0.1 S27 20.0 11.2 14.4 42.5 4.5 120 FTG ---- PE 0.0 S28 20.0 11.2 14.5 42.7 0.017 TL 8.00 PV 0.1 Pipe: 80 -122.3 2.703 PL 8.00 PF 0.3 S28 20.0 11.2 14.5 42.7 6.8 120 FTG ---- PE 0.0 S29 20.0 11.2 14.8 43.1 0.037 TL 8.00 PV 0.3 Pipe: 81 -165.5 2.703 PL 8.00 PF 0.5 S29 20.0 11.2 14.8 43.1 9.3 120 FTG ---- PE 0.0 S30 20.0 11.2 15.3 43.9 0.065 TL 8.00 PV 0.6 Pipe: 82 -209.3 2.703 PL 8.00 PF 0.8 S30 20.0 11.2 15.3 43.9 11.7 120 FTG ---- PE 0.0 S31 20.0 11.2 16.1 45.0 0.100 TL 8.00 PV 0.9 Pipe: 83 -254.3 2.703 PL 8.00 PF 1.1 S31 20.0 11.2 16.1 45.0 14.2 120 FTG ---- PE 0.0 S32 20.0 11.2 17.3 46.6 0.143 TL 8.00 PV 1.4 Pipe: 84 -300.9 2.703 PL 180.33 PF 50.4 S32 20.0 11.2 17.3 46.6 16.8 120 FTG T9L PE 0.0 R12 20.0 0.0 67.7 0.0 0.195 TL 258.33 PV 1.9 Pipe: 85 -300.9 2.703 PL 2.17 PF 5.3 R12 20.0 0.0 67.7 0.0 16.8 120 FTG TL PE 1.1 M3 17.5 0.0 74.1 0.0 0.195 TL 27.37 PV 1.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2E 'JOB TITLE: Grey Hawk Bldg. I .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: 86 -1513.5 6.403 PL 3.91 PF 1.0 M3 17.5 0.0 74.1 0.0 15.1 120 F-TG L PE 0.1 TOR 17.2 0.0 75.2 0.0 0.058 TL 16.88 PV 1.5 Pipe: 87 -1513.5 6.403 PL 15.25 PF 0.9 TOR 17.2 0.0 75.2 0.0 15.1 120 FTG ---- PE 6.6 BOR 2.0 0.0 82.7 0.0 0.058 TL 15.25 PV 1.5 Pipe: 88 -1513.5 8.390 PL 13.00 PF 0.9 BOR 2.0 0.0 82.7 0.0 8.8 140 FTG 3L PE 2.2 DI -3.0 0.0 85.8 0.0 0.012 TL 79.00 PV 0.5 Pipe: 89 -1513.5 7.980 PL 295.00 PF 4.4 DI -3.0 0.0 85.8 0.0 9.7 150 FTG 2L FE 0.0 UG2 -3.0 0.0 90.2 0.0 0.013 TL 333.00 PV 0.6 Pipe: 90 -1513.5 8.390 PL 6.00 PF 1.0 UG2 -3.0 0.0 90.2 0.0 8.8 140 FTG TL PE -2.6 BF2 3.0 0.0 88.6 0.0 0.012 TL 88.00 PV 0.5 Pipe: 91 FIXED PRESSURE LOSS DEVICE BF1 3.0 0.0 92.6 0.0 4.0 psi, 1513.5 gpm BF2 3.0 0.0 88.6 0.0 Pipe: 92 -1513.5 8.390 PL 6.00 PF 0.3 BF1 3.0 0.0 92.6 0.0 8.8 140 FTG L PE 2.6 UG1 -3.0 0.0 95.5 0.0 0.012 TL 28.00 PV 0.5 Pipe: 92A -1513.5 7.980 PL 20.00 PF 1.0 UG1 -3.0 0.0 95.5 0.0 9.7 150 FTG TG PE 0.0 UG -3.0 0.0 96.5 0.0 0.013 TL 74.00 PV 0.6 Pipe: 94 -737.3 7.980 PL 625.00 PF 2.4 UG -3.0 0.0 96.5 0.0 4.7 150 FTG TL PE -6.1 Ui 11.0 0.0 92.9 0.0 0.003 TL 694.00 PV 0.2 Pipe: 94A -737.3 7.980 PL 360.00 PF 1.3 Ui 11.0 0.0 92.9 0.0 4.7 150 FTG ---- FE 0.0 U 11.0 0.0 94.1 0.0 0.003 TL 360.00 PV 0.2 Pipe: 95 -776.2 7.980 PL 785.00 PF 3.3 UG -3.0 0.0 96.5 0.0 5.0 150 FTG T2L FE -6.1 HYD 11.0 H.S. 93.8 500.0 0.004 TL 873.00 PV 0.2 Pipe: 95A -1276.2 7.980 PL 30.00 PF 0.3 HYD 11.0 H.S. 93.8 500.0 8.2 150 FTG G PE 0.0 U 11.0 0.0 94.1 0.0 0.010 TL 34.00 PV 0.5 Pipe: 96 -2013.4 7.980 PL 1.00 PF 1.1 U 11.0 0.0 94.1 0.0 12.9 150 FTG T PE -1.1 SOURCE 13.5 SRCE 94.2 (N/A) 0.022 TL 51.00 PV 1.1 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2 JOB TITLE: Grey Hawk Bldg. I .45 NOTES: (1) 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 (2) 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 0.105 gpm. (3) 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 73. (4) a. System remote area HAS been proven