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5610 PASEO DEL NORTE; ; AS970065; Permit
2/27/26, 2:12 PM AS970065 Permit Data City of Carlsbad AUTOMATIC SPRINKLER-COMM Job Address: 5610 PASEO DEL NORTE Permit Type: ASC Parcel No: Lot#: 0 Reference No.: Permit No: AS970065 Status: ISSUED Applied 6/30/1997 Approved: 7/10/1997 Issued: 7/10/1997 PC #: Inspector: Project Title: BLDG. 1100 -21,427 SF BLDG. COMPANY STORES/SYSTEM 1/BELLEFLEUR Applicant: Owner: LINDLEY FIRE PROTECTION 2220 E VIA BURTON ANAHEIM CA 714 535-5761 about:blank Fees($) 416.75 Add'I Fees {$) 0 Total{$) 416.75 Balance($) 0 1/1 -.. ... --.. -- .... - -.. ... .. --- - - - --.. - LINDLEY FIRE PROTECTION 2220 E. VIA BUTRON ANAHEIM, CA. 714-535-5761 HYDRAULIC CALCULATIONS FOR CARLSBAD COMPANY STORES 5610 PASEO DEL NORTE NORTH SIDE CARLSBAD, CALIFORNIA -.. .. - - .. - .. .. .. .. .. .. .. ----- - - Via Facsimile November 14, 1996 Mr. Martin Aguilera, Fire Prevention Officer City of Carlsbad Fire Department 2560 Orion Way Oceanside, California 92008-7280 RE: CARLSBAD FACTORY STORES PROJECT PASEODELNORTE CARLSBAD, CALIFORNIA Dear Martin, Ti!~ following are data observed during a flow test performed on November 12, 1996 on Paseo Del Norte just west of Palomar Airport Road. The static and residual pressure data were taken from a fire hydrant immediately behind Anderson's Restaurant and Hotel on Paseo Del Norte while the flow data were observed from a fire hydrant 567' west in front of the new development. Static Pressure Residual Pressure Flow-Observed 84 p.s.i 72 p.s.i 30 p.s.i@ 4" outlet, calculated to 2354 g.p.m. The test was witnessed by yourself and representatives of the City of Carlsbad Water Department. The time of said test was 12:30 p.m. and all valves were checked by the Water Department representatives for position and integrity . Pursuant to our discussion, a 10% reduction will be taken from the aforementioned figures and a 1,500 g.p.m. fire flow will be calculated into the site requirements. We trust you find the aforementioned acceptable and ask that you call if you have questions regarding this or any other matter. Best Regards, Lindley Fire Protection Co., Inc. Chip Lindley 0..,/bf .. .. - - .. - .. - - - - .. - LINDLEY FIRE PROTECTION CO. 2220 E. VIA BURTON ANAHEIM, CA 92806 HYDRAULIC CALCULATIONS FOR CARLSBARD COMPANY STORES BUILDING 1100 NORTH SIDE AREA "A" DATE: 3-28-97 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: Ordinary Hazard; Group II .20 gpm/sq. ft. 1500 sq. ft. 108 sq. ft. 15 sprinklers 369.2 gpm TOTAL WATER REQUIRED (including hose): 619.2 gpm FLOW AND PRESSURE (@ BOR): SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: 369.2 gpm@ 44.3 psi 1/2 inch Lindley Fire Protection Co. San Diego Fire Dept. Cl6/C34 No. 713562 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 825A408 HRS SYSTEMS, INC. ATLANTA, GA ... .... .. .. - - - - -.. - - ... - ... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA11 A 11 WATER SUPPLY DATA SOURCE STATIC RESID . FLOW AVAIL. NODE PRESS. PRESS. @ PRESS.@ TAG (PSI) (PSI) (GPM) (PSI} Ul 84.0 72.0 2354.0 83.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 1 ELEVATION (FT) 17.0 NODE TYPE PRESSURE {PSI) 24.4 TOTAL DEMAND (GPM) 619.2 619.2 150.0 100.0 369.2 DISCHARGE (GPM) REQ'D PRESS. {PSI) 50.6 GPM GPM GPM GPM -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF • JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" ... NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) -2 18.0 ----25.3 ----3 18.0 26.0 ------- 4 18.0 26.7 --- 5 18.0 ----27.4 --- ,.. 