or 'peaked'. Minimum pressure at any sprinkler: 13.962 psi Minimum pressure with remote area shifted one sprinkler space toward left cross main: 14.119 psi Remote area is located adjacent to right cross main (5) 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 A SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\6-2 JOB TITLE: Grey Hawk Bldg. I .45 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 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 Supply Flow Curve C PALOMAR FORUM BUILDING 1.45 Test Date: 6/28/2007 Static Hydrant: NE INTERSECTION OF K STREET AND 13 1/2 STREET. Design GPM: 2013 GPM Flow Hydrant: NEW CONNECTION OF FIRE SERVICE BACKFLOW PREVENTER Design PSI: 82.7 PSI Ps 125.0 PSI Test Static Pressure Reading Available Pressure at Design GPM: 108.0 PSI Pr 20.0 PSI Test Residual Pressure Reading PSI Headroom: 25.30 PSI 23% GPMr 5390 GPM Test Flow at Residual Pressure GPM Headroom: 1284 GPM 64% Flow Test Summary Curve 0A185 —.---------------. ---------------. ---------------. F MMMMI -------------l.. ---------------. SI ---------------. ____--------------- ---------------. ---------------. ____---------------. ---------------. ---------------. ____---------------u I iJs [sills —.—ps' Desion Point 2000 2500 3000 3500 4000 Flow GPM REMOTE AREA 1 Printed 6/28/2007 PRO-TECH FIRE PROTECTION 179 ROYMAR ROAD SUITE G OCEANSIDE, CA 92054 HYDRAULIC CALCULATIONS BUILDING FOR APPROVED SUBMED CARLS09 1c7E-Dkp—A—R—T—Mj_ij— GREY HAWK BUSINESS PART LOT 801 NATIONAL S. 1,2,8 PHASE I CARLSBAD CA DATE: June 28, 2007 BUILDING I OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: 0.1 gpm/980 sq. ft. AREA OF APPLICATION: 980 sq. ft. COVERAGE PER SPRINKLER: 225 FT. MAX. NUMBER OF SPRINKLERS CALCULATED: 9 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 203.9 gpm TOTAL WATER REQUIRED (including hose): 303.9 gpm FLOW AND PRESSURE (@ BOR): 203.9 gpm @ 26.1 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: PRO-TECH FIRE PROTECTION DESIGN/LAYOUT BY: SEFPF AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C16 HIC SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RES JOB TITLE: Grey Hawk Bldg. I .1 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 125.0 20.0 5390.0 124.5 303.9 25.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 303.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 203.9 GPM NODE ANALYSIS DATA DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT-2) (GPM/FT-2) Si 20.0 - - - - 16.9 --- S2 20.0 - - - - 16.9 --- S3 20.0 - - - - 16.9 --- - S4 20.0 - - - - 17.0 --- S5 20.0 - - - - 17.0 --- S6 20.0 - - - - 17.0 --- .S7 20.0 - - - - 17.0 --- S8 20.0 - - - - 17.1 - - - - S8A 20.0 - - - - 17.2 --- S9 20.0 - - - - 17.0 - - - Sic 20.0 - - - - 17.0 - - - Sii 20.0 - - - - 17.0 --- S12 20.0 - - - - 17.0 --- Si3 20.0 - - - - 17.1 --- S14 20.0 - - - - 17.1 --- S15 20.0 - - - - 17.1 --- S16 20.0 - - - - 17.2 --- S16A 20.0 - - - - 17.2 --- S17 20.0 - - - - 17.0 --- Si8 20.0 - - - - 17.0 --- Si9 20.0 - - - - 17.0 S20 20.0 - - - - 17.1 --- S2i 20.0 - - - - 17.1 --- S22 20.0 - - - - 17.1 --- S23 20.0 - - - - 17.2 --- S24 20.0 - - - - 17.2 --- 524A 20.0 - - - - 17.2 --- S25 20.0 - - - - 17.0 --- S26 20.0 - - - - 17.0 --- S27 20.0 - - - - 17.0 --- S28 20.0 - - - - 17.1 --- S29 20.0 - - - - 17.1 --- S30 20.0 - - - - 17.1 ---- S3i 20.0 - - - - 17.1 --- S32 20.0 - - - - 17.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS . Page .2 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .1 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT A2) (GPMIFT"2) M14 17.5 - - - - 17.7 --- Mi3 17.5 - - - - 17.7 --- M12 17.5 - - - - .17.8 - - - Mu 17.5 ---- 17.8 --- Mi0 17.5 - - - - 17.8 --- M9 17.5 - - - - 17.8 --- M8 17.5 - - - - 19.3 --- M7 17.5 - - - - 19.3 --- M6 17.5 - - - - 19.3 --- M5. . 17.5 - - - - 19.3 --- M4 17.5 - - - - 19.3 M3 17.5 - - - - 19.3 - - - Li 20.0 - - - - 15.8 --- L2 20.0 - - - - 15.6 --- L3 20.0 ---.- 15.6 --- L4 20.0 - - - - 15.6 --- L5 20.0 - - - - 15.5 --- L6 20.0 - - - - 15.5 --- L7 20.0 - - - -. 15.4 --- L8 20.0 - - - - 15.4 --- L9 20.0 - - - - 15.4 --- L10 20.0 - - - - 16.7 - - - Lii 20.0 - - - - 17.6 --- P1 8.9 K= 5.60 16.2 22.6 225.0 0.100 0.100 P2 8.9 K= 5.60 16.6 22.8 225.0 0.100 0.101 P3 8.9 K= 5.60 16.5 22.8 225.0 0.100 0.101 P4 8.9 K= 5.60 16.1 22.5 225.0 0.100 0.100 P5 8.9 K= 5.60 16.3 22.6 225.0 0.100 0.100 P6 8.9 K= 5.60 16.2 22.5 225.0 0.100 0.100 P7 8.9 K= 5.60 16.7 22.9 225.0 0.100 0.102 P8 8.9 K= 5.60 16.4 22.7 225.0 0.100 0.101 P9 8.9 K= 5.60 16.4 22.7 225.0 0.100 0.101 R2 20.0 - - - - 16.1 - - - Ri 20.0 - - - - 16.3 --- R3 20.0 - - - - 16.8 --- R4 20.0 - - - - 16.8 --- R5 20.0 - - - - 16.8 --- R6 20.0 - - - - 16.8 --- R7 20.0 - ---' 18.1 --- R8 20.0 - - - - 18.1 --- R9 20.0 - - - - 18.1 - - - RiO 20.0 - - - - 18.1 - - - Ru 20.0 - - - - 18.1 --- R12 20.0 - - - - 18.1 - - - TOR 17.2 - - - - 19.4 - - - BOR 2.0 - - - - 26.1 - - - DI -3.0 - ---. 28.3 --- UG2 -3.0 - - - - 28.4 --- 3F2 3.0 - - - - 25.8 - - - BFi 3.0 - - - - 29.8 --- UG1 -3.0 ---- 32.4 - - - UG -3.0 - - - - 32.4 - - - Ui 11.0 - - - - 26.4 - - - U 11.0 ---- 26.4 - - - HYD 11.0 . HOSE STREAM 26.4 100.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .1 NODE ANALYSIS DATA (cont.) DENSITY NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE AREA REQ. ACT. (FT) (PSI) (GPM) (FT A2) (GPM/FTA2) SOURCE 13.5 SOURCE 25.4 303.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 PATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt .JOB TITLE: Grey Hawk Bldg. I .