6 18.0 ----28.4 --- 7 17.0 ----33.9 --- 8 17.0 ----24.4 ----9 19.0 ----25.2 --- 10 19.0 ----26.1 --- 11 19.0 27.0 --- 12 19.0 27.9 ---.. 13 19.0 -28.8 ------ 14 17.0 ----33.9 --- 15 17.0 ----24.2 ---.. 16 19.0 ----25.1 --- 17 19.0 ----26.0 --- 18 19.0 26.9 ----19 19.0 ----27.8 --- 20 19.0 ----28.7 --- 21 17.0 ----33.9 --- 22 17.0 ----23.8 ----23 17.0 34.0 ------- 24 14. 0 ----23.6 --- ~ 25 14. 0 ----35.5 ----26 14.0 ----23.3 --- 27 14.0 ----35.6 --- 28 14.0 ----23.3 --- • 29 15.0 ----32.7 --- 30 14. 0 ----35.8 --- ~ 31 14.0 ----36.5 --- 32 14.0 ----36.5 ---... 33 15.0 27.4 ------- 34 18.0 27.6 --- Al 15.0 K= 5.70 14.4 21. 6 -A2 15.0 K= 5.70 14.6 21. 8 A3 15.0 K= 5.70 15.3 22.3 A4 15.0 K= 5.70 16.9 23.5 -AS 15.0 K= 5.70 21. 3 26.3 A6 15.0 K= 5.70 21. 8 26.6 A7 15.0 K= 5.70 15.5 22.5 AB 15.0 K= 5.70 15.8 22.6 -A9 15.0 K= 5.70 16.6 23.2 Al0 15.0 K= 5.70 18.3 24.4 ~ All 15.0 K= 5.70 21. 0 26.1 -A12 15.0 K= 5.70 21.5 26.4 A13 15.0 K= 5.70 22.4 26.9 A14 15.0 K= 5.70 22.9 27.3 -AlS 15.0 K= 5.70 23.6 27.7 24A 15.0 ----21.3 --- 26A 15.0 ----21.0 --- 28A 15.0 ----22.8 ----TOR 14.0 37.8 --- BOR 0.0 HOSE STREAM 44.3 100.0 U2 0.0 ----50.6 ---- .. • ... .. -.. -- - ... ... .. - --- - - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 06/25/1997 JOB TITLE: CARLSBAD NODE TAG ELEVATION U3 Ul (FT) o.o 0.0 C:\DATA\CARLSBAD\1100\ll00NB.SDF COMPNAY STORES; 1100 NORTH AREA"A" NODE TYPE PRESSURE DISCHARGE SOURCE (PSI) (GPM) 47.1 50.6 469.2 -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF -JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" PIPE DATA --PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. -NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 39.5 2.731 PL 9.50 PF 0.0 -1 17.0 0.0 24.4 0.0 2.2 120 FTG PE 0.0 8 17.0 0.0 24.4 0.0 0.004 TL 9.50 PV 0.0 Pipe: 2 84.2 2.731 PL 10.00 PF 0.2 -8 17.0 0.0 24.4 0.0 4.6 120 FTG PE 0.0 -15 17.0 0.0 24.2 0.0 0.018 TL 10.00 PV 0.1 .. Pipe: 3 129.4 2.731 PL 11. 00 PF 0.4 15 17.0 0.0 24.2 0.0 7.1 120 FTG PE 0.0 22 17.0 0.0 23.8 0.0 0.039 TL 11.00 PV 0.3 -Pipe: 4 176.2 2.731 PL 14.75 PF 1.5 .. 22 17.0 0.0 23.8 0.0 9.6 120 FTG 2L PE 1.3 24 14.0 0.0 23.6 0.0 0.069 TL 21. 75 PV 0.6 - Pipe: 5 95.4 2.731 PL 12.00 PF 0.3 24 14.0 0.0 23.6 o.o 5.2 120 FTG PE 0.0 -26 14.0 o.o 23.3 0.0 0.022 TL 12.00 PV 0.2 Pipe: 6 12.8 2.731 PL 12.00 PF 0.0 -26 14.0 0.0 23.3 0.0 0.7 120 FTG PE 0.0 28 14.0 0. 0 23.3 0.0 0.001 TL 12.00 PV 0.0 Pipe: 7 -49.7 4.328 PL 9.50 PF 0.0 -7 17.0 0.0 33.9 0.0 1.1 120 FTG PE 0.0 14 17.0 0.0 33.9 0.0 0.001 TL 9.50 PV 0.0 -Pipe: 8 -94.4 4.328 PL 10.00 PF 0.0 14 17.0 0.0 33.9 0.0 2.1 120 FTG PE 0.0 21 17.0 0.0 33.9 0.0 0.002 TL 10.00 PV 0.0 -Pipe: 9 -139.6 4.328 PL 11. 00 PF 0.1 21 17.0 0.0 33.9 0.0 3.0 120 FTG PE 0.0 23 17.0 0.0 34.0 0.0 0.005 TL 11.00 PV 0.1 - Pipe: 10 -186.4 4.328 PL 13.80 PF 0.2 23 17.0 0.0 34.0 0.0 4.1 120 FTG 2L PE 1. 3 -25 14. 0 0.0 35.5 0.0 0.008 TL 25.80 PV 0.1 Pipe: 11 -247.7 4.328 PL 10.00 PF 0.1 -25 14.0 0.0 35.5 0.0 5.4 120 FTG PE 0.0 27 14.0 0.0 35.6 0.0 0.014 TL 10.00 PV 0.2 -Pipe: 12 -300.2 4.328 PL 10.00 PF 0.2 27 14. 0 0.0 35.6 0.0 6.5 120 FTG PE 0.0 30 14. 0 0.0 35.8 0.0 0.020 TL 10.00 PV 0.3 -Pipe: 13 -332.8 4.328 PL 7.66 PF 0.7 30 14.0 0.0 35.8 0.0 7.3 120 FTG T PE 0.0 32 14.0 0.0 36.5 0.0 0.024 TL 27.66 PV 0.4 .. • '·----~•··~-~--........... --·-~ . -.. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF .. JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" .. PIPE DATA (cont.) ... PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS . END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM . .. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI} ... Pipe: 13A 36.4 4.328 PL 2.33 PF 0.0 ·• 32 14.0 0.0 36.5 0.0 0.8 120 FTG T PE 0.0 31 14. 0 0.0 36.5 0.0 0.000 TL 22.33 PV 0.0 .. -Pipe: 14 -39.5 1.542 PL 6.25 PF 1.3 1 17.0 o.o 24.4 0.0 6.8 120 FTG 2T PE -0.4 ... 2 18.0 a.a 25.3 0.0 0.070 TL 18.25 PV 0.3 -Pipe: 15 -39.5 1. 542 PL 10.00 PF 0.7 2 18.0 o.o 25.3 0.0 6.8 120 FTG PE 0.0 -3 18.0 o.o 26.0 0.0 0.070 TL 10.00 PV 0.3 ... Pipe: 16 -39.5 1.542 PL 10.00 PF 0.7 .. 3 18.0 o.o 26.0 0.0 6.8 120 FTG PE 0.0 -4 18.0 o.o 26.7 0.0 0.070 TL 10.00 PV 0.3 ... Pipe: 17 -39.5 1.542 PL 10.00 PF 0.7 4 18.0 o.o 26.7 0.0 6.8 120 FTG PE 0.0 -s 18.0 o.o 27.4 0.0 0.070 TL 10.00 PV 0.3 ... Pipe: 18 -39.5 1.542 PL 2.90 PF 0.2 ·-5 18.0 0.0 27.4 0.0 6.8 120 FTG PE 0.0 34 18.0 0.0 27.6 0.0 0.070 TL 2.90 PV 0.3 -.. Pipe: 18A -49.7 1.542 PL 7.10 PF 0.8 34 18.0 0.0 27.6 0.0 8.5 120 FTG PE 0.0 .. 6 18.0 0.0 28.4 0.0 0.107 TL 7.10 PV 0.5 -Pipe: 19 -49.7 1. 542 PL 35.25 PF 5.1 6 18.0 o.o 28.4 0.0 8.5 120 FTG 2T PE 0.4 -7 17.0 0.0 33.9 0.0 0.107 TL 47.25 PV 0.5 -Pipe: 20 -44.7 1.542 PL 7.25 PF 1.7 8 17.0 0.0 24.4 0.0 7.7 120 FTG 2T PE -0.9 -9 19.0 0.0 25.2 0.0 0.088 TL 19.25 PV 0.4 -Pipe: 21 -44.7 1.542 PL 10.00 PF 0.9 9 19.0 0.0 25.2 0.0 7.7 120 FTG PE o.o -10 19.0 0.0 26.1 0.0 0.088 TL 10.00 PV 0.4 Pipe: 22 -44.7 1.542 PL 10.00 PF 0.9 ... 10 19.0 0.0 26.1 0.0 7.7 120 FTG PE 0.0 11 19.0 0.0 27.0 0.0 0.088 TL 10.00 PV 0.4 -Pipe: 23 -44.7 1.542 PL 10.00 PF 0.9 11 19.0 0.0 27.0 0.0 7.7 120 FTG PE o.o ... 12 19.0 0.0 27.9 0.0 0.088 TL 10.00 PV 0.4 ·-Pipe: 24 -44.7 1.542 PL 10.00 PF 0.9 ... 12 19.0 0.0 27.9 0.0 7.7 120 FTG PE 0.0 13 19.0 0.0 28.8 0.0 0.088 TL 10.00 PV 0.4 - -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" -PIPE DATA (cont.) • PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS . END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. -NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 25 -44.7 1.542 PL 36.25 PF 4.3 -13 19.0 0.0 28.8 0.0 7.7 120 FTG 2T PE 0.9 14 17.0 o.o 33.9 0.0 0.088 TL 48.25 PV 0.4 -Pipe: 26 -45.2 1.542 PL 7.25 PF 1. 7 15 17.0 0.0 24.2 0.0 7.8 120 FTG 2T PE -0.9 ~ 16 19.0 o.o 25.1 0.0 0.090 TL 19.25 PV 0.4 -Pipe: 27 -45.2 1. 542 PL 10.00 PF 0.9 16 19.0 o.o 25.1 0.0 7.8 120 FTG PE 0.0 17 19.0 o.o 26.0 0.0 0.090 TL 10.00 PV 0.4 -Pipe: 28 -45.2 1.542 PL 10.00 PF 0.9 17 19.0 0.0 26.0 0.0 7.8 120 FTG PE 0.0 -18 19.0 0.0 26.9 0.0 0.090 TL 10.00 PV 0.4 ◄ Pipe: 29 -45.2 1.542 PL 10.00 PF 0.9 18 19.0 o.o 26.9 0.0 7.8 120 FTG PE 0.0 -19 19.0 o.o 27.8 0.0 0.090 TL 10.00 PV 0.4 Pipe: 30 -45.2 1.542 PL 10.00 PF 0.9 -19 19.0 0.0 27.8 0.0 7.8 120 FTG PE 0.0 20 19.0 0.0 28.7 0.0 0.090 TL 10.00 PV 0.4 -Pipe: 31 -45.2 1.542 PL 36.25 PF 4.3 20 19.0 0.0 28.7 0.0 7.8 120 FTG 2T PE 0.9 21 17.0 0.0 33.9 0.0 0.090 TL 48.25 PV 0.4 -Pipe: 32 -46.8 1. 542 PL 82.00 PF 10.2 22 17.0 0.0 23.8 0.0 8.0 120 FTG 4T PE 0.0 23 17.0 o.o 34.0 0.0 0.096 TL 106.00 PV 0.4 -Pipe: 36 -32.7 1.542 PL 34.66 PF 2.7 29 15.0 0.0 32.7 0.0 5.6 120 FTG 3TL PE 0.4 -30 14.0 o.o 35.8 0.0 0.049 TL 54.66 PV 0.2 Pipe: 37 -36.4 1.542 PL 35.50 PF 3.3 29 15.0 0.0 32.7 0.0 6.3 120 FTG 3TL PE 0.4 -31 14.0 0.0 36.5 0.0 0.060 TL 55.50 PV 0.3 Pipe: 38 -369.2 4.328 PL 28.16 PF 1.3 -32 14.0 0.0 36.5 0.0 8.1 120 FTG 3L PE 0.0 TOR 14. 0 o.o 37.8 0.0 0.029 TL 46.16 PV 0.4 -Pipe: 39 -369.2 4.328 PL 14.00 PF 0.4 TOR 14. 0 0.0 37.8 0.0 8.1 120 FTG PE 6.1 BOR o.o H.S. 44.3 100.0 0.029 TL 14.00 PV 0.4 -Pipe: 40 -469.2 6.403 PL 499.00 PF 2.8 BOR o.o H.S. 44.3 100.0 4.7 150 FTG T7LG PE 0.0 U3 0.0 0.0 47.1 0.0 0.004 TL 644.06 PV 0.1 .. ~~---·~· • .. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF -JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" -PIPE DATA (cont.) -PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) (FT) SUM. -NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) ~ Pipe: 41 FIXED PRESSURE LOSS DEVICE -U2 0.0 0.0 50.6 0.0 3.5 psi, 469.2 gpm U3 0.0 0.0 47.1 0.0 -.. Pipe: 42 -469.2 8.044 PL 0.50 PF 0.0 U2 0.0 0.0 50.6 0.0 3.0 150 FTG 2L PE 0.0 Ul 0.0 SRCE 50.6 (N/A) 0.001 TL 24.50 PV 0.1 -Pipe: 43 80.8 1.542 PL 1.00 PF 1.8 24 14.0 0.0 23.6 0.0 13.9 120 FTG T PE -0.4 24A 15.0 0.0 21.3 0.0 0.264 TL 7.00 PV 1.3 -Pipe: 44 82.6 1.542 PL 1.00 PF 1. 9 26 14.0 0.0 23.3 0.0 14.2 120 FTG T PE -0.4 -26A 15.0 0.0 21.0 0.0 0.275 TL 7.00 PV 1.4 Pipe: 45 12.8 1.542 PL 1.00 PF 0.1 28 14.0 0.0 23.3 0.0 2.2 120 FTG T PE -0.4 .. 28A 15.0 0.0 22.8 0.0 0.009 TL 7.00 PV 0.0 Pipe: 46 -21.6 1.542 PL 9.00 PF 0.2 -Al 15.0 5.7 14.4 21. 6 3.7 120 FTG PE 0.0 A2 15.0 5.7 14.6 21.8 0.023 TL 9.00 PV 0.1 .. Pipe: 47 -43.4 1.542 PL 9.00 PF 0.8 A2 15.0 5.7 14.6 21.8 7.4 120 FTG PE 0.0 A3 15.0 5.7 15.3 22.3 0.083 TL 9.00 PV 0.4 .. Pipe: 48 -65.7 1. 542 PL 9.00 PF 1. 6 A3 15.0 5.7 15.3 22.3 11. 3 120 FTG PE 0.0 A4 15.0 5.7 16.9 23.5 0.180 TL 9.00 PV 0.9 -Pipe: 49 -89.1 1. 542 PL 7.86 PF 4.4 A4 15.0 5.7 16.9 23.5 15.3 120 FTG T PE 0.0 -24A 15.0 0.0 21. 3 0.0 0.316 TL 13. 86 PV 1.6 Pipe: so -8.4 1. 542 PL 1.16 PF 0.0 24A 15.0 o.o 21. 3 0.0 1.4 120 FTG T PE o.o AS 15.0 5.7 21. 3 26.3 0.004 TL 7.16 PV 0.0 Pipe: 51 -34.7 1. 542 PL 9.00 PF 0.5 AS 15.0 5.7 21. 3 26.3 6.0 120 FTG PE 0.0 A6 15.0 5.7 21.8 26.6 0.055 TL 9.00 PV 0.2 -Pipe: 52 -61.3 1.542 PL 71. 25 PF 13.2 A6 15.0 5.7 21.8 26.6 10.5 120 FTG 2T PE 0.4 25 14.0 0.0 35.5 0.0 0.158 TL 83.25 PV 0.7 -Pipe: 53 1. 542 -22.5 PL 9.00 PF 0.2 A7 15.0 5.7 15.5 22.5 3.9 120 FTG PE 0.0 AB 15.0 5.7 15.8 22.6 0.025 TL 9.00 PV 0.1 ------·--· --SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF -JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" PIPE DATA (cont.) - ·-PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) HW (C) (FT) SUM. -NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 54 -45.1 1.542 PL 9.00 PF 0.8 -AS 15.0 5.7 15.8 22.6 7.7 120 FTG PE 0.0 A9 15.0 5.7 16.6 23.2 0.090 TL 9.00 PV 0.4 Pipe: 55 -68.3 1. 542 PL 9.00 PF 1. 7 -A9 15.0 5.7 16.6 23.2 11. 7 120 FTG PE 0.0 Al0 15.0 5.7 18.3 24.4 0.193 TL 9.00 PV 0.9 -Pipe: 56 -92.7 1.542 PL 7.86 PF 2.7 Al0 15.0 5.7 18.3 24.4 15.9 120 FTG PE 0.0 26A 15.0 0.0 21. 0 0.0 0.340 TL 7.86 PV 1. 7 -Pipe: 57 -10.1 1.542 PL 1.16 PF 0.0 26A 15.0 0.0 21. 0 0.0 1. 7 120 FTG PE 0.0 All 15.0 5.7 21. 0 26.1 0.006 TL 1.16 PV 0.0 - Pipe: 58 -36.2 1.542 PL 9.00 PF 0.5 All 15.0 5.7 21. 0 26.1 6.2 120 FTG PE o.o -A12 15.0 5.7 21. 5 26.4 0.060 TL 9.00 PV 0.3 Pipe: 59 -62.6 1.542 PL 29.50 PF 5.8 -A12 15.0 5.7 21. 5 26.4 10.8 120 FTG T PE 0.0 33 15.0 0.0 27.4 0.0 0.165 TL 35.50 PV 0.8 Pipe: 59A -52.5 1.542 PL 43.80 PF 7.8 .. 33 15.0 0.0 27.4 0.0 9.0 120 FTG 3T2L PE 0.4 27 14. 0 0.0 35.6 0.0 0.119 TL 65.80 PV 0.5 .. Pipe: 60 -26.9 1. 542 PL 7.86 PF 0.5 A13 15.0 5.7 22.4 26.9 4.6 120 FTG T PE 0.0 28A 15.0 o.o 22.8 0.0 0.035 TL 13.86 PV 0.1 -Pipe: 61 -14.1 1.542 PL 1.16 PF 0.1 28A 15.0 0.0 22.8 0.0 2.4 120 FTG T PE 0.0 A14 15.0 5.7 22.9 27.3 0.010 TL 7.16 PV o.o - Pipe: 62 -41.4 1. 542 PL 9.00 PF 0.7 A14 15.0 5.7 22.9 27.3 7.1 120 FTG PE 0.0 .. A15 15.0 5.7 23.6 27.7 0.076 TL 9.00 PV 0.3 Pipe: 63 -69.1 1. 542 PL 40.00 PF 9.1 -A15 15.0 5.7 23.6 27.7 11. 9 120 FTG T PE o.o 29 15.0 0.0 32.7 0.0 0.197 TL 46.00 PV 0.9 Pipe: 64 -10.2 1.542 PL 207.00 PF 1.5 -33 15.0 0.0 27.4 o.o 1. 7 120 FTG 9T4L PE -1.3 34 18.0 0.0 27.6 0.0 0.006 TL 269.00 PV 0.0 - .. .. - .. .. .. .. .... ... - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" NOTES: (1) Calculations were performed by the HASS 6.1.0 computer program under license no. 825A408 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.151 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 15.9 ft/sec at pipe 56. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G A Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 1. 542 3.00 6.00 2.00 7.00 1.00 1.00 12.00 2.731 6.00 12.00 3.50 14.00 1. 00 1. 00 14.00 4.328 10.00 20.00 6.00 22.00 2.00 2.00 25.00 6.403 14.00 30.00 9.00 32.00 3.00 3.00 15.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G F Ell Tee LngEll ChkVlv BfyVlv GatVlv FRTY5 8.044 18.00 33.00 12.00 40.00 4.00 3.00 9.00 D DPVlv 10.00 10.00 10.00 15.00 .. - -.. - -... - .. .. .. --- --- - .. - ... - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00NB.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"A" WATER SUPPLY CURVE 84*\\\ 0 \\\ \\\\ \\\ 77+ \\\\ 70+ 63+ P 56+ R E \\\ \\\ * <-72.0 psi@ 2354 gpm Flow Test Point S X S 49+ u R E 42+ ( p s I 35+ ) 28+ 21+ 14+ 7+ ======================-======= LEGEND X = Required Water Supply 50.64 psi@ 619.2 gpm 0 = Available Water Supply 82.99 psi@ 619.2 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM} ... - - ... .... - - .. .. .. - --- - - ... - .... LINDLEY FIRE PROTECTION CO. 2220 E. VIA BURTON ANAHEIM, CA 92806 HYDRAULIC CALCULATIONS FOR CARLSBARD COMPANY STORES BUILDING 1100 NORTH SIDE AREA "B" DATE: 3-28-97 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: Ordinary Hazard; Group II .20 gpm/sq. ft. 1500 sq. ft. 115 sq. ft. 15 sprinklers 353.2 gpm TOTAL WATER REQUIRED (including hose): 603.2 gpm FLOW AND PRESSURE (@ BOR): SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: 353.2 gpm@ 37.4 psi 1/2 inch Lindley Fire Protection Co. San Diego Fire Dept. C16/C34 No. 713562 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 825A408 HRS SYSTEMS, INC. ATLANTA, GA - - .. - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 06/25/1997 JOB TITLE: CARLSBAD WATER SUPPLY DATA C:\DATA\CARLSBAD\1100\ll00N.SDF COMPNAY STORES; 1100 NORTH AREA"B" SOURCE NODE TAG Ul STATIC PRESS. (PSI) 84.0 RESID. PRESS. (PSI) 72.0 @ FLOW (GPM) 2354.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE AVAIL. PRESS.@ (PSI) 83.0 TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 ELEVATION (FT) 17.0 18.0 18.0 18.0 18.0 18.0 17.0 17.0 19.0 19.0 19.0 19.0 19.0 17.0 17.0 19.0 19.0 19.0 19.0 19.0 17.0 17.0 17.0 14.0 14.0 14. 0 14.0 14. 0 15.0 14.0 14.0 14.0 15.0 18.0 NODE TYPE K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 K= 5.70 PRESSURE (PSI) 19.5 17.7 17.5 17.5 18.0 18.8 26.9 19.6 16.6 16.3 16.3 16.5 17.3 26.9 19.8 16.8 16.4 16.4 16.6 17.4 27.0 20.3 27.1 22.2 28.7 22.3 28.9 22.4 27.7 29.1 29.7 29.7 23.4 18.3 TOTAL DEMAND (GPM) 603.2 REQ'D PRESS. (PSI) 43.6 603.2 GPM 150.0 GPM 100.0 GPM 353.2 GPM DISCHARGE (GPM) 24.0 23.9 23.9 24.2 24.7 23.2 23.0 23.0 23.1 23.7 23.3 23.1 23.1 23.2 23.8 .. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF • JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" -NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) Al 15.0 22.2 ----A2 15.0 ----22.2 --- A3 15.0 22.2 --- A4 15.0 ----22.2 ----AS 15.0 22.6 --- A6 15.0 23.2 --- • A7 15.0 22.1 --- AB 15.0 22.1 ---.. A9 15.0 22.1 ----Al0 15.0 22.1 --- All 15.0 22.1 ----Al2 15.0 22.4 --- Al3 15.0 22.5 --- Al4 15.0 23.1 ----AlS 15.0 23.9 --- 24A 15.0 ----22.2 --- 26A 15.0 ----22.1 --- 28A 15.0 22.5 ---.. TOR 14.0 30.9 --- BOR 0.0 HOSE STREAM 37.4 100.0 U2 0.0 ----43.5 ---... U3 0.0 ----40.0 --- Ul 0.0 SOURCE 43.6 453.2 .. - - -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" 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) F.L./FT (PSI) Pipe: 1 -41. 