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 -62.0 4.310 PL 12.25 PF 0.0 M14 17.5 0.0 17.7 0.0 1.4 120 FTG ---- PE 0.0 M13 17.5 0.0 17.7 0.0 0.001 TL 12.25 PV 0.0 Pipe: 2 -144.6 4.310 FL 12.00 PF 0.1 M13 17.5 0.0 17.7 0.0 3.2 120 FTG ---- PE 0.0' M12 17.5 0.0 17.8 0.0 0.005 TL 12.00 PV 0.1 Pipe: 3 -109.2 4.310 PL 11.00 PF 0.0 M12 17.5 0.0 17.8 0.0 2.4 120 FTG ---- PE 0.0 Mil 17.5 0.0 17.8 0.0 0.003 TL 11.00 PV 0.0 Pipe: 4 -72.7 4.310 PL 11.00 PF 0.0 Mil 17.5 0.0 17.8 0.0 1.6 120 FTG ---- FE 0.0 M10 17.5 0.0 17.8 0.0 0.001 TL 11.00 PV 0.0 Pipe: 5 -35.7 4.310 PL 11.00 PF 0.0 M10 17.5 0.0 17.8 0.0 0.8 120 FTG ---- FE 0.0 M9 17.5 0.0 17.8 0.0 0.000 TL 11.00 PV 0.0 Pipe: 6 -28.1 6.403 PL 12.25 PF 0.0 M8 17.5 0.0 19.3 0.0 0.3 120 FTG ---- FE 0.0 M7 17.5 0.0 19.3 0.0 0.000 TL 12.25 PV 0.0 Pipe: 7 -59.3 6.403 FL 11.41 PF 0.0 M7 17.5 0.0 19.3 0.0 0.6 120 FTG ---- FE 0.0 M6 17.5 0.0 19.3 0.0 0.000 TL 11.41 PV 0.0 Pipe: 8 -94.7 6.403 FL 9.75 PF 0.0 M6 17.5 0.0 19.3 0.0 0.9 120 FTG ---- PE 0.0 M5 17.5 0.0 19.3 0.0 0.000 TL 9.75 PV 0.0 Pipe: 9 -131.3 6.403 PL 9.75 PF 0.0 M5 17.5 0.0 19.3 0.0 1.3 120 FTG ---- FE 0.0 M4 17.5 0.0 19.3 A.0. 0.001 TL 9.75 PV 0.0 Pipe: 10 -168.3 6.403 FL 9.75 PF 0.0 M4 17.5 0.0 19.3 0.0 1.7 120 FTG ---- FE 0.0 M3 17.5 0.0 19.3 0.0 0.001 TL 9.75 PV 0.0 Pipe: ii 62.0 2.203 FL 1.50 PF 0.3 M14 17.5 0.0 17.7 0.0 5.2 120 FTG T FE -1.1 Ri 20.0 0.0 16.3 0.0 0.028 TL 12.15 PV 0.2 Pipe: 12 62.0 2.203 FL 7.42 PF 0.5 Ri 20.0 0.0 16.3 0.0 5.2 120 FTG T PE 0.0 Li 20.0 0.0 15.8 0.0 0.028 TL 18.07 PV 0.2 Pipe: 13 39.5 2.203 PL 12.00 PF 0.1 Li 20.0 0.0 15.8 0.0 3.3 120 FTG ---- FE 0.0' L2 20.0 0.0 15.6 0.0 0.012 TL 12.00 PV 0.1 Pipe: 14 16.7 2.203 FL 11.67 PF 0.0. L2 20.0 0.0 15.6 0.0 1.4 120 FTG ---- FE 0.0 L3 20.0 0.0 15.6 0.0 0.003 TL 11.67 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .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: 15 -6.1 2.203 PL 12.08 PF 0.0 L3 20.0 0.0 15.6 0.0 0.5 120 FTG ---- PE 0.0 L4 20.0 0.0 15.6 0.0 0.000 TL 12.08 PV 0.0 Pipe: 16 -28.6 2.203 PL 152.75 PF 1.1 L4 20.0 0.0 15.6 0.0 2.4 120 FTG TL PE 0.0 L10 20.0 0.0 16.7 0.0 0.007 TL 167.13 PV 0.0 Pipe: 17 82.6 2.203 PL 7.42 PF 0.5 R2 20.0 0.0 16.1 0.0 7.0 120 FTG L PE 0.0 L5 20.0 0.0 15.5 0.0 0.048 TL 11.15 PV 0.3 Pipe: 18 60.0 2.203 PL 1.67 PF 0.0 L5 20.0 0.0 15.5 0.0 5.0 120 FTG ---- PE 0.0 L6 20.0 0.0 15.5 0.0 0.027 TL 1.67 PV 0.2 Pipe: 19 37.5 2.203 PL 4.25 PF 0.0 L6 20.0 0.0 15.5 0.0 3.2 120 FTG ---- PE 0.0 L7 20.0 0.0 15.4 0.0 0.011 TL 4.25 PV 0.1 Pipe: 20 14.6 2.203 PL 6.08 PF 0.0 L7 20.0 0.0 15.4 0.0 1.2 120 FTG ---- PE 0.0 L8 20.0 0.0 15.4 0.0 0.002 TL 6.08 PV 0.0 Pipe: 21 -8.1 2.203 PL 11.67 PF 0.0 L8 20.0 0.0 15.4 0.0 0.7 120 FTG ---- PE 0.0 L9 20.0 0.0 15.4 0.0 0.001 TL 11.67 PV 0.0 Pipe: 22 -30.7 2.203 PL 154.00 PF 1.3 L9 20.0 0.0 15.4 0.0 2.6 120 FTG 4L PE 0.0 L10 20.0 0.0 16.7 0.0 0.008 TL 168.92 PV 0.0 Pipe: 23 -59.3 2.703 PL 64.00 PF 0.9 L10 20.0 0.0 16.7 0.0 3.3 120 FTG TL PE 0.0 Lii 20.0 0.0 17.6 0.0 0.010 TL 89.20 PV 0.1 Pipe: 24 -31.2 2.203 PL 48.58 PF 0.5 Lii 20.0 0.0 17.6 0.0 2.6 120 FTG T PE 0.0 RB 20.0 0.0 18.1 0.0 0.008 TL 59.23 PV 0.0 Pipe: 25 -28.1 2.203 PL 60.83 PF 0.5 Lii 20.0 0.0 17.6 0.0 2.4 120 FTG TL PE 0.0 R7 20.0 0.0 18.1 0.0 0.007 TL 75.21 PV 0.0 Pipe: 26 22.6 1.049 PL 12.67 PF 4.3 Li 20.0 0.0 15.8 0.0 8.4 120 FTG 2E2T PE 4.8 P1 8.9 5.6 16.2 22.6 0.163 TL 26.67 PV 0.5 Pipe: 27 22.8 1.049 PL 11.42 PF 3.9 L2 20.0 0.0 15.6 0.0 8.5 120 FTG E2T PE 4.8 P2 8.9 5.6 16.6 22.8 0.166 TL 23.42 PV 0.5 Pipe: 28 22.8 1.049 PL 11.42 PF 3.9 L3 20.0 0.0 15.6 0.0 8.5 120 FTG E2T PE 4.8 P3 8.9 5.6 16.5 22.8 0.165 TL 23.42 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .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: 29 22.5 1.049 PL 12.33 PF 4.3 L4 . 20.0 0.0 15.6 0.0 8.4 120 FTG 2E2T PE 4.8 P4 8.9 5.6 16.1 •22.5 0.162 TL 26.33 PV 0.5 Pipe:-30 22.6 1.049 PL 12.75 PF 4.0 L5 20.0 0.0 15.5 0.0 8.4 120 FTG E2T PE 4.8 P5 8.9 5.6 16.3 22.6 0.163 TL 24.75 PV 0.5 Pipe: 31 22.5 .1.049 PL 16.25 PF 4.1 L6 20.0 0.0 15.5 0.0 8.4 120 FTG 2ET FE 4.8 P6 8.9 5.6 16.2 22.5 0.162 TL 25.25 PV 0.5 Pipe: 32 22.9 1.049 PL 12.42 PF 3.6 L7 20.0 0.0 15.4 0.0 8.5 120 FTG 2ET PE 4.8 P7 8.9 5.6 16.7 22.9 0.167 TL 21.42 PV 0.5 Pipe: 33 22.7 1.049 PL 11.33 PF 3.8 L8 20.0 0.0 15.4 0.0 8.4 120 FTG E2T PE 4.8 PB . 8.9 5.6 16.4 22.7 0.164 TL 23.33 PV 0.5 Pipe: 34 22.7 1.049 PL 11.33 PF 3.8 L9 20.0 0.0 . 15.4 0.0 8.4 120 FTG E2T PE 4.8 P9 8.9 5.6 16.4 22.7 0.164 TL 23.33 PV 0.5 Pipe: 35 -28.1 2.203 FL 2.17 PF 0.1 R7 20.0 0.0 18.1 0.0 2.4 120 FTG TL PE 1.1 M8 17.5 0.0 19.3 0.0 0.007 TL 16.55 PV 0.0 Pipe: 36 82.6 2.203 PL 1.50 PF 0.6 M13 17.5 0.0 17.7 0.0 7.0 120 FTG T PE -1.1 R2 20.0 0.0 16.1 0.0 0.048 TL 12.15 PV 0.3 Pipe: 38 -31.2 2.203 PL 2.00 PF 0.1 R8 20.0 0.0 18.1 0.0 2.6 120. FTG TL PE 1.1 M7 17.5 0.0 19.3 0.0 0.008 TL 16.38 PV 0.0 Pipe: 39 -35.4 2.703 PL 2.17 PF 0.1 M12 17.5 0.0 17.8 0.0 2.0 120 FTG T FE -1.1 R3 20.0 0.0 16.8 0.0 0.004 TL 20.77 PV 0.0 Pipe: 40 -35.4 2.703 PL 13.50 PF 0.1 R3 20.0 0.0 16.8 0.0 2.0 120 FTG L PE 0.0 Si 20.0 0.0 16.9 0.0 0.004 TL 20.10 PV 0.0 Pipe: 41 -35.4 2.703 PL 8.00 PF 0.0 Si 20.0 0.0 . 16.9 0.0 2.0 120 FTG ---- PE 0.0 S2 20.0 0.0 16.9 0.0 0.004 TL 8.00 PV 0.0 Pipe: 42 -35.4 2.703 PL 8.00 PF 0.0 S2 20.0 0.0 16.9 0.0 2.0 120 FTG ---- PE 0.0 S3 . 20.0 0.0 16.9 0.0 0.004 TL 8.00 PV 0.0 Pipe: 43 -35.4 2.703 PL 8.00 PF 0.0 S3 20.0 0.0 16.9 0.0 2.0 120 FTG ---- PE 0.0 S4 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .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: 44 -35.4 2.703 PL 8.00 PF 0.0 S4 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S5 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 45 -35.4 2.703 PL 8.00 PF 0.0 S5 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S6 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 46 -35.4 2.703 PL 8.00 PF 0.0 S6 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S7 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 47 . -35.4 2.703 PL 8.00 PF 0.0 S7 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S8 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 48 -35.4 2.703 PL 8.67 PF 0.1 S8 20.0 0.0 17.1 0.0 2.0 120 FTG 2L PE 0.0 S8A 20.0 0.0 17.2 0.0 0.004 TL 21.87 PV 0.0 Pipe: 49. . -35.4 2.703 PL 197.00 PF 1.0 S8A 20.0 0.0 17.2 0.0 2.0 120 FTG T6L PE 0.0 R9 20.0 0.0 18.1 0.0 0.004 TL 255.20 PV 0.0 Pipe: 50 -35.4 2.703 FL 2.67 PF 0.1 R9. 20.0 0.0 18.1 0.0 2.0 120 FTG TL FE 1.1 M6 17.5 0.0 19.3 0.0 0.004 TL 27.87 PV 0.0 Pipe: 51 -36.5 2.703 FL 2.17 PF 0.1 Mil 17.5 0.0 17.8 0.0 2.0 120 FTG T PE -1.1 R4 20.0 0.0 16.8 0.0 0.004 TL 20.77 PV 0.0 Pipe: 52 -36.5 2.703 PL 13.50 PF 0.1 R4 20.0 0.0 16.8 0.0 2.0 120 FTG T PE 0.0 S9 20.0 0.0 17.0 0.0 0.004 TL 32.10 PV 0.0 Pipe: 53 -36.5 2.703 PL 8.00 PF 0.0 S9 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 sio 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 54 -36.5 2.703 FL 8.00 PF 0.0 sio 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S11 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0. Pipe: 55 -36.5 2.703 PL 8.00 PF 0.0 Sil 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S12 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 56 -36.5 2.703 FL 8.00 PF 0.0 S12 20.0 0.0 17.0 0.0 2.0 120 FTG ---- FE 0.0 S13 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 57 -36.5 2.703 FL 8.00 PF 0.0 S13 20.0 0.0 17.1 0.0 2.0 120 FTG ---- FE 0.0 S14 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 PATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt 'JOB TITLE: Grey Hawk Bldg. I .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: 58 -36.5 2.703 PL 8.00 PF 0.0 S14 20.0 0.0 17.1 0.0 2.0 120 FTG ---- PE 0.0 S15 20.0 0.0 17.1 O.O 0.004 TL 8.00 PV 0.0 Pipe: 59 -36.5 2.703 PL 8.00 PF 0.0 S15 20.0 0.0 17.1 0.0 2.0 120 FTG ---- PE 0.0 S16 20.0 0.0 17.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 60 -36.5 2.703 PL 8.00 PF 0.0 S16 20.0 0.0 17.2 0.0 2.0 120 FTG ---- PE 0.0 S16A 20.0 0.0 17.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 61 -36.5 2.703 PL 175.67 PF 0.9 S16A 20.0 0.0 17.2 0.0 2.0 120 FTG T5L PE 0.0 RiO 20.0 0.0 18.1 0.0 0.004 TL 227.27 PV 0.0 Pipe: 62 -36.5 2.703 PL 2.16 PF 0.1 RiO 20.0 0.0 18.1 0.0 2.0 120 FTG TL PE 1.1 M5 17.5 0.0 19.3 0.0 0.004 TL 27.36 PV 0.0 Pipe: 63 -37.0 2.703 PL 2.16 PF 0.1 M10 17.5 0.0 17.8 0.0 2.1 120 FTG T PE -1.1 R5 20.0 0.0 16.8 0.0 0.004 TL 20.76 PV 0.0 Pipe: 64 -37.0 2.703 PL 13.50 PF 0.1 R5 20.0 0.0 16.8 0.0 2.1 120 FTG T PE 0.0 S17 20.0 0.0 17.0 0.0 0.004 TL 32.10 PV 0.0 Pipe: 65 -37.0 2.703 PL 8.00 PF 0.0 S17 20.0 0.0 17.0 0.0 2.1 120 FTG ---- PE 0.0 S18 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 66 -37.0 2.703 PL 8.00 PF 0.0 S18 20.0 0.0 17.0 0.0 2.1 120 FTG ---- PE 0.0 S19 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 67 -37.0 2.703 PL 8.00 PF 0.0 S19 20.0 0.0 17.0 0.0 2.1 120 FTG ---- PE 0.0 S20 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 68 -37.0 2.703 PL 8.00 PF 0.0 S20 20.0 0.0 17.1 0.0 2.1 120 FTG ---- PE 0.0 S21 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 69 -37.0 2.703 PL 8.00 PF 0.0 S21 20.0. 0.0 17.1 0.0 2.1 120 FTG ---- PE 0.0 S22 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 70 -37.0 2.703 PL 8.00 PF 0.0 S22 20.0 0.0 17.1 0.0 2.1 120 FTG ---- PE 0.0 S23 20.0 0.0 17.