7 2.731 PL 9.50 PF 0.0 -1 17.0 0.0 19.5 0.0 2.3 120 FTG PE 0.0 8 17.0 0.0 19.6 0.0 0.005 TL 9.50 PV 0.0 -Pipe: 2 -91. 6 2.731 PL 10.00 PF 0.2 8 17.0 0.0 19.6 0.0 5.0 120 FTG PE 0.0 15 17.0 0.0 19.8 0.0 0.021 TL 10.00 PV 0.2 -Pipe: 3 -142.2 2.731 PL 11.00 PF 0.5 15 17.0 0.0 19.8 0.0 7.8 120 FTG PE 0.0 22 17.0 0.0 20.3 0.0 0.046 TL 11.00 PV 0.4 -Pipe: 4 -104.6 2.731 PL 14.75 PF 0.6 -• 22 17.0 0.0 20.3 o.o 5.7 120 FTG 2L PE 1. 3 24 14.0 0.0 22.2 0.0 0.026 TL 21. 75 PV 0.2 - Pipe: 5 -67.9 2.731 PL 12.00 PF 0.1 24 14. 0 0.0 22.2 0.0 3.7 120 FTG PE 0.0 -26 14. 0 0.0 22.3 0.0 0.012 TL 12.00 PV 0.1 Pipe: 6 -43.2 2.731 PL 12.00 PF 0.1 -26 14.0 0.0 22.3 0.0 2.4 120 FTG PE 0.0 28 14.0 0.0 22.4 0.0 0.005 TL 12.00 PV 0.0 -Pipe: 7 -62.3 4.328 PL 9.50 PF 0.0 7 17.0 0.0 26.9 0.0 1. 4 120 FTG PE 0.0 14 17.0 0.0 26.9 0.0 0.001 TL 9.50 PV 0.0 -Pipe: 8 -128.5 4.328 PL 10.00 PF 0.0 14 17.0 0.0 26.9 0.0 2.8 120 FTG PE 0.0 21 17.0 0.0 27.0 0.0 0.004 TL 10.00 PV 0.1 -Pipe: 9 -194.4 4.328 PL 11.00 PF 0.1 21 17.0 0.0 27.0 0.0 4.2 120 FTG PE 0.0 23 17.0 0.0 27.1 0.0 0.009 TL 11.00 PV 0.1 - Pipe: 10 -232.0 4.328 PL 13.80 PF 0.3 23 17.0 0.0 27.1 0.0 5.1 120 FTG 2L PE 1. 3 -25 14. 0 0.0 28.7 0.0 0.012 TL 25.80 PV 0.2 Pipe: 11 -268.7 4.328 PL 10.00 PF 0.2 -25 14.0 0.0 28.7 0.0 5.9 120 FTG PE 0.0 27 14.0 0.0 28.9 0.0 0.016 TL 10.00 PV 0.2 -Pipe: 12 -310.0 4.328 PL 10.00 PF 0.2 27 14. 0 0.0 28.9 0.0 6.8 120 FTG PE 0.0 30 14. 0 0.0 29.1 0.0 0.021 TL 10.00 PV 0.3 -Pipe: 13 -328.7 4.328 PL 7.66 PF 0.6 30 14.0 0.0 29.1 0.0 7.2 120 FTG T PE 0.0 32 14.0 o.o 29.7 o.o 0.023 TL 27.66 PV 0.3 - .. ''" _,_",, -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF • JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" PIPE DATA (cont.) - PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. -NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 13A 24.5 4.328 PL 2.33 PF 0.0 -32 14. 0 0.0 29.7 0.0 0.5 120 FTG T PE 0.0 31 14. 0 0.0 29.7 0.0 0.000 TL 22.33 PV 0.0 Pipe: 14 41.7 1. 542 PL 6.25 PF 1.4 -1 17.0 0.0 19.5 0.0 7.2 120 FTG 2T PE -0.4 2 18.0 5.7 17.7 24.0 0.078 TL 18.25 PV 0.3 -Pipe: 15 17.7 1.542 PL 10.00 PF 0.2 2 18.0 5.7 17.7 24.0 3.0 120 FTG PE 0.0 ·~ 3 18.0 5.7 17.5 23.9 0.016 TL 10.00 PV 0.1 -Pipe: 16 -6.1 1.542 PL 10.00 PF 0.0 3 18.0 5.7 17.5 23.9 1.1 120 FTG PE 0.0 4 18.0 5.7 17.5 23.9 0.002 TL 10.00 PV 0.0 .. Pipe: 17 -30.0 1.542 PL 10.00 PF 0.4 4 18.0 5.7 17.5 23.9 5.2 120 FTG PE o.o -5 18.0 5.7 18.0 24.2 0.042 TL 10.00 PV 0.2 Pipe: 18 -54.2 1.542 PL 2.90 PF 0.4 -5 18.0 5.7 18.0 24.2 9.3 120 FTG PE 0.0 34 18.0 0.0 18.3 0.0 0.126 TL 2.90 PV 0.6 Pipe: 18A -37.6 1.542 PL 7.10 PF 0.5 -34 18.0 0.0 18.3 0.0 6.5 120 FTG PE 0.0 6 18.0 5.7 18.8 24.7 0.064 TL 7.10 PV 0.3 -Pipe: 19 -62.3 1.542 PL 35.25 PF 7.7 6 18.0 5.7 18.8 24.7 10.7 120 FTG 2T PE 0.4 7 17.0 0.0 26.9 0.0 0.163 TL 47.25 PV 0.8 -Pipe: 20 49.9 1.542 PL 7.25 PF 2.1 8 17.0 0.0 19.6 0.0 8.6 120 FTG 2T PE -0.9 9 19.0 5.7 16.6 23.2 0.108 TL 19.25 PV 0.5 - Pipe: 21 26.6 1. 542 PL 10.00 PF 0.3 9 19.0 5.7 16.6 23.2 4.6 120 FTG PE 0.0 -10 19.0 5.7 16.3 23.0 0.034 TL 10.00 PV 0.1 Pipe: 22 3.6 1.542 PL 10.00 PF 0.0 -10 19.0 5.7 16.3 23.0 0.6 120 FTG PE 0.0 11 19.0 5.7 16.3 23.0 0.001 TL 10.00 PV 0.0 Pipe: 23 -19.4 1.542 PL 10.00 PF 0.2 -11 19.0 5.7 16.3 23.0 3.3 120 FTG PE 0.0 12 19.0 5.7 16.5 23.1 0.019 TL 10.00 PV 0.1 -Pipe: 24 -42.5 1. 542 PL 10.00 PF 0.8 12 19.0 5.7 16.5 23.1 7.3 120 FTG PE 0.0 13 19.0 5.7 17.3 23.7 0.080 TL 10.00 PV 0.4 - --~· ~-----·-~ ~.----·•' -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF • JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" PIPE DATA (cont.) .. PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. .. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 25 -66.2 1.542 PL 36.25 PF 8.8 -13 19.0 5.7 17.3 23.7 11.4 120 FTG 2T PE 0.9 14 17.0 0.0 26.9 0.0 0.182 TL 48.25 PV 0.9 Pipe: 26 50.6 1.542 PL 7.25 PF 2.1 -15 17.0 0.0 19.8 0.0 8.7 120 FTG 2T PE -0.9 16 19.0 5.7 16.8 23.3 0.111 TL 19.25 PV 0.5 .. Pipe: 27 27.3 1.542 PL 10.00 PF 0.4 16 19.0 5.7 16.8 23.3 4.7 120 FTG PE o.o 17 19.0 5.7 16.4 23.1 0.035 TL 10.00 PV 0.1 .. Pipe: 28 4.2 1.542 PL 10.00 PF 0.0 17 19.0 5.7 16.4 23.1 0.7 120 FTG PE 0.0 18 19.0 5.7 16.4 23.1 0.001 TL 10.00 PV 0.0 - Pipe: 29 -18.9 1.542 PL 10.00 PF 0.2 18 19.0 5.7 16.4 23.1 3.3 120 FTG PE 0.0 -19 19.0 5.7 16.6 23.2 0.018 TL 10.00 PV 0.1 Pipe: 30 -42.1 1.542 PL 10.00 PF 0.8 -19 19.0 5.7 16.6 23.2 7.2 120 FTG PE 0.0 20 19.0 5.7 17.4 23.8 0.079 TL 10.00 PV 0.4 Pipe: 31 -65.9 1.542 PL 36.25 PF 8.7 ~ 20 19.0 5.7 17.4 23.8 11.3 120 FTG 2T PE 0.9 21 17.0 0.0 27.0 0.0 0.181 TL 48.25 PV 0.9 .. Pipe: 32 -37.6 1. 542 PL 82.00 PF 6.8 22 17.0 0.0 20.3 0.0 6.5 120 FTG 4T PE 0.0 23 17.0 0.0 27.1 0.0 0.064 TL 106.00 PV 0.3 -Pipe: 36 -18.7 1.542 PL 34.66 PF 1.0 29 15.0 0.0 27.7 0.0 3.2 120 FTG 3TL PE 0.4 30 14. 0 o.o 29.1 0.0 0.018 TL 54.66 PV 0.1 Pipe: 37 -24.5 1.542 PL 35.50 PF 1. 6 29 15.0 0.0 27.7 0.0 4.2 120 FTG 3TL PE 0.4 31 14.0 0.0 29.7 0.0 0.029 TL 55.50 PV 0.1 Pipe: 38 -353.2 4.328 PL 28.16 PF 1.2 .. 32 14. 0 0.0 29.7 0.0 7.7 120 FTG 3L PE o.o TOR 14. 0 o.o 30.9 0.0 0.027 TL 46.16 PV 0.4 Pipe: 39 -353.2 4.328 PL 14.00 PF 0.4 -TOR 14.0 0.0 30.9 0.0 7.7 120 FTG PE 6.1 BOR 0.0 H.S. 37.4 100.0 0.027 TL 14. 00 PV 0.4 -Pipe: 40 -453.2 6.403 PL 499.00 PF 2.7 BOR 0.0 H.S. 37.4 100.0 4.5 150 FTG T7LG PE 0.0 ~ U3 0.0 0.0 40.0 0.0 0.004 TL 644.06 PV 0.1 • .. ,., ____ "··-- -SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF -JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" PIPE DATA (cont.) - PIPE TAG Q{GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. -NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 41 FIXED PRESSURE LOSS DEVICE -U2 0.0 0.0 43.5 0.0 3.5 psi, 453.2 gpm U3 0.0 0.0 40.0 0.0 Pipe: 42 -453.2 8.044 PL 0.50 PF 0.0 -U2 0.0 0.0 43.5 0.0 2.9 150 FTG 2L PE 0.0 Ul o.o SRCE 43.6 (N/A) 0.001 TL 24.50 PV 0.1 -Pipe: 43 -36.7 1. 542 PL 1.00 PF 0.4 24 14.0 0.0 22.2 0.0 6.3 120 FTG T PE -0.4 24A 15.0 0.0 22.2 0.0 0.061 TL 7.00 PV 0.3 -Pipe: 44 -24.7 1. 542 PL 1.00 PF 0.2 26 14. 0 0.0 22.3 0.0 4.2 120 FTG T PE -0.4 26A 15.0 0.0 22.1 0.0 0.029 TL 7.00 PV 0.1 .. Pipe: 45 -43.2 1.542 PL 1.00 PF 0.6 28 14.0 0.0 22.4 0.0 7.4 120 FTG T PE -0.4 -28A 15.0 0.0 22.5 0.0 0.083 TL 7.00 PV 0.4 Pipe: 46 0.0 1.542 PL 9.00 PF 0.0 -Al 15.0 0.0 22.2 o.o 0.0 120 FTG PE o.o A2 15.0 0.0 22.2 o.o 0.000 TL 9.00 PV 0.0 Pipe: 47 0.0 1. 542 PL 9.00 PF 0.0 -A2 15.0 0.0 22.2 o.o 0.0 120 FTG PE 0.0 A3 15.0 0.0 22.2 0.0 0.000 TL 9.00 PV 0.0 -Pipe: 48 0.0 1. 542 PL 9.00 PF 0.0 A3 15.0 0.0 22.2 0.0 0.0 120 FTG PE o.o A4 15.0 0.0 22.2 0.0 0.000 TL 9.00 PV o.o -Pipe: 49 0.0 1.542 PL 7.86 PF 0.0 A4 15.0 0.0 22.2 0.0 0.0 120 FTG T PE 0.0 24A 15.0 0.0 22.2 0.0 0.000 TL 13.86 PV o.o - Pipe: 50 -36.7 1. 542 PL 1.16 PF 0.4 24A 15.0 0.0 22.2 0.0 6.3 120 FTG T PE 0.0 -AS 15.0 0.0 22.6 0.0 0.061 TL 7.16 PV 0.3 Pipe: 51 -36.7 1. 542 PL 9.00 PF 0.6 -AS 15.0 0.0 22.6 0.0 6.3 120 FTG PE 0.0 A6 15.0 0.0 23.2 0.0 0.061 TL 9.00 PV 0.3 -Pipe: 52 -36.7 1.542 PL 71.25 PF 5.1 A6 15.0 0.0 23.2 0.0 6.3 120 FTG 2T PE 0.4 25 14. 