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 71 -37.0 2.703 PL 8.00 PF. 0.0 S23 .20.0 0.0 17.2 0.0 2.1 120 FTG ---- PE 0.0 S24 20.0 0.0 17.2 0.0 0.004 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .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: 72 -37.0 2.703 PL 8.00 PF 0.0 S24 20.0 0.0 17.2 0.0 2.1 120 FTG ---- FE 0.0 524A 20.0 0.0 17.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 73 -37.0 2.703 FL 158.00 PF 0.9 524A 20.0 0.0 17.2 0.0 2.1 120 FTG T6L PE 0.0 Rll 20.0 0.0 18.1 0.0 0.004 TL 216.20 PV 0.0 Pipe: 74 -37.0 2.703 PL 2.16 PF 0.1 Rll 20.0 0.0 18.1 0.0 2.1 120 FTG TL PE 1.1 M4 17.5 0.0 19.3 0.0 0.004 TL 27.36 PV 0.0 Pipe: 75 -35.7 2.703 PL 2.16 PF 0.1 M9 17.5 0.0 17.8 0.0 2.0 120 FTG T FE -1.1 R6 20.0 0.0 16.8 0.0 0.004 TL 20.76 PV 0.0 Pipe: 76 -35.7 2.703 FL 13.50 PF 0.1 R6 20.0 0.0 16.8 0.0 2.0 120 FTG T PE 0.0 S25 20.0 0.0 17.0 0.0 0.004 TL 32.10 PV 0.0 Pipe:. 77 -35.7 2.703 PL 8.00 PF 0.0 S25 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S26 20.0 0.0. 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 78 -35.7 2.703 PL 8.00 PF 0.0 S26 20.0 0.0 17.0 0.0 2.0 120 FTG ---- PE 0.0 S27 20.0 0.0 17.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 79 -35.7 2.703 FL 8.00 PF 0.0 S27 20.0 0.0 17.0 0.0 2.0 120 FTG ---- FE 0.0 S28 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0- Pipe: 80 - -35.7 2.703 FL 8.00 PF 0.0 S28 20.0 0.0 17.1, 0.0 2.0 120 FTG ---- FE 0.0 S29 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 81 -35.7 2.703 FL 8.00 PF 0.0 S29 20.0 0.0 17.1 0.0 2.0 120 FTG ---- FE 0.0 S30 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 82 -35.7 2.703 PL 8.00 PF 0.0 S30 20.0 0.0 17.1 0.0 2.0 120 FTG ---- FE 0.0 S31 20.0 0.0 17.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 83 -35.7 2.703 PL 8.00 PF 0.0 S31 20.0 0.0 11.1 0.0 2.0 120 FTG ---- PE 0.0 S32 20.0 0.0 17.2 '0.0 0.004 TL 8.00 PV 0.0 Pipe: 84 -35.7 2.703 PL 172.33 PF 0.9 S32 20.0 0.0 17.2 0.0 2.0 120 FTG T9L FE 0.0 R12 20.0 0.0 18.1 0.0 0.004 TL 250.33 PV 0.0 Pipe: 85 -35.7 2.703 PL 2.17 PF 0.1 R12 20.0 0.0 18.1 0.0 2.0 120 FTG TL PE 1.1 M3 17.5 0.0 19.3 0.0 0.004 TL 27.37 PV 0.0 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .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: 86 -203.9 6.403 PL 3.91 PF 0.0 M3 17.5 0.0 19.3 0.0 2.0 120 FTG L PE 0.1 TOR 17.2 0.0 19.4 0.0 0.001 TL 16.88. PV 0.0 Pipe: 87 -203.9 6.403 PL 15.25 PF 0.0 TOR 17.2 0.0 19.4 0.0 2.0 120 FTG ---- PE 6.6 3CR 2.0 0.0 26.1 0.0 0.001 TL 15.25 PV 0.0 Pipe: 88 -203.9 8.390 PL 13.00 PF 0.0 BOR 2.0 0.0 26.1 0.0 1.2 140 FTG 3L PE 2.2 DI -3.0 0.0 28.3 0.0 0.000 TL 79.00 PV 0.0 Pipe: 89 -203.9 7.980 PL 295.00 PF 0.1 DI -3.0 0.0 28.3 0.0 1.3 150 FTG 2L PE 0.0 UG2 . -3.0 0.0 28.4 0.0 0.000 TL 333.00 PV 0.0 Pipe: 9.0 -203.9 8.390 PL 6.00 PF 0.0 UG2 -3.0 0.0 28.4 0.0 1.2 140 FTG TL PE -2.6 BF2 3.0 0.0 25.8 0.0 0.000 TL 88.00 PV 0.0 Pipe: 91 FIXED PRESSURE LOSS DEVICE BF1 3.0 0.0 29.8 0.0 4.0 psi, 203.9 gpm BF2 3.0 0.0 25.8 0.0 Pipe: 92 -203.9 8.390 PL 6.00 PF 0.0 BF1 3.0 0.0 29.8 0.0 1.2 140 FTG L PE 2.6 UG1 -3.0 0.0 32.4 0.0 0.000. TL 28.00 PV 0.0 Pipe: 92A -203.9 7.980 PL 20.00 PF 0.0 UG1 -3.0 0.0 32.4 0.0 1.3 150 FTG TG PE 0.0 UG -3.0 0.0 32.4 0.0 0.000 TL 74.00 PV 0.0 Pipe: 94 -100.3 7.980 PL 625.00 PF 0.1 UG -3.0 0.0 32.4 0.0 0.6 150 FTG TL PE -6.1 Ui 11.0 0.0 26.4 0.0 0.000 TL 694.00 PV 0.0 Pipe: 94A -100.3 7.980 PL 360.00 PF 0.0 Ui 11.0 0.0 26.4 0.0 0.6 150 FTG ---- PE 0.0 U 11.0 0.0 26.4 0.0 0.000 TL 360.00 PV 0.0 Pipe: 95 -103.7 7.980 PL 785.00 PF 0.1 UG -3.0 0.0 32.4 0.0 0.7 150 FTG T2L PE -6.1 HYD 11.0 H.S. 26.4 100.0 0.000 TL 873.00 PV 0.0 Pipe: 95A -203.7 7.980 PL 30.00 PF 0.0 HYD 11.0 H.S. 26.4 100.0 1.3 150 FTG G PE 0.0 U 11.0 0.0 26.4 0.0 0.000 TL 34.00 PV 0.0 Pipe: 96 -303.9 7.980 PL 1.00 PF 0.0 U 11.0 0.0 26.4 0.0 1.9 150 FTG T PE -1.1 SOURCE 13.5 SRCE 25.4 (N/A) 0.001 TL 51.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/16/2001C:\DWG\FIRE SPRINKLER\JOBS IN PROGRESS\PALOMAR FORUM\SEFP\CALCS\BLDG. I\RESt JOB TITLE: Grey Hawk Bldg. I .1 NOTES: Calculations were performed by the HASS 7.3 computer program under.licerise 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 0.002 gpm and a maximum imbalance at any node of 0.138 gpm. Velocity pressures are printed for information only and are not used in balancing the system. Maximum water velocity is 8.5 ft/sec at pipe 32. 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 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 4I S Supply Flow Curve C PALOMAR FORUM BUILDING 1.1 Test Date: 6/28/2007 Static Hydrant: NE INTERSECTION OF K STREET AND 13 1/2 STREET. Design GPM: 304 GPM Flow Hydrant: NEW CONNECTION OF FIRE SERVICE BACKFLOW PREVENTER Design PSI: 26.1 PSI Ps 125.0 PSI Test Static Pressure Reading Available Pressure at Design GPM: 124.5 PSI Pr 20.0 PSI Test Residual Pressure Reading PSI Headroom: 98.40 PSI 79% GPMr 5390 GPM Test Flow at Residual Pressure GPM Headroom: 4915 GPM 16170/6 Flow Test Summary Curve QA1 .85 140 120 100 80 --*---PSI Desiqn Point OL 60 40 20 0 0 500 1000 1500 2000 2500 3000 3500 4000 Flow GPM REMOTE AREA 2 Printed 6128/2007 Sep 26 2007 12:57PM 7607222456 p.1 ' -1 el.-. I&A Flow Test Record Test Hydrant Loóation 3/4e Ier Q,,n cr Hydrant II) No. •. Size Main__________ locaec @ IIE Co'* 13 L E Static ................. JZ&c Residual ......... ifl.c Pressure Drop.. 1 (P1)1 1).... K factor for P1)1 1 t 0 Flow Hydrant(s) Hydrant I location N \AJ (m .( 13( £ ( hcs) Hydrant 2 location Hydrant 3 location Hydrant 1 Pitot PSI GPM:jj3. Size of Orifice Hydrant 2- Pitot PSI GPM: Size of Orifice - Hydrant 3 Pitot PSI GPM Size of Orifice_________ Toad: :K (Qi) calculated test and flow data - 0 PD2 k =Q2 PDI*k Static: ....... . ........... .•.________ Desired Residual....... 20 Pressure Drop (PD 2)10 K factor PD 2:1 q x iZ O divided by I 0 equals Z91 q 21cGPM at 20 psi residual Q PD2k :PD1k • Q2: Comments: ROIL Test conducted for: v i • • Pro- Tec( )/p0?U Zq -c Conducted by:AJ !16, Date: k Z(4/Time: )3O C' APPROVEI A SUBMITTED