0 0.0 28.7 0.0 0.061 TL 83.25 PV 0.3 -Pipe: 53 0.0 1. 542 PL 9.00 PF 0.0 A7 15.0 o.o 22.1 o.o 0.0 120 FTG PE 0.0 -AS 15.0 0.0 22.1 0.0 0.000 TL 9.00 PV 0.0 - .. , •• -........... ",.__....,,....,_+ ____ ~" .. .... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF ◄ JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" PIPE DATA (cont.) 4 PIPE TAG Q(GPM) DIA (IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT} SUM. ... NODES (FT) ( K) (PSI) (GPM) F .L. /FT (PSI) Pipe: 54 0.0 1.542 PL 9.00 PF 0.0 .. AB 15.0 0.0 22.1 0.0 0.0 120 FTG PE 0.0 A9 15.0 0.0 22.1 0.0 0.000 TL 9.00 PV 0.0 Pipe: 55 o.o 1.542 PL 9.00 PF 0.0 ~ A9 15.0 0.0 22.1 0.0 0.0 120 FTG PE 0.0 Al0 15.0 0.0 22.1 0.0 0.000 TL 9.00 PV 0.0 -Pipe: 56 0.0 1. 542 PL 7.86 PF 0.0 Al0 15.0 0.0 22.1 0.0 0.0 120 FTG PE 0.0 26A 15.0 0.0 22.1 0.0 0.000 TL 7.86 PV 0.0 ... Pipe: 57 -24.7 1. 542 PL 1.16 PF 0.0 ·~ 26A 15.0 0.0 22.1 0.0 4.2 120 FTG PE 0.0 All 15.0 0.0 22.1 0.0 0.029 TL 1.16 PV 0.1 -Pipe: 58 -24.7 1. 542 PL 9.00 PF 0.3 All 15.0 0.0 22.1 0.0 4.2 120 FTG PE 0.0 ... A12 15.0 0.0 22.4 0.0 0.029 TL 9.00 PV 0.1 Pipe: 59 -24.7 1.542 PL 29.50 PF 1.0 -A12 15.0 0.0 22.4 0.0 4.2 120 FTG T PE 0.0 33 15.0 0.0 23.4 0.0 0.029 TL 35.50 PV 0.1 Pipe: 59A -41. 2 1. 542 PL 43.80 PF 5.0 ... 33 15.0 0.0 23.4 0.0 7.1 120 FTG 3T2L PE 0.4 27 14.0 0.0 28.9 0.0 0.076 TL 65.80 PV 0.3 Pipe: 60 0.0 1.542 PL 7.86 PF 0.0 Al3 15.0 0.0 22.5 0.0 0.0 120 FTG T PE 0.0 28A 15.0 0.0 22.5 0.0 0.000 TL 13.86 PV 0.0 ... Pipe: 61 -43.2 1. 542 PL 1.16 PF 0.6 28A 15.0 0.0 22.5 0.0 7.4 120 FTG T PE 0.0 Al4 15.0 0.0 23.1 o.o 0.083 TL 7.16 PV 0.4 Pipe: 62 -43.2 1. 542 PL 9.00 PF 0.7 A14 15.0 0.0 23.1 0.0 7.4 120 FTG PE 0.0 .. AlS 15.0 0.0 23.9 0.0 0.083 TL 9.00 PV 0.4 .. Pipe: 63 -43.2 1. 542 PL 40.00 PF 3.8 -A15 15.0 0.0 23.9 0.0 7.4 120 FTG T PE 0.0 29 15.0 0.0 27.7 0.0 0.083 TL 46.00 PV 0.4 Pipe: 64 16.6 1. 542 PL 207.00 PF 3.8 -33 15.0 0.0 23.4 0.0 2.8 120 FTG 9T4L PE -1. 3 34 18.0 o.o 18.3 0.0 0.014 TL 269.00 PV 0.1 - .. .. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page B Date: 06/25/1997 C:\DATA\CARLSBAD\1100\ll00N.SDF • JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA"B" .. .. .. .. NOTES: (1) Calculations were performed by the HASS 6.1.0 computer program under license no. 825A408 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.072 gpm. ( 3) Velocity pressures are printed for not used in balancing the system. is 11.4 ft/sec at pipe 25. information only, and are Maximum water velocity (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G A Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 1.542 3.00 6.00 2.00 7.00 1.00 1.00 12.00 2.731 6.00 12.00 3.50 14.00 1.00 1.00 14.00 4.328 10.00 20.00 6.00 22.00 2.00 2.00 25.00 6.403 14.00 30.00 9.00 32.00 3.00 3.00 15.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G F Ell Tee LngEll ChkVlv BfyVlv GatVlv FRTY5 8.044 18.00 33.00 12.00 40.00 4.00 3.00 9.00 D DPVlv 10.00 10.00 10.00 15.00 • --. .. .. .. ... ... - - - - - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 06/25/1997 C:\DATA\CARLSBAD\1100\llOON.SDF JOB TITLE: CARLSBAD COMPNAY STORES; 1100 NORTH AREA11 B11 WATER SUPPLY CURVE 84*\\\ 0 \\\ \\\\ \\\ 77+ \\\\ \\\ \\\ 70+ * <-72.0 psi@ 2354 gpm Flow Test Point 63+ P 56+ R E s S 49+ u R E X 42+ ( p s I 35+ ) 28+ 21+ 14+ 7+ ============~================= LEGEND X = Required Water Supply 43.56 psi@ 603.2 gpm 0 = Available Water Supply 83.03 psi@ 603.2 gpm II II " " " II II II 0++-+---+----+-----+------+--------+--------+---------+-----------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM)