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2742 LOKER AVE WEST; ; AS030124; Permit
10/10/25, 12:18 PM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: about blank Fees($) 537.5 AS030124 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS030124 2742 LOKER AV Status: WEST SPRINK Applied 2090813500 Approved: 0 Issued: Inspector: CARLSBAD OAKS BLDG. A Owner: Add'I Fees ($) 0 Total ($) 537.5 ISSUED 7/1/2003 9/16/2003 9/16/2003 Balance($) 0 1/1 ------------- GENERAL UNDERGROUND FIRE PROTECTION INC 3930 E. Coronado street Anaheim, CA 92807 (714) 632-8646 FAX (714) 632-0579 TO CITY OF CARLSBAD FIRE PREVENTION 1635 FARADAY AVE. CARLSBAD, CA. 92008 DATE I 8/01/03 I JOB No. I 745 r ATTENTION I PLAN CHECK PROJECT: CARLSBAD OAKS 2742-2748 LOKER AVENUE WEST. LOT 7, PARCEL 3 PHONE #(760)602- WE ARE SENDING YOU O Attached [SJ Under separate cover via cover via HAND CARRIED The following items: [SJ Shop drawings D Prints D plans D Specifications D Copy of letter D change order □ COPIES DATE NO. DESCRIPTION 3 8/01/03 FP1-FP5 CARLSBAD OAKS FIRE SPRINKLER DRAWINGS 2 8/01/03 HYDRAULIC CALCULATIONS (FOR EACH BLDG) -- •< ... WE ARE SENDING YOU as checked below: [SJ For Approval [SJ For your use D As requested D For review and comment 0 Approved as submitted 0 Approved as noted D Returned for corrections ........ ----~ -----~ • ·-'J.\r . . D resumitted ----- D Sumi! ------- D Return ------- . ;: ', ' f';,_..i,W: -~. •~:·::.t ·.,·~ ., ' ··~~ ' • .,, ' •• ·, 1'- Copies for approval Copies for distribution Corrected prints 0 FORBID DUE REMARKS 19 0 PRINTS RETURNED AFTER LOAN TO US ---------------- COPY TO JOB FILE SIGNED ··,-.. GENERAL UNDERGROUND FIRE PROTECTION, Inc. HYDRAULIC CALCULATIONS FOR CARLSBAD OAKS su1;..01NG A AREA A PARCEL 3, LOKER AVENUE CARLSBAD, CALIFORNIA GUFP JOB #745 ► OCCUPANCY CLASSIFICATION: EX. HAZ. ► DENSITY: .33GPM/SQ.FT. ► REQUIRED AREA OF APPLICATION: 3000 SQ.FT. ► COVERAGE PER SPRINKLER: 92 SQ. FT. ► NUMBER OF SPRINKLERS FLOWING: ► TOTAL SPRINKLER FLOW REQUIRED: 1229.6 GPM ► TOTAL WATER REQUIRED (INCLUDING HOSE): 1729.6 GPM ► DEMAND AT BASE OF RISER: 1229.6GPM@79.5PSI ► SPRINKLER ORIFICE SIZE: 3/4" (K-FACTOR =8.0) ► CALCULATIONS BY: ROBERT MAHONEY ► AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE ► COMMENTS: WATER AVAILABLE FOR DESIGN 90% OF CITY SUPPLY Ca1cu1at1on tJy hass cornputer program HRS Systems, Inc General Underground Fire Protection Inc tt 16031158 3930 EAST CORONADO STREET + ANAHEIM, CA 92807 + PHONE 714-632-8646 FAX 714-632-0579 CONTRACTOR'S LICENSE NO. 485748 C-16/C-34 ···~~~-•--·--· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 132. 3 128.7 1683.0 128.5 1729.6 92.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1729.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1229.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.0 K= 7.55 16.8 30.9 2 18.0 K= 7.55 16.8 31. 0 3 18.0 K= 7.55 17.1 31. 3 4 18.0 K= 7.55 17.8 31. 9 5 18.0 K= 7.55 18.9 32.9 6 18.0 K= 7.55 20.7 34.4 7 18.0 ----25.2 8 18.0 K= 7.55 25. 3 38.0 9 18.0 K= 7.55 25.6 38.2 10 18.0 K= 7.55 26.2 38.7 11 18.0 K= 7.55 16.5 30.7 12 18.0 K= 7.55 16.6 30.7 13 18.0 K= 7.55 16.9 31. 0 14 18.0 K= 7.55 17.5 31. 6 15 18.0 K= 7.55 18.7 32.6 16 18.0 K= 7.55 20.4 34.1 17 18.0 ----24.8 18 18.0 K= 7.55 24.9 37.6 19 18.0 K= 7.55 25.0 37.8 20 18.0 K= 7.55 26.3 38.7 21 18.0 K= 7.55 16.7 30.9 22 18.0 K= 7.55 16.8 30.9 23 18.0 K= 7.55 17.1 31.2 24 18.0 K= 7.55 17.8 31. 8 25 18.0 K= 7.55 18.9 32.8 26 18.0 K= 7.55 20.7 34.3 27 18.0 ----25.1 28 18.0 K= 7.55 25.2 37.9 29 18.0 K= 7.55 25.3 38.0 30 18.0 K= 7.55 26.6 38.9 31 18.0 K= 7.55 17.2 31. 3 32 18.0 K= 7.55 17.2 31. 4 33 18.0 K= 7.55 17.6 31. 6 34 18.0 K= 7.55 18.2 32.2 35 18.0 K= 7.55 19.4 33.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 18.0 K= 7.55 21. 2 34.8 37 18.0 ----25.8 38 18.0 K= 7.55 25.8 38.3 39 18.0 K= 7.55 26.0 38.5 40 18.0 K= 7.55 27.2 39.3 41 18.0 28.1 42 18.0 ----28.1 43 18.0 ----28.1 44 18.0 ----28.1 45 18.0 ----28.1 46 18.0 ----28.1 47 18.0 ----28.1 48 18.0 ----28.1 49 18.0 ----28.1 50 18.0 ----28.1 51 18.0 ----29.1 52 18.0 29.1 53 18.0 ----29.1 54 18.0 ----29.1 55 18.0 29.1 56 18.0 29.1 57 18.0 29.1 58 18.0 ----29.1 59 18.0 29.1 60 18.0 ----29.1 61 18.0 ----30.1 62 18.0 ----30.1 63 18.0 ----30.1 64 18.0 ----30.1 65 18.0 ----30.1 66 18.0 ----30.1 67 18.0 ----30.1 68 18.0 30.1 69 18.0 30.1 70 18.0 30.1 71 18.0 31. 0 72 18.0 ----31. 0 73 18.0 ----31. 0 74 18.0 ----31. 0 75 18.0 ----31. 0 76 18.0 ----31. 0 77 18.0 31. 0 78 18.0 ----31. 0 79 18.0 ----31. 0 80 18.0 ----31. 0 81 18.0 ----28.1 82 18.0 ----28.2 83 18.0 ----28.6 84 18.0 ----29.5 TR 15.0 ----71. 6 BR 3.0 79.5 Al 0.0 ----82.0 A2 0.0 ----84.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 NODE ANALYSIS DATA NODE TAG A3 A4 SRC ELEVATION (FT) 0.0 0.0 0. 0 NODE TYPE SOURCE PRESSURE (PSI) 89.7 92.1 92.6 DISCHARGE (GPM) 1229.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 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 -30.9 2.067 PL 8.00 PF 0 .1 1 18.0 7.5 16.8 30.9 3.0 120 FTG PE 0. 0 2 18.0 7.5 16.8 31. 0 0. 011 TL 8.00 PV Pipe: 2 -61.9 2.067 PL 8.00 PF 0.3 2 18.0 7.5 16.8 31. 0 5.9 120 FTG PE 0.0 3 18.0 7.5 17.1 31. 3 0.039 TL 8.00 PV Pipe: 3 -93.1 2.067 PL 8.00 PF 0.7 3 18.0 7.5 17 .1 31. 3 8.9 120 FTG PE 0.0 4 18.0 7. 5 17.8 31. 9 0.082 TL 8.00 PV Pipe: 4 -125.0 2.067 PL 8.00 PF 1.1 4 18.0 7.5 17.8 31. 9 12.0 120 FTG PE 0.0 5 18.0 7.5 18.9 32.9 0.142 TL 8.00 PV Pipe: 5 -157.9 2.067 PL 8.17 PF 1.8 5 18.0 7.5 18.9 32.9 15.1 120 FTG PE 0.0 6 18.0 7. 5 20.7 34.4 0.219 TL 8.17 PV Pipe: 6 -192.2 2.067 PL 4.17 PF 4.5 6 18.0 7.5 20.7 34.4 18.4 120 FTG T PE 0.0 7 18.0 0.0 25.2 0.0 0.315 TL 14.17 PV Pipe: 7 -31. 3 2.067 PL 1.50 PF 0.1 7 18.0 0.0 25.2 0.0 3.0 120 FTG T PE 0.0 8 18.0 7.5 25.3 38.0 0.011 TL 11.50 PV Pipe: 8 -69.3 2.067 PL 6.00 PF 0.3 8 18.0 7. 5 25.3 38.0 6.6 120 FTG PE 0.0 9 18.0 7.5 25.6 38.2 0.048 TL 6.00 PV Pipe: 9 -107.5 2.067 PL 5.83 PF 0.6 9 18.0 7.5 25.6 38.2 10.3 120 FTG PE 0.0 10 18.0 7.5 26.2 38.7 0.107 TL 5.83 PV Pipe: 10 -30.7 2.067 PL 8.00 PF 0.1 11 18.0 7.5 16.5 30.7 2.9 120 FTG PE 0.0 12 18.0 7.5 16.6 30.7 0.011 TL 8.00 PV Pipe: 11 -61.4 2.067 PL 8.00 PF 0.3 12 18.0 7.5 16.6 30.7 5.9 120 FTG PE 0.0 13 18.0 7. 5 16.9 31. 0 0.038 TL 8.00 PV Pipe: 12 -92. 4 2.067 PL 8.00 PF 0.6 13 18.0 7. 5 16.9 31. 0 8.8 120 FTG PE 0.0 14 18.0 7. 5 17. 5 31. 6 0.081 TL 8.00 PV Pipe: 13 -124.1 2.067 PL 8.00 PF 1.1 14 18.0 7.5 17.5 31. 6 11. 9 120 FTG PE 0.0 15 18.0 7. 5 18.7 32.6 0.140 TL 8.00 PV ··-·--·· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 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 -156.7 2.067 PL 8.17 PF 1.8 15 18.0 7.5 18.7 32.6 15.0 120 FTG PE 0.0 16 18.0 7.5 20.4 34.1 0.216 TL 8.17 PV Pipe: 15 -190.8 2.067 PL 4.17 PF 4.4 16 18.0 7.5 20.4 34.1 18.2 120 FTG T PE 0.0 17 18.0 0.0 24.8 0.0 0.310 TL 14.17 PV Pipe: 16 -16.5 2.067 PL 1.50 PF 0.0 17 18.0 0.0 24.8 0.0 1. 6 120 FTG T PE 0.0 18 18.0 7.5 24.9 37.6 0.003 TL 11. 50 PV Pipe: 17 -54.1 2.067 PL 6.00 PF 0.2 18 18.0 7.5 24.9 37.6 5.2 120 FTG PE 0.0 19 18.0 7.5 25.0 37.8 0.030 TL 6.00 PV Pipe: 18 -91. 9 2.067 PL 5.83 PF 1.3 19 18.0 7.5 25.0 37.8 8.8 120 FTG T PE 0.0 20 18.0 7.5 26.3 38.7 0.080 TL 15.83 PV Pipe: 19 -30.9 2.067 PL 8.00 PF 0.1 21 18.0 7.5 16.7 30.9 3.0 120 FTG PE 0.0 22 18.0 7. 5 16.8 30.9 0.011 TL 8.00 PV Pipe: 20 -61. 8 2.067 PL 8.00 PF 0.3 22 18.0 7.5 16.8 30.9 5.9 120 FTG PE 0.0 23 18.0 7.5 17.1 31. 2 0.039 TL 8.00 PV Pipe: 21 -93.0 2.067 PL 8.00 PF 0.7 23 18.0 7.5 17.1 31. 2 8.9 120 FTG PE 0.0 24 18.0 7.5 17. 8 31. 8 0.082 TL 8.00 PV Pipe: 22 -124.9 2.067 PL 8.00 PF 1.1 24 18.0 7.5 17.8 31. 8 11. 9 120 FTG PE 0.0 25 18.0 7.5 18.9 32.8 0.142 TL 8.00 PV Pipe: 23 -157.7 2.067 PL 8.17 PF 1.8 25 18.0 7.5 18.9 32.8 15.1 120 FTG PE 0.0 26 18.0 7.5 20.7 34.3 0.218 TL 8.17 PV Pipe: 24 -192.0 2.067 PL 4.17 PF 4.5 26 18.0 7.5 20.7 34.3 18.4 120 FTG T PE 0.0 27 18.0 0.0 25.1 0.0 0.314 TL 14.17 PV Pipe: 25 -15.3 2.067 PL 1.50 PF 0.0 27 18.0 0.0 25.1 0.0 1.5 120 FTG T PE 0.0 28 18.0 7.5 25.2 37.9 0.003 TL 11. 50 PV Pipe: 26 -53.1 2.067 PL 6.00 PF 0.2 28 18.0 7.5 25.2 37.9 5.1 120 FTG PE 0.0 29 18.0 7.5 25.3 38.0 0.029 TL 6.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 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 -91.1 2.067 PL 5.83 PF 1.3 29 18.0 7.5 25.3 38.0 8.7 120 FTG T PE 0.0 30 18.0 7.5 26.6 38.9 0.079 TL 15.83 PV Pipe: 28 -31. 3 2.067 PL 8.00 PF 0.1 31 18.0 7.5 17.2 31. 3 3.0 120 FTG PE 0. 0 32 18.0 7.5 17.2 31. 4 0.011 TL 8.00 PV Pipe: 29 -62.6 2.067 PL 8.00 PF 0.3 32 18.0 7.5 17.2 31. 4 6.0 120 FTG PE 0.0 33 18.0 7.5 17.6 31. 6 0.040 TL 8.00 PV Pipe: 30 -94.3 2.067 PL 8.00 PF 0.7 33 18.0 7.5 17.6 31. 6 9.0 120 FTG PE 0.0 34 18.0 7.5 18.2 32.2 0.084 TL 8.00 PV Pipe: 31 -126.5 2.067 PL 8.00 PF 1.2 34 18.0 7. 5 18.2 32.2 12.1 120 FTG PE 0.0 35 18.0 7.5 19.4 33.2 0.145 TL 8.00 PV Pipe: 32 -159.7 2.067 PL 8.17 PF 1.8 35 18.0 7.5 19.4 33.2 15.3 120 FTG PE 0.0 36 18.0 7.5 21. 2 34.8 0.223 TL 8.17 PV Pipe: 33 -194.5 2.067 PL 4.17 PF 4.6 36 18.0 7.5 21.2 34.8 18.6 120 FTG T PE 0.0 37 18.0 0.0 25.8 0.0 0.322 TL 14.17 PV Pipe: 34 -12.1 2.067 PL 1. 50 PF 0.0 37 18.0 0.0 25.8 0.0 1.2 120 FTG T PE 0.0 38 18.0 7.5 25.8 38.3 0.002 TL 11. 50 PV Pipe: 35 -50.4 2.067 PL 6.00 PF 0.2 38 18.0 7.5 25.8 38.3 4.8 120 FTG PE 0.0 39 18.0 7.5 26.0 38.5 0.026 TL 6.00 PV Pipe: 36 -88.9 2.067 PL 5.83 PF 1.2 39 18.0 7.5 26.0 38.5 8.5 120 FTG T PE 0.0 40 18.0 7.5 27.2 39.3 0.076 TL 15.83 PV Pipe: 37 -146.2 4.026 PL 11. 50 PF 0.1 10 18.0 7.5 26.2 38.7 3.7 120 FTG PE 0.0 20 18.0 7.5 26.3 38.7 0.007 TL 11. 50 PV Pipe: 38 -276.8 4.026 PL 11. 50 PF 0.3 20 18.0 7. 5 26.3 38.7 7.0 120 FTG PE 0.0 30 18.0 7.5 26.6 38.9 0.024 TL 11. 50 PV Pipe: 39 -406.9 4.026 PL 11. 50 PF 0.6 30 18.0 7.5 26.6 38.9 10.3 120 FTG PE 0.0 40 18.0 7.5 27.2 39.3 0.049 TL 11. 50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 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: 40 0.0 2.067 PL 8.00 PF 0.0 41 18.0 0.0 28 .1 0.0 0.0 120 FTG PE 0.0 42 18.0 0.0 28.1 0.0 0.000 TL 8.00 PV Pipe: 41 0.0 2.067 PL 8.00 PF 0.0 42 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 43 18.0 0.0 28 .1 0.0 0.000 TL 8.00 PV Pipe: 42 0.0 2.067 PL 8.00 PF 0.0 43 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 44 18.0 0.0 28.1 0.0 0.000 TL 8.00 PV Pipe: 43 0.0 2.067 PL 7.42 PF 0.0 44 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 45 18.0 0.0 28.1 0.0 0.000 TL 7.42 PV Pipe: 44 0.0 2.067 PL 7.34 PF 0.0 45 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 46 18.0 0.0 28.1 0.0 0.000 TL 7.34 PV Pipe: 45 0.0 2.067 PL 8.00 PF 0.0 46 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 47 18.0 0.0 28.1 0.0 0.000 TL 8.00 PV Pipe: 46 0.0 2.067 PL 8.00 PF 0.0 47 18.0 0.0 28.1 0.0 0.0 120 FTG PE 0.0 48 18.0 0.0 28.1 0.0 0.000 TL 8.00 PV Pipe: 47 0.0 2.067 PL 6.71 PF 0.0 48 18.0 0.0 28 .1 0.0 0.0 120 FTG PE 0.0 49 18.0 0.0 28.1 0.0 0.000 TL 6.71 PV Pipe: 48 0.0 2.067 PL 17. 86 PF 0.0 49 18.0 0.0 28.1 0. 0 0.0 120 FTG T PE 0.0 50 18.0 0.0 28.1 0.0 0.000 TL 27.86 PV Pipe: 49 0.0 2.067 PL 8.00 PF 0.0 51 18.0 0.0 29.1 0. 0 0.0 120 FTG PE 0.0 52 18.0 0. 0 29.1 0.0 0.000 TL 8.00 PV Pipe: 50 0.0 2.067 PL 8.00 PF 0.0 52 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 53 18.0 0.0 29.1 0.0 0.000 TL 8.00 PV Pipe: 51 0.0 2.067 PL 8.00 PF 0.0 53 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 54 18.0 0.0 29.l 0.0 0.000 TL 8.00 PV Pipe: 52 0.0 2.067 PL 7.42 PF 0.0 54 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 55 18.0 0.0 29.1 0.0 0.000 TL 7.42 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 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: 53 0.0 2.067 PL 7.34 PF 0.0 55 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 56 18.0 0.0 29.1 0.0 0.000 TL 7.34 PV Pipe: 54 0.0 2.067 PL 8.00 PF 0.0 56 18.0 0.0 29.1 0. 0 0.0 120 FTG PE 0.0 57 18.0 0.0 29.1 0.0 0.000 TL 8.00 PV Pipe: 55 0.0 2.067 PL 8.00 PF 0.0 57 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 58 18.0 0.0 29.1 0.0 0.000 TL 8.00 PV Pipe: 56 0.0 2.067 PL 6.71 PF 0.0 58 18.0 0.0 29.1 0.0 0.0 120 FTG PE 0.0 59 18.0 0.0 29.1 0.0 0.000 TL 6.71 PV Pipe: 57 0.0 2.067 PL 17.86 PF 0.0 59 18.0 0.0 29.1 0.0 0.0 120 FTG T PE 0.0 60 18.0 0.0 29.1 0. 0 0.000 TL 27.86 PV Pipe: 58 0.0 2.067 PL 8.00 PF 0.0 61 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 62 18.0 0.0 30.1 0.0 0.000 TL 8.00 PV Pipe: 59 0.0 2.067 PL 8.00 PF 0.0 62 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 63 18.0 0.0 30.1 0.0 0.000 TL 8.00 PV Pipe: 60 0.0 2.067 PL 8.00 PF 0.0 63 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 64 18.0 0.0 30.1 0.0 0.000 TL 8.00 PV Pipe: 61 0.0 2.067 PL 7.42 PF 0.0 64 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 65 18.0 0.0 30.1 0.0 0.000 TL 7.42 PV Pipe: 62 0.0 2.067 PL 7.34 PF 0.0 65 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 66 18.0 0.0 30.1 0. 0 0.000 TL 7.34 PV Pipe: 63 0.0 2.067 PL 8.00 PF 0.0 66 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 67 18.0 0.0 30.1 0.0 0.000 TL 8.00 PV Pipe: 64 0.0 2.067 PL 8.00 PF 0.0 67 18.0 0.0 30.1 0.0 0.0 120 FTG PE 0.0 68 18.0 0.0 30.1 0.0 0.000 TL 8.00 PV Pipe: 65 0.0 2.067 PL 6.71 PF 0.0 68 18.0 0.0 30.1 0. 0 0.0 120 FTG PE 0.0 69 18.0 0.0 30.1 0.0 0.000 TL 6.71 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33/3000 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: 66 0.0 2.067 PL 17.86 PF 0.0 69 18.0 0.0 30.1 0. 0 0.0 120 FTG T PE 0.0 70 18.0 0.0 30.1 0.0 0.000 TL 27.86 PV Pipe: 67 0.0 2.067 PL 8.00 PF 0.0 71 18.0 0.0 31. 0 0. 0 0.0 120 FTG PE 0.0 72 18.0 0.0 31. 0 0.0 0.000 TL 8.00 PV Pipe: 68 0.0 2.067 PL 8.00 PF 0.0 72 18.0 0.0 31. 0 0. 0 0.0 120 FTG PE 0.0 73 18.0 0.0 31. 0 0. 0 0.000 TL 8.00 PV Pipe: 69 0.0 2.067 PL 8.00 PF 0.0 73 18.0 0.0 31. 0 0.0 0.0 120 FTG PE 0.0 74 18.0 0.0 31. 0 0.0 0.000 TL 8.00 PV Pipe: 70 0.0 2.067 PL 7.42 PF 0.0 74 18.0 0.0 31. 0 0.0 0.0 120 FTG PE 0.0 75 18.0 0.0 31. 0 0.0 0.000 TL 7.42 PV Pipe: 71 0.0 2.067 PL 7.34 PF 0.0 75 18.0 0.0 31. 0 0.0 0.0 120 FTG PE 0.0 76 18.0 0.0 31. 0 0.0 0.000 TL 7.34 PV Pipe: 72 0.0 2.067 PL 8.00 PF 0.0 76 18.0 0.0 31. 0 0.0 0.0 120 FTG PE 0.0 77 18.0 0.0 31. 0 0.0 0.000 TL 8.00 PV Pipe: 73 0.0 2.067 PL 8.00 PF 0.0 77 18.0 0.0 31. 0 0. 0 0.0 120 FTG PE 0.0 78 18.0 0.0 31. 0 0.0 0.000 TL 8.00 PV Pipe: 74 0.0 2.067 PL 6.71 PF 0.0 78 18.0 0.0 31. 0 0.0 0.0 120 FTG PE 0.0 79 18.0 0.0 31. 0 0.0 0.000 TL 6.71 PV Pipe: 75 0.0 2.067 PL 17.86 PF 0.0 79 18.0 0.0 31. 0 0. 0 0.0 120 FTG T PE 0.0 80 18.0 0.0 31. 0 0. 0 0.000 TL 27.86 PV Pipe: 76 -535.1 4.026 PL 11. 67 PF ·o. 9 40 18.0 7.5 27.2 39.3 13. 5 120 FTG PE 0.0 50 18.0 0.0 28.1 0.0 0.081 TL 11. 67 PV Pipe: 77 -535.1 4.026 PL 12.00 PF 1.0 50 18.0 0.0 28.1 0.0 13 .5 120 FTG PE 0.0 60 18.0 0.0 29.1 0.0 0.081 TL 12.00 PV Pipe: 78 -535.1 4.026 PL 12.00 PF 1.0 60 18.0 0.0 29.1 0.0 13. 5 120 FTG PE 0.0 70 18.0 0.0 30.1 0.0 0.081 TL 12.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 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: 79 -535.1 4.026 PL 12.00 PF 1.0 70 18.0 0.0 30.1 0.0 13.5 120 FTG PE 0.0 80 18.0 0.0 31. 0 0.0 0.081 TL 12.00 PV Pipe: 80 -1229.6 4.026 PL 77.50 PF 39.3 80 18.0 0.0 31. 0 0.0 31. 0 120 FTG TL PE 1. 3 TR 15.0 0.0 71. 6 0.0 0.379 TL 103.50 PV Pipe: 81 -1229.6 6.065 PL 12.00 PF 2.7 TR 15.0 0.0 71. 6 0.0 13.7 120 FTG LGA PE 5.2 BR 3.0 0.0 79.5 0.0 0.052 TL 52.00 PV Pipe: 82 -1229.6 6.280 PL 10.00 PF 1.3 BR 3.0 0.0 79.5 0.0 12.7 140 FTG 2L PE 1. 3 Al 0.0 0.0 82.0 0.0 0.033 TL 38.36 PV Pipe: 83 -1229.6 6.080 PL 65.00 PF 2.7 Al 0.0 0.0 82.0 0.0 13. 6 150 FTG L PE 0.0 A2 0.0 0.0 84.7 0.0 0.034 TL 78.76 PV Pipe: 84 FIXED PRESSURE LOSS DEVICE A3 0.0 0.0 89.7 0.0 5.0 psi, 1229.6 gpm A2 0.0 0.0 84.7 0.0 Pipe: 85 -1229.6 6.080 PL 21.00 PF 2.4 A3 0.0 0.0 89.7 0.0 13. 6 150 FTG TG PE 0.0 A4 0.0 0.0 92 .1 0.0 0.034 TL 71. 47 PV Pipe: 86 -1229.6 9.790 PL 73.00 PF 0.5 A4 0.0 0.0 92.1 0.0 5.2 150 FTG TG PE 0.0 SRC 0.0 SRCE 92.6 (N/A) 0.003 TL 143.04 PV Pipe: 87 -160.9 2.067 PL 3.00 PF 2.9 7 18.0 0.0 25.2 0.0 15.4 120 FTG T PE 0.0 81 18.0 0.0 28.1 0.0 0.227 TL 13. 00 PV Pipe: 88 -174.3 2.067 PL 3.00 PF 3.4 17 18.0 0.0 24.8 0.0 16.7 120 FTG T PE 0.0 82 18.0 0.0 28.2 0.0 0.263 TL 13.00 PV Pipe: 89 -176.7 2.067 PL 3.00 PF 3. 5 27 18.0 0.0 25.1 0.0 16.9 120 FTG T PE 0.0 83 18.0 0.0 28.6 0.0 0.269 TL 13.00 PV Pipe: 90 -182.5 2.067 PL 3.00 PF 3. 7 37 18.0 0.0 25.8 0.0 17.4 120 FTG T PE 0.0 84 18.0 0.0 29.5 0.0 0.286 TL 13.00 PV Pipe: 91 -160.9 4.026 PL 11. 50 PF 0.1 81 18.0 0.0 28.1 0.0 4.1 120 FTG PE 0.0 82 18.0 0.0 28.2 0. 0 0.009 TL 11. 50 PV ·••<--•-·" SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: . 33 /3000 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 92 -335.3 4.026 PL 11. 50 PF 0.4 82 18.0 0.0 28.2 0.0 8.4 120 FTG PE 0.0 83 18.0 0.0 28.6 0.0 0.034 TL 11. 50 PV Pipe: 93 -512.0 4.026 PL 11. 50 PF 0.9 83 18.0 0. 0 28.6 0.0 12.9 120 FTG PE 0.0 84 18.0 0.0 29.5 0.0 0.075 TL 11. 50 PV Pipe: 94 -694.5 4.026 PL 11. 67 PF 1. 5 84 18.0 0.0 29.5 0.0 17.5 120 FTG PE 0. 0 80 18.0 0.0 31. 0 0.0 0 .132 TL 11. 67 PV NOTES: (1) Calculations were performed by the HASS 7.4 computer program under license no. 16031158 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 0.002 gpm and a maximum imbalance at any node of 0.182 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 31.0 ft/sec at pipe 80. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A Diameter (in) MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee F 45 2.067 5.00 10.00 3.00 11. 00 6.00 1.00 10.00 10.00 10.00 2.00 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 10.00 20.00 4.00 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 19.00 30.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 PAGE: D MATERIAL: DIRON HWC: 140 Diameter (in) 6.280 PAGE: E Diameter (in) 6.080 9.790 E Ell 22.06 Equivalent Fitting Lengths in Feet T L C B G N Tee LngEll ChkVlv BfyVlv GatVlv NPTee 47.28 14.18 50.43 15.76 4.73 47.28 MATERIAL: PVC150 HWC: 150 E Ell 21. 41 28.02 Equivalent Fitting Lengths in Feet T L C B G Tee LngEll ChkVlv BfyVlv GatVlv 45.88 13.76 48.94 15.29 4.59 63.67 20.38 70.04 24.20 6.37 N NPTee 45.88 63.67 F 45 11. 03 F 45 10.71 11.46 140.0 Gll2.0 A u G E p R 84. 0 E s s u R E 56.0 ( p s i ) 28.0 0.0 -14.7 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 132.30 psi Resid: 128.70 psi Flow: 1683.0 gpm 1200 1 ~ 2 ~ 1400 FLOW (GPM) LEGEND l Available pressure 128.51 psi@ 1729.6 gprn Required pressure 92.55 psi@ 1729.6 gpm 2 1600 1800 '-l tl O:<> to >-3 t'l >-3 •• H >-3 "' t" ...._ t'l f-' .. -.J ...._ n"' :<> 0 :,, 0 t" /fl to :<> tl 0 en :<> "' :,; :,, en H z to :,; C: t" H t'l t" :,, tl H en z ~ Gl en cl :<> t'l :s: :<> :r: ~ :,, tl t'l ~ :<> :<> t" H n w ~ w ...._ w t" 0 ~ 0 en 0 H n en / ~ en en -.J ,,,. / -.J ,,,. V1 :<> I "' :<, Pl <Q en ro 0 "l f-' w j 2000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 WATER SUPPLY CURVE 144+ I I I 132*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 128.7 psi@ 1683 gpm-> * O I Flow Test Point I 120+ I I I 108+ I I I P 96+ R I E I s I S 84+ u I R I E I 72+ I p I s I I 60+ l I I I 48+ I I I 36+ I I I============================== 24+ LEGEND I I X = Required Water Supply I 92.55 psi@ 1729.6 gpm 12+ I O = Available Water Supply I 128.51 psi@ 1729.6 gpm I • X 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 6/17/2003 C:\HASS74\745A-A.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA A: .33/3000 Utility Report: Equivalent K-Factor Calculator Node Sprinkler Pres. Dia. Name K-Factor (psi) (in) X 8.00 7.00 1.049 Pipe Ftgs. Len. (ft) 1.00 T Total H-W Equivalent Len. (ft) coef. K-factor 6.00 120.00 7.55 HYDRAULIC CALCULATIONS FOR CARLSBAD OAKS BUILDING A AREAB PARCEL 3, LOKER AVENUE CARLSBAD, CALIFORNIA GUFP JOB #745 ► OCCUPANCY CLASSIFICATION: EX. HAZ . ► DENSITY: . 33GPM/SQ.FT. ► REQUIRED AREA OF APPLICATION: 3000 SQ.FT. ► COVERAGE PER SPRINKLER: 96 SQ. FT. ► NUMBER OF SPRINKLERS FLOWING: ► TOTAL SPRINKLER FLOW REQUIRED: 1213.8 GPM ► TOTAL WATER REQUIRED {INCLUDING HOSE): 1713.8 GPM ► DEMAND AT BASE OF RISER: 1213.8GPM@106.6PSI ► SPRINKLER ORIFICE SIZE: 3/4" {K-FACTOR =8.0) ► CALCULATIONS BY: ROBERT MAHONEY ► AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE ► COMMENTS: WATER AVAILABLE FOR DESIGN 90% OF CITY SUPPLY Ca1cu1at1on by has~ cornputH1· u1ogran1 HHS Svswm::i Inc Cinneral Underground Fire 1Jmtect1011. inc 11 1003115b 3930 EAST CORONADO STREET+ ANAHEIM, CA 92807 + PHONE 714-632-8646 FAX 714-632-0579 CONTRACTOR'S LICENSE NO. 485748 C-16/C-34 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: .33/3000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 132.3 128.7 1683.0 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 ELEVATION NODE TYPE (FT) 1 18.0 2 18.0 3 18.0 4 18.0 5 18.0 6 18.0 7 18.0 8 18.0 9 18.0 10 18.0 11 18.0 12 18.0 13 18.0 14 18.0 15 18.0 16 18.0 17 18.0 18 18.0 19 18.0 20 18.0 21 18.0 22 18.0 23 18.0 24 18.0 25 18.0 26 18.0 27 18.0 28 18.0 29 18.0 30 18.0 31 18.0 32 18.0 33 18.0 34 18.0 35 18.0 AVAIL. PRESS. @ (PSI) 128.6 1713. 8 GPM 500.0 GPM 0.0 GPM 1213. 8 GPM PRESSURE (PSI) 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 54.5 TOTAL REQ'D DEMAND PRESS. (GPM) (PSI) 1713. 8 119. 6 DISCHARGE (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 18.0 ----54.5 37 18.0 ----54.5 38 18.0 ----54.5 39 18.0 ----54.5 40 18.0 ----54.5 41 18.0 K; 7.55 18.0 32.0 42 18.0 K; 7.55 18.1 32.1 43 18.0 K; 7.55 18.4 32.4 44 18.0 K; 7.55 19.1 33.0 45 18.0 K; 7.55 20.2 34.0 46 18.0 K; 7.55 21. 9 35.4 47 18.0 K; 7.55 24.6 37.5 48 18.0 K; 7.55 28.3 40.2 49 18.0 K; 7.55 33.2 43.5 50 18.0 ----54.5 51 18.0 K; 7.55 18.1 32.1 52 18.0 K; 7.55 18.2 32.2 53 18.0 K; 7.55 18.5 32.5 54 18.0 K; 7.55 19.2 33.1 55 18.0 K; 7.55 20.4 34.1 56 18.0 K; 7.55 22.1 35.5 57 18.0 K; 7.55 24.8 37.6 58 18.0 K; 7.55 28.5 40.3 59 18.0 K; 7.55 33.5 43.7 60 18.0 ----54.9 61 18.0 K; 7.55 18.6 32.6 62 18.0 K; 7.55 18.7 32.6 63 18.0 K; 7.55 19.0 32.9 64 18.0 K; 7.55 19.8 33.6 65 18.0 K; 7.55 20.9 34.5 66 18.0 K; 7.55 22.7 36.0 67 18.0 K; 7.55 25.4 38.1 68 18.0 K; 7.55 29.2 40.8 69 18.0 K; 7.55 34.3 44.2 70 18.0 ----56.3 71 18.0 K; 7.55 27.9 39.9 72 18.0 K; 7.55 28.0 40.0 73 18.0 K; 7.55 28.5 40.3 74 18.0 K; 7.55 29.6 41.1 75 18.0 K; 7.55 31. 3 42.2 76 18.0 K; 7.55 33.8 43.9 77 18.0 37.8 78 18.0 ----41. 8 79 18.0 ----45.2 80 18.0 59.2 TR 15.0 ----98.8 BR 3.0 ----106.6 Al 0. 0 ----109.1 A2 0.0 ----111. 7 A3 0.0 116. 7 A4 0.0 119 .1 SRC 0.0 SOURCE 119. 6 1213. 8 -----~··- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 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 0.0 2.067 PL 8.00 PF 0. 0 1 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 2 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 2 0.0 2.067 PL 8.00 PF 0.0 2 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 3 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 3 0.0 2.067 PL 8.00 PF 0.0 3 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0. 0 4 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 4 0.0 2.067 PL 8.00 PF 0.0 4 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 5 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 5 0.0 2.067 PL 8.17 PF 0.0 5 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 6 18.0 0.0 54.5 0.0 0.000 TL 8.17 PV Pipe: 6 0.0 2.067 PL 4.17 PF 0.0 6 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 9 18.0 0.0 54.5 0.0 0.000 TL 14.17 PV Pipe: 7 0.0 2.067 PL 4.50 PF 0.0 9 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 7 18.0 0.0 54.5 0.0 0.000 TL 14.50 PV Pipe: 8 0.0 2.067 PL 8.67 PF 0.0 7 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 8 18.0 0.0 54.5 0.0 0.000 TL 8.67 PV Pipe: 9 0.0 2.067 PL 3.00 PF 0.0 9 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 10 18.0 0.0 54.5 0.0 0.000 TL 13. 00 PV Pipe: 10 0.0 2.067 PL 8.00 PF 0.0 11 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 12 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 11 0.0 2.067 PL 8.00 PF 0.0 12 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 13 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 12 0.0 2.067 PL 8.00 PF 0.0 13 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 14 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 13 0.0 2.067 PL 8.00 PF 0.0 14 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 15 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 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 0.0 2.067 PL 8.17 PF 0.0 15 18.0 0.0 54.5 0. 0 0.0 120 FTG PE 0.0 16 18.0 0.0 54.5 0.0 0.000 TL 8.17 PV Pipe: 15 0.0 2.067 PL 4.17 PF 0.0 16 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 19 18.0 0.0 54.5 0. 0 0.000 TL 14.17 PV Pipe: 16 0.0 2.067 PL 4.50 PF 0.0 19 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 17 18.0 0.0 54.5 0.0 0.000 TL 14.50 PV Pipe: 17 0.0 2.067 PL 8.67 PF 0.0 17 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 18 18.0 0.0 54.5 0.0 0.000 TL 8.67 PV Pipe: 18 0.0 2.067 PL 3.00 PF 0. 0 19 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 20 18.0 0.0 54.5 0.0 0.000 TL 13. 00 PV Pipe: 19 0.0 2.067 PL 8.00 PF 0. 0 21 18.0 0.0 54.5 0. 0 0.0 120 FTG PE 0.0 22 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 20 0.0 2.067 PL 8.00 PF 0.0 22 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 23 18.0 0.0 54.5 0. 0 0.000 TL 8.00 PV Pipe: 21 0.0 2.067 PL 8.00 PF 0. 0 23 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0. 0 24 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 22 0.0 2.067 PL 8.00 PF 0.0 24 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 25 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 23 0.0 2.067 PL 8.17 PF 0.0 25 18.0 0.0 54.5 0. 0 0.0 120 FTG PE 0.0 26 18.0 0. 0 54.5 0. 0 0.000 TL 8.17 PV Pipe: 24 0.0 2.067 PL 4.17 PF 0.0 26 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 29 18.0 0.0 54.5 0.0 0.000 TL 14.17 PV Pipe: 25 0.0 2.067 PL 4.50 PF 0.0 29 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 27 18.0 0.0 54.5 0.0 0.000 TL 14.50 PV Pipe: 26 0.0 2.067 PL 8.67 PF 0. 0 27 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0. 0 28 18.0 0.0 54.5 0. 0 0.000 TL 8.67 PV ···---·~--,--,· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: .33/3000 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 0.0 2.067 PL 3.00 PF 0.0 29 18.0 0. 0 54.5 0.0 0.0 120 FTG T PE 0.0 30 18.0 0. 0 54.5 0.0 0.000 TL 13. 00 PV Pipe: 28 0.0 2.067 PL 8.00 PF 0.0 31 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 32 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 29 0.0 2.067 PL 8.00 PF 0.0 32 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 33 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 2.067 PL 8.00 PF 0.0 33 18.0 0.0 54.5 0. 0 0.0 120 FTG PE 0.0 34 18.0 0.0 54.5 0. 0 0.000 TL 8.00 PV Pipe: 31 0.0 2.067 PL 8.00 PF 0. 0 34 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 35 18.0 0.0 54.5 0.0 0.000 TL 8.00 PV Pipe: 32 0.0 2.067 PL 8.17 PF 0.0 35 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 36 18.0 0.0 54.5 0.0 0.000 TL 8.17 PV Pipe: 33 0.0 2.067 PL 4.17 PF 0.0 36 18.0 0.0 54.5 0. 0 0.0 120 FTG T PE 0.0 39 18.0 0.0 54.5 0.0 0.000 TL 14.17 PV Pipe: 34 0.0 2.067 PL 4.50 PF 0.0 39 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 37 18.0 0.0 54.5 0.0 0.000 TL 14.50 PV Pipe: 35 0.0 2.067 PL 8.67 PF 0.0 37 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 38 18.0 0.0 54.5 0. 0 0.000 TL 8.67 PV Pipe: 36 0.0 2.067 PL 3.00 PF 0.0 39 18.0 0.0 54.5 0.0 0.0 120 FTG T PE 0.0 40 18.0 0. 0 54.5 0.0 0.000 TL 13. 00 PV Pipe: 37 0.0 4.026 PL 11. 50 PF 0.0 10 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 20 18.0 0.0 54.5 0. 0 0.000 TL 11. 50 PV Pipe: 38 0.0 4.026 PL 11. 50 PF 0.0 20 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 30 18.0 0.0 54.5 0.0 0.000 TL 11. 50 PV Pipe: 39 0.0 4.026 PL 11. 50 PF 0.0 30 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 40 18.0 0.0 54.5 0. 0 0.000 TL 11. 50 PV -·--··· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 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: 40 -32.0 2.067 PL 8.00 PF 0.1 41 18.0 7.5 18.0 32.0 3.1 120 FTG PE 0.0 42 18.0 7.5 18.1 32.1 0. 011 TL 8.00 PV Pipe: 41 -64.1 2.067 PL 8.00 PF 0.3 42 18.0 7.5 18.1 32.1 6.1 120 FTG PE 0.0 43 18.0 7.5 18.4 32.4 0.041 TL 8.00 PV Pipe: 42 -96. 5 2.067 PL 8.00 PF 0.7 43 18.0 7.5 18.4 32.4 9.2 120 FTG PE 0.0 44 18.0 7.5 19.1 33.0 0.088 TL 8.00 PV Pipe: 43 -129.5 2.067 PL 7.42 PF 1.1 44 18.0 7.5 19.1 33.0 12.4 120 FTG PE 0.0 45 18.0 7.5 20.2 34.0 0.152 TL 7.42 PV Pipe: 44 -163.5 2.067 PL 7.34 PF 1. 7 45 18.0 7.5 20.2 34.0 15.6 120 FTG PE 0.0 46 18.0 7.5 21. 9 35.4 0.233 TL 7.34 PV Pipe: 45 -198.8 2.067 PL 8.00 PF 2.7 46 18.0 7.5 21. 9 35.4 19.0 120 FTG PE 0.0 47 18.0 7.5 24.6 37.5 0.335 TL 8.00 PV Pipe: 46 -236.3 2.067 PL 8.00 PF 3.7 47 18.0 7.5 24.6 37.5 22.6 120 FTG PE 0.0 48 18.0 7.5 28.3 40.2 0.461 TL 8.00 PV Pipe: 47 -276.5 2.067 PL 8.00 PF 4.9 48 18.0 7.5 28.3 40.2 26.4 120 FTG PE 0.0 49 18.0 7.5 33.2 43.5 0.616 TL 8.00 PV Pipe: 48 -320.0 2.067 PL 16.34 PF 21. 3 49 18.0 7.5 33.2 43.5 30.6 120 FTG T PE 0.0 50 18.0 0.0 54.5 0.0 0.808 TL 26.34 PV Pipe: 49 -32.1 2.067 PL 8.00 PF 0.1 51 18.0 7. 5 18.1 32.1 3.1 120 FTG PE 0.0 52 18.0 7.5 18.2 32.2 0.011 TL 8.00 PV Pipe: 50 -64.3 2.067 PL 8.00 PF 0.3 52 18.0 7.5 18.2 32.2 6.2 120 FTG PE 0.0 53 18.0 7.5 18.5 32.5 0.042 TL 8.00 PV Pipe: 51 -96.9 2.067 PL 8.00 PF 0.7 53 18.0 7. 5 18.5 32.5 9.3 120 FTG PE 0.0 54 18.0 7.5 19.2 33.1 0.089 TL 8.00 PV Pipe: 52 -130. 0 2.067 PL 7.42 PF 1.1 54 18.0 7.5 19.2 33.1 12.4 120 FTG PE 0.0 55 18.0 7.5 20.4 34.1 0.153 TL 7.42 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 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: 53 -164.1 2.067 PL 7.34 PF 1. 7 55 18.0 7.5 20.4 34.1 15.7 120 FTG PE 0. 0 56 18.0 7.5 22.1 35.5 0.235 TL 7.34 PV Pipe: 54 -199.6 2.067 PL 8.00 PF 2.7 56 18.0 7.5 22.1 35.5 19.1 120 FTG PE 0.0 57 18.0 7.5 24.8 37.6 0.337 TL 8.00 PV Pipe: 55 -237.1 2.067 PL 8.00 PF 3. 7 57 18.0 7.5 24.8 37.6 22.7 120 FTG PE 0.0 58 18.0 7.5 28.5 40.3 0.464 TL 8.00 PV Pipe: 56 -277.5 2.067 PL 8.00 PF 5. 0 58 18.0 7.5 28.5 40.3 26.5 120 FTG PE 0.0 59 18.0 7.5 33.5 43.7 0.621 TL 8.00 PV Pipe: 57 -321.1 2.067 PL 16.34 PF 21. 4 59 18.0 7.5 33.5 43.7 30.7 120 FTG T PE 0.0 60 18.0 0.0 54.9 0.0 0. 813 TL 26.34 PV Pipe: 58 -32.6 2.067 PL 8.00 PF 0.1 61 18.0 7.5 18.6 32.6 3.1 120 FTG PE 0.0 62 18.0 7. 5 18.7 32.6 0.012 TL 8.00 PV Pipe: 59 -65.2 2.067 PL 8.00 PF 0.3 62 18.0 7.5 18.7 32.6 6.2 120 FTG PE 0.0 63 18.0 7.5 19.0 32.9 0.043 TL 8.00 PV Pipe: 60 -98.1 2.067 PL 8.00 PF 0.7 63 18.0 7.5 19.0 32.9 9.4 120 FTG PE 0.0 64 18.0 7.5 19.8 33.6 0.091 TL 8.00 PV Pipe: 61 -131. 7 2.067 PL 7.42 PF 1. 2 64 18.0 7.5 19.8 33.6 12.6 120 FTG PE 0.0 65 18.0 7.5 20.9 34.5 0.156 TL 7.42 PV Pipe: 62 -166.2 2.067 PL 7.34 PF 1. 8 65 18.0 7.5 20.9 34.5 15.9 120 FTG PE 0. 0 66 18.0 7.5 22.7 36.0 0.240 TL 7.34 PV Pipe: 63 -202.2 2.067 PL 8.00 PF 2.8 66 18.0 7.5 22.7 36.0 19.3 120 FTG PE 0.0 67 18.0 7.5 25.4 38.1 0.345 TL 8.00 PV Pipe: 64 -240.2 2.067 PL 8.00 PF 3.8 67 18.0 7. 5 25.4 38.1 23.0 120 FTG PE 0.0 68 18.0 7.5 29.2 40.8 0.475 TL 8.00 PV Pipe: 65 -2 81.1 2.067 PL 8.00 PF 5.1 68 18.0 7.5 29.2 40.8 26.9 120 FTG PE 0. 0 69 18.0 7.5 34.3 44.2 0. 636 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: . 33/3000 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (Kl (PSI) (GPM) FL/FT (PSI) Pipe: 66 -325.3 2.067 PL 16.34 PF 21. 9 69 18.0 7.5 34.3 44.2 31.1 120 FTG T PE 0.0 70 18.0 0.0 56.3 0.0 0.833 TL 26.34 PV Pipe: 67 -39.9 2.067 PL 8.00 PF 0 .1 71 18.0 7.5 27.9 39.9 3.8 120 FTG PE 0.0 72 18.0 7.5 28.0 40.0 0.017 TL 8.00 PV Pipe: 68 -79.8 2.067 PL 8.00 PF 0.5 72 18.0 7.5 28.0 40.0 7.6 120 FTG PE 0.0 73 18.0 7.5 28.5 40.3 0.062 TL 8.00 PV Pipe: 69 -120.1 2.067 PL 8.00 PF 1.1 73 18.0 7.5 28.5 40.3 11. 5 120 FTG PE 0.0 74 18.0 7.5 29.6 41.1 0 .132 TL 8.00 PV Pipe: 70 -161.2 2.067 PL 7.42 PF 1. 7 74 18.0 7.5 29.6 41.1 15.4 120 FTG PE 0. 0 75 18.0 7.5 31.3 42.2 0.227 TL 7.42 PV Pipe: 71 -203.4 2.067 PL 7.34 PF 2.6 75 18.0 7.5 31. 3 42.2 19.4 120 FTG PE 0.0 76 18.0 7.5 33.8 43.9 0.349 TL 7.34 PV Pipe: 72 -247.3 2.067 PL 8.00 PF 4.0 76 18.0 7.5 33.8 43.9 23.6 120 FTG PE 0.0 77 18.0 0.0 37.8 0.0 0.502 TL 8.00 PV Pipe: 73 -247.3 2.067 PL 8.00 PF 4.0 77 18.0 0.0 37.8 0.0 23.6 120 FTG PE 0.0 78 18.0 0.0 41. 8 0.0 0.502 TL 8.00 PV Pipe: 74 -247.3 2.067 PL 6.71 PF 3. 4 78 18.0 0.0 41. 8 0.0 23.6 120 FTG PE 0.0 79 18.0 0.0 45.2 0.0 0.502 TL 6.71 PV Pipe: 75 -247.3 2.067 PL 17.86 PF 14.0 79 18.0 0.0 45.2 0.0 23.6 120 FTG T PE 0. 0 80 18.0 0.0 59.2 0.0 0.502 TL 27.86 PV Pipe: 76 0.0 4.026 PL 11. 67 PF 0.0 40 18.0 0.0 54.5 0.0 0.0 120 FTG PE 0.0 50 18.0 0.0 54.5 0.0 0.000 TL 11. 67 PV Pipe: 77 -320.0 4.026 PL 12.00 PF 0.4 50 18.0 0.0 54.5 0.0 8.1 120 FTG PE 0.0 60 18.0 0.0 54.9 0.0 0.031 TL 12.00 PV Pipe: 78 -641.1 4.026 PL 12.00 PF 1. 4 60 18.0 0.0 54.9 0.0 16.2 120 FTG PE 0.0 70 18.0 0.0 56.3 0.0 0 .114 TL 12.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/17/2003 JOB TITLE: CARLSBAD PIPE TAG C:\HASS74\745A-B.SDF OAKS BUILDING A -AREA B: .33/3000 Q(GPM) DIA(IN) LENGTH PRESS. END NODES ELEV. (FT) NOZ. (K) PT (PSI) DISC. VEL(FPS) HW(C) (FT) (GPM) FL/FT SUM. (PSI) 70 80 Pipe: 79 18.0 18.0 0.0 0.0 56.3 59.2 -966.4 0.0 24.4 0. 0 4.026 PL 12.00 PF 120 FTG PE 0.243 TL 12.00 PV 2.9 0.0 80 TR Pipe: 80 18.0 15.0 0.0 0.0 59.2 98.8 -1213.7 0.0 30.6 0.0 4.026 PL 120 FTG 0.370 TL 77.50 TL 103.50 PF PE PV 38.3 1. 3 TR BR BR Al Al A2 A3 A2 A3 A4 A4 SRC Pipe: 81 15.0 3.0 Pipe: 82 3.0 0.0 Pipe: 83 0.0 0.0 Pipe: 84 0. 0 0.0 Pipe: 85 0.0 0.0 Pipe: 86 0. 0 0.0 0.0 98.8 0.0 106.6 0.0 0.0 106.6 109.1 0.0 109.1 0.0 111. 7 0.0 116. 7 0.0 111. 7 0.0 116.7 0.0 119.1 0.0 119.1 SRCE 119. 6 -1213.7 0.0 13.5 0.0 -1213.7 0.0 12.6 0.0 -1213.7 0.0 13.4 0.0 0.0 0.0 -1213.7 0.0 13.4 0.0 -1213. 8 0.0 5.2 (N/A) 6.065 PL 12.00 PF 120 FTG LGA PE 0.050 TL 52.00 PV 6.280 PL 140 FTG 0.032 TL 10.00 2L 38.36 PF PE PV 6.080 PL 65.00 PF 150 FTG L PE 0.033 TL 78.76 PV FIXED PRESSURE LOSS DEVICE 5.0 psi, 1213.7 gpm 6.080 PL 21.00 PF 150 FTG TG PE 0.033 TL 71.47 PV 9.790 PL 150 FTG 0.003 TL 73.00 TG 143.04 PF PE PV NOTES: (1) Calculations were performed by the HASS 7.4 computer program under license no. 16031158 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 0.074 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 31.1 ft/sec at pipe 66. 2. 6 5.2 1. 2 1. 3 2.6 0.0 2. 4 0.0 0.5 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: .33/3000 (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A Diameter (in) 2.067 4.026 6.065 PAGE: D Diameter (in) 6.280 PAGE: E Diameter (in) 6.080 9.790 MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in Feet E Ell T L C B G A Tee LngEll ChkVlv BfyVlv GatVlv AlmChk F 45 5.00 10.00 3.00 11. 00 6.00 1.00 10.00 2.00 10. 00 20.00 6.00 22.00 12.00 2.00 20.00 4.00 14.00 30.00 9.00 32.00 10.00 3.00 28.00 7.00 MATERIAL: DIRON HWC: 140 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 22.06 47.28 14.18 50.43 15.76 4.73 47.28 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 21. 41 45.88 13. 76 48.94 15.29 4.59 45.88 28.02 63.67 20.38 70.04 24.20 6.37 63.67 D N DPVlv NPTee 10.00 10.00 10.00 20.00 19.00 30.00 F 45 11.03 F 45 10.71 11. 46 y 0 o:,, to >3 ts WATER SUPPLY ANALYSIS >3 •• H 140.0 Static: 132.30 psi Resid: 128.70 psi Flow: 1683.0 gprn >3 er, ~' ts f-' •• ..J LEGEND / I() ;:; .l ~~ :,, 0 :,:, 0 ~w 1 ~ Available pressurey Ul to 128.58 psi@ 1713.8 gprn :,, 0 G112. 0 l 2~ Required pressure 0 Ul A 119.55 psi@ 1713.8 gprn ~ 'c1 :,:, u / Ul H z G to ~ C: ~ E H ts ~ :,:, 0 H Ul p z ~ R 84.0 G) Ul >3 E :,, ts :s: s I :i: s :,, ~ :,:, 0 u ts ~ :,, R C: to ~ E 56.0 H () w i w ' p j w ~ 0 ~ s 0 Ul 0 H i () Ul / 28.0 :i: :,, Ul Ul ..J ,,,. / ..J ,,,. V, :,, I 'c1 to OJ 0.0 _J/ I • IQ Ul rD 0 "' f-' f-' I -14.7 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: .33/3000 WATER SUPPLY CURVE 144+ I I I 132*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 128.7 psi@ 1683 gpm-> * 0 I Flow Test Point I 120+ I I I 108+ I I I P 96+ R I E I s I S 84+ u I R I E I 72+ I p I s I I 60+ l I I I 48+ I I I 36+ I I !============================== 24+ LEGEND I I X = Required Water Supply I 119.55 psi@ 1713.8 gpm 12+ I O = Available Water Supply I 128.58 psi@ 1713.8 gpm I " X O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 6/17/2003 C:\HASS74\745A-B.SDF JOB TITLE: CARLSBAD OAKS BUILDING A -AREA B: .33/3000 Utility Report: Equivalent K-Factor Calculator Node Sprinkler Pres. Dia. Name K-Factor (psi) (in) X 8.00 7.00 1.049 Pipe Ftgs. Len. (ft) 1.00 T Total H-W Equivalent Len. (ft) coef. K-factor 6.00 120.00 7.55 ► ► ► ► ► ► ► ► ► ► ► ► HYDRAULIC CALCULATIONS FOR CARLSBAD OAKS BUILDING B PARCEL 3, LOKER AVENUE CARLSBAD, CALIFORNIA GUFP JOB #745 OCCUPANCY CLASSIFICATION: EX. HAZ. DENSITY: .33GPM/SQ.FT. REQUIRED AREA OF APPLICATION: 3000 SQ.FT. COVERAGE PER SPRINKLER: 96 SQ. FT. NUMBER OF SPRINKLERS FLOWING: 32 TOTAL SPRINKLER FLOW REQUIRED: 1124.7 GPM TOTAL WATER REQUIRED (INCLUDING HOSE): 1624.7 GPM DEMAND AT BASE OF RISER: 1124. 7GPM@95.2PSI SPRINKLER ORIFICE SIZE: 17/32" (K-FACTOR =8.0) CALCULATIONS BY: ROBERT MAHONEY AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE COMMENTS: WATER AVAILABLE FOR DESIGN 90% OF CITY SUPPLY Calculation by hass computer program HRS System::;, Inc General Underground Fire Pro1ect1on, inc. # 16031158 3930 EAST CORONADO STREET+ ANAHEIM, CA 92807 + PHONE 714-632-8646 FAX 714-632-0579 CONTRACTOR'S LICENSE NO. 485748 C-16/C-34 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/19/2003 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: .33/3000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 132. 3 128.7 1683.0 128.9 1624.7 105.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1624.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0. 0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1124. 7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.0 K= 7.55 18.5 32.5 2 18.0 K= 7.55 18.5 32.5 3 18.0 K= 7.55 18.6 32.6 4 18.0 K= 7.55 18.8 32.7 5 18.0 K= 7.55 19.1 33.0 6 18.0 K= 7.55 19.6 33.5 7 18.0 K= 7.55 20.3 34.1 8 18.0 K= 7.55 21. 3 34.8 9 18.0 K= 7.55 22.5 35.8 10 15.0 ----40.2 11 18.0 K= 7.55 18.6 32.6 12 18.0 K= 7.55 18.6 32.6 13 18.0 K= 7.55 18.7 32.7 14 18.0 K= 7.55 18.9 32.8 15 18.0 K= 7.55 19.3 33.1 16 18.0 K= 7.55 19.8 33.6 17 18.0 K= 7.55 20.5 34.2 18 18.0 K= 7.55 21.4 35.0 19 18.0 K= 7.55 22.7 36.0 20 15.0 ----40.4 21 18.0 K= 7.55 19.0 32.9 22 18.0 K= 7.55 19.1 33.0 23 18.0 K= 7.55 19.2 33.0 24 18.0 K= 7.55 19.4 33.2 25 18.0 K= 7.55 19.7 33.5 26 18.0 K= 7.55 20.2 33.9 27 18.0 K= 7.55 20.9 34.6 28 18.0 K= 7.55 21. 9 35.4 29 18.0 K= 7.55 23.2 36.4 30 15.0 ----41. 3 31 18.0 K= 7.55 32.1 42.7 32 18.0 K= 7.55 32.1 42.8 33 18.0 K= 7.55 32.2 42.9 34 18.0 K= 7.55 32.6 43.1 35 18.0 K= 7.55 33.1 43.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/19/2003 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: .33/3000 NODE ANALYSIS DATA NODE TAG ELEVATION (FT) 36 15.0 37 15.0 TR 15.0 BR 0.0 Bl 0.0 B2 0.0 B3 0.0 B4 0.0 SRC 0.0 NODE TYPE SOURCE PRESSURE (PSI) 43.1 51. 0 87.8 95.2 96.4 97.3 102.3 104.4 105.5 DISCHARGE (GPM) 1124. 7 ----.. ··~-· -- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/19/2003 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: .33/3000 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 -163.8 2.703 PL 8.00 PF 0.5 15 18.0 7.5 19.3 33.1 9.2 120 FTG PE 0.0 16 18.0 7.5 19.8 33.6 0.063 TL 8.00 PV Pipe: 15 -197.3 2.703 PL 8.00 PF 0.7 16 18.0 7.5 19.8 33.6 11. 0 120 FTG PE 0.0 17 18.0 7.5 20.5 34.2 0.089 TL 8.00 PV Pipe: 16 -231. 5 2.703 PL 8.00 PF 1.0 17 18.0 7.5 20.5 34.2 12.9 120 FTG PE 0.0 18 18.0 7.5 21. 4 35.0 0.120 TL 8.00 PV Pipe: 17 -266.5 2.703 PL 8.00 PF 1. 2 18 18.0 7.5 21.4 35.0 14.9 120 FTG PE 0.0 19 18.0 7.5 22.7 36.0 0.156 TL 8.00 PV Pipe: 18 -302.4 2.703 PL 46.00 PF 16.4 19 18.0 7.5 22.7 36.0 16.9 120 FTG 2T PE 1. 3 20 15.0 0.0 40.4 0.0 0.197 TL 83.30 PV Pipe: 19 -32.9 2.703 PL 8.00 PF 0.0 21 18.0 7.5 19.0 32.9 1.8 120 FTG PE 0.0 22 18.0 7.5 19.1 33.0 0.003 TL 8.00 PV Pipe: 20 -65.9 2.703 PL 8.00 PF 0.1 22 18.0 7.5 19.1 33.0 3.7 120 FTG PE 0.0 23 18.0 7.5 19.2 33.0 0.012 TL 8.00 PV Pipe: 21 -99.0 2.703 PL 8.00 PF 0.2 23 18.0 7.5 19.2 33.0 5. 5 120 FTG PE 0.0 24 18.0 7.5 19.4 33.2 0. 025 TL 8.00 PV Pipe: 22 -132.2 2.703 PL 8.00 PF 0.3 24 18.0 7.5 19.4 33.2 7.4 120 FTG PE 0.0 25 18.0 7.5 19.7 33.5 0.043 TL 8.00 PV Pipe: 23 -165.7 2.703 PL 8.00 PF 0.5 25 18.0 7.5 19.7 33.5 9.3 120 FTG PE 0.0 26 18.0 7.5 20.2 33.9 0.065 TL 8.00 PV Pipe: 24 -199.6 2.703 PL 8.00 PF 0.7 26 18.0 7.5 20. 2 33.9 11. 2 120 FTG PE 0.0 27 18.0 7.5 20.9 34.6 0.091 TL 8.00 PV Pipe: 25 -234.2 2.703 PL 8.00 PF 1.0 27 18.0 7.5 20.9 34.6 13 .1 120 FTG PE 0.0 28 18.0 7.5 21. 9 35.4 0.123 TL 8.00 PV Pipe: 26 -269.6 2.703 PL 8.00 PF 1. 3 28 18.0 7.5 21. 9 35.4 15.1 120 FTG PE 0.0 29 18.0 7.5 23.2 36.4 0.159 TL 8.00 PV ,~-~-----~· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/19/2003 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: . 33/3000 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 -305.9 2.703 PL 46.00 PF 16.8 29 18.0 7.5 23.2 36.4 17.1 120 FTG 2T PE 1. 3 30 15.0 0.0 41. 3 0.0 0.201 TL 83.30 PV Pipe: 28 -42.7 2.703 PL 8.00 PF 0. 0 31 18.0 7.5 32.1 42.7 2.4 120 FTG PE 0.0 32 18.0 7.5 32.1 42.8 0.005 TL 8.00 PV Pipe: 29 -85.5 2.703 PL 8.00 PF 0.2 32 18.0 7.5 32.1 42.8 4.8 120 FTG PE 0.0 33 18.0 7. 5 32.2 42.9 0.019 TL 8.00 PV Pipe: 30 -128.4 2.703 PL 8.00 PF 0.3 33 18.0 7.5 32.2 42.9 7.2 120 FTG PE 0.0 34 18.0 7.5 32.6 43.1 0.040 TL 8.00 PV Pipe: 31 -171.5 2.703 PL 8.00 PF 0.6 34 18.0 7.5 32.6 43.1 9.6 120 FTG PE 0. 0 35 18.0 7.5 33.1 43.4 0.069 TL 8.00 PV Pipe: 32 -214.9 2.703 PL 46.00 PF 8.7 35 18.0 7.5 33.1 43.4 12.0 120 FTG 2T PE 1.3 36 15.0 0.0 43.1 0.0 0.105 TL 83.30 PV Pipe: 33 -301. 4 4.310 PL 12.00 PF 0.2 10 15.0 0.0 40.2 0.0 6.6 120 FTG PE 0.0 20 15.0 0.0 40.4 0. 0 0.020 TL 12.00 PV Pipe: 34 -603.9 4.310 PL 12.00 PF 0. 9 20 15.0 0.0 40.4 0.0 13 .3 120 FTG PE 0. 0 30 15.0 0.0 41. 3 0.0 0.073 TL 12.00 PV Pipe: 35 -909.8 4. 310 PL 12.00 PF 1. 9 30 15.0 0.0 41.3 0.0 20.0 120 FTG PE 0. 0 36 15.0 0.0 43.1 0.0 0.156 TL 12.00 PV Pipe: 36 -1124. 7 4.310 PL 6.25 PF 7. 9 36 15.0 0.0 43.1 0.0 24.7 120 FTG T PE 0.0 37 15.0 0.0 51. 0 0.0 0.231 TL 34.12 PV Pipe: 37 -1124. 7 4.310 PL 142.50 PF 36.7 37 15.0 0.0 51. 0 0. 0 24.7 120 FTG 2L PE 0. 0 TR 15.0 0.0 87.8 0.0 0.231 TL 159.22 PV Pipe: 38 -1124. 7 6.357 PL 15.00 PF 0.9 TR 15.0 0.0 87.8 0.0 11.4 120 FTG L PE 6. 5 BR 0.0 0.0 95.2 0.0 0.035 TL 26.00 PV Pipe: 39 -1124. 7 6.357 PL 15.00 PF 1. 3 BR 0.0 0. 0 95.2 0.0 11.4 120 FTG 2L PE 0. 0 Bl 0.0 0.0 96.4 0. 0 0.035 TL 37.00 PV ~~., ._ _____ ---------- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/19/2003 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: . 33/3000 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: 40 -1124. 7 6.080 PL 15.00 PF 0.8 Bl 0.0 0.0 96.4 0.0 12.4 150 FTG L PE 0.0 B2 0.0 0.0 97.3 0.0 0.029 TL 28.76 PV Pipe: 41 FIXED PRESSURE LOSS DEVICE B3 0. 0 0.0 102.3 0. 0 5.0 psi, 1124. 7 gpm B2 0. 0 0.0 97.3 0.0 Pipe: 42 -1124.7 6.080 PL 25.00 PF 2.2 B3 0.0 0.0 102.3 0.0 12.4 150 FTG TG PE 0.0 B4 0.0 0.0 104.4 0.0 0.029 TL 75.47 PV Pipe: 43 -1124. 7 9.790 PL 290.00 PF 1.0 B4 0. 0 0.0 104.4 0.0 4.8 150 FTG TGF PE 0.0 SRC 0. 0 SRCE 105.5 (N/A) 0.003 TL 371. 50 PV NOTES: (1) Calculations were performed by the HASS 7.4 computer program under license no. 16031158 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 0.003 gpm and a maximum imbalance at any node of 0.146 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 24.7 ft/sec at pipe 37. (4) 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 Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv 2.703 9.33 18.65 6.22 21. 76 10.88 1. 55 15.54 15.54 4.310 13. 94 27.87 8.36 30.66 16. 72 2.79 27.87 27.87 N NPTee 18.65 27.87 SPRINKLER SYSTEM HYDRAULIC ANALYSIS DATE: 6/19/2003 Page 7 C:\HASS74\745B.SDF JOB TITLE: Carlsbad Oaks Building B: .33/3000 PAGE: B MATERIAL: THNWL HWC: 120 Diameter (in) 6.357 PAGE: E Diameter (in) 6.080 9.790 E Ell 18.00 Equivalent Fitting Lengths in Feet T L C B G A Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 38.00 11.00 40.00 13.00 4.00 35.00 MATERIAL: PVC150 HWC: 150 E Ell 21. 41 28.02 Equivalent Fitting Lengths in Feet T L C B G N Tee LngEll ChkVlv BfyVlv GatVlv NPTee 45.88 13.76 48.94 15.29 4.59 45.88 63.67 20.38 70.04 24.20 6.37 63.67 D N DPVlv NPTee 24.00 38.00 F 45 10.71 11. 46 y tl 0 :i, td rJ t'l WATER SUPPLY ANALYSIS rJ .. H 140.0 Static: 132.30 psi Resid: 128.70 psi Flow: 1683.0 gprn rJ °' t" '-t'l f-' •• '-0 LEGEND / lo~ 1~ p, 0 Ii 0 f--' w 1 ~ Available pressure / "' tr 128.93 psi@ 1624.7 gprn p, p, G112. 0 I 2~ Required pressure 0 u, A 105.47 psi@ 1624.7 gprn p, "' ;,;' ::0 u / "' H z G td ~ "' t" E r'• t'l f--' ::0 p, r'· u, p :; >< R 84.0 lQ u, rJ E td ~ .. s :r: s w >< w tl u '-~ w R 0 c:: 0 t" E 56.0 0 H () ~ :i, p J t" >< s u, H i u, () 28.0 / ii; u, u, -.J "" / -.J "" '" "' td p, 0.0 _y I • lQ [J) (1) tl ',JOO I -14.7 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/19/2003 JOB TITLE: Carlsbad Oaks Building B: .33/3000 WATER SUPPLY CURVE 144+ I I I 132*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 128.7 psi@ 1683 gpm0> * I Flow Test Point I 120+ I I I 108+ I X I I P 96+ R I E I s I S 84+ u I R I E I 72+ I P I s I I 60+ > I I I 48+ I I I 36+ I I I============================== 24+ LEGEND I I X = Required Water Supply I 105.47 psi@ 1624.7 gpm 12+ I O = Available Water Supply I 128.93 psi@ 1624.7 gpm I " " C:\HASS74\745B.SDF 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/19/2003 JOB TITLE: Carlsbad Oaks Building B: .33/3000 Utility Report: Equivalent K-Factor Calculator Node Sprinkler Pres. Dia. Name K-Factor (psi) ( in) SPRIG UP 8.00 7.00 1.049 Pipe Ftgs. Len. (ft) 1.00 T C:\HASS74\745B.SDF Total H-W Equivalent Len. (ft) coef. K-factor 6.00 120.00 7.55 ~►'" ;;::.t.,., /~'''\, • • . , -. "'.. ,~ . , , "o, • c~ ,a ► ► ► ► ► ► ► ► ► ► ► ► GENERAL UNDERGROUND FIRE PROTECTION, Inc. HYDRAULIC CALCULATIONS FOR CARLSBAD OAKS BUILDING C PARCEL 3, LOKER AVENUE CARLSBAD, CALIFORNIA GUFP JOB #745 --- OCCUPANCY CLASSIFICATION: EX. HAZ. DENSITY: .33GPM/SQ.FT. REQUIRED AREA OF APPLICATION: 3000 SQ.FT. COVERAGE PER SPRINKLER: 96 SQ. FT. NUMBER OF SPRINKLERS FLOWING: 32 TOTAL SPRINKLER FLOW REQUIRED: 1209.7 GPM TOTAL WATER REQUIRED (INCLUDING HOSE): 1709.7 GPM DEMAND AT BASE OF RISER: 1209. 7@66.SPSI SPRINKLER ORIFICE SIZE: 17/32" (K-FACTOR =8.0) CALCULATIONS BY: ROBERT MAHONEY AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE COMMENTS: WATER AVAILABLE FOR DESIGN 90% OF CITY SUPPLY Ca1cu1at1on by hass cornpute1 µrograrn HRS System;;, Inc General lJndergmunrl Fire ProtecthHl. lnc 11 16031158 3930 EAST CORONADO STREET + ANAHEIM, CA 92807 + PHONE 714-632-8646 FAX 714-632-0579 CONTRACTOR'S LICENSE NO, 485748 C-16/C-34 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 D.'\TE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: . 33/3000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 132. 3 128.7 1683.0 128.6 1709.7 77.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1709.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0. 0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1209.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.0 K= 7.55 18.5 32.5 2 18.0 K= 7.55 18.5 32.5 3 18.0 K= 7.55 18.8 32.7 4 18.0 K= 7.55 19.3 33.2 5 18.0 K= 7.55 20.2 33.9 6 18.0 K= 7.55 21. 6 35.1 7 18.0 K= 7.55 23.6 36.6 8 18.0 K= 7.55 28.5 40.3 9 18.0 K= 7.55 28.6 40.4 10 18.0 ----29.4 11 18.0 K= 7.55 18.6 32.6 12 18.0 K= 7.55 18.7 32.6 13 18.0 K= 7.55 18.9 32.9 14 18.0 K= 7.55 19.5 33.3 15 18.0 K= 7.55 20.4 34.1 16 18.0 K= 7.55 21. 8 35.2 17 18.0 K= 7.55 23.8 36.8 18 18.0 K= 7.55 28.8 40.5 19 18.0 K= 7.55 28.9 40.6 20 18.0 ----29.7 21 18.0 K= 7.55 19.3 33.1 22 18.0 K= 7.55 19.3 33.2 23 18.0 K= 7.55 19.6 33.4 24 18.0 K= 7.55 20.1 33.9 25 18.0 K= 7.55 21.1 34.7 26 18.0 K= 7.55 22.5 35.8 27 18.0 K= 7.55 24.6 37.4 28 18.0 K= 7.55 29.7 41.2 29 18.0 K= 7.55 29.8 41.2 30 18.0 ----30.7 31 18.0 K= 7.55 29.1 40.7 32 18.0 K= 7.55 29.2 40.8 33 18.0 K= 7.55 29.6 41. 0 34 18.0 K= 7.55 30.4 41. 6 35 18.0 K= 7.55 32.3 42.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/24/2003 JOB TITLE: Carlsbad Oaks Building C: .33/3000 NODE ANALYSIS DATA NODE TAG 36 37 38 39 40 41 TR BR Cl C2 C3 C4 SRC ELEVATION (FT) 18.0 18.0 18.0 18.0 18.0 18.0 18.0 0. 0 0.0 0.0 0.0 0.0 0.0 NODE TYPE K= 7.55 SOURCE PRESSURE (PSI) 32.4 33.3 30.6 30.9 31. 9 34.1 57.4 66.5 67.9 68.9 73.9 76.0 77.1 C:\HASS74\745C.SDF DISCHARGE (GPM) 43.0 1209.7 ---~-----·~·-·· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: . 33/3000 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 -32.5 2.703 PL 8.00 PF 0.0 1 18.0 7.5 18.5 32.5 1. 8 120 FTG PE 0. 0 2 18.0 7.5 18.5 32.5 0.003 TL 8.00 PV Pipe: 2 -64.9 2.203 PL 8.00 PF 0.2 2 18.0 7.5 18.5 32.5 5.5 120 FTG PE 0.0 3 18.0 7.5 18.8 32.7 0.031 TL 8.00 PV Pipe: 3 -97.6 2.203 PL 8.00 PF 0.5 3 18.0 7.5 18.8 32.7 8.2 120 FTG PE 0. 0 4 18.0 7.5 19.3 33.2 0.066 TL 8.00 PV Pipe: 4 -130. 8 2.203 PL 8.00 PF 0.9 4 18.0 7.5 19.3 33.2 11. 0 120 FTG PE 0.0 5 18.0 7.5 20.2 33.9 0 .113 TL 8.00 PV Pipe: 5 -164.7 2.203 PL 8.00 PF 1. 4 5 18.0 7. 5 20.2 33.9 13. 9 120 FTG PE 0.0 6 18.0 7. 5 21. 6 35.1 0.173 TL 8.00 PV Pipe: 6 -199.8 2.203 PL 8.00 PF 2.0 6 18.0 7.5 21. 6 35.1 16.8 120 FTG PE 0.0 7 18.0 7.5 23.6 36.6 0.248 TL 8.00 PV Pipe: 7 -236.4 2.203 PL 3.75 PF 5.9 7 18.0 7.5 23.6 36.6 19.9 120 FTG T PE 0.0 10 18.0 0.0 29.4 0.0 0.338 TL 17.39 PV Pipe: 8 -40.3 2.203 PL 8.00 PF 0.1 8 18.0 7.5 28.5 40.3 3.4 120 FTG PE 0.0 9 18.0 7.5 28.6 40.4 0.013 TL 8.00 PV Pipe: 9 -80.7 2 .203 PL 4.25 PF 0.8 9 18.0 7.5 28.6 40.4 6.8 120 FTG T PE 0.0 10 18.0 0.0 29.4 0.0 0.046 TL 17.89 PV Pipe: 10 -32.6 2. 203 PL 8.00 PF 0.1 11 18.0 7.5 18.6 32.6 2.7 120 FTG PE 0.0 12 18.0 7.5 18.7 32.6 0.009 TL 8.00 PV Pipe: 11 -65.2 2 .203 PL 8.00 PF 0.2 12 18.0 7.5 18.7 32.6 5.5 120 FTG PE 0.0 13 18.0 7.5 18.9 32.9 0.031 TL 8.00 PV Pipe: 12 -98.1 2 .203 PL 8.00 PF 0.5 13 18.0 7.5 18.9 32.9 8.3 120 FTG PE 0.0 14 18.0 7.5 19.5 33.3 0.066 TL 8.00 PV Pipe: 13 -131. 4 2 .203 PL 8.00 PF 0.9 14 18.0 7.5 19.5 33.3 11.1 120 FTG PE 0.0 15 18.0 7.5 20.4 34.1 0 .114 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 D!,TE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: . 33 /3000 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 -165.5 2 .203 PL 8.00 PF 1. 4 15 18.0 7.5 20.4 34.1 13.9 120 FTG PE 0.0 16 18.0 7.5 21. 8 35.2 0.175 TL 8.00 PV Pipe: 15 -200.7 2.203 PL 8.00 PF 2. 0 16 18.0 7.5 21. 8 35.2 16.9 120 FTG PE 0.0 17 18.0 7.5 23.8 36.8 0.250 TL 8.00 PV Pipe: 16 -237.5 2.203 PL 3.75 PF 5.9 17 18.0 7.5 23.8 36.8 20.0 120 FTG T PE 0.0 20 18.0 0.0 29.7 0.0 0.341 TL 17.39 PV Pipe: 17 -40.5 2 .203 PL 8.00 PF 0.1 18 18.0 7.5 28.8 40.5 3.4 120 FTG PE 0.0 19 18.0 7.5 28.9 40.6 0. 013 TL 8.00 PV Pipe: 18 -81.1 2.203 PL 4.25 PF 0.8 19 18.0 7.5 28.9 40.6 6.8 120 FTG T PE 0.0 20 18.0 0.0 29.7 0.0 0.047 TL 17.89 PV Pipe: 19 -33.1 2.203 PL 8.00 PF 0.1 21 18.0 7.5 19.3 33.1 2.8 120 FTG PE 0.0 22 18.0 7.5 19.3 33.2 0.009 TL 8.00 PV Pipe: 20 -66.3 2.203 PL 8.00 PF 0.3 22 18.0 7.5 19.3 33.2 5.6 120 FTG PE 0.0 23 18.0 7.5 19.6 33.4 0.032 TL 8.00 PV Pipe: 21 -99.7 2.203 PL 8.00 PF 0.5 23 18.0 7. 5 19.6 33.4 8.4 120 FTG PE 0.0 24 18.0 7. 5 20.1 33.9 0.069 TL 8.00 PV Pipe: 22 -133. 6 2.203 PL 8.00 PF 0.9 24 18.0 7.5 20.1 33.9 11.2 120 FTG PE 0.0 25 18.0 7.5 21.1 34.7 0 .118 TL 8.00 PV Pipe: 23 -168.3 2.203 PL 8.00 PF 1. 4 25 18.0 7. 5 21.1 34.7 14.2 120 FTG PE 0.0 26 18.0 7.5 22.5 35.8 0.180 TL 8.00 PV Pipe: 24 -204.1 2.203 PL 8.00 PF 2.1 26 18.0 7.5 22.5 35.8 17.2 120 FTG PE 0.0 27 18.0 7.5 24.6 37.4 0.258 TL 8.00 PV Pipe: 25 -241. 5 2.203 PL 3.75 PF 6.1 27 18.0 7.5 24.6 37.4 20.3 120 FTG T PE 0.0 30 18.0 0.0 30.7 0.0 0.352 TL 17.39 PV Pipe: 26 -41.2 2.203 PL 8.00 PF 0.1 28 18.0 7.5 29.7 41. 2 3.5 120 FTG PE 0.0 29 18.0 7. 5 29.8 41.2 0. 013 TL 8.00 PV -·-~~---~-·- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 D.'\TE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: . 33 /3000 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 -82.4 2.203 PL 4.25 PF 0.9 29 18.0 7.5 29.8 41. 2 6.9 120 FTG T PE 0.0 30 18.0 0.0 30.7 0.0 0.048 TL 17.89 PV Pipe: 28 -40.7 2.203 PL 8.00 PF 0.1 31 18.0 7.5 29.l 40.7 3.4 120 FTG PE 0.0 32 18.0 7.5 29.2 40.8 0. 013 TL 8.00 PV Pipe: 29 -81. 5 2.203 PL 8.00 PF 0.4 32 18.0 7.5 29.2 40.8 6.9 120 FTG PE 0.0 33 18.0 7.5 29.6 41. 0 0.047 TL 8.00 PV Pipe: 30 -122.5 2.203 PL 8.00 PF 0.8 33 18.0 7.5 29.6 41. 0 10.3 120 FTG PE 0.0 34 18.0 7.5 30.4 41. 6 0.100 TL 8.00 PV Pipe: 31 -164.1 2.203 PL 3.75 PF 3.0 34 18.0 7.5 30.4 41. 6 13.8 120 FTG T PE 0.0 37 18.0 0.0 33.3 0.0 0.172 TL 17.39 PV Pipe: 32 -42.9 2.203 PL 8.00 PF 0.1 35 18.0 7.5 32.3 42.9 3.6 120 FTG PE 0.0 36 18.0 7.5 32.4 43.0 0.014 TL 8.00 PV Pipe: 33 -85.9 2.203 PL 4.25 PF 0.9 36 18.0 7.5 32.4 43.0 7.2 120 FTG T PE 0.0 37 18.0 0.0 33.3 0.0 0.052 TL 17.89 PV Pipe: 34 -317.1 2.203 PL 2.00 PF 1. 2 10 18.0 0.0 29.4 0.0 26.7 120 FTG PE 0.0 38 18.0 0.0 30.6 0.0 0.583 TL 2.00 PV Pipe: 35 -318.6 2 .203 PL 2.00 PF 1. 2 20 18.0 0.0 29.7 0.0 26.8 120 FTG PE 0.0 39 18.0 0.0 30. 9 0.0 0.588 TL 2.00 PV Pipe: 36 -323.9 2.203 PL 2.00 PF 1. 2 30 18.0 0.0 30.7 0.0 27.3 120 FTG PE 0.0 40 18.0 0.0 31. 9 0.0 0.606 TL 2.00 PV Pipe: 37 -250.0 2.203 PL 2.00 PF 0. 8 37 18.0 0.0 33.3 0.0 21. 0 120 FTG PE 0.0 41 18.0 0.0 34.1 0.0 0.375 TL 2.00 PV Pipe: 38 -317 .1 4.260 PL 12.00 PF 0.3 38 18.0 0.0 30.6 0.0 7.1 120 FTG PE 0. 0 39 18.0 0.0 30.9 0.0 0.023 TL 12.00 PV Pipe: 39 -635.8 4.260 PL 12.00 PF 1.0 39 18.0 0.0 30.9 0.0 14.3 120 FTG PE 0.0 40 18.0 0.0 31. 9 0. 0 0.085 TL 12.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/24/2003 C:\HASS74\745C.SDF Oaks Building C: .33/3000 JOB TITLE: Carlsbad PIPE TAG Q(GPM) DIA(IN) PT DISC. VEL(FPS) HW(C) LENGTH (FT) PRESS. END NODES ELEV. (FT) NOZ. (K) (PSI) (GPM) FL/FT SUM. (PSI) 40 41 Pipe: 40 18.0 18.0 0. 0 0.0 31. 9 34.1 -959.7 0.0 21.6 0.0 4.260 PL 12.00 PF 120 FTG PE 0.182 TL 12.00 PV 2.2 0.0 41 TR Pipe: 41 18.0 18.0 0.0 0.0 34.1 57.4 -1209.7 0.0 27.2 0.0 4.260 PL 120 FTG 0.279 TL 67.50 2L 83.50 PF PE PV 23.3 0.0 TR BR BR Cl Cl C2 C3 C2 C3 C4 C4 SRC Pipe: 42 18.0 0.0 Pipe: 43 0.0 0.0 Pipe: 44 0.0 0.0 Pipe: 45 0.0 0.0 Pipe: 46 0.0 0.0 Pipe: 47 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 SRCE 57.4 66.5 66.5 67.9 67.9 68.9 73.9 68.9 73.9 76.0 76.0 77.1 -1209.7 0.0 12.2 0. 0 -1209.7 0.0 12.2 0.0 -1209.7 0.0 13.4 0.0 0.0 0.0 -1209.7 0.0 13.4 0. 0 -1209.7 0.0 5.2 (N/A) 6.357 PL 120 FTG 0.040 TL 6.357 PL 120 FTG 0.040 TL 20.00 L 31. 00 15.00 2L 37.00 PF PE PV PF PE PV 6.080 PL 15.00 PF 150 FTG L PE 0.033 TL 28.76 PV FIXED PRESSURE LOSS DEVICE 5.0 psi, 1209.7 gpm 6.080 PL 15.00 PF 150 FTG TG PE 0.033 TL 65.47 PV 9.790 PL 150 FTG 0.003 TL 276.00 TG 346.04 PF PE PV NOTES: (1) Calculations were performed by the HASS 7.4 computer program under license no. 16031158 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 0.002 gpm and a maximum imbalance at any node of 0.096 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 27.3 ft/sec at pipe 36. 1. 2 7.8 1. 5 0.0 0.9 0.0 2.1 0. 0 1.1 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 (4) 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 BfyVlv GatVlv AlmChk DPVlv NPTee 2.203 6.82 13. 64 4.09 15.00 8.18 1. 36 13. 64 13. 64 13. 64 2.703 9.33 18.65 6.22 21.76 10.88 1. 55 15.54 15.54 18.65 PAGE: B MATERIAL: THNWL 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 4.260 13. 00 26.00 8.00 29.00 16.00 3.00 26.00 13.00 26.00 6.357 18.00 38.00 11. 00 40.00 13. 00 4.00 35.00 24.00 38.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N F Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 45 6.080 21. 41 45.88 13. 76 48.94 15.29 4.59 45.88 10.71 9.790 28.02 63.67 20.38 70.04 24.20 6.37 63.67 11.46 140.0 G112.0 A u G E p R 84.0 E s s u R E 56.0 ( p s i ) 28.0 0.0 -14.7 WATER SUPPLY ANALYSIS Static: 132.30 psi Resid: 128.70 psi Flow: 1683.0 gpm LEGEND ,---------______________ 1.-0~lli-'----------- 1 ~ 2 ~ Available pressure 128.59 psi@ 1709.7 gpm Required pressure 77.13 psi@ 1709.7 gpm 2 • ~ 0 o:,, tJj 8 t'l 8 .. H 8 "' t" '- t'l "' .. "' '-n "' OJ 0 " 0 f--" w (/l tr OJ 0. 0 C/l OJ :,;- H z 0, ~ " t:"' >-'· t'l f--" :,i 0. >-'· C/l ~ ~ lQ C/l 8 n t'l :,: :,: w ~ w 0 '-~ w 0 0 t:"' 0 H n ~ t' ~ C/l H C/l n ..... ~ C/l C/l -.J "'" ..... -.J "'" u, "' n OJ <O r.n ro 0 "' (X) 400 600 800 1000 1200 1400 FLOW (GPM) 1600 1800 2000 ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/24/2003 C:\HASS74\745C.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 WATER SUPPLY CURVE 144+ I I I 132*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 128.7 psi@ 1683 gprn-> * 0 I Flow Test Point I 120+ I I I 108+ I I I p 96+ R I E I s I S 84+ u I R I E I 72+ I p I s I I 60+ > I I I 48+ I I I 36+ I I I============================== 24+ LEGEND I I X = Required Water Supply I 77.13 psi@ 1709.7 gprn 12+ I O = Available Water Supply I 128.59 psi@ 1709.7 gpm I " " X O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) ~\. """".t ··~·· .;c,,: ·• •• . ~ . • . -. .... ,• . . . "o~.c~ '"' ► ► ► ► ► ► ► ► ► ► ► ► HYDRAULIC CALCULATIONS FOR CARLSBAD OAKS BUILDING D PARCEL 3, LOKER AVENUE CARLSBAD, CALIFORNIA GUFP JOB #745 OCCUPANCY CLASSIFICATION: EX. HAZ. DENSITY: .33GPM/SQ.FT. REQUIRED AREA OF APPLICATION: 3000 SQ.FT. COVERAGE PER SPRINKLER: 96 SQ. FT. NUMBER OF SPRINKLERS FLOWING: 39 TOTAL SPRINKLER FLOW REQUIRED: 1217.4 GPM TOTAL WATER REQUIRED (INCLUDING HOSE): 1717.4 GPM DEMAND AT BASE OF RISER: 1217 .4@65.9PSI SPRINKLER ORIFICE SIZE: 17/32" (K-FACTOR =8.0) CALCULATIONS BY: ROBERT MAHONEY AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE COMMENTS: WATER AVAILABLE FOR DESIGN 90% OF CITY SUPPLY ( :a1r:u1at1or1 tiv noss 1:rnnp1ner proqrarn HHS Syste1m,. Inc (.Je11eral lJmjerwuuncJ Fire Protect1u11. Inc;_ 11 Hi031158 3930 EAST CORONADO STREET ♦ ANAHEIM, CA 92807 • PHONE 714-632-8646 FAX 714-632-0579 CONTRACTOR'S LICENSE NO. 485748 C-16/C-34 -----•---··-· _____ ., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 132. 3 128.7 1683.0 128.6 1717.4 76.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1717.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1217.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.0 K= 7.55 18.0 32.0 2 18.0 K= 7.55 18.0 32.1 3 18.0 K= 7.55 18.3 32.3 4 18.0 K= 7.55 18.8 32.7 5 18.0 K= 7.55 19.7 33.5 6 18.0 K= 7.55 21. 0 34.6 7 18.0 K= 7.55 23.0 36.2 8 18.0 ----30.8 9 18.0 K= 7.55 20.4 34.1 10 18.0 K= 7.55 20.4 34.1 11 18.0 K= 7.55 20.7 34.4 12 18.0 K= 7.55 21. 3 34.8 13 18.0 K= 7.55 22.3 35.6 14 18.0 K= 7.55 23.8 36.8 15 18.0 K= 7.55 26.0 38.5 16 18.0 ----34.8 17 18.0 K= 7.55 33.4 43.6 18 18.0 K= 7.55 32.6 43. µ. 19 18.0 K= 7.55 32.3 42.9 20 18.0 K= 7.55 32.2 42.8 21 18.0 K= 7.55 32.2 42.8 22 18.0 K= 7.55 32.4 42.9 23 18.0 K= 7.55 32.9 43.3 24 18.0 ----35.8 25 18.0 K= 7.55 21. 9 35.3 26 18.0 K= 7.55 22.0 35.4 27 18.0 K= 7.55 22.3 35.6 28 18.0 K= 7.55 22.9 36.1 29 18.0 K= 7.55 24.0 37.0 30 18.0 K= 7.55 25.6 38.2 31 18.0 K= 7.55 27.9 39.9 32 18.0 ----37.3 33 18.0 K= 7.55 33.7 43.8 34 18.0 K= 7.55 33.8 43.9 35 18.0 K= 7.55 34.2 44.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/24/2003 JOB TITLE: Carlsbad Oaks Building C: .33/3000 NODE ANALYSIS DATA NODE TAG 36 37 TR BR Cl C2 C3 C4 SRC ELEVATION (FT) 18.0 18.0 18.0 0.0 0.0 0.0 0.0 0.0 0.0 NODE TYPE K= 7.55 SOURCE PRESSURE (PSI) 35.2 39.8 56.8 65.9 67.4 68.3 73.3 75.5 76.6 C;\HASS74\745D.SDF DISCHARGE (GPM) 44.8 1217.4 .. ·---··· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: . 33 /3000 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 -32.0 2.203 PL 8.00 PF 0.1 1 18.0 7.5 18.0 32.0 2.7 120 FTG PE 0.0 2 18.0 7.5 18.0 32.1 0.008 TL 8.00 PV Pipe: 2 -64.1 2.203 PL 8.00 PF 0.2 2 18.0 7.5 18.0 32.1 5.4 120 FTG PE 0.0 3 18.0 7.5 18.3 32.3 0.030 TL 8.00 PV Pipe: 3 -96.3 2.203 PL 8.00 PF 0.5 3 18.0 7.5 18.3 32.3 8.1 120 FTG PE 0.0 4 18.0 7.5 18.8 32.7 0.064 TL 8.00 PV Pipe: 4 -129.1 2.203 PL 8.00 PF 0.9 4 18.0 7.5 18.8 32.7 10.9 120 FTG PE 0.0 5 18.0 7. 5 19.7 33.5 0 .110 TL 8.00 PV Pipe: 5 -162.5 2.203 PL 8.00 PF 1. 4 5 18.0 7.5 19.7 33.5 13.7 120 FTG PE 0.0 6 18.0 7.5 21. 0 34.6 0.169 TL 8.00 PV Pipe: 6 -197.2 2.203 PL 8.00 PF 1. 9 6 18.0 7.5 21. 0 34.6 16.6 120 FTG PE 0.0 7 18.0 7.5 23.0 36.2 0.242 TL 8.00 PV Pipe: 7 -233.3 2.203 PL 6.00 PF 7.8 7 18.0 7.5 23.0 36.2 19.6 120 FTG TL PE 0.0 8 18.0 0.0 30.8 0.0 0.330 TL 23.73 PV Pipe: 8 -34.1 2.203 PL 8.00 PF 0.1 9 18.0 7.5 20.4 34.1 2.9 120 FTG PE 0.0 10 18.0 7.5 20.4 34.1 0.009 TL 8.00 PV Pipe: 9 -68.2 2.203 PL 8.00 PF 0.3 10 18.0 7.5 20.4 34.1 5.7 120 FTG PE 0.0 11 18.0 7.5 20.7 34.4 0.034 TL 8.00 PV Pipe: 10 -102.6 2.203 PL 8.00 PF 0.6 11 18.0 7.5 20.7 34.4 8.6 120 FTG PE 0.0 12 18.0 7.5 21.3 34.8 0.072 TL 8.00 PV Pipe: 11 -137.4 2. 203 PL 8.00 PF 1.0 12 18.0 7.5 21.3 34.8 11. 6 120 FTG PE 0.0 13 18.0 7.5 22.3 35.6 0.124 TL 8.00 PV Pipe: 12 -173.0 2.203 PL 8.00 PF 1. 5 13 18.0 7.5 22.3 35.6 14.6 120 FTG PE 0.0 14 18.0 7.5 23.8 36.8 0.190 TL 8.00 PV Pipe: 13 -209.8 2.203 PL 8.00 PF 2.2 14 18.0 7.5 23.8 36.8 17.7 120 FTG PE 0.0 15 18.0 7.5 26.0 38.5 0. 271 TL 8.00 PV . -------~--· -·--·--· -· SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: . 33/3000 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 -248.3 2.203 PL 6.00 PF 8.8 15 18.0 7. 5 26.0 38.5 20.9 120 FTG TL PE 0.0 16 18.0 0.0 34.8 0.0 0. 371 TL 23.73 PV Pipe: 15 163.9 2.203 PL 8.00 PF 1. 4 16 18.0 0.0 34.8 0.0 13. 8 120 FTG PE 0.0 17 18.0 7.5 33.4 43.6 0 .172 TL 8.00 PV Pipe: 16 120.2 2.203 PL 8.00 PF 0.8 17 18.0 7. 5 33.4 43.6 10.1 120 FTG PE 0.0 18 18.0 7.5 32.6 43.1 0.097 TL 8.00 PV Pipe: 17 77.1 2.203 PL 8.00 PF 0.3 18 18.0 7.5 32.6 43.1 6.5 120 FTG PE 0.0 19 18.0 7.5 32.3 42.9 0.043 TL 8.00 PV Pipe: 18 34.2 2. 203 PL 8.00 PF 0.1 19 18.0 7.5 32.3 42.9 2.9 120 FTG PE 0. 0 20 18.0 7.5 32.2 42.8 0.009 TL 8.00 PV Pipe: 18A -8.6 2.203 PL 8.00 PF 0.0 20 18.0 7.5 32.2 42.8 0.7 120 FTG PE 0.0 21 18.0 7.5 32.2 42.8 0.001 TL 8.00 PV Pipe: 18B -51. 4 2. 203 PL 8.00 PF 0.2 21 18.0 7.5 32.2 42.8 4.3 120 FTG PE 0.0 22 18.0 7. 5 32.4 42.9 0.020 TL 8.00 PV Pipe: 18C -94.4 2.203 PL 8.00 PF 0.5 22 18.0 7.5 32.4 42.9 7.9 120 FTG PE 0.0 23 18.0 7.5 32.9 43.3 0.062 TL 8.00 PV Pipe: 19 -137.7 2. 203 PL 6.00 PF 3.0 23 18.0 7.5 32.9 43.3 11. 6 120 FTG TL PE 0.0 24 18.0 0.0 35.8 0.0 0.124 TL 23.73 PV Pipe: 20 -35.3 2.203 PL 8.00 PF 0.1 25 18.0 7.5 21. 9 35.3 3.0 120 FTG PE 0.0 26 18.0 7.5 22.0 35.4 0.010 TL 8.00 PV Pipe: 21 -70.7 2.203 PL 8.00 PF b.3 26 18.0 7.5 22.0 35.4 6.0 120 FTG PE 0.0 27 18.0 7.5 22.3 35.6 0.036 TL 8.00 PV Pipe: 22 -106.4 2.203 PL 8.00 PF 0. 6 27 18.0 7. 5 22.3 35.6 9.0 120 FTG PE 0.0 28 18.0 7. 5 22.9 36.1 0.077 TL 8.00 PV Pipe: 23 -142.5 2. 203 PL 8.00 PF 1.1 28 18.0 7.5 22.9 36-.1 12.0 120 FTG PE 0.0 29 18.0 7.5 24.0 37.0 0 .133 TL 8.00 PV "'""-~-~-··-~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: . 33 /3000 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: 24 -179.5 2. 203 PL 8.00 PF 1. 6 29 18.0 7.5 24.0 37.0 15.1 120 FTG PE 0. 0 30 18.0 7.5 25.6 38.2 0. 203 TL 8.00 PV Pipe: 25 -217. 6 2.203 PL 8.00 PF 2.3 30 18.0 7. 5 25.6 38.2 18.3 120 FTG PE 0.0 31 18.0 7.5 27.9 39.9 0.290 TL 8.00 PV Pipe: 26 -257.5 2.203 PL 6.00 PF 9.4 31 18.0 7.5 27.9 39.9 21. 7 120 FTG TL PE 0. 0 32 18.0 0. 0 37.3 0.0 0 .396 TL 23.73 PV Pipe: 27 -43.8 2.203 PL 8.00 PF 0.1 33 18.0 7.5 33.7 43.8 3.7 120 FTG PE 0.0 34 18.0 7. 5 33.8 43.9 0.015 TL 8.00 PV Pipe: 28 -87.7 2.203 PL 8.00 PF 0.4 34 18.0 7.5 33.8 43.9 7.4 120 FTG PE 0.0 35 18.0 7.5 34.2 44.2 0.054 TL 8.00 PV Pipe: 29 -131. 9 2.203 PL 8.00 PF 0.9 35 18.0 7.5 34.2 44.2 11.1 120 FTG PE 0. 0 36 18.0 7.5 35.2 44.8 0.115 TL 8.00 PV Pipe: 30 -176.7 2 .203 PL 6.00 PF 4.7 36 18.0 7.5 35.2 44.8 14.9 120 FTG 'rL PE 0.0 37 18.0 0.0 39.8 0.0 0.197 TL 23.73 PV Pipe: 31 -233.3 2.203 PL 12.00 PF 4.0 8 18.0 0.0 30.8 0.0 19.6 120 FTG PE 0.0 16 18.0 0.0 34.8 0.0 0.330 TL 12.00 PV Pipe: 32 -645.5 4.260 PL 12.00 PF 1.0 16 18.0 0.0 34.8 0.0 14.5 120 FTG PE 0.0 24 18.0 0.0 35.8 0.0 0.087 TL 12.00 PV Pipe: 33 -783.2 4.260 PL 12.00 PF 1. 5 24 18.0 0. 0 35.8 0. 0 17.6 120 FTG PE 0.0 32 18.0 0. 0 37.3 0.0 0.125 TL 12.00 PV Pipe: 34 -1040.7 4.260 PL 12.00 PF 2. 5 32 18.0 0. 0 37.3 0.0 23.4 120 F'l'G PE 0.0 37 18.0 0. 0 39.8 0.0 0.212 TL 12.00 PV Pipe: 41 -1217.4 4.260 PL 44.00 PF 17.0 37 18.0 0. 0 39.8 0.0 27.4 120 FTG 2L PE 0. 0 TR 18.0 0.0 56.8 0.0 0.283 TL 60.00 PV Pipe: 42 -1217.4 6.357 PL 20.00 PF 1. 2 TR 18.0 0. 0 56.8 0.0 12.3 120 FTG L PE 7.8 BR 0.0 0. 0 65.9 0.0 0.040 TL 31. 00 PV ~--------·· -···· , ... ··-·· _,., ... , SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 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: 43 -1217.4 6.357 PL 15.00 PF 1. 5 BR 0.0 0.0 65.9 0.0 12.3 120 FTG 2L PE 0.0 Cl 0.0 0.0 67.4 0.0 0.040 TL 37.00 PV Pipe: 44 -1217.4 6.080 PL 15.00 PF 1.0 Cl 0. 0 0.0 67.4 0.0 13.5 150 FTG L PE 0. 0 C2 0. 0 0.0 68.3 0.0 0.033 TL 28.76 PV Pipe: 45 FIXED PRESSURE LOSS DEVICE C3 0.0 0.0 73.3 0.0 5.0 psi, 1217.4 gpm C2 0.0 0.0 68.3 0.0 Pipe: 46 -1217.4 6.080 PL 15.00 PF 2.2 C3 0.0 0.0 73.3 0.0 13.5 150 FTG TG PE 0.0 C4 0.0 0.0 75.5 0.0 0.033 TL 65.47 PV Pipe: 47 -1217.4 9.790 PL 276.00 PF 1.1 C4 0.0 0.0 75.5 0.0 5.2 150 FTG TG PE 0.0 SRC 0.0 SRCE 76.6 (N/A) 0.003 TL 346.04 PV NOTES: (1) Calculations were performed by the HASS 7.4 computer program under license no. 16031158 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 0.002 gpm and a maximum imbalance at any node of 0.094 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 27.4 ft/sec at pipe 41. (4) 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 Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13. 64 13.64 N NPTee 13. 64 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlrnChk DPVlv NPTee 4.260 6.357 PAGE: E Diameter (in) 6.080 9.790 13.00 26.00 8.00 29.00 16.00 3.00 18.00 38.00 11. 00 40.00 13. 00 4.00 MATERIAL: PVC150 HWC: 150 E Ell 21. 41 28.02 Equivalent Fitting Lengths in Feet T L C B G Tee LngEll ChkVlv BfyVlv GatVlv 45.88 13.76 48.94 15.29 4.59 63.67 20.38 70.04 24.20 6.37 26.00 35.00 N NPTee 45.88 63.67 13.00 26.00 24.00 38.00 F 45 10. 71 11. 46 140.0 G112. 0 A u G E p R 84. 0 E s s u R E 56.0 ( p s i ) 28.0 0.0 -14.7 I 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 132.30 psi Resid: 128.70 psi Flow: 1683.0 gpm 1 ~ 2 ~ LEGEND ~"--"""-------------J Available pressure 128.56 psi@ 1717.4 gpm Required pressure 76.59 psi@ 1717.4 gpm 2 ~ I; to 8 M 8 .. H '"'"' t< ----MN '' .. ----() N Pl o " 0 ..., w {/l tr Pl 0, 0 (/J Pl "j ~ Ill ~ C: t< ,-,. M ..., ~ 0, ,-,. (/J " ><: lQ (/J 8 () M :,: ::i: w ><: w tJ ----~ w 0 0 t< 0 H () ~ t< ><: (/J H (/J () ..... ~ (/J (/J ...J .. ..... ...J .. u, "j tl Pl lQ (/J (1) tl "l C, 1200 1400 FLOW (GPM) 1600 1800 2000 , SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/24/2003 C:\HASS74\745D.SDF JOB TITLE: Carlsbad Oaks Building C: .33/3000 WATER SUPPLY CURVE 144+ I I I 132*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 128.7 psi@ 1683 gpm-> * 0 I Flow Test Point I 120+ I I I 108+ I I I P 96+ R I E I s I S 84+ u I R I E I 72+ I p I s I I 60+ l I I I 48+ I I I 36+ I I I============================== 24+ LEGEND I I X = Required Water Supply I 76.59 psi@ 1717.4 gpm 12+ I O = Available Water Supply I 128.56 psi@ 1717.4 gpm I X O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) 3930 East * GENERAL UNDERGROUND FIRE PROT., INC.* ~ Coronado Street, Anaheim, CA 92807 (714) c{<"'8646 * HYDRAULIC DESIGN INFORMATION SHEET* ta Name-,-__ _,CAR,,..,~L~S~B~AD"""----"Q~A~K~S'-"'L~O~T'------'7~,,___,B~L.,_,_._A2.L,__,,AR""'E~A'--'l~:'---'.~3~3~/~3~0"'-"-0~0 __ Date ___ _,0~2~-~~~9~~""'-'"-"-'0i Location 2742 LOKER AVE. WEST, CARLSBAD, CALIFORNIA System No. ------Building A Drawing No._~F~P__.,2'---_ Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No. 745 ~~---Construction: * COMBUSTIBLE --~NON-COMBUSTIBLE Ceiling Ht. ___ ~1~9_f Occupancy STORAGE --------------------------------------------=-----======--=======--===-=======-s y s T __ NFPA 13: __ Lt.Raz. ** Ord.Raz. Gr. __ 1 __ 2 __ 3 ** Ex.Raz. __ NFPA: __ 13D 13R 231 __ 231C Figure _____ Curve. ___ _ ~Other (Specific ruling) .33 GPM/SF OVER 3000 SF l _ Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E :---------------------------------------------------------------------------- M D E s I G Area of Sprinkler operation. __ =3~0~0~0-** SYSTEM TYPE** Density .33 : _*_Wet __ Dry __ Deluge __ Pre-Actior. Area per sprinkler ---=9=2---------------------------------------- Hose allowance GPM: inside __ __.,1=0=0- Hose allowance GPM: outside __ ~4~0~0- Rack sprinklers allowance ** SPRINKLER or NOZZLE** Make TYCO Model TY-L Orifice Size 17/32" K-Factor 8.0 Temperature rating 280 deg CALCULATION SUMMARY GPM required GPM required C-Factor used: 1193.7 PSI required 1693.7 PSI required 78.5 at base of A.S.Rise 90.0 at point of supply. Overhead _ _,._1~2~0 __ _ Underground 150 w .--------------------------------------------------------. A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK* WELL ** Pump Capacity N.A. Pump Pressure Pump Elevation Tank Capacity N.A. Tank Elevation Well Proof Flow N.A. p :--------------------------------------------------------: L y : Location CONNECTION TO 16" CIRC MAIN IN LOKER AVE. WEST : Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT C 0 M M 0 Commodity __________________________________ _ Location ___________________________ : Class. ____ _ Storage Height _______ Aisle width, __________ : Area. _____ _ Storage Method: Solid piled, _____ % Palletized, _____ % Rack. ____ _ Plastics, __________________________________ _ D ·---------------------------------------------------------------------------- I T y :R S :A T :C 0 :K R A G __ Single row __ Conventional __ Double row __ Slave pallet __ Multiple row pallet __ Automatic storage __ Solid shelving __ Open __ Encapsulate __ Non- Encapsulate ·------------------------------------------------------------------------- ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILIN : Longitudinal ___ Transverse __ _____ ft. _____ in. ·-------------------------------------------------------------------------: Horiz. barriers provided E .------------------------------------------------------=----------==--------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet Sprinkler System Analysis Small Sample Output Comments TOTAL FLOW AVAILABLE; Supply pressure is 70.0 PSI1 BUFFER ALLOWED:10%2 Residual pressure is 60.0 PSI at Discharge of 1210 GPM 1. The report indicates the total available supply which includes the static pressure, as well as the residual pressure and volume. This is the total available at the supply point node. NODE NO. ELEVATION FEET SPRK COEF PRESSURE PSI DISCHARGE GPM ---------------------------------------------------------------------- 2. The buffer allowance is included to indicate the percentage or fixed pressure buffer for both the static and residual supply pressures. 3 4 5 6 7 1 15.0 3.85 21.9 18.0 3. Nodes refer to hydraulic reference points. 2 15.0 22.9 4. Elevation measured in feet above datum. 8 3 0.0 30.6 5.0 Hydrant Flow Supply Point 9 4 0.0 35.2 5. K-Factor of open sprinkler or nozzles. 6. Pressure calculated at reference point. 7. Discharge (q) = K x (P)112 8. Hydrant discharge is independant of pressure. 9. Supply point may be anywhere in the system. 10. Only pipes actually flowing water are reported. PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE PSI 11. Q represents total flow in any particular pipe. NO. NODE GPM NO. FITTING TYPE FTG LOSS DIAMETER TOTAL PSI/FT 12. Vf/s is the water velocity in feet per second. 13. Dis the actual internal diameter of the pipe. ----------------------------------------------------------------------14. F refers to the fittings used. The list may be 3 7 5 15 6 applies: 1 q• 18.0 K• 3.85 10.0 Pt 21.9 Pt 21. 9 up to ten characters. The following 110 11 14 16 18 20 letter without number is singular. Q• 18.0 F• o.o C• 120 Pe 0.0 Pv -0.3 A a preceeding 12 1.04913 17 19 21 preceeding is a multiple fitting. Vf/s= 6. 7 D• 10.0 0.1077 Pf 1.1 Pn 21. 6 A number of the A number alone represents its numeric value only. 2' 7 5 15 6 length of pipe shown. q• 0.0 K• 0.00 25.0 Pt 22.9 Pt 22. 9 15. L represents the actual the 2' 11 14 16 18 20 Fitting value is the equivalent footage of pipe. Q• 18.0 F=G2T 14.5 C• 120 Pe 6.5 Pv -0.1 16. Vf/s .. 12 13 17 0.028319 21 22.8 Total is the of fitting value & pipe length. 3.9 D• 1. 380 39.5 Pf 1.1 Pn 17. sum 18. C-factor is the Hazen Williams Coeficient. ,' FLOl.,a 100.015 6 loss foot based formula. q• 5 .0 ADD HYD Pt 30.6 Pt 30.6 19. Friction per on H-W 10 11 F=GLT14 16 18 20 due elevation differential. 3 Q• 23.0 13. 7 C• 150 Pe 0.0 Pv -0.2 20. Pe= pressure loss to 12 1.29113 17 0. 040819 21 loss (length x foot) Vf/s= 5.6 D• 113. 7 Pf 4.6 Pn 30.4 21. Pf• total friction loss per 9 22 Total each node. (Pt+Pe+Pf) 4 <<<<<<<< Supply point >>>>>>>> Pt 35.2 22. Pt• pressure at --------------------------------------------------------------------------------------------------------------------------------- A~alarm va., B~butterfly va., C=cplg, E=short turn elbow, F=45o ell, G=gate va., L=long ell, R=CPVC Tee Run, T=Tee, V=swing check --------------------------------------------------------------------------------------------------------------------------------- Sample Calculation Placard * HYDRAULICALLY DESIGNED AUTOMATIC SPRINKLER SYSTEM INFORMATION Job name: __ ....s===•~BAD.,.,c.eO~ilS=c..eL~O=T-'-7L,c..eB~L~-..... A~,....,,===-='~'~·~'~'Lt~3=0=0=0----- Location: 2742 LOXBR AVB'. PiBST, CARLSBAD, CALIFORNIA Contract No. 745 Drawing No: TP 2 Date: 02-19-2004 This system is designed to discharge at a rate of--~·~'~'-g.p.m. per square foot of floor area over a maximum of 3000 feet when supplied at a rate of----------='='~'~'~·~'- at the base of riser with a pressure of-------~'=•~·=•- square g.p.m. p.s.i. The above information includes hose stream allowance of _o_ g.p.m. 2 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 3 p r e s s u r e p s I CARLSBAD OAKS LOT 7, BL. A, AREA 1: .33/3000 160 144 .. . ..• . .. . :e. 128 --------•••••••••••••·······• ··················· -····--······················· ...... , ........ . D 112 96 G 88.0 80 F .. 64 48 32 16 8 . o-1:l.W.l.UllilllWillillWllWilWWllilllJJ.lllillW..WJillillJWWJlllilllilill.LLUIJIJWWlillllllllillilillillWJlWJlill-800 200 400 600 Water Flow GPM LETTER DESCRIPTION A Static Pressure of 147.0 p.s.i. B Residual Pressure of 143.0 p.s. i. at 1683.0 G.P.M. C = 90.0 percent Static 132.3 p.s.i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s. i. Elev of 19.0 ft. F = Base of Riser Demand 78.5 p.s. i. at 1193.7 G.P.M. G = Point of Conn Demand 90.0 p.s.i. at 1693.7 G.P.M. The City Supply provides 143.0 p.s.i. at 1693.7 G.P.M. which leaves a buffer of 53.0 p.s. i. at system demand. GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 4 PIPE NO. NODE NO. FLOW GPM CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 K-FACTOR CALCULATIONS K-FACTOR FITTING TYPE DIAMETER LENGTH FTG TOTAL FRICTION LOSS PSI/FT PRESSURE PSI NOTES -------------------------------------------------------------------------------1 q= 31. 7 A Q= 31.7 2 K= 8.00 F=T D= 1.080 1.0 5.8 6.8 Pt 15.70 C= 120 Pe 0.00 0.2648 Pf 1.79 Pt 17 .49 1 FT SPRI~ UP K= Q/ (P) • K= 31. 7 0 / ( 1 7 . 4 9 ) • 5 K= 7.58 ------------------------------------------------------------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Sprinkler System Analysis Date: 02-19-04 CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 Sheet TOTAL FLOW AVAILABLE: Static Pressure Residual Pressure at Discharge of 147.0 PSI 143.0 PSI 1683 GPM BUFFER ALLOWED: NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM 5 10 ------------------------------------------------------------------VERSION 3.0-- 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 35 36 37 38 39 40 41 42 43 44 45 46 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 16.1 16.2 16.4 16.9 17.7 18.9 23.0 30.9 21. 8 21. 6 21. 5 16.3 16.3 16.5 17.0 17.8 19.1 23.2 31.1 22.0 21. 8 21. 7 16.7 16.8 17.0 17.5 18.3 19.6 23.8 31.9 22.6 22.3 22.3 17.7 17.7 18.0 18.5 19.4 20.7 25.1 33.6 23.8 23.6 23.5 36.2 36.2 30.4 30.5 30.7 31.2 31.9 33.0 35.4 35.2 35.2 30.6 30.6 30.8 31.3 32.0 33.1 35.5 35.4 35.3 31.0 31.0 31.2 31.7 32.4 33.6 36.0 35.8 35.8 31.9 31.9 32.1 32.6 33.4 34.5 37.0 36.8 36.8 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 NODE NO. 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 ELEVATION FEET 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 17.0 0.0 0.0 0.0 0.0 SPRK COEF PRESSURE PSI 36.2 36.2 36.2 36.2 36.2 36.2 36.2 36.6 39.3 39.3 39.3 39.3 39. 3 39.3 39.3 39.3 39.3 39.8 42.5 42.5 42.5 42.5 42.5 42.5 42.5 42.5 42.5 42.9 45.6 45.6 45.6 45.6 45.6 45.6 46.0 69.3 78.5 80.1 81.1 90.0 DISCHARGE GPM 100.0 400.0 Hydrant Flow Hydrant Flow Supply Point 6 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 7 CARLSBAD OAKS LOT 7' BL. A AREA 1 : CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 1 q= 30.4 K= 7.58 8.0 Pt 16.1 Pt 1 Q= 30.4 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 2.6 D= 2.203 8.0 0.0077 Pf 0.1 Pn ------------ 2 q= 30.5 K= 7.58 8.0 Pt 16.2 Pt 2 Q= 61. 0 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 5.1 D= 2.203 8.0 0.0278 Pf 0.2 Pn ------------ 3 q= 30.7 K= 7.58 8.0 Pt 16.4 Pt 3 Q= 91. 7 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 7.7 D= 2.203 8.0 0.0591 Pf 0.5 Pn ------------ 4 q= 31. 2 K= 7.58 8.0 Pt 16.9 Pt 4 Q= 122.8 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 10.3 D= 2.203 8.0 0.1016 Pf 0.8 Pn ------------ 5 q= 31. 9 K= 7.58 8.0 Pt 17.7 Pt 5 Q= 154.7 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 13.0 D= 2.203 8.0 0.1559 Pf 1.2 Pn ------------ 6 q= 33.0 K= 7.58 4.5 Pt 18.9 Pt 6 Q= 187.7 F=T 13.6 C= 120 Pe 0.0 Pv Vf/s= 15.8 D= 2.203 18.1 0.2230 Pf 4.0 Pn ------------ 7 q= 0.0 K= 0.00 1.0 Pt 23.0 Pt 7 Q= 293.5 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 24.7 D= 2.203 14.6 0.5103 Pf 7.4 Pn 8 Pt 30.9 16.1 -0.0 16.1 16.2 -0.2 16.0 16.4 -0.4 16.0 16.9 -0.7 16.2 17.7 -1.1 16.6 18.9 -1. 7 17.3 23.0 -4.1 18.9 --------------- --------------- --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 9 q= 35.4 K= 7.58 1.5 Pt 21.8 Pt 21.8 8 Q= 105.8 F=T 13.6 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.9 D= 2.203 15.1 0.0773 Pf 1.2 Pn 21.3 7 Pt 23.0 --------------------------------------GENERAL---------------------------------- 10 q= 35.2 K= 7.58 6.0 Pt 21.6 Pt 21.6 9 Q= 70.4 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.9 D= 2.203 6.0 0.0363 Pf 0.2 Pn 21.4 9 Pt 21.8 --------------------------------------GENERAL----------------.----------------- 11 q= 35.2 K= 7.58 6.0 Pt 21.5 Pt 21.5 10 Q= 35.2 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.0 D= 2.203 6.0 0.0100 Pf 0.1 Pn 21.5 10 Pt 21.6 --------------------------------------GENERAL---------------------------------- 12 q= 30.6 K= 7.58 8.0 Pt 16.3 Pt 16.3 11 Q= 30.6 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.6 D= 2.203 8.0 0.0077 Pf 0.1 Pn 16.2 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 8 CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 13 q= 30.6 K= 7.58 8.0 Pt 16.3 Pt 16.3 12 Q= 61.2 F= 0.0 C= 120 Pe 0.0 Pv -0.2 13 14 15 16 17 Vf/s= 5.1 D= 2.203 8.0 0.0280 Pf 0.2 Pn 16.1 14 q= Q= Vf/s= 15 q= Q= Vf/s= 16 q= Q= Vf/s= 17 q= Q= Vf/s= 30.8 K= 7.58 92.0 F= 7.7 D= 2.203 31. 3 K= 7.58 123.3 F= 10.4 D= 2.203 32.0 K= 7.58 155.3 F= 13.1 D= 2.203 33.1 K= 7.58 188.4 F=T 15.9 D= 2.203 ------- 8.0 0.0 8.0 ------- 8.0 0.0 8.0 ------- 8.0 0.0 8.0 ------- 4.5 13.6 18.1 ------- ----- Pt 16.5 Pt C= 120 Pe 0.0 Pv 0.0595 Pf 0.5 Pn ----- Pt 17.0 Pt C= 120 Pe 0.0 Pv 0.1024 Pf 0.8 Pn ----- Pt 17.8 Pt C= 120 Pe 0.0 Pv 0.1570 Pf 1.3 Pn ----- Pt 19.1 Pt C= 120 Pe 0.0 Pv 0.2245 Pf 4.1 Pn ----- 18 q= 0.0 K= 0.00 1.0 Pt 23.2 Pt Q= 294.6 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 24.8 D= 2.203 14.6 0.5138 Pf 7.5 Pn 19 Pt 31.1 16.5 -0.4 16.1 17.0 -0.7 16.3 17.8 -1.1 16.7 19.1 -1. 7 17.4 23.2 -4.1 19.0 --------------- --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 20 q= 35.5 K= 7.58 1.5 Pt 22.0 Pt 22.0 18 Q= 106.2 F=T 13.6 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.9 D= 2.203 15.1 0.0779 Pf 1.2 Pn 21.4 18 Pt 23.2 --------------------------------------GENERAL---------------------------------- 21 q= 35.4 K= 7.58 6.0 Pt 21.8 Pt 21.8 19 Q= 70.7 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.9 D= 2.203 6.0 0.0365 Pf 0.2 Pn 21.5 20 Pt 22.0 --------------------------------------GENERAL---------------------------------- 22 q= 35.3 K= 7.58 6.0 Pt 21.7 Pt 21.7 20 Q= 35.3 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.0 D= 2.203 6.0 0.0101 Pf 0.1 Pn 21.6 21 Pt 21.8 --------------------------------------GENERAL---------------------------------- 23 q= 31.0 K= 7.58 8.0 Pt 16.7 Pt 16.7 21 Q= 31.0 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.6 D= 2.203 8.0 0.0079 Pf 0.1 Pn 16.7 ---------------------------24 q= 31. 0 K= 7.58 8.0 Pt 16.8 Pt 16.8 22 Q= 62.0 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.2 D= 2.203 8.0 0.0287 Pf 0.2 Pn 16.6 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 9 CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 25 q= 31.2 K= 7.58 8.0 Pt 17.0 Pt 17.0 23 Q= 93.3 F= 0.0 C= 120 Pe 0.0 Pv -0.4 24 25 26 27 Vf/s= 7.8 D= 2.203 8.0 0.0611 Pf 0.5 Pn 16.6 26 q= Q= Vf/s= 27 q= Q= Vf/s= 28 q= Q= Vf/s= 31. 7 K= 7.58 125.0 F= 10.5 D= 2.203 32.4 K= 7.58 157.4 F= 13.2 D= 2.203 33.6 K= 7.58 191.0 F=T 16.1 D= 2.203 ------- 8.0 0.0 8.0 ------- 8.0 0.0 8.0 ------- 4.5 13.6 18.1 ------- ----- Pt 17.5 Pt C= 120 Pe 0.0 Pv 0.1050 Pf 0.8 Pn ----- Pt 18.3 Pt C= 120 Pe 0.0 Pv 0.1609 Pf 1. 3 Pn ----- Pt 19.6 Pt C= 120 Pe 0.0 Pv 0.2302 Pf 4.2 Pn ----- 29 q= 0.0 K= 0.00 1.0 Pt 23.8 Pt Q= 298.6 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 25.1 D= 2.203 14.6 0.5268 Pf 7.7 Pn 30 Pt 31.9 17.5 -0.7 16.7 18.3 -1. 2 17.1 19.6 -1. 7 17.9 23.8 -4.2 19.5 --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 31 q= 36.0 K= 7.58 1.5 Pt 22.6 Pt 22.6 28 Q= 107.6 F=T 13.6 C= 120 Pe 0.0 Pv -0.6 Vf/s= 9.1 D= 2.203 15.1 0.0798 Pf 1.2 Pn 22.0 29 Pt 23.8 --------------------------------------GENERAL---------------------------------- 32 q= 35.8 K= 7.58 6.0 Pt 22.3 Pt 22.3 29 Q= 71.6 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 6.0 D= 2.203 6.0 0.0374 Pf 0.2 Pn 22.1 31 Pt 22.6 --------------------------------------GENERAL---------------------------------- 33 q= 35.8 K= 7.58 6.0 Pt 22.3 Pt 22.3 30 Q= 35.8 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.0 D= 2.203 6.0 0.0104 Pf 0.1 Pn 22.2 32 Pt 22.3 --------------------------------------GENERAL---------------------------------- 34 q= 31.9 K= 7.58 8.0 Pt 17.7 Pt 17.7 31 Q= 31.9 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0084 Pf 0.1 Pn 17.6 --------------------------- 35 q= 31. 9 K= 7.58 8.0 Pt 17.7 Pt 17.7 32 Q= 63.8 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0302 Pf 0.2 Pn 17.5 --------------------------- 36 q= 32.1 K= 7.58 8.0 Pt 18.0 Pt 18.0 33 Q= 95.9 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 8.0 0.0643 Pf 0.5 Pn 17.5 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 10 CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 37 q= 32.6 K= 7.58 8.0 Pt 18.5 Pt 18.5 34 Q= 128.5 F= 0.0 C= 120 Pe 0.0 Pv -0.8 35 36 37 Vf/s= 10.8 D= 2.203 8.0 0.1105 Pf 0.9 Pn 17.7 ------------ 38 q= 33.4 K= 7.58 8.0 Pt 19.4 Pt Q= 161. 8 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 13.6 D= 2.203 8.0 0.1694 Pf 1.4 Pn ------------ 39 q= 34.5 K= 7.58 4.5 Pt 20.7 Pt Q= 196.3 F=T 13.6 C= 120 Pe 0.0 Pv Vf/s= 16.5 D= 2.203 18.1 0.2423 Pf 4.4 Pn ------------ 40 q= 0.0 K= 0.00 1.0 Pt 25.1 Pt Q= 307.0 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 25.8 D= 2.203 14.6 0.5543 Pf 8.1 Pn 41 Pt 33.6 19.4 -1. 2 18.1 20.7 -1.8 18.9 25.1 -4.5 20.6 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 42 q= 37.0 K= 7.58 1.5 Pt 23.8 Pt 23.8 38 Q= 110.6 F=T 13.6 C= 120 Pe 0.0 Pv -0.6 Vf/s= 9.3 D= 2.203 15.1 0.0839 Pf 1.3 Pn 23.3 40 Pt 25.1 --------------------------------------GENERAL---------------------------------- 43 q= 36.8 K= 7.58 6.0 Pt 23.6 Pt 23.6 39 Q= 73.6 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.2 D= 2.203 6.0 0.0394 Pf 0.2 Pn 23.3 42 Pt 23.8 --------------------------------------GENERAL---------------------------------- 44 q= 36.8 K= 7.58 6.0 Pt 23.5 Pt 23.5 40 Q= 36.8 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.1 D= 2.203 6.0 0.0109 Pf 0.1 Pn 23.5 43 Pt 23.6 --------------------------------------GENERAL---------------------------------- 74 75 76 77 8 q= 0.0 K= 0.00 11.5 Pt 30.9 Pt 30.9 Q= 293.5 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.5 D= 4.310 11.5 0.0194 Pf 0.2 Pn 30.6 19 q= Q= Vf/s= 30 q= Q= Vf/s= 41 q= 0.0 K= 0.00 588.2 F= 12.9 D= 4.310 0.0 K= 0.00 886.8 F= 19.5 D= 4.310 0.0 K= 0.00 Q=1193.7 F= Vf/s= 26.2 D= 4.310 ------- 11. 5 0.0 11. 5 ------- 11. 5 0.0 11.5 ------- 11. 5 0.0 11.5 ------- ----- Pt 31.1 Pt 31.1 C= 120 Pe 0.0 Pv -1.1 0.0704 Pf 0.8 Pn 30.0 ----- Pt 31.9 Pt 31.9 C= 120 Pe 0.0 Pv -2.6 0.1505 Pf 1. 7 Pn 29.3 ----- Pt 33.6 Pt 33.6 C= 120 Pe 0.0 Pv -4.6 0.2610 Pf 3.0 Pn 29.0 ----- --------------- --------------- --------------- --------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 11 CARLSBAD OAKS LOT 7, BL. A AREA 1: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 54 q= 0.0 K= 0.00 12.0 Pt 36.6 Pt 36.6 78 Q=1193.7 F= 0.0 C= 120 Pe 0.0 Pv -4.6 Vf/s= 26.2 D= 4.310 12.0 0.2610 Pf 3.1 Pn 32.0 64 q= 0.0 K= 0.00 79 Q=1193.7 F= 12.0 0.0 12.0 C= 120 0.2610 Pt Pe Pf 80 81 82 83 Vf/s= 26.2 D= 4.310 74 q= 0.0 K= 0.00 Q=1193.7 F= Vf/s= 26.2 D= 4.310 81 q= 0.0 K= 0.00 Q=1193.7 F=2LF Vf/s= 26.2 D= 4.310 82 q= 0.0 K= 0.00 Q=l193.7 F=2L Vf/s= 12.0 D= 6.385 83 q= 100.0 ADD HYD FLOW Q=1293.7 F=4L Vf/s= 8.3 D= 7.970 84 q= 0.0 K= 0.00 12.0 0.0 12.0 67.0 22.3 89.3 C= 120 0.2610 C= 120 0.2610 Pt Pe Pf Pt Pe Pf 24. 0 Pt 23.1 C= 120 Pe 47.1 0.0385 Pf 85.0 73.9 158.9 C= 150 0.0100 Pt Pe Pf 84 Q=1293.7 F=LGT 20. 0 Pt 73.9 C= 150 Pe 93.9 0.0100 Pf Vf/s= 8.3 D= 7.970 85 q= 400.0 ADD HYD FLOW 75.0 85 Q=1693.7 F=GT 80.2 C= 150 Vf/s= 7.2 D= 9.780 155.2 0.0061 86 <<<<<<<< Supply point>>>>>>>> Pt Pe Pf Pt 39.8 Pt 0.0 Pv 3.1 Pn 42.9 Pt 0.0 Pv 3.1 Pn 46.0 Pt 0. 0 Pv 23. 3 Pn 69. 3 Pt 7.4 Pv 1.8 Pn 78.5 Pt 0.0 Pv 1. 6 Pn 80.l Pt 0 .0 Pv 0.9 Pn 81.1 Pt 0.0 Pv 0.9 Pn 82.0 39.8 -4.6 35.1 42.9 -4.6 38.3 46.0 -4.6 41.4 69.3 -1.0 68.4 78.5 -0.5 78.0 80.1 -0.5 79.6 81.1 -0.4 80.7 FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 90.0 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-1100 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 1 * HYDRAULIC DESIGN INFORMATION SHEET* Name CARLSBAD OAKS LOT 7, BL. A, AREA 2: .33/3000 Date 02-19-2004 Location 2742 LOKER AVE. WEST, CARLSBAD, CALIFORNIA System No. _____ _ Building _ _..,A,_ _______________________ Drawing No. FP 2 Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No._,_7_.,,4..,,5'---- Construction: * COMBUSTIBLE ___ NON-COMBUSTIBLE Ceiling Ht. 19 f Occupancy STORAGE -----------------------------------------------------=------==----====-======== s y s T __ NFPA 13: __ Lt.Raz. ** Ord.Raz. Gr. __ 1 __ 2 __ 3 ** Ex.Raz. 1 __ NFPA: 13D 13R __ 231 __ 231C Figure. _____ Curve. ___ _ ~Other (Specific ruling) .33 GPM/SF OVER 3000 SF Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E ·----------------------------------------------------------------------------M D E s I G Area of Sprinkler operation __ ..,,3-"0~0~0_ ** SYSTEM TYPE** Density .33 : _*_Wet __ Dry __ Deluge __ Pre-Action Area per sprinkler ---~9..,,6_·-------------------------------------- Hose allowance GPM: inside 100 Hose allowance GPM: outside __ __.4..,,0..,,0_ Rack sprinklers allowance ** SPRINKLER or NOZZLE** Make TYCO Model TY-L Orifice Size 17/32" K-Factor 8.0 Temperature rating 280 deg N .---------------------------------------------------------------------------- CALCULATION SUMMARY GPM required GPM required C-Factor used: 1175.5 PSI required 1675.5 PSI required 87.0 at base of A.S.Rise 98.4 at point of supply. Overhead, _ __.,_1~2~0 __ _ Underground 150 w .----------------------------------------------------------------------------A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK * WELL ** Pump Capacity N.A. Pump Pressure Pump Elevation Tank Capacity N.A. Tank Elevation Well Proof Flow N.A. p ·---------------------------------------------------------------------------- L: Location CONNECTION TO 16" CIRC MAIN IN LOKER AVE. WEST Y: Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT C 0 M M 0 Commodity __________________________________ _ Location __________________________ : Class ____ _ Storage Height--.,....,.----,-.,,--Aisle width-::--:-----:---,,------= Area _____ _ Storage Method: Solid piled _____ % Palletized ____ ~% Rack ____ _ Plastics, ___________________________________ _ D ·---------------------------------------------------------------------------- I T y :R S :A T :C 0 :K R __ Single row __ Conventional __ Double row __ Slave pallet __ Multiple row pallet __ Automatic storage __ Solid shelving __ Open __ Encapsulate, __ Non- Encapsulate, ·------------------------------------------------------------------------- ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILINI : Longitudinal. ___ Transverse__ _ ____ ft. _____ in. A ·-------------------------------------------------------------------------G : Horiz. barriers provided ________________________ _ E .---=====--------------===-------------------------=------------------------=· GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 CARLSBAD OAKS LOT 7, BL. A, AREA 2: .33/3000 160 144 128 p r 112 e 96 ........ ·····-·····•·······•··········--············ ··········· . ····················~----·-··········· s s u 88. 01~~~~~~~~~'--'-UF~----r r 80 e p s I 64 48 40.0 32 24.0 16 ...... ' ....... B .. D Sheet 13 8. 0-3J..Jlll.lJWJ.UJ.11UilllilJ.llLLlll.lll.1.lll.ll.L.Ll..UULI.J.J.J..Jc.L.L.LLlllliilllllliJLillJllillilJ.lJJJUlliJIJ.li.LllllllJ.llLLlll.lll.LLU.lll.lllJLU..E 200 400 600 800 1000 1200 1400 1600 1800 2000 Water Flow GPM LETTER DESCRIPTION A = Static Pressure of 147.0 p.s.i. B = Residual Pressure of 143.0 p.s.i. at 1683.0 G.P.M. C = 90.0 percent Static 132.3 p.s.i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s. i. Elev of 19.0 ft. F = Base of Riser Demand 87.0 p.s. i. at 1175.5 G.P.M. G = Point of Conn Demand 98.4 p.s. i. at 1675.5 G.P.M. The City Supply provides 143.0 p.s. i. at 1675.5 G.P.M. which leaves a buffer of 44.6 p.s.i. at system demand. GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Sprinkler System Analysis Date: 02-19-04 CARLSBAD OAKS LOT 7, BL. A AREA 2: CALC .33/3000 Sheet TOTAL FLOW AVAILABLE: Static Pressure Residual Pressure at Discharge of 147.0 PSI 143.0 PSI 1683 GPM BUFFER ALLOWED: NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM 14 10 ------------------------------------------------------------------VERSION 3.0-- 1 18.0 51. 6 2 18.0 51.6 3 18.0 51.6 4 18.0 51. 6 5 18.0 51. 6 6 18.0 51.6 7 18.0 51.6 8 17.0 52.0 9 18.0 51. 6 10 18.0 51.6 11 18.0 51. 6 12 18.0 51. 6 13 18.0 51.6 14 18.0 51. 6 15 18.0 51.6 16 18.0 51. 6 17 18.0 51.6 18 18.0 51.6 19 17.0 52.0 20 18.0 51.6 21 18.0 51.6 22 18.0 51. 6 23 18.0 51. 6 24 18.0 51.6 25 18.0 51.6 26 18.0 51. 6 27 18.0 51.6 28 18.0 51. 6 29 18.0 51.6 30 17.0 52.0 31 18.0 51. 6 32 18.0 51. 6 33 18.0 51. 6 34 18.0 51. 6 35 18.0 51.6 36 18.0 51.6 37 18.0 51. 6 38 18.0 51. 6 39 18.0 51. 6 40 18.0 51.6 41 17.0 52.0 42 18.0 51.6 43 18.0 51. 6 44 18.0 51.6 45 18.0 7.58 17.5 31.7 46 18.0 7.58 17.6 31.8 'GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet CARLSBAD OAKS LOT 7, BL. A AREA 2: CALC .33/3000 NODE NO. 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 ELEVATION FEET 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 17.0 0.0 0.0 0.0 0.0 SPRK COEF 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 PRESSURE PSI 17.8 18.3 19.2 20.4 22.3 24.9 28.4 52.0 17.6 17.7 17.9 18.4 19.3 20.5 22.4 25.0 28.5 52.3 17.9 18.0 18.2 18.8 19.7 20.9 22.8 25.5 29.1 53.2 27.1 27.2 27.5 28.3 29.6 31.4 55.2 77.9 87.0 88.6 89.5 98.4 DISCHARGE GPM 32.0 32.4 33.2 34.2 35.8 37.8 40 .4 31.8 31.9 32.1 32.5 33.3 34.3 35.9 37.9 40.5 32.1 32.2 32.4 32.8 33.6 34.6 36.2 38.3 40.9 39.4 39.5 39.8 40.3 41.2 42.5 100.0 400.0 Hydrant Flow Hydrant Flow Supply Point 15 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 16 CARLSBAD OAKS LOT 7, BL. A AREA 2 : CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3. 0-- 45 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17.5 41 Q= 31. 7 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0083 Pf 0.1 Pn 17.5 ---------------------------46 q= 31.8 K= 7.58 8.0 Pt 17.6 Pt 17.6 42 Q= 63.5 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.3 D= 2.203 8.0 0.0300 Pf 0.2 Pn 17.4 ---------------------------47 q= 32.0 K= 7.58 8.0 Pt 17.8 Pt 17.8 43 Q= 95.5 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.0 D= 2.203 8.0 0.0638 Pf 0.5 Pn 17.4 ---------------------------48 q= 32.4 K= 7.58 8.0 Pt 18.3 Pt 18.3 44 Q= 127.9 F= 0.0 C= 120 Pe o.o Pv -0.8 Vf/s= 10.8 D= 2.203 8.0 0.1096 Pf 0.9 Pn 17.5 --------------------------- 49 q= 33.2 K= 7.58 7.0 Pt 19.2 Pt 19.2 45 Q= 161. 2 F= 0.0 C= 120 Pe 0.0 Pv -1. 2 Vf/s= 13.6 D= 2.203 7.0 0.1681 Pf 1. 2 Pn 18.0 --------------------------- 50 q= 34.2 K= 7.58 8.0 Pt 20.4 Pt 20.4 46 Q= 195.4 F= 0.0 C= 120 Pe 0.0 Pv -1.8 Vf/s= 16.4 D= 2.203 8.0 0.2401 Pf 1.9 Pn 18.6 --------------------------- 51 q= 35.8 K= 7.58 8.0 Pt 22.3 Pt 22.3 47 Q= 231.2 F= 0.0 C= 120 Pe 0.0 Pv -2.5 Vf/s= 19.5 D= 2.203 8.0 0.3279 Pf 2.6 Pn 19.8 --------------------------- 52 q= 37.8 K= 7.58 8.0 Pt 24.9 Pt 24.9 48 Q= 269.0 F= 0.0 C= 120 Pe 0.0 Pv -3.4 Vf/s= 22.6 D= 2.203 8.0 0.4342 Pf 3.5 Pn 21. 5 --------------------------- 53 q= 40.4 K= 7.58 14. 0 Pt 28.4 Pt 28.4 49 Q= 309.4 F=TT 27.3 C= 120 Pe 0.4 Pv -4.6 Vf/s= 26.0 D= 2.203 41. 3 0.5623 Pf 23.2 Pn 23.8 54 Pt 52.0 --------------------------------------GENERAL---------------------------------- 55 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 50 Q= 31. 8 F= 0.0 C= 120 Pe 0.0 Pv -o·. o Vf/s= 2.7 D= 2.203 8.0 0.0083 Pf 0.l Pn 17.6 --------------------------- 56 q= 31. 9 K= 7.58 8.0 Pt 17.7 Pt 17.7 51 Q= 63.7 F= 0.0 C= 120 Pe o.o Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0301 Pf 0.2 Pn 17.5 --------------------------- 57 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 17.9 52 Q= 95.7 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 8.0 0.0641 Pf 0.5 Pn 17.5 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 17 CARLSBAD OAKS LOT 7' BL. A AREA 2 : CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0--58 q= 32.5 K= 7.58 8.0 Pt 18.4 Pt 18.4 53 Q= 128.3 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.8 D= 2.203 8.0 0.1102 Pf 0.9 Pn 17.6 ---------------------------59 q= 33.3 K= 7.58 7.0 Pt 19.3 Pt 19.3 54 Q= 161.6 F= 0.0 C= 120 Pe 0.0 Pv -1. 2 Vf/s= 13.6 D= 2.203 7.0 0.1689 Pf 1. 2 Pn 18.1 --------------------------- 60 q= 34.3 K= 7.58 8.0 Pt 20.5 Pt 20.5 55 Q= 195.9 F= 0.0 C= 120 Pe 0.0 Pv -1.8 Vf/s= 16.5 D= 2.203 8.0 0.2413 Pf 1.9 Pn 18.7 ---------------------------61 q= 35.9 K= 7.58 8.0 Pt 22.4 Pt 22.4 56 Q= 231.8 F= 0.0 C= 120 Pe 0.0 Pv -2.6 Vf/s= 19.5 D= 2.203 8.0 0.3295 Pf 2.6 Pn 19.9 --------------------------- 62 q= 37.9 K= 7.58 8.0 Pt 25.0 Pt 25.0 57 Q= 269.7 F= 0.0 C= 120 Pe 0.0 Pv -3. 5 Vf/s= 22.7 D= 2.203 8.0 0.4363 Pf 3.5 Pn 21. 6 ---------------------------63 q= 40.5 K= 7.58 14.0 Pt 28.5 Pt 28.5 58 Q= 310.2 F=TT 27.3 C= 120 Pe 0.4 Pv -4.6 Vf/s= 26.1 D= 2.203 41.3 0.5650 Pf 23.3 Pn 24.0 64 Pt 52.3 --------------------------------------GENERAL---------------------------------- 65 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 17.9 59 Q= 32.1 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn 17.9 ---------------------------66 q= 32.2 K= 7.58 8.0 Pt 18.0 Pt 18.0 60 Q= 64.3 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0306 Pf 0.2 Pn 17.8 --------------------------- 67 q= 32.4 K= 7.58 8.0 Pt 18.2 Pt 18.2 61 Q= 96.6 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 8.0 0.0652 Pf 0.5 Pn 17.8 --------------------------- 68 q= 32.8 K= 7.58 8.0 Pt 18.8 Pt 1~.8 62 Q= 129.5 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.9 D= 2.203 8.0 0.1121 Pf 0.9 Pn 18.0 --------------------------- 69 q= 33.6 K= 7.58 7.0 Pt 19.7 Pt 19.7 63 Q= 163.1 F= 0.0 C= 120 Pe 0.0 Pv -1.3 Vf/s= 13.7 D= 2.203 7.0 0.1719 Pf 1.2 Pn 18.4 --------------------------- 70 q= 34.6 K= 7.58 8.0 Pt 20.9 Pt 20.9 64 Q= 197.7 F= 0.0 C= 120 Pe 0.0 Pv -1. 9 Vf/s= 16.6 D= 2. 203 8.0 0.2455 Pf 2.0 Pn 19.0 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 18 CARLSBAD OAKS LOT 7, BL. A AREA 2: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 71 q= 36.2 K= 7.58 8.0 Pt 22.8 Pt 22.8 65 Q= 234.0 F= 0.0 C= 120 Pe 0.0 Pv -2.6 66 67 Vf/s= 19.7 D= 2.203 8.0 0.3352 Pf 2.7 Pn 20.2 ------------ 72 q= 38.3 K= 7.58 8.0 Pt 25.5 Pt Q= 272.2 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 22.9 D= 2.203 8.0 0.4439 Pf 3.6 Pn ------------ 73 q= 40.9 K= 7.58 14.0 Pt 29.1 Pt Q= 313.1 F=TT 27.3 C= 120 Pe 0.4 Pv Vf/s= 26.3 D= 2.203 41.3 0.5748 Pf 23.7 Pn 74 Pt 53.2 25.5 -3.5 22.0 29.1 -4.7 24.4 --------------- --------------- --------------------------------------GENERAL---------------------------------- 68 69 70 71 72 73 75 q= 39.4 K= 7.58 8.0 Pt 27.1 Pt 27.1 Q= 39.4 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.3 D= 2.203 8.0 0.0124 Pf 0.1 Pn 27.0 ------------ 76 q= 39.5 K= 7.58 8.0 Pt 27.2 Pt Q= 78.9 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 6.6 D= 2.203 8.0 0.0448 Pf 0.4 Pn ------------ 77 q= 39.8 K= 7.58 8.0 Pt 27.5 Pt Q= 118.7 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 10.0 D= 2.203 8.0 0.0954 Pf 0.8 Pn ------------ 78 q= 40.3 K= 7.58 8.0 Pt 28.3 Pt Q= 159.0 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 13.4 D= 2.203 8.0 0.1640 Pf 1. 3 Pn ------------ 79 q= 41. 2 K= 7.58 7.0 Pt 29.6 Pt Q= 200.3 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 16.9 D= 2.203 7.0 0.2514 Pf 1.8 Pn ------------ 80 CJ'.= 42.4 K= 7.58 38.0 Pt 31.4 Pt Q= 242.7 F=TT 27.3 C= 120 Pe 0.4 Pv Vf/s= 20.4 D= 2.203 65.3 0.3588 Pf 23.4 Pn 81 Pt 55.2 27.2 -0.3 26.9 27.5 -0.7 26.9 28.3 -1. 2 27.1 29.6 -1. 9 27.7 31.4 -2.8 28.6 --------------- --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 54 q= 0.0 K= 0.00 12.0 Pt 52.0 Pt 52.0 78 Q= 309.4 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.8 D= 4.310 12.0 0.0214 Pf 0.3 Pn 51.7 --------------------------- 64 q= 0.0 K= 0.00 12.0 Pt 52.3 Pt 52.3 79 Q= 619.6 F= 0.0 C= 120 Pe 0.0 Pv -1. 2 Vf/s= 13.6 D= 4.310 12.C 0.0775 Pf 0.9 Pn 51.1 ---------------------------74 q= 0.0 K= 0.00 12.0 Pt 53.2 Pt 53.2 80 Q= 932.7 F= 0.0 C= 120 Pe 0.0 Pv -2.8 Vf/s= 20.5 D= 4.310 12.0 0.1653 Pf 2.0 Pn 50.4 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 19 CARLSBAD OAKS LOT 7, BL. A AREA 2: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 81 q= 0.0 K= 0.00 67.0 Pt 55.2 Pt 55.2 81 Q=ll75.5 F=2LF 22.3 C= 120 Pe 0.0 Pv -4.5 Vf/s= 25.8 D= 4.310 89.3 0.2536 Pf 22.7 Pn 50.7 ---------------------------82 q= 0.0 K= 0.00 24.0 Pt 77.9 Pt 77.9 82 Q=ll75.5 F=2L 23.1 C= 120 Pe 7.4 Pv -0.9 Vf/s= 11.8 D= 6.385 47.1 0.0374 Pf 1.8 Pn 76.9 ---------------------------83 q= 100.0 ADD HYD FLOW 85.0 Pt 87.0 Pt 87.0 83 Q=l275.5 F=4L 73.9 C= 150 Pe 0.0 Pv -0.5 Vf/s= 8.2 D= 7.970 158.9 0.0098 Pf 1.6 Pn 86.5 ---------------------------84 q= 0.0 K= 0.00 20.0 Pt 88.6 Pt 88.6 84 Q=l275.5 F=LGT 73.9 C= 150 Pe 0.0 Pv -0.5 Vf/s= 8.2 D= 7.970 93.9 0.0098 Pf 0.9 Pn 88.1 ---------------------------85 q= 400.0 ADD HYD FLOW 75.0 Pt 89.5 Pt 89.5 85 Q=l675.5 F=GT 80.2 C= 150 Pe 0.0 Pv -0.3 Vf/s= 7.2 D= 9.780 155.2 0.0060 Pf 0.9 Pn 89.1 86 <<<<<<<< Supply point >>>>>>>> Pt 90.4 ---------------------------FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 98.4 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-ll0C • * GENERAL UNDERGROUND FIRE PROT., INC. * ~ 3930 East Coronado Street, Anaheim, CA 92807 (714) 63~~6 * HYDRAULIC DESIGN INFORMATION SHEET * ~ Name CARLSBAD OAKS LOT 7, BLDG. B: CALC .33/3000 Date 02-19-~ Location 2744 LOKER AVE. WEST, CARLSBAD, CALIFORNIA System No. _____ 7_ Building _ _,,B'---________________________ Drawing No. FP 3 Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No. 745 -'--"-"----Construction: * COMBUSTIBLE ___ NON-COMBUSTIBLE Ceiling Ht. ___ =1~9_f Occupancy STORAGE ----------------------------------------------------------------------=--======: s y s T __ NFPA 13: __ Lt.Raz. ** Ord.Raz. Gr. __ 1 __ 2 __ 3 ** Ex.Raz. 1 __ . __ NFPA: __ 13D 13R __ 231 __ 231C Figure. _____ Curve ___ _ ~Other (Specific ruling) .33 GPMISF OVER 3000 SF Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E ·---------------------------------------------------------------------------- M D E s I G Area of Sprinkler operation __ =3=0=0=0-** SYSTEM TYPE** Density .33 : _*_Wet __ Dry __ Deluge __ Pre-Action Area per sprinkler ---=9=6_:--------------------------------------· Hose allowance GPM: inside 100 Hose allowance GPM: outside __ ~4=0=0- Rack sprinklers allowance ** SPRINKLER or NOZZLE** Make TYCO Model TY-L Orifice Size 17/32n K-Factor 8.0 Temperature rating 280 deg N .----------------------------------------------------------------------------- CALCULATION SUMMARY GPM required 1100.1 PSI required 88.5 at base of A.S.Rise1 GPM required 1600.1 PSI required 101.0 at point of supply. C-Factor used: Overhead_-=1=2=0___ Underground 150 w .-=------------------------------------------------------. A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK * WELL ** Pump Capacity N.A. Pump Pressure Pump Elevation Tank Capacity N.A. Tank Elevation Well Proof Flow N.A. p :--------------------------------------------------------: L y : Location CONNECTION TO 16n CIRC MAIN IN LOKER AVE. WEST : Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT C 0 M M 0 Commodity __________________________________ _ Location. ___________________________ : Class _____ _ Storage Height---,-------,--,---Aisle width __________ : Area _____ _ Storage Method: Solid piled _____ % Palletized ____ ~% Rack _____ % Plastics ___________________________________ _ D ·----------------------------------------------------------------------------- I T y :R S :A T :C 0 :K R A G __ Single row __ Conventional __ Double row __ Slave pallet __ Multiple row pallet __ Automatic storage __ Solid shelving __ Open __ Encapsulated __ Non- Encapsulated ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILING : Longitudinal ___ Transverse __ _____ ft. _____ in. : Horiz. barriers provided E .-=------------------------------------------------------------------====-=--- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet Sprinkler System Analysis Small Sample Output TOTAL FLOW AVAILABLE: Supply pressure is 70.0 PSI 1 BUFFER ALLOWED:10%2 Residual pressure is 60.0 PSI at Discharge of 1210 GPM NODE NO. ELEVATION FEET SPRK COEF PRESSURE PSI DISCHARGE GPM ----------------------------------------------------------------------3 4 5 6 7 1 15.0 3.85 21. 9 18.0 2 15.0 22.9 3 0.0 30.6 5.0 Hydrant Flow 8 4 0.0 35.2 Supply Point 9 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FI'ITING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT ---------------------------------------------------------------------- 1' q= 18.0 7 K= 3.85 5 10.0 15 Pt 21.9 6 Pt 21. 9 10 11 14 16 18 20 Comments 1. The report indicates the total available supply which includes the static pressure, as well as the residual pressure and volume. This is the total available at the supply point node. 2. The buffer allowance is included to indicate the percentage or fixed pressure buffer for both the static and residual supply pressures. 3. Nodes refer to hydraulic reference points. 4. Elevation measured in feet above datum. 5. K-Factor of open sprinkler or nozzles. 6. Pressure calculated at reference • I I I 112 7. Discharge q = K x P) point. 8. Hydrant discharge is independant of pressure. 9. Supply point may be anywhere in the system. 10. Only pipes actually flowing water are reported. 11. Q represents total flow in any particular pipe. 12. Vf/s is the water velocity in feet per second. 13. Dis the actual internal diameter of the pipe. 14. F refers to the fittings used. The list may be up to ten characters. The following applies: ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) 1 Q= 18.0 F= 0.0 C= 120 Pe 0.0 Pv -0.3 12 13 17 19 21 A letter without a preceeding number is singular. } Vf/s= 6.7 o. 1.049 10.0 0 .1077 Pf 1.1 Pn 21.6 A preceeding number is a multiple of the fitting. 3 7 5 15 6 2 q= 0.0 K= 0.00 25.0 Pt 22.9 Pt 22.9 29 11 FmG2T14 16 18 20 Q= 18.0 14.5 c. 120 Pe 6.5 Pv -0.1 12 1. 38013 17 0.028319 21 Vf/s= 3.9 D= 39.5 Pf 1.1 Pn 22.8 A number alone represents its numeric value only. 15. L represents the actual length of the pipe shown. 16. Fitting value is the equivalent footage of pipe. 17. Total is the sum of fitting value & pipe length. 3 FLOWS 100.015 6 3 q• 5.0 ADD HYO Pt 30.6 Pt 30.6 10 11 14 16 15018 20 -0.2 3 Q= 23.0 F=GLT 13.7 C= Pe 0.0 Pv 12 1.29113 17 0.040819 21 Vf/s= 5.6 o-113. 7 Pf 4.6 Pn 30.4 49 22 <<<<<<<< Supply point >>>>>>>> Pt 35.2 18. C-factor is the Hazen Williams Coeficient. 19. Friction loss per foot based on H-W formula. 20. Pe= pressure loss due to elevation differential. 21. Pf= total friction loss (length x loss per foot) 22. Pt= Total pressure at each node. (Pt+Pe+Pf) ---------------------------------------------------------------------------------------------------------------------------- ) ) ) ) ) ) ) ) ) ) A=alarm va., B=butterfly va., C=cplg, E=short turn elbow, F=45o ell, G=gate va., L=long ell, R=CPVC Tee Run, T=Tee, v~swing check --------------------------------------------------------------------------------------------------------------------------------- Sample Calculation Placard * HYDRAULICALLY DESIGNED AtrrOMATIC SPRINKLER SYSTEM INFORMATION* Job name: __ _sCARL,,,.e,eS~BADe,ec.,O~.U:e,eS:....,L~O~T'--'-7~,_,B~LDG""'~·-"B~,--"CAL'°=~C~.~3~3~/~3~0~0~0c_ ___ _ Location: 2744 LOUR AVB'. WEST, CARLSBAD, CALIFORNIA Contract No. 745 Drawing No: FP 3 Date: 02-19-2004 This system is designed to discharge at a rate of--~-~•~•- per square foot of floor area over a maximum of---~•~•~•~•'- feet when supplied at a rate of ----------~1~1~•~•~-~1~ at the base of riser with a pressure of-------~•~•~-~•'-- g.p.m. square g.p.m. p.a. i. The above information includes hose stream allowance of _o_ g.p.m. 2 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet p r e s s u r e p s I CARLSBAD OAKS LOT 7, BLDG. B: CALC .33/3000 160 128-~~-~-~--~-~·----~--~----~----------~---~---~-------~----------~---~···-···~---~----~---~-~-~-~--~---~----~---~---~---,._.,.,.,.,.,.,_.,;~D 120.0 112 96 80 64 56.0 48 40.0 32 24.0 16 8. 0 G 200 400 600 800 1000 1200 1400 1600 1800 Water Flow GPM LETTER DESCRIPTION A = Static Pressure of 147.0 p.s.i. B Residual Pressure of 143.0 p.s.i. at 1683.0· G.P.M. C = 90.0 percent Static 132.3 p.s.i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s.i. Elev of 19.0 ft. F = Base of Riser Demand 88.5 p.s.i. at 1100.1 G.P.M. G = Point of Conn Demand 101. 0 p.s.i. at 1600.1 G.P.M. The City Supply provides 143.4 p.s. i. at 1600.1 G.P.M. which leaves a buffer of 42.4 p.s.i. at system demand. 2000 3 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 4 PIPE NO. NODE NO. FLOW GPM CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 K-FACTOR CALCULATIONS K-FACTOR FITTING TYPE DIAMETER LENGTH FTG TOTAL FRICTION LOSS PSI/FT PRESSURE PSI NOTES -------------------------------------------------------------------------------1 q= 31. 7 K= A Q= 31. 7 F=T D= 2 8.00 1.080 1. 0 5.8 6.8 Pt 15.70 C= 120 Pe 0.00 0.2648 Pf 1.79 Pt 17.49 1 FT SPRig UP K= Q/(P) • K= 31.70/( 17.49) •5 K= 7.58 ------------------------------------------------------------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Sprinkler System Analysis Date: 02-19-04 CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 Sheet TOTAL FLOW AVAILABLE: Static Pressure Residual Pressure at Discharge of 147.0 PSI 143.0 PSI 1683 GPM BUFFER ALLOWED: NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM 5 10 % ------------------------------------------------------------------VERSION 3.0-- 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 35 36 37 38 39 40 41 42 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 17.0 18.0 18.0 18.0 18.0 18.0 17.0 17.0 17.0 0.0 0.0 0.0 0.0 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 7.58 17.5 17.5 17.6 17.8 18.1 18.6 19.3 20.2 21.4 37.5 17.6 17.6 17.7 17.9 18.2 18.7 19.4 20.4 21. 6 37.7 18.0 18.1 18.2 18.3 18.7 19.2 19.9 20.8 22.1 38.6 30.5 30.6 30.7 31. 0 31. 6 40.4 48.1 79.5 88.5 89.5 90.3 101.0 31.7 31.7 31.8 32.0 32.3 32.7 33.3 34.1 35.1 31. 8 31.8 31. 9 32.1 32.4 32.8 33.4 34.2 35.2 32.2 32.2 32.3 32.5 32.8 33.2 33.8 34.6 35.6 41.9 41.9 42.0 42.2 42.6 100.0 400.0 Hydrant Flow Hydrant Flow Supply Point GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 6 CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 1 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17.5 1 Q= 31. 7 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 1. 8 D= 2.703 8.0 0.0031 Pf 0.0 Pn 17.5 ---------------------------2 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17.5 2 Q= 63.4 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.5 D= 2.703 8.0 0.0110 Pf 0.1 Pn 17.4 --------------------------- 3 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 3 Q= 95.3 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.3 D= 2.703 8.0 0.0234 Pf 0.2 Pn 17.4 ---------------------------4 q= 32.0 K= 7.58 8.0 Pt 17.8 Pt 17.8 4 Q= 127.2 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 7.1 D= 2.703 8.0 0.0401 Pf 0.3 Pn 17.5 ---------------------------5 q= 32.3 K= 7.58 8.0 Pt 18.1 Pt 18.1 5 Q= 159.5 F= 0.0 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.9 D= 2.703 8.0 0.0609 Pf 0.5 Pn 17.6 ---------------------------6 q= 32.7 K= 7.58 8.0 Pt 18.6 Pt 18.6 6 Q= 192.2 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.7 D= 2.703 8.0 0.0860 Pf 0.7 Pn 17.8 ---------------------------7 q= 33.3 K= 7.58 8.0 Pt 19.3 Pt 19.3 7 Q= 225.5 F= 0.0 C= 120 Pe 0.0 Pv -1.1 Vf/s= 12.6 D= 2.703 8.0 0.1157 Pf 0.9 Pn 18.2 --------------------------- 8 q= 34.1 K= 7.58 8.0 Pt 20.2 Pt 20.2 8 Q= 259.6 F= 0.0 C= 120 Pe 0.0 Pv -1.4 Vf/s= 14.5 D= 2.703 8.0 0.1501 Pf 1. 2 Pn 18.8 --------------------------- 9 q= 35.1 K= 7.58 45.0 Pt 21. 4 Pt 21.4 9 Q= 294.7 F=TT 37.3 C= 120 Pe 0.4 Pv -1. 8 Vf/s= 16.5 D= 2.703 82.3 0.1898 Pf 15.6 Pn 19.6 10 Pt 37.5 --------------------------------------GENERAL---------------------------------- 11 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 10 Q= 31. 8 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 1. 8 D= 2.703 8.0 0.0031 Pf 0.0 Pn 17.6 --------------------------- 12 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 11 Q= 63.7 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.6 D= 2.703 8.0 0.0111 Pf 0.1 Pn 17.6 --------------------------- 13 q= 31. 9 K= 7.58 8.0 Pt 17.7 Pt 17.7 12 Q= 95.6 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.3 D= 2.703 8.0 0.0236 Pf 0.2 Pn 17.5 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 7 CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 14 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 17.9 13 Q= 127.7 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 7.1 D= 2.703 8.0 0.0403 Pf 0.3 Pn 17.6 ---------------------------15 q= 32.4 K= 7.58 8.0 Pt 18.2 Pt 18.2 14 Q= 160.0 F= 0.0 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.9 D= 2.703 8.0 0.0613 Pf 0.5 Pn 17.7 --------------------------- 16 q= 32.8 K= 7.58 8.0 Pt 18.7 Pt 18.7 15 Q= 192.8 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.8 D= 2.703 8.0 0.0866 Pf 0.7 Pn 17.9 ---------------------------17 q= 33.4 K= 7.58 8.0 Pt 19.4 Pt 19.4 16 Q= 226.2 F= 0.0 C= 120 Pe 0.0 Pv -1.1 Vf/s= 12.6 D= 2.703 8.0 0.1164 Pf 0.9 Pn 18.3 --------------------------- 18 q= 34.2 K= 7.58 8.0 Pt 20.4 Pt 20.4 17 Q= 260.4 F= 0.0 C= 120 Pe 0.0 Pv -1. 4 Vf/s= 14.6 D= 2.703 8.0 0.1510 Pf 1. 2 Pn 18.9 --------------------------- 19 q= 35.2 K= 7.58 45.0 Pt 21. 6 Pt 21. 6 18 Q= 295.6 F=TT 37.3 C= 120 Pe 0.4 Pv -1. 8 Vf/s= 16.5 D= 2.703 82.3 0.1910 Pf 15.7 Pn 19.7 20 Pt 37.7 --------------------------------------GENERAL---------------------------------- 21 q= 32.2 K= 7.58 8.0 Pt 18.0 Pt 18.0 19 Q= 32.2 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 1. 8 D= 2.703 8.0 0.0031 Pf 0.0 Pn 18.0 --------------------------- 22 q= 32.2 K= 7.58 8.0 Pt 18.1 Pt 18.1 20 Q= 64.4 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.6 D= 2.703 8.0 0.0114 Pf 0.1 Pn 18.0 --------------------------- 23 q= 32.3 K= 7.58 8.0 Pt 18.2 Pt 18.2 21 Q= 96.7 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.703 8.0 0.0241 Pf 0.2 Pn 18.0 --------------------------- 24 q= 32.5 K= 7.58 8.0 Pt 18.3 Pt 18.3 22 Q= 129.2 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 7.2 D= 2. 703 8.0 0.0412 Pf 0.3 Pn 18.0 --------------------------- 25 q= 32.8 K= 7.58 8.0 Pt 18.7 Pt 18.7 23 Q= 161.9 F= 0.0 C= 120 Pe 0.0 Pv -0.6 Vf/s= 9.1 D= 2.703 8.0 0.0626 Pf 0.5 Pn 18.1 --------------------------- 26 q= 33.2 K= 7.58 8.0 Pt 19.2 Pt 19.2 24 Q= 195.1 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.9 D= 2.703 8.0 0.0885 Pf 0.7 Pn 18.4 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 8 CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 27 q= 33.8 K= 7.58 8.0 Pt 19.9 Pt 19.9 25 Q= 228.9 F= 0.0 C= 120 Pe 0.0 Pv -1.1 26 27 Vf/s= 12.8 D= 2.703 8.0 0.1189 Pf 1.0 Pn 18.8 ------------ 28 q= 34.6 K= 7.58 8.0 Pt 20.8 Pt Q= 263.5 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 14.7 D= 2.703 8.0 0.1543 Pf 1. 2 Pn ------------ 29 q= 35.6 K= 7.58 45.0 Pt 22.1 Pt Q= 299.1 F=TT 37.3 C= 120 Pe 0.4 Pv Vf/s= 16.7 D= 2.703 82.3 0.1952 Pf 16.1 Pn 30 Pt 38.6 20.8 -1.5 19.4 22.1 -1. 9 20.2 --------------- --------------- --------------------------------------GENERAL---------------------------------- 28 29 30 31 32 31 q= 41.9 K= 7.58 8.0 Pt 30.5 Pt 30.5 Q= 41.9 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.3 D= 2.703 8.0 0.0051 Pf 0.0 Pn 30.5 ------------ 32 q= 41. 9 K= 7.58 8.0 Pt 30.6 Pt Q= 83.8 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 4.7 D= 2.703 8.0 0.0185 Pf 0.1 Pn ------------ 33 q= 42.0 K= 7.58 8.0 Pt 30.7 Pt Q= 125.8 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 7.0 D= 2.703 8.0 0.0392 Pf 0.3 Pn ------------ 34 q= 42.2 K= 7.58 8.0 Pt 31. 0 Pt Q= 168.0 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 9.4 D= 2.703 8.0 0.0671 Pf 0.5 Pn ------------ 35 q= 42.6 K= 7.58 45.0 Pt 31.6 Pt Q= 210.6 F=TT 37.3 C= 120 Pe 0.4 Pv Vf/s= 11.8 D= 2.703 82.3 0.1019 Pf 8.4 Pn 36 Pt 40.4 30.6 -0.1 30.4 30.7 -0.3 30.4 31. 0 -0.6 30.4 31.6 -0.9 30.6 --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 10 q= 0.0 K= 0.00 12.0 Pt 37.5 Pt 37.5 33 Q= 294.7 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.5 D= 4.310 12.0 0.0196 Pf 0.2 Pn 37.2 --------------------------- 20 q= 0.0 K= 0.00 12.0 Pt 37.7 Pt 37.7 34 Q= 590.3 F= 0.0 C= 120 Pe 0.0 Pv -1.1 Vf/s= 13.0 D= 4.310 12.0 0.0708 Pf 0.9 Pn 36.6 --------------------------- 30 q= 0.0 K= 0.00 12.0 Pt 38.6 Pt 38.6 35 Q= 889.5 F= 0.0 C= 120 Pe 0.0 Pv -2.6 Vf/s= 19.6 D= 4.310 12.0 0.1514 Pf 1. 8 Pn 36.0 --------------------------- 36 q= 0.0 K= 0.00 6.5 Pt 40.4 Pt 40.4 36 Q=ll00.1 F=T 27.9 C= 120 Pe 0.0 Pv -3.9 Vf/s= 24.2 D= 4.310 34.4 0.2243 Pf 7.7 Pn 36.4 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 9 CARLSBAD OAKS, LOT 7, BLDG. B: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL. PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 37 q= 0.0 K= 0.00 115.0 Pt 48.1 Pt 48.1 37 Q=ll00.1 F=3L 25.1 C= 120 Pe 0.0 Pv -3.9 Vf/s= 24.2 D= 4.310 140.1 0.2243 Pf 31.4 Pn 44.2 ---------------------------38 q= 0.0 K= 0.00 24.0 Pt 79.5 Pt 79.5 38 Q=ll00.1 F=2L 23.1 C= 120 Pe 7.4 Pv -0.8 Vf/s= 11. 0 D= 6.385 47.1 0.0331 Pf 1.6 Pn 78.7 --------------------------- 39 q= 100.0 ADD HYD FLOW 60.0 Pt 88.5 Pt 88.5 39 Q=1200.1 F=3L 55.4 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.7 D= 7.970 115.4 0.0087 Pf 1.0 Pn 88.1 ---------------------------40 q= 0.0 K= 0.00 25.0 Pt 89.5 Pt 89.5 40 Q=1200.1 F=LGT 73.9 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.7 D= 7.970 98.9 0.0087 Pf 0.9 Pn 89.1 --------------------------- 41 q= 400.0 ADD HYD FLOW 295.0 Pt 90.3 Pt 90.3 41 Q=1600.1 F=F3GT 106.5 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.4 D= 9.400 401. 5 0.0067 Pf 2.7 Pn 90.0 42 <<<<<<<< Supply point >>>>>>>> Pt 93.0 ---------------------------FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 101. 0 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-1100 ~ 6~646 * GENERAL UNDERGROUND FIRE PROT., INC.* 3930 East Coronado Street, Anaheim, CA 92807 (714) * HYDRAULIC DESIGN INFORMATION SHEET* ~ Name CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 Date 02-~004 Location 2746 LOKER AVE. WEST, CARLSBAD, CALIFORNIA Syst_e_m_N~o-.~~~~~-r=~ Building_~c'-=----=~------,--.,,.------------------Drawing No._F"--"-P_4.,__ __ Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No. 745 ~~---Construction: * COMBUSTIBLE --~NON-COMBUSTIBLE Ceiling Ht. ___ 1=9~f Occupancy STORAGE s y s T __ NFPA 13: __ Lt.Haz. ** Ord.Haz. Gr. __ 1 __ 2 __ 3 ** Ex.Haz. __ 1 __ __ NFPA: __ 13D __ 13R __ 231 __ 231C Figure _____ Curve ___ _ ~Other (Specific ruling) .33 GPM/SF OVER 3000 SF Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E .------------------------------------------------------------------------ M D E s I G Area of Sprinkler operation. __ =3=0=0=0-** SYSTEM TYPE** Density .33 : _*_Wet __ Dry __ Deluge __ Pre-Action Area per sprinkler ---~9=6-·-------------------------------------- Hose allowance GPM: inside 100 ** SPRINKLER or NOZZLE** Hose allowance GPM: outside 400 --~~-Make TYCO Model TY-L Rack sprinklers allowance Orifice Size 17/32" K-Factor 8.0 Temperature rating 280 deg N .-------------------------------------------------~------~-------------------· CALCULATION SUMMARY 97.7 at base of A.S.Risei 110.8 at point of supply. GPM required 1445.1 PSI required GPM required 1945.1 PSI required C-Factor used: Overhead 120 -~~---Underground 150 w .--------------------------------------------------------. A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK* WELL ** Pump Capacity N.A. Pump Pressure Pump Elevation Tank Capacity N.A. Tank Elevation Well Proof Flow N.A. p :--------------------------------------------------------: L y C 0 M M 0 : Location CONNECTION TO 16" CIRC MAIN IN LOKER AVE. WEST : Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT CommoditY----------------------------=--------Location ___________________________ : Class _____ _ Storage Height ____ __,.-c---Aisle width_,.-,,---,----,------= Area _____ _ Storage Method: Solid piled. _____ % Palletized _____ % Rack _____ % Plastics ___________________________________ _ D ·----------------------------------------------------------------------------- I T y __ Single row __ Conventional pallet __ Automatic storage __ Encapsulated __ Double row __ Slave pallet __ Solid shelving Non- :R __ Multiple row __ Open --Encapsulated S :A·-------------------------------------------------------------------------- T :C ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILING O :K: Longitudinal ___ Transverse__ _ ____ ft. _____ in. R A G E : Horiz. barriers provided _________________________ _ .==--==-==---=---=--=-------------------------=------=---=--------------====== GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet Sprinkler System Analysis Small Sample Output TOTAL FLOW AVAILABLE: Supply pressure is 70.0 PSI 1 BUFFER ALLOWED:10%2 Residual pressure is 60. 0 PSI at Discharge of 1210 GPM NODE NO. 1' 2 3 4 PIPE NO. NODE NO. ELEVATION FEET 15.0 4 15.0 o.o o.o SPRK COEF 3.85 FLOW K-FACTOR 5 GPM FITTING TYPE DIAMETER PRESSURE PSI 21.9 6 22.9 30.6 35.2 LENGTH FTG TOTAL DISCHARGE GPM 7 18.0 5.0 Hydrant Flow Supply Point FRICTION PRESSURE LOSS PSI PSI/FT 8 9 ---------------------------------------------------------------------- 1' 7 5 q• 18.0 K• 3.85 10.0 15 Pt 21. 9 6 Pt 2l. 9 Comments 1. The report indicates the total available supply which includes the static pressure, as well as the residual pressure and volume. This is the total available at the supply point node. 2. The buffer allowance is included to indicate the percentage or fixed pressure buffer for both the static and residual supply pressures. 3. Nodes refer to hydraulic reference points. 4. Elevation measured in feet above datum. 5. K-Factor of open sprinkler or nozzles. 6. Pressure calculated at reference 7. Discharge (q) -K x (PJ 112 point. 8. Hydrant discharge is independant of pressure. 9. Supply point may be anywhere in the system. 10, Only pipes actually flowing water are reported. 11. Q represents total flow in any particular pipe. 12. Vf/s is the water velocity in feet per second. 13. Dis the actual internal diameter of the pipe. 14. F refers to the fittings used. The list may be up to ten characters. The following applies: 2 } } } } } } } } } } } } } } } } } } } } 110 Q• 18.0 11 F• 14 a.a 16 C• 12018 Pe o.o 20 Pv -0.3 A letter without a preceeding number is singular. } Vf/s• 6.7 12 D• 1.04913 10.0 17 0.107719 23 q• 0.0 7 K• 0.00 5 25.0 15 9 11 14 16 12018 2 Q• 18.0 F:G2T 14 .5 C• Vf/s= 3.9 12 D• 1. 380 13 39.5 17 o. 02al9 ,' q-5.0 ADD HYD FLOW8 100.0 15 10 3 Q• 23.0 11 F.,GLT 14 13.7 16 c-1so18 Vf/s= 5.6 12 D• 1.29113 113. 7 17 0.040819 ,• <<<<<<<< Supply point >>>>>>>> Pf 1.1 21 Pn Pt 22.9 6 Pt Pe 6.5 20 Pv Pf 1.1 21 Pn Pt 30.6 6 Pt Pe 0.0 20 Pv Pf 4.6 21 Pn Pt 35.2 22 21. 6 22.9 -0.l 22.8 30,6 -0.2 30.4 A preceeding number is a multiple of the fitting. A number alone represents its numeric value only. 15. L represents the actual length of the pipe shown. 16. Fitting value is the equivalent footage of pipe. 17. Total is the sum of fitting value & pipe length. 18. C-factor is the Hazen Williams Coeficient. 19. Friction loss per foot based on H-W formula. 20. Pe• pressure loss due to elevation differential. 21. Pf= total friction loss (length x 22. Pt= Total pressure at each node. loss per foot) (Pt+Pe+Pf) } } } } } } } } } } 0 . k A=alarm va., B•butterfly va., C•cplg, E=short turn elbow, F=45 ell, G=gate va., L•long ell, R=CPVC Tee Run, T=Tee, V=swing chec Sample Calculation Placard • HYDRAULICALLY DESIGNED AUTOMATIC SPRINKLER SYSTEM INFORMATION• Job name : __ __,,CARL,,,,.,.s~BAD,,.c....O~ile,eSc..,L~O~T'-'7~,_,B~LDG=~-_;C~,__,,CAL=~c~.~'~3~/~3~0~0~0'----- Location: 2746 LOJCER AVE'. WEST, CARLSBAD, CALIJ!ORNIA Contract No. 745 Drawing No: PP 4 Date: 02-19-2004 This system is designed to discharge at a rate of .33 g.p.m. per square foot of floor area over a maximum of 3000 square feet when supplied at a rate of 1445. l g.p.m. at the base of riser with a pressure of 97.7 p.s.i. The above information includes hose stream allowance of _o_ g.p.m. GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet p r e s s u r e p s I 160 144 128 112 96 88.0 80 64 48 32 16 8. 0 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 B .. .... , .... G. F 200 400 600 800 1000 1200 1400 1600 1800 2000 Water Flow GPM LETTER DESCRIPTION A = Static Pressure of 147. 0 p.s. i. B Residual Pressure of 143.0 p.s.i. at 1683.0.G.P.M. C 90.0 percent Static 132.3 p.s. i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s.i. Elev of 19.0 ft. F = Base of Riser Demand 97.7 p.s.i. at 1445.1 G.P.M. G Point of Conn Demand 110.8 p.s. i. at 1945.1 G.P.M. The City Supply provides 141.8 p.s. i. at 1945.1 G.P.M. which leaves a buffer of 31. 0 p.s. i. at system demand. 3 = GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 4 PIPE NO. NODE NO. FLOW GPM CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 K-FACTOR CALCULATIONS K-FACTOR FITTING TYPE DIAMETER LENGTH FTG TOTAL FRICTION LOSS PSI/FT PRESSURE PSI NOTES -------------------------------------------------------------------------------1 q= 31. 7 K= A Q= 31.7 F=T D= 2 8.00 1.080 1.0 5.8 6.8 Pt C= 120 Pe 0.2648 Pf Pt 15.70 0.00 1. 79 17.49 1 FT SPRI~ UP K= Q/(P) • K= 31. 7 0 / ( 1 7 . 4 9 ) • 5 K= 7.58 ------------------------------------------------------------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 5 Sprinkler System Analysis CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 TOTAL FLOW AVAILABLE: Static Pressure 147.0 PSI BUFFER ALLOWED: 10 % Residual Pressure 143.0 PSI at Discharge of 1683 GPM NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM ------------------------------------------------------------------VERSION 3.0--1 18.0 7.58 34.4 44.4 2 18.0 7.58 34.5 44.5 3 17.0 36.7 4 18.0 7.58 24.0 37.2 5 18.0 7.58 24.1 37.2 6 18.0 7.58 24.4 37.5 7 18.0 7.58 25.1 38.0 8 18.0 7.58 26.3 38.9 9 18.0 7.58 28.1 40.2 10 17.0 36.7 11 18.0 7.58 17.5 31.7 12 18.0 7.58 17.5 31.7 13 18.0 7.58 17.8 32.0 14 18.0 7.58 18.3 32.4 15 18.0 7.58 19.2 33.2 16 18.0 7.58 20.5 34.3 17 18.0 7.58 22.4 35.9 18 18.0 28.2 19 17.0 36.9 20 18.0 7.58 27.5 39.7 21 18.0 7.58 27.4 39.7 22 18.0 7.58 17.9 32.1 23 18.0 7.58 18.0 32.1 24 18.0 7.58 18.2 32.3 25 18.0 7.58 18.7 32.8 26 18.0 7.58 19.6 33.6 27 18.0 7.58 21. 0 34.7 28 18.0 7.58 23.0 36.3 29 18.0 28.9 30 17.0 37.7 31 18.0 7.58 28.1 40.2 32 18.0 7.58 28.0 40.1 33 18.0 7.58 18.9 32.9 34 18.0 7.58 18.9 33.0 35 18.0 7.58 19.2 33.2 36 18.0 7.58 19.7 33.7 37 18.0 7.58 20.7 34.5 38 18.0 7.58 22.1 35.7 39 18.0 7.58 24.2 37.3 40 18.0 30.4 41 17.0 39.7 42 18.0 7.58 29.6 41. 3 43 18.0 7.58 29.5 41.2 44 18.0 7.58 34.6 44.6 45 18.0 7.58 34.7 44.7 46 18.0 7.58 35.1 44.9 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 NODE NO. ELEVATION FEET SPRK COEF PRESSURE PSI DISCHARGE GPM Sheet 6 -------------------------------------------------------------------------------47 18.0 48 17.0 49 17.0 50 17.0 51 0.0 52 0.0 53 0.0 54 0.0 55 17.0 7.58 36.1 43.2 49.9 87.8 97.7 98.6 99.9 110.8 70.1 45.5 100.0 400.0 Hydrant Flow Hydrant Flow Supply Point GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 7 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 1 q= 44.4 K= 7.58 8.0 Pt 34.4 Pt 34.4 1 Q= 44.4 F= 0.0 C= 120 Pe 0.0 Pv -0.1 2 Vf/s= 3.7 D= 2.203 8.0 0.0155 Pf 0.1 Pn 34.3 2 q= 44.5 K= 7.58 5.0 Pt 34.5 Pt Q= 89.0 F=TT 27.3 C= 120 Pe 0.4 Pv Vf/s= 7.5 D= 2.203 32.3 0.0559 Pf 1.8 Pn 3 Pt 36. 7 34.5 -0.4 34.1 --------------------------------------GENERAL---------------------------------- 4 q= 37.2 K= 7.58 8.0 Pt 24.0 Pt 24.0 3 Q= 37.2 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.1 D= 2.203 8.0 0.0111 Pf 0.1 Pn 24.0 ------------ 5 q= 8.0 Pt 24.1 Pt 24.1 4 Q= 37.2 K= 7.58 74. 4 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.3 D= 2.203 8.0 0.0402 Pf 0.3 Pn 23.9 ------------ 6 q= 37.5 K= 7.58 8.0 Pt 24.4 Pt 24.4 5 Q= 111.9 F= 0.0 C= 120 Pe 0.0 Pv -0.6 Vf/s= 9.4 D= 2.203 8.0 0.0855 Pf 0.7 Pn 23.8 ------------ 7 q= 38.0 K= 7.58 8.0 Pt 25.1 Pt 25.1 6 Q= 149.9 F= 0.0 C= 120 Pe 0.0 Pv -1.1 Vf/s= 12.6 D= 2.203 8.0 0.1470 Pf 1.2 Pn 24.1 ------------ 8 q= 38.9 K= 7.58 8.0 Pt 26.3 Pt 26.3 7 Q= 188.8 F= 0.0 C= 120 Pe 0.0 Pv -1.7 Vf/s= 15.9 D= 2.203 8.0 0.2253 Pf 1. 8 Pn 24.6 ------------ 9 q= 40.2 K= 7.58 5.0 Pt 28.1 Pt 28.1 8 Q= 228.9 F=ET 20.5 C= 120 Pe 0.4 Pv -2.5 Vf/s= 19.3 D= 2.203 25.5 0.3215 Pf 8.2 Pn 25.6 10 Pt 36.7 --------------- --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 11 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17.5 9 Q= 31. 7 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0083 Pf 0.1 Pn 17.4 ---------------------------12 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17·. 5 10 Q= 63.4 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.3 D= 2.203 8.0 0.0299 Pf 0.2 Pn 17.3 --------------------------- 13 q= 32.0 K= 7.58 8.0 Pt 17.8 Pt 17.8 11 Q= 95.4 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.0 D= 2.203 8.0 0.0636 Pf 0.5 Pn 17.3 ---------------------------14 q= 32.4 K= 7.58 8.0 Pt 18.3 Pt 18.3 12 Q= 127.8 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.8 D= 2.203 8.0 0.1094 Pf 0.9 Pn 17.5 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 8 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 15 q= 33.2 K= 7.58 8.0 Pt 19.2 Pt 19.2 13 Q= 161.0 F= 0.0 C= 120 Pe 0.0 Pv -1.2 14 15 16 Vf/s= 13.5 D= 2.203 8.0 0.1677 Pf 1.3 Pn 17.9 ------------ 16 q= 34.3 K= 7.58 8.0 Pt 20.5 Pt Q= 195.3 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 16.4 D= 2.203 8.0 0.2399 Pf 1.9 Pn ------------ 17 q= 35.9 K= 7.58 4.0 Pt 22.4 Pt Q= 231.2 F=T 13.6 C= 120 Pe 0.0 Pv Vf/s= 19.5 D= 2.203 17.6 0.3279 Pf 5.8 Pn ------------ 18 q= 0.0 K= 0.00 1.0 Pt 28.2 Pt Q= 310.6 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 26.1 D= 2.203 14.6 0.5664 Pf 8.3 Pn 19 Pt 36.9 20.5 -1.8 18.7 22.4 -2.5 19.9 28.2 -4.6 23.6 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 20 q= 39.7 K= 7.58 2.0 pt 27.5 Pt 27.5 17 Q= 79.4 F=T 13.6 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.7 D= 2.203 15.6 0.0453 Pf 0.7 Pn 27.2 18 Pt 28.2 --------------------------------------GENERAL---------------------------------- 21 q= 39.7 K= 7.58 8.0 Pt 27.4 Pt 27.4 18 Q= 39.7 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.3 D= 2.203 8.0 0.0125 Pf 0.1 Pn 27.3 20 Pt 27.5 --------------------------------------GENERAL---------------------------------- 22 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 17.9 19 Q= 32.1 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn 17.8 ---------------------------23 q= 32.1 K= 7.58 8.0 Pt 18.0 Pt 18.0 20 Q= 64.2 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0306 Pf 0.2 Pn 17.8 ---------------------------24 q= 32.3 K= 7.58 8.0 Pt 18.2 Pt 18.2 21 Q= 96.5 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 8.0 0.0651 Pf 0.5 Pn 17.8 --------------------------- 25 q= 32.8 K= 7.58 8.0 Pt 18.7 Pt 18.7 22 Q= 129.3 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.9 D= 2.203 8.0 0.1119 Pf 0.9 Pn 17.9 --------------------------- 26 q= 33.6 K= 7.58 8.0 Pt 19.6 Pt 19.6 23 Q= 162.9 F= 0.0 C= 120 Pe 0.0 Pv -1. 3 Vf/s= 13.7 D= 2.203 8.0 0.1715 Pf 1.4 Pn 18.4 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 9 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 27 q= 34.7 K= 7.58 8.0 Pt 21.0 Pt 21.0 24 Q= 197.6 F= 0.0 C= 120 Pe 0.0 Pv -1.9 25 26 Vf/s= 16.6 D= 2.203 8.0 0.2453 Pf 2.0 Pn 19.1 ------------ 28 q= 36.3 K= 7.58 4.0 Pt 23.0 Pt Q= 234.0 F=T 13.6 C= 120 Pe 0.0 Pv Vf/s= 19.7 D= 2.203 17.6 0.3353 Pf 5.9 Pn ------------ 29 q= 0.0 K= 0.00 1.0 Pt 28.9 Pt Q= 314.3 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 26.5 D= 2.203 14.6 0.5792 Pf 8.5 Pn 30 Pt 37.7 23.0 -2.6 20.3 28.9 -4.7 24.1 --------------- --------------- --------------------------------------GENERAL---------------------------------- 31 q= 40.2 K= 7.58 2.0 Pt 28.1 Pt 28.1 27 Q= 80.3 F=T 13.6 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.8 D= 2.203 15.6 0.0463 Pf 0.7 Pn 27.8 29 Pt 28.9 --------------------------------------GENERAL---------------------------------- 32 q= 40.1 K= 7.58 8.0 Pt 28.0 Pt 28.0 28 Q= 40.1 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.4 D= 2.203 8.0 0.0128 Pf 0.1 Pn 28.0 31 Pt 28.1 --------------------------------------GENERAL---------------------------------- 33 q= 32.9 K= 7.58 8.0 Pt 18.9 Pt 18.9 29 Q= 32.9 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 2.8 D= 2.203 8.0 0.0089 Pf 0.1 Pn 18.8 --------------------------- 34 q= 33.0 K= 7.58 8.0 Pt 18.9 Pt 18.9 30 Q= 65.9 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.5 D= 2.203 8.0 0.0321 Pf 0.3 Pn 18.7 --------------------------- 35 q= 33.2 K= 7.58 8.0 Pt 19.2 Pt 19.2 31 Q= 99.1 F= 0.0 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.3 D= 2.203 8.0 0.0683 Pf 0.5 Pn 18.7 ---------------------------36 q= 33.7 K= 7.58 8.0 Pt 19.7 Pt 19.7 32 Q= 132.8 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 11. 2 D= 2. 203 8.0 0.1175 Pf 0.9 Pn 18.9 --------------------------- 37 q= 34.5 K= 7.58 8.0 Pt 20.7 Pt 20.7 33 Q= 167.3 F= 0.0 C= 120 Pe 0.0 Pv -1. 3 Vf/s= 14.1 D= 2.203 8.0 0.1801 Pf 1.4 Pn 19.3 --------------------------- 38 q= 35.6 K= 7.58 8.0 Pt 22.1 Pt 22.1 34 Q= 202.9 F= 0.0 C= 120 Pe 0.0 Pv -2.0 Vf/s= 17.1 D= 2.203 8.0 0.2576 Pf 2.1 Pn 20.2 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 10 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 39 q= 37.3 K= 7.58 4.0 Pt 24.2 Pt 24.2 35 Q= 240.2 F=T 13.6 C= 120 Pe 0.0 Pv -2.7 36 Vf/s= 20.2 D= 2.203 17.6 0.3520 Pf 6.2 Pn 21.4 40 q= 0.0 K= 0.00 1.0 Pt 30.4 Pt Q= 322.6 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 27.2 D= 2.203 14.6 0.6079 Pf 8.9 Pn 41 Pt 39.7 30.4 -5.0 25.4 --------------------------------------GENERAL---------------------------------- 42 q= 41.3 K= 7.58 2.0 Pt 29.6 Pt 29.6 37 Q= 82.4 F=T 13.6 C= 120 Pe 0.0 Pv -0.3 Vf/s= 6.9 D= 2.203 15.6 0.0486 Pf 0.8 Pn 29.3 40 Pt 30.4 --------------------------------------GENERAL---------------------------------- 43 q= 41.2 K= 7.58 8.0 Pt 29.5 Pt 29.5 38 Q= 41.2 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.5 D= 2.203 8.0 0.0134 Pf 0.1 Pn 29.4 42 Pt 29.6 --------------------------------------GENERAL---------------------------------- 39 40 41 42 44 q= 44.6 K= 7.58 8.0 Pt 34.6 Pt 34.6 Q= 44.6 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 3.8 D= 2.203 8.0 0.0156 Pf 0.1 Pn 34.5 ------------ 45 q= 44.6 K= 7.58 8.0 Pt 34.7 Pt Q= 89.2 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 7.5 D= 2.203 8.0 0.0562 Pf 0.4 Pn ------------ 46 q= 44.9 K= 7.58 8.0 Pt 35.1 Pt Q= 134.2 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 11. 3 D= 2.203 8.0 0.1197 Pf 1.0 Pn ------------ 47 q= 45.5 K= 7.58 5.0 Pt 36.1 Pt Q= 179.7 F=TT 27.3 C= 120 Pe 0.4 Pv Vf/s= 15.1 D= 2.203 32.3 0.2055 Pf 6.6 Pn 48 Pt 43.2 34.7 -0.4 34.3 35.1 -0.9 34.3 36.1 -1.5 34.6 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 3 q= 0.0 K= 0.00 4.5 Pt 36.7 Pt 36.7 43 Q= 89.0 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.0 D= 4.310 4.5 0.0021 Pf 0.0 Pn 36.7 --------------------------- 10 q= 0.0 K= 0.00 6.5 Pt 36.7 Pt 36.7 44 Q= 317.9 F= 0.0 C= 120 Pe 0.0 Pv -0.3 Vf/s= 7.0 D= 4.310 6.5 0.0225 Pf 0.1 Pn 36.4 --------------------------- 19 q= 0.0 K= 0.00 10.8 Pt 36.9 Pt 36.9 45 Q= 628.5 F= 0.0 C= 120 Pe 0.0 Pv -1.3 Vf/s= 13.8 D= 4.310 10.8 0.0796 Pf 0.9 Pn 35.6 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 11 CARLSBAD OAKS LOT 7, BLDG. C: CALC .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 30 q= 0.0 K= 0.00 11.5 Pt 37.7 Pt 37.7 46 Q= 942.8 F= 0.0 C= 120 Pe 0.0 Pv -2.9 Vf/s= 20.7 D= 4.310 11.5 0.1686 Pf 1.9 Pn 34.9 41 q= 0.0 K= 0.00 47 Q=1265.4 F= Vf/s= 27.8 D= 4.310 48 q= 0.0 K= 0.00 48 Q=1445.l F= Vf/s= 31.8 D= 4.310 49 q= 0.0 K= 0.00 50 Q=1445.1 F=L Vf/s= 31.8 D= 4.310 55 q= 0.0 K= 0.00 51 Q=l445.1 F=LLT Vf/s= 31.8 D= 4.310 12.0 0.0 12.0 18.0 0.0 18.0 46.0 8.4 54.4 3.0 44.6 47.6 C= 120 0.2908 C= 120 0.3718 C= 120 0.3716 C= 120 0.3718 Pt Pe Pf Pt Pe Pf Pt Pe Pf Pt Pe Pf 39.7 Pt 0. 0 Pv 3.5 Pn 43.2 Pt 0.0 Pv 6.7 Pn 49.9 Pt 0.0 Pv 20.2 Pn 70.1 Pt 0.0 Pv 17.7 Pn 39.7 -5.2 34.5 43.2 -6.8 36.4 49.9 -6.8 43.1 70.1 -6.8 63.3 50 q= 0.0 K= 0.00 52 Q=1445.l F=LL Vf/s= 14.5 D= 6.385 24.0 Pt 23.1 C= 120 Pe 47.1 0.0549 Pf 87.8 Pt 87.8 7 .4 Pv -1.4 2.6 Pn 86.4 51 q= 100.0 ADD HYD FLOW 53 Q=1545.l F=LL Vf/s= 9.9 D= 7.970 52 q= 0.0 K= 0.00 54 Q=1545.l F=LGT Vf/s= 9.9 D= 7.970 25.0 Pt 37.0 C= 150 Pe 62.0 0.0139 Pf 20.0 73.9 93.9 Pt C= 150 Pe 0.0140 Pf 97.7 Pt 0.0 Pv 0.9 Pn 98.6 Pt 0.0 Pv 1.3 Pn 53 q= 400.0 ADD HYD FLOW 280.0 Pt 99. 9 Pt Pe O. O Pv Pf 2.9 Pn Pt 102.8 55 Q=1945.l F=2GT 87.5 C= 150 Vf/s= 8.3 D= 9.780 367.5 0.0079 54 <<<<<<<< Supply point>>>>>>>> 97.7 -0.7 97.1 98.6 -0.7 97.9 99.9 -0.5 99.4 FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 110.8 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-1100 ~ 63~46 * GENERAL UNDERGROUND FIRE PROT., INC.* 3930 East Coronado Street, Anaheim, CA 92807 (714) * HYDRAULIC DESIGN INFORMATION SHEET * ~ Name CARLSBAD OAKS LOT 7, BL. D, AREA 1: .33/3000 Date ___ __,,0=2_-=1~9~A=.,,__.4 Location 2748 LOKER AVE. WEST, CARLSBAD, CALIFORNIA System No. _____ _ Building_~D _________________________ Drawing No._=F=P--"'5 __ Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No. 745 ~~---Construction: * COMBUSTIBLE --~NON-COMBUSTIBLE Ceiling Ht. __ ~1~9,c__f Occupancy STORAGE s y s T __ NFPA 13: __ Lt.Raz. ** Ord.Raz. Gr. __ 1 __ 2 __ 3 ** Ex.Raz. 1 __ __ NFPA: __ 13D 13R __ 231 __ 231C Figure _____ Curve ___ _ ~Other (Specific ruling) .33 GPMISF OVER 3000 SF Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E ·---------------------------------------------------------------------------- M D E s I G Area of Sprinkler operation __ =3=0=0=0-** SYSTEM TYPE** Density .33 : ~Wet __ Dry __ Deluge __ Pre-Action Area per sprinkler ---=9=2-·-------------------------------------- Hose allowance GPM: inside 100 ** SPRINKLER or NOZZLE** Hose allowance GPM: outside 400 --~~-Make TYCO Model TY-L Rack sprinklers allowance Orifice Size 17/32" K-Factor 8.0 Temperature rating 280 deg N .---------------------------------------------------------------------------- CALCULATION SUMMARY GPM required GPM required C-Factor used: 1117.9 PSI required 1617.9 PSI required Overhead __ 1=2~0~--- 71.0 at base of A.S.Rise 81.7 at point of supply. Underground 150 w .--------------------------------------------------------. A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK* Pump Capacity Pump Pressure Pump Elevation Tank Capacity Tank Elevation Well Proof Flow WELL ** N.A. N.A. N.A. :::) s C-16 485748 "-'<ro -:,i p :--------------------------------------------------------: L y : Location CONNECTION TO 16" CIRC MAIN IN LOKER AVE. WEST : Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT C 0 M M 0 Commodity ___________________________ ~------- Location ___________________________ : Class _____ _ Storage Height Aisle width. __ ___, _______ : Area _____ _ Storage Method: Solid piled _____ % Palletized _____ % Rack ____ _ Plastics ___________________________________ _ D ·----------------------------------------------------------------------------· I T y :R S :A T :C 0 :K R A G __ Single row __ Conventional __ Double row __ Slave pallet __ Multiple row pallet __ Automatic storage __ Solid shelving __ Open __ Encapsulatec __ Non- Encapsulatec ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILINC : Longitudinal ___ Transverse __ _____ ft. _____ in. : Horiz. barriers provided ________________________ _ E .=------------------------------------------------------------------------==== GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet Sprinkler System Analysis Small Sample Output Comments TOTAL FLOW AVAILABLE: Supply pressure is 70.0 PSI 1 BUFFER ALLOWED:10%2 Residual pressure is 60.0 PSI NODE NO. 3 1 2 3 4 PIPE NO. NODE NO. at Discharge of 1210 GPM ELEVATION FEET 4 15.0 15.0 o.o o.o SPRK COEF 3.85 FLOW K-FACTOR 5 GPM FITTING TYPE DIAMETER PRESSURE PSI 21. 9 6 22.9 30.6 35.2 LENGTH FTG TOTAL DISCHARGE GPM 7 18.0 5.0 Hydrant Flow Supply Point FRICTION PRESSURE LOSS PSI PSI/FT 8 9 ---------------------------------------------------------------------- 1' 7 5 q. 18.0 K• 3.85 10.0 15 Pt 21. 9 6 Pt 2l. 9 1. The report indicates the total available supply which includes the static pressure, as well as the residual pressure and volume. This is the total available at the supply point node. 2. The buffer allowance is included to indicate the percentage or fixed pressure buffer for both the static and residual supply pressures. 3. Nodes refer to hydraulic reference points. 4. Elevation measured in feet above datum. 5. K-Factor of open sprinkler or nozzles. 6. Pressure calculated at reference point. 7. Discharge (q) = K x (p)112 8. Hydrant discharge is independant of pressure. 9. Supply point may be anywhere in the system. 10. Only pipes actually flowing water are reported. 11. Q represents total flow in any particular pipe. 12. Vf/s is the water velocity in feet per second. 13. Dis the actual internal diameter of the pipe. 14. F refers to the fittings used. The list may be up to ten characters. The following applies: 2 ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) ) I ) I ) 10 11 14 16 1 Q• 18.0 p. 0.0 C• 12018 Pe 0.0 20 Pv -0.3 A letter without a preceeding number is singular. } 12 13 17 0. 101119 Vf/s"" 6.7 D• 1. 049 10.0 2' q• 0.0 7 K• 0.00 5 25.0 15 29 Q• 18.0 11 F=G2T14 14. 5 16 C• 12018 Vf/S= 3.9 12 D• 1. 38013 39,5 17 0.028319 ,' q• 5.0 ADD HYD FLOWS 100.0 15 ,10 Q• 23.0 11 F=GLT14 13.7 16 C• 1so18 Vf/s• 5.6 12 D• 1.29113 113.7 17 0.040819 49 <<<<<<<< Supply point >>>>>>>> Pf 1.1 21 Pn Pt 22 .9 6 Pt Pe 6.5 20 Pv Pf 1.1 21 Pn Pt 30.6 6 Pt Pe 0.0 20 Pv Pf 4.6 21 Pn Pt 3s.222 21. 6 22.9 -0.1 22.8 30.6 -0.2 30.4 A preceeding number is a multiple of the fitting. A number alone represents its numeric value only. 15. L represents the actual length of the pipe shown. 16. Fitting value is the equivalent footage of pipe. 17. Total is the sum of fitting value & pipe length. 18. C-factor is the Hazen Williams Coeficient. 19. Friction loss per foot based on H-W formula. 20. Pe= pressure loss due to elevation differential. 21. Pf• total friction loss (length x loss per foot) 22. Pt= Total pressure at each node. (Pt+Pe+Pf) ) I I ) ) ) ) ) ) ) A=alarm va., B=butterfly va., C=cplg, E=short turn elbow, F~45o ell, G=gate va., L•long ell, R=CPVC Tee Run, T=Tee, V=swing check Sample Calculation Placard * HYDRAULICALLY DESIGNED AUTOMATIC SPRINKLER SYSTEM INFORMATION* Job name : __ _sCARLe,,""'S~BADe,;c...,O.Ue,,~S,._,L~O~Tc..,7~.~B~L~._;D~ • ...,ARUe,,.,__~1~,~-~3~3~/~3~•~·~·'------- Location: 2748 LOUR AVB. WEST, CARLSBAD, CA.LI.ll'ORNIA Contract No. 745 Drawing No: FP 5 Date: 02-19-2004 This system is designed to discharge at a rate of --~·~3~3'-- per square foot of floor area over a maximum of ---~3~0~0~0c_ feet when supplied at a rate of----------~'~'~'~'~·~•- at the base of riser with a pressure of-------~'~'~·~•'- g.p.m. square g.p.m. p.s .i. The above information includes hose stream allowance of _o_ g.p.m, GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 3 CARLSBAD OAKS LOT 7, BL. D, AREA 1: .33/3000 160 144 p r 112 e s s u r e p s I 96 64 48 32 16 8. 01-.3l.il.LJ...llllJlilWlilllW.llll.l.ilJllll.lll.lll.LlJL.Ll.l..U...l..Ll..U...LL.lillliWlllillilllllllllllll.llllillllJ.l.illlllllllJ.lll.l.W.lll..l.ilJllllJ.J.li 800 1000 1200 1400 1600 1800 2000 200 400 600 Water Flow GPM LETTER DESCRIPTION A Static Pressure of 147.0 p.s. i. B = Residual Pressure of 143.0 p.s.i. at 1683.0 G.P.M. C = 90.0 percent Static 132.3 p.s.i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s.i. Elev of 19.0 ft. F = Base of Riser Demand 71. 0 p.s.i. at 1117.9 G.P.M. G = Point of Conn Demand 81. 7 p.s.i. at 1617.9 G.P.M. The City Supply provides 143.3 p.s. i. at 1617.9 G.P.M. which leaves a buffer of 61. 6 p.s. i. at system demand. GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 4 PIPE NO. NODE NO. FLOW GPM CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .45/3000 K-FACTOR CALCULATIONS K-FACTOR FITTING TYPE DIAMETER LENGTH FTG TOTAL FRICTION LOSS PSI/FT PRESSURE PSI NOTES ------------------------------------------------------------------------------- 1 q; 31. 7 A Q; 31. 7 2 K; 8.00 F;T D; 1.080 1. 0 5.8 6.8 Pt 15.70 C; 120 Pe 0.00 0.2648 Pf 1.79 Pt 17.49 1 FT SPRig UP K; Q/ (P) • K; 31.70/( 17.49 ) •5 K; 7.58 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Sprinkler System Analysis Date: 02-19-04 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 Sheet TOTAL FLOW AVAILABLE: Static Pressure Residual Pressure at Discharge of 147.0 PSI 143.0 PSI 1683 GPM BUFFER ALLOWED: NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM 5 10 % ------------------------------------------------------------------VERSION 3.0-- 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 35 36 37 38 39 40 41 42 43 44 45 46 17.0 17.0 16.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 16.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 16.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 16.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 16.0 17.0 17.0 17.0 17.0 17.0 17.0 17.0 16.0 17.0 17.0 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 7.60 19.1 19.3 21. 3 18.2 18.0 17.9 16.3 16.4 16.6 17.8 21.4 16.8 16.6 16.5 16.0 16.1 16.3 16.8 18.5 22.2 18.0 17.9 16.1 16.1 16.4 16.8 18.6 22.3 18.1 18.0 16.7 16.7 16.9 17.4 19.3 23.1 18.7 18.7 17.9 18.0 18.2 18.8 20.8 24.8 20.2 20.1 33.2 32.4 32.2 32.1 30.7 30.8 31. 0 31.1 30.9 30.9 30.4 30.5 30.7 31.1 32.2 32.2 30.5 30.5 30.7 31.2 32.3 32.3 31.0 31.1 31.3 31.7 32.9 32.8 32.2 32.2 32.5 32.9 34.1 34.1 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 6 CARLSBAD OAKS LOT 7, BLDG. D AREA 1 : .33/3000 NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM ------------------------------------------------------------------------------- 47 17.0 26.5 48 17.0 26.5 49 17.0 26.5 50 17.0 26.5 51 17.0 26.5 52 17.0 26.5 53 17.0 7.60 26.5 39.1 54 16.0 27.3 55 17.0 29.6 56 17.0 29.6 57 17.0 29.6 58 17.0 29.6 59 17.0 29.6 60 17.0 29.6 61 17.0 29.6 62 16.0 30.0 63 17.0 32.4 64 17.0 32.4 65 17.0 32.4 66 17.0 32.4 67 17.0 32.4 68 17.0 32.4 69 17.0 32.4 70 16.0 32.8 71 17.0 35.2 72 17.0 35.2 73 17.0 35.2 74 17.0 35.2 75 17.0 35.2 76 17.0 35.2 77 17.0 35.2 78 16.0 35.6 79 17.0 37.9 80 17.0 37.9 81 17.0 37.9 82 17.0 37.9 83 16.0 38.4 84 16.0 41.1 85 16.0 46.8 86 16.0 62.4 87 0.0 71. 0 100.0 Hydrant Flow 88 0.0 72.1 89 0.0 72.9 400.0 Hydrant Flow 90 0.0 81. 7 Supply Point 91 16.0 22.5 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 7 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 1 q= 33.2 K= 7.60 6.0 Pt 19.1 Pt 19.1 1 Q= 33.2 F=FT 16.4 C= 120 Pe 0.0 Pv -0.1 2 Vf/s= 2.8 D= 2.203 22.4 0.0090 Pf 0.2 Pn 19.0 2 q= 0.0 K= 0.00 1.0 Pt 19.3 Pt Q= 129.9 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 10.9 D= 2.203 14.6 0.1128 Pf 1.6 Pn 3 Pt 21.3 19.3 -0.8 18.4 --------------------------------------GENERAL---------------------------------- 4 q= 32.4 K= 7.60 2.5 Pt 18.2 Pt 18.2 3 Q= 96.8 F=T 13.6 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 16.1 0.0655 Pf 1.1 Pn 17.8 2 Pt 19.3 --------------------------------------GENERAL---------------------------------- 5 q= 32.2 K= 7.60 8.0 Pt 18.0 Pt 18.0 4 Q= 64.3 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0307 Pf 0.2 Pn 17.8 4 Pt 18.2 --------------------------------------GENERAL---------------------------------- 6 q= 32.1 K= 7.60 8.0 Pt 17.9 Pt 17.9 5 Q= 32.1 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn 17.8 5 Pt 18.0 --------------------------------------GENERAL---------------------------------- 6 7 8 9 7 q= 30.7 K= 7.60 8.0 Pt 16.3 Pt 16.3 Q= 30.7 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.6 D= 2.203 8.0 0.0078 Pf 0.1 Pn 16.3 ------------ 8 q= 30.8 K= 7.60 8.0 Pt 16.4 Pt Q= 61.5 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 5.2 D= 2.203 8.0 0.0282 Pf 0.2 Pn ------------ 9 q= 31.0 K= 7.60 5.5 Pt 16.6 Pt Q= 92.5 F=T 13.6 C= 120 Pe 0.0 Pv Vf/s= 7.8 D= 2.203 19.1 0.0602 Pf 1.1 Pn ------------ 10 q= 0.0 K= 0.00 1.0 Pt 17.8 Pt Q= 185.4 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 15.6 D= 2.203 14.6 0.2179 Pf 3.2 Pn 11 Pt 21.4 16.4 -0.2 16.2 16.6 -0.4 16.2 17.8 -1.6 16.1 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 12 q= 31.1 K= 7.60 2.5 Pt 16.8 Pt 16.8 10 Q= 92.9 F=T 13.6 C= 120 Pe 0.0 Pv -0.4 Vf/s= 7.8 D= 2.203 16.1 0.0608 Pf 1.0 Pn 16.4 10 Pt 17.8 --------------------------------------GENERAL---------------------------------- 13 q= 30.9 K= 7.60 8.0 Pt 16.6 Pt 16.6 11 Q= 61.8 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.2 D= 2.203 8.0 0.0285 Pf 0.2 Pn 16.4 12 Pt 16.8 --------------------------------------GENERAL---------------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 8 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 14 q= 30.9 K= 7.60 8.0 Pt 16.5 Pt 16.5 12 Q= 30.9 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.6 D= 2.203 8.0 0.0079 Pf 0.1 Pn 16.4 13 Pt 16.6 --------------------------------------GENERAL---------------------------------- 15 q= 30.4 K= 7.60 8.0 Pt 16.0 Pt 16.0 13 Q= 30.4 F= 0.0 C= 120 Pe 0.0 Pv -0.0 14 15 16 17 Vf/s= 2.6 D= 2.203 8.0 0.0077 Pf 0.1 Pn 16.0 16 q= Q= Vf/s= 17 q= Q= Vf/s= 18 q= Q= Vf/s= 30.5 60.9 5.1 30.7 91.5 7.7 31.1 122.7 10.3 K= 7.60 F= D= 2.203 K= 7.60 F= D= 2.203 K= 7.60 F=T D= 2.203 ------- 8.0 0.0 8.0 ------- 8.0 0.0 8.0 ------- 4.0 13.6 17.6 ------- ----- Pt 16.1 Pt C= 120 Pe 0.0 Pv 0.0277 Pf 0.2 Pn ----- Pt 16.3 Pt C= 120 Pe 0.0 Pv 0.0590 Pf 0.5 Pn ----- Pt 16.8 Pt C= 120 Pe 0.0 Pv 0.1014 Pf 1. 8 Pn ----- 19 q= 0.0 K= 0.00 1.0 Pt 18.5 Pt Q= 187.1 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 15.7 D= 2.203 14.6 0.2216 Pf 3.2 Pn 20 Pt 22.2 16.1 -0.2 15.9 16.3 -0.4 15.9 16.8 -0.7 16.0 18.5 -1. 7 16.9 --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 21 q= 32.2 K= 7.60 4.0 Pt 18.0 Pt 18.0 18 Q= 64.4 F=T 13.6 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 17.6 0.0308 Pf 0.5 Pn 17.8 19 Pt 18.5 --------------------------------------GENERAL---------------------------------- 22 q= 32.2 K= 7.60 8.0 Pt 17.9 Pt 17.9 19 Q= 32.2 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn 17.9 21 Pt 18.0 --------------------------------------GENERAL---------------------------------- 23 q= 30.5 K= 7.60 8.0 Pt 16.1 Pt 16.1 20 Q= 30.5 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.6 D= 2.203 8.0 0.0077 Pf 0.1 Pn 16.0 ---------------------------24 q= 30.5 K= 7.60 8.0 Pt 16.1 Pt 16.1 21 Q= 61. 0 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.1 D= 2.203 8.0 0.0278 Pf 0.2 Pn 16.0 --------------------------- 25 q= 30.7 K= 7.60 8.0 Pt 16.4 Pt 16.4 22 Q= 91. 7 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 7.7 D= 2.203 8.0 0.0592 Pf 0.5 Pn 16.0 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 9 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 26 q; 31.2 K; 7.60 4.0 Pt 16.8 Pt 16.8 23 Q; 122.9 F;T 13.6 C; 120 Pe 0.0 Pv -0.7 24 Vf/s; 10.3 D; 2.203 17.6 0.1018 Pf 1.8 Pn 16.1 27 q; 0.0 K; 0.00 1.0 Pt 18.6 Pt Q; 187.5 F;T 13.6 C; 120 Pe 0.4 Pv Vf/s; 15.8 D; 2.203 14.6 0.2225 Pf 3.2 Pn 28 Pt 22.3 18.6 -1. 7 16.9 --------------------------------------GENERAL---------------------------------- 29 q; 32.3 K; 7.60 4.0 Pt 18.1 Pt 18.1 25 Q; 64.6 F;T 13.6 C; 120 Pe 0.0 Pv -0.2 Vf/s; 5.4 D; 2.203 17.6 0.0309 Pf 0.5 Pn 17.9 27 Pt 18.6 --------------------------------------GENERAL---------------------------------- 30 q; 32.3 K; 7.60 8.0 Pt 18.0 Pt 18.0 26 Q; 32.3 F; 0.0 C; 120 Pe 0.0 Pv -0.0 Vf/s; 2.7 D; 2.203 8.0 0.0085 Pf 0.1 Pn 18.0 29 Pt 18.1 --------------------------------------GENERAL---------------------------------- 27 28 29 30 31 31 q; 31.0 K; 7.60 8.0 Pt 16.7 Pt 16.7 Q; 31.0 F; 0.0 C; 120 Pe 0.0 Pv -0.0 Vf/s; 2.6 D; 2.203 8.0 0.0079 Pf 0.1 Pn 16.6 32 q; Q; Vf/s; 33 q; Q; Vf/s; 34 q; Q; Vf/s; 31.1 K; 7.60 62.1 F; 5.2 D; 2.203 31. 3 K; 7.60 93.4 F; 7.9 D; 2.203 31. 7 K; 7. 60 125.1 F;T 10.5 D; 2.203 ------------ 8.0 Pt 16.7 Pt 0.0 C; 120 Pe 0.0 Pv 8·. o 0.0287 Pf 0.2 Pn ------------ 8.0 Pt 16.9 Pt 0.0 C; 120 Pe 0.0 Pv 8.0 0.0612 Pf 0.5 Pn ------------ 4.0 Pt 17.4 Pt 13.6 C; 120 Pe 0.0 Pv 17.6 0.1052 Pf 1. 9 Pn ------------ 35 q; 0.0 K; 0.00 1.0 Pt 19.3 Pt Q; 190.8 F;T 13.6 C; 120 Pe 0.4 Pv Vf/s; 16.1 D; 2.203 14.6 0.2299 Pf 3.4 Pn 36 Pt 23.1 16.7 -0.2 16.5 16.9 -0.4 16.5 17.4 -0.7 16.7 19.3 -1. 7 17.6 --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 37 q; 32.9 K; 7.60 4.0 Pt 18.7 Pt 18.7 32 Q; 65.7 F;T 13.6 C; 120 Pe 0.0 Pv -0.2 Vf/s; 5.5 D; 2.203 17.6 0.0319 Pf 0.6 Pn 18.5 35 Pt 19.3 --------------------------------------GENERAL---------------------------------- 38 q; 32.8 K; 7.60 8.0 Pt 18.7 Pt 18.7 33 Q; 32.8 F; 0.0 C; 120 Pe 0.0 Pv -0.1 Vf/s; 2.8 D; 2.203 8.0 0.0088 Pf 0.1 Pn 18.6 37 Pt 18.7 --------------------------------------GENERAL---------------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 10 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 39 q= 32.2 K= 7.60 8.0 Pt 17.9 Pt 17.9 34 Q= 32.2 F= 0.0 C= 120 Pe 0.0 Pv -0.0 35 36 37 38 Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn 17.9 40 q= Q= Vf/s= 41 q= Q= Vf/s= 42 q= Q= Vf/s= 32.2 K= 7. 60 64.4 F= 5.4 D= 2.203 32.5 K= 7.60 96.9 F= 8.2 D= 2.203 32.9 K= 7.60 129.8 F=T 10.9 D= 2.203 ------- 8.0 0.0 8.0 ------- 8.0 0.0 8.0 ------- 4.0 13.6 17.6 ------- ----- Pt 18.0 Pt C= 120 Pe 0.0 Pv 0.0308 Pf 0.2 Pn ----- Pt 18.2 Pt C= 120 Pe 0.0 Pv 0.0655 Pf 0.5 Pn ----- Pt 18.8 Pt C= 120 Pe 0.0 Pv 0.1127 Pf 2.0 Pn ----- 43 q= 0.0 K= 0.00 1.0 Pt 20.8 Pt Q= 198.0 F=T 13.6 C= 120 Pe 0.4 Pv Vf/s= 16.7 D= 2.203 14.6 0.2462 Pf 3.6 Pn 44 Pt 24.8 18.0 -0.2 17.8 18.2 -0.4 17.8 18.8 -0.8 18.0 20.8 -1.9 18.9 --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 45 q= 34.1 K= 7.60 4.0 Pt 20.2 Pt 20.2 39 Q= 68.2 F=T 13.6 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.7 D= 2.203 17.6 0.0342 Pf 0.6 Pn 19.9 43 Pt 20.8 --------------------------------------GENERAL---------------------------------- 46 q= 34.1 K= 7.60 8.0 Pt 20.1 Pt 20.1 40 Q= 34.1 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 2.9 D= 2.203 8.0 0.0095 Pf 0.1 Pn 20.0 45 Pt 20.2 --------------------------------------GENERAL---------------------------------- 53 q= 39.1 K= 7.60 5.0 Pt 26.5 Pt 26.5 47 Q= 39.1 F=ET 20.5 C= 120 Pe 0.4 Pv -0.1 Vf/s= 3.3 D= 2.203 25.5 0.0122 Pf 0.3 Pn 26.5 54 Pt 27.3 --------------------------------------GENERAL---------------------------------- 73 74 3 q= 0.0 K= 0.00 9.5 Pt 21.3 Pt 21.3 Q= 129.9 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 2.9 D= 4.310 9.5 0.0043 Pf 0.0 Pn 21.3 11 q= 0.0 K= 0.00 21.0 Pt 21.4 Pt Q= 315.3 F=T 27.9 C= 120 Pe 0.0 Pv Vf/s= 6.9 D= 4.310 48.9 0.0222 Pf 1.1 Pn 91 Pt 22.5 21.4 -0.3 21.1 --------------------------------------GENERAL---------------------------------- 20 q= 0.0 K= 0.00 11.5 Pt 22.2 Pt 22.2 75 Q= 187.1 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 4.1 D= 4.310 11.5 0.0084 Pf 0.1 Pn 22.1 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 11 CARLSBAD OAKS LOT 7, BLDG. D AREA 1 : .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 28 q= 0.0 K= 0.00 5.0 Pt 22.3 Pt 22.3 76 Q= 374.6 F= 0.0 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.2 D= 4.310 5.0 0.0305 Pf 0.2 Pn 21.9 --------------------------- 91 q= 0.0 K= 0.00 6.5 Pt 22.5 Pt 22.5 77 Q= 689.9 F= 0.0 C= 120 Pe 0.0 Pv -1.5 Vf/s= 15.2 D= 4.310 6.5 0.0946 Pf 0.6 Pn 20.9 --------------------------- 36 q= 0.0 K= 0.00 11. 5 Pt 23.1 Pt 23.1 78 Q= 880.8 F= 0.0 C= 120 Pe 0.0 Pv -2.5 Vf/s= 19.4 D= 4.310 11.5 0.1486 Pf 1. 7 Pn 20.6 --------------------------- 44 q= 0.0 K= 0.00 11. 5 Pt 24.8 Pt 24.8 79 Q=1078.8 F= 0.0 C= 120 Pe 0.0 Pv -3.8 Vf/s= 23.7 D= 4.310 11. 5 0.2164 Pf 2.5 Pn 21. 0 --------------------------- 54 q= 0.0 K= 0.00 12.0 Pt 27.3 Pt 27.3 80 Q=1117.9 F= 0.0 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 12.0 0.2311 Pf 2.8 Pn 23.2 --------------------------- 62 q= 0.0 K= 0.00 12.0 Pt 30.0 Pt 30.0 81 Q=1117.9 F= 0.0 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 12.0 0.2311 Pf 2.8 Pn 26.0 --------------------------- 70 q= 0.0 K= 0.00 12.0 Pt 32.8 Pt 32.8 82 Q=1117.9 F= 0.0 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 12.0 0.2311 Pf 2.8 Pn 28.8 --------------------------- 78 q= 0.0 K= 0.00 12.0 Pt 35.6 Pt 35.6 83 Q=1117.9 F= 0.0 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 12.0 0.2311 Pf 2.8 Pn 31.5 --------------------------- 83 q= 0.0 K= 0.00 12.0 Pt 38.4 Pt 38.4 84 Q=1117.9 F= 0.0 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 12.0 0.2311 Pf 2.8 Pn 34.3 --------------------------- 84 q= 0.0 K= 0.00 16.0 Pt 41.1 Pt 41.1 85 Q=1117.9 F=L 8.4 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 24.4 0.2308 Pf 5.6 Pn 37.1 --------------------------- 85 q= 0.0 K= 0.00 51. 0 Pt 46.8 Pt 46.8 86 Q=1117.9 F=2L 16.7 C= 120 Pe 0.0 Pv -4.1 Vf/s= 24.6 D= 4.310 67.7 0.2312 Pf 15.7 Pn 42.7 --------------------------- 86 q= 0.0 K= 0.00 24.0 Pt 62.4 Pt 62.4 87 Q=1117.9 F=2L 23.1 C= 120 Pe 6.9 Pv -0.8 Vf/s= 11.2 D= 6.385 47.1 0.0341 Pf 1. 6 Pn 61. 6 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 12 CARLSBAD OAKS LOT 7, BLDG. D AREA 1: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 87 q= 100.0 ADD HYD FLOW 85.0 Pt 71.0 Pt 71.0 88 Q=1217.9 F=2L 37.0 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.8 D= 7.970 122.0 0.0090 Pf 1.1 Pn 70.6 --------------------------- 88 q= 0.0 K= 0.00 15.0 Pt 72.1 Pt 72.1 89 Q=1217.9 F=LGT 73.9 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.8 D= 7.970 88.9 0.0090 Pf 0.8 Pn 71. 6 ---------------------------89 q= 400.0 ADD HYD FLOW 70.0 Pt 72.9 Pt 72.9 90 Q=1617.9 F=GT 80.2 C= 150 Pe 0.0 Pv -0.3 Vf/s= 6.9 D= 9.780 150.2 0.0056 Pf 0.8 Pn 72.5 90 <<<<<<<< Supply point >>>>>>>> Pt 73.7 --------------------------- FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 81.7 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-1100 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 1 * HYDRAULIC DESIGN INFORMATION SHEET * Name CARLSBAD OAKS LOT 7, BL. D, AREA 2: .33/3000 Date ___ ___,0~2~-~1~9"-----'-2~0"-"'-0~4 Location 2748 LOKER AVE. WEST, CARLSBAD, CALIFORNIA System No. _____ _ Building_~D~ _________________________ Drawing No. FP 5 Contractor GENERAL UNDERGROUND FIRE PROT., INC. Contract No. 745 ~=---Construction: * COMBUSTIBLE --~NON-COMBUSTIBLE Ceiling Ht. 19 f Occupancy STORAGE ------------------------------------------------------=====----=-=======-------s y s T __ NFPA 13: __ Lt.Haz. ** Ord.Haz. Gr. __ 1 __ 2 __ 3 ** Ex.Haz. 1 __ NFPA: __ 13D __ 13R 231 __ 231C Figure _____ Curve ___ _ ~Other (Specific ruling) .33 GPM/SF OVER 3000 SF Authority having Jurisdiction CITY OF CARLSBAD FIRE DEPARTMENT E :---------------------------------------------------------------------------- M D E s I G Area of Sprinkler operation. __ ~3~0=0~0-** SYSTEM TYPE** Density .33 : _*_Wet __ Dry __ Deluge __ Pre-Action Area per sprinkler ---~9=6_:-------------------------------------- Hose allowance GPM: inside 100 ** SPRINKLER or NOZZLE** Hose allowance GPM: outside 400 ---=~ Make TYCO Model TY-L Rack sprinklers allowance Orifice Size 17/32" K-Factor 8.0 Temperature rating 280 deg N .---------------==------------=-============================================= CALCULATION SUMMARY GPM required GPM required C-Factor used: 1100.0 PSI required 1600.0 PSI required 66.9 at base of A.S.Rise 77.6 at point of supply. Overhead._~1~2~0~---Underground 150 W .-----------------------------------------=================================== A T E R s u p **** WATER FLOW Test Date Static PSI Residual PSI GPM Flowing Elevation TEST **** 4-03 147 143 1683 Grade ** PUMP * TANK* WELL ** Pump Capacity N.A. Pump Pressure Pump Elevation Tank Capacity N.A. Tank Elevation Well Proof Flow N.A. p ·---------------------------------------------------------------------------- L: Location CONNECTION TO 16" CIRC MAIN IN LOKER AVE. WEST Y: Source of information FLOW TEST BY CARLSBAD FIRE DEPARTMENT =============================================================================== C 0 M M 0 Commodity _____________________________ .,..-______ _ Location : Class --,--,-----------:--::-----:-:--,-----------------Storage Height ___ -=----Aisle width __________ : Area _____ _ Storage Method: Solid piled ______ % Palletized ______ % Rack _____ _ Plastics -------------------------------------D ·---------------------------------------------------------------------------- I T y :R S :A T :C 0 :K R A G __ Single row __ Conventional __ Double row __ Slave pallet __ Multiple row pallet __ Automatic storage __ Solid shelving __ Open __ Encapsulate __ Non- Encapsulate ** FLUE SPACING IN INCHES** CLEARANCE FROM TOP OF STORAGE TO CEILIN : Longitudinal ___ Transverse __ _ _____ ft. ______ in. : Horiz. barriers provided E .-------------------------------============================================= GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 14 p r e s s u r e p s I 160 144 128 112 96 80 64 48 32 16 8. 0 CARLSBAD OAKS LOT 7, BL. D, AREA 2: .33/3000 ······································= . ·····-:·········:-······· ~ . :-·······•: ••······• .••········;······················· .... ·------·····' D F 200 400 600 800 1000 1200 1400 1600 1800 2000 Water Flow GPM LETTER DESCRIPTION A = Static Pressure of 147. 0 p.s. i. B = Residual Pressure of 143.0 p.s. i. at 1683.0 G.P.M. C 90.0 percent Static 132.3 p.s.i. D =90.0 percent Residual 128.7 p.s.i. at 1683.0 G.P.M. E = Elevation Pressure 8.2 p.s. i. Elev of 19.0 ft. F = Base of Riser Demand 66.9 p.s. i. at 1100.0 G.P.M. G = Point of Conn Demand 77.6 p.s.i. at 1600.0 G.P.M. The City Supply provides 143.4 p.s.i. at 1600.0 G.P.M. which leaves a buffer of 65.8 p.s.i. at system demand. GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Sprinkler System Analysis Date: 02-19-04 CARLSBAD OAKS LOT 7, BLDG. D AREA 2: .33/3000 Sheet TOTAL FLOW AVAILABLE: Static Pressure Residual Pressure at Discharge of 147.0 PSI 143.0 PSI 1683 GPM BUFFER ALLOWED: NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM 15 10 % ------------------------------------------------------------------VERSION 3.0-- 1 17.0 30.8 2 17.0 30.8 3 16.0 31. 3 4 17.0 30.8 5 17.0 30.8 6 17.0 30.8 7 17.0 30.8 8 17.0 30.8 9 17.0 30.8 10 17.0 30.8 11 16.0 31. 3 12 17.0 30.8 13 17.0 30.8 14 17.0 30.8 15 17.0 30.8 16 17.0 30.8 17 17.0 30.8 18 17.0 30.8 19 17.0 30.8 20 16.0 31. 3 21 17.0 30.8 22 17.0 30.8 23 17.0 30.8 24 17.0 30.8 25 17.0 30.8 26 17.0 30.8 27 17.0 30.8 28 16.0 31. 3 29 17.0 30.8 30 17.0 30.8 31 17.0 30.8 32 17.0 30.8 33 17.0 30.8 34 17.0 30.8 35 17.0 30.8 36 16.0 31.3 37 17.0 30.8 38 17.0 30.8 39 17.0 30.8 40 17.0 30.8 41 17.0 30.8 42 17.0 30.8 43 17.0 30.8 44 16.0 31. 3 45 17.0 30.8 46 17.0 30.8 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 16 CARLSBAD OAKS LOT 7, BLDG. D AREA 2: .33/3000 NODE ELEVATION SPRK PRESSURE DISCHARGE NO. FEET COEF PSI GPM ------------------------------------------------------------------------------- 47 17.0 7.58 17.5 31. 7 48 17.0 7.58 17.6 31.8 49 17.0 7.58 17.8 32.0 50 17.0 7.58 18.3 32.4 51 17.0 7.58 19.2 33.2 52 17.0 7.58 20.5 34.3 53 17.0 7.58 22.4 35.9 54 16.0 31. 3 55 17.0 7.58 17.6 31.8 56 17.0 7.58 17.6 31.8 57 17.0 7.58 17.9 32.1 58 17.0 7.58 18.4 32.5 59 17.0 7.58 19.3 33.3 60 17.0 7.58 20.6 34.4 61 17.0 7.58 22.6 36.0 62 16.0 31. 4 63 17.0 7.58 17.9 32.1 64 17.0 7.58 18.0 32.l 65 17.0 7.58 18.2 32.3 66 17.0 7.58 18.7 32.8 67 17.0 7.58 19.6 33.6 68 17.0 7.58 21.0 34.7 69 17.0 7.58 23.0 36.3 70 16.0 31.9 71 17.0 7.58 18.6 32.7 72 17.0 7.58 18.6 32.7 73 17.0 7.58 18.9 33.0 74 17.0 7.58 19.4 33.4 75 17.0 7.58 20.4 34.2 76 17.0 7.58 21.8 35.4 77 17.0 7.58 23.8 37.0 78 16.0 33.1 79 17.0 7.58 28.9 40.8 80 17.0 7.58 29.0 40.8 81 17.0 7.58 29.4 41.l 82 17.0 7.58 30.2 41.7 83 16.0 35.1 84 16.0 37.8 85 16.0 43.3 86 16.0 58.4 87 o.o 66.9 100.0 Hydrant Flow 88 o.o 68.0 89 o.o 68.8 400.0 Hydrant Flow 90 o.o 77.6 Supply Point 91 16.0 31.3 GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 17 CARLSBAD OAKS LOT 7, BLDG. D AREA 2: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0--47 q= 31. 7 K= 7.58 8.0 Pt 17.5 Pt 17.5 41 Q= 31.7 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0083 Pf 0.1 Pn 17.4 ---------------------------48 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 42 Q= 63.5 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.3 D= 2.203 8.0 0.0299 Pf 0.2 Pn 17.4 --------------------------- 49 q= 32.0 K= 7.58 8.0 Pt 17.8 Pt 17.8 43 Q= 95.4 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.0 D= 2.203 8.0 0.0637 Pf 0.5 Pn 17.4 ---------------------------50 q= 32.4 K= 7.58 8.0 Pt 18.3 Pt 18.3 44 Q= 127.9 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.8 D= 2.203 8.0 0.1095 Pf 0.9 Pn 17.5 ---------------------------51 q= 33.2 K= 7.58 8.0 Pt 19.2 Pt 19.2 45 Q= 161.1 F= 0.0 C= 120 Pe 0.0 Pv -1.2 Vf/s= 13.6 D= 2.203 8.0 0.1679 Pf 1.3 Pn 17.9 ---------------------------52 q= 34.3 K= 7.58 8.0 Pt 20.5 Pt 20.5 46 Q= 195.4 F= 0.0 C= 120 Pe 0.0 Pv -1.8 Vf/s= 16.4 D= 2.203 8.0 0.2402 Pf 1. 9 Pn 18.7 --------------------------- 53 q= 35.9 K= 7.58 5.0 Pt 22.4 Pt 22.4 47 Q= 231. 3 F=ET 20.5 C= 120 Pe 0.4 Pv -2.6 Vf/s= 19.5 D= 2.203 25.5 0.3283 Pf 8.4 Pn 19.9 54 Pt 31. 3 --------------------------------------GENERAL---------------------------------- 55 q= 31.8 K= 7.58 8.0 Pt 17.6 Pt 17.6 48 Q= 31. 8 F= 0.0 C= 120 Pe 0.0 Pv -0.0 Vf/s= 2.7 D= 2.203 8.0 0.0083 Pf 0.1 Pn 17.5 ---------------------------56 q= 31. 8 K= 7.58 8.0 Pt 17.6 Pt 17.6 49 Q= 63.6 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.4 D= 2.203 8.0 0.0301 Pf 0.2 Pn 17.5 --------------------------- 57 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 1 ';7. 9 50 Q= 95.7 F= 0.0 C= 120 Pe 0.0 Pv -0.4 Vf/s= 8.1 D= 2.203 8.0 0.0640 Pf 0.5 Pn 17.4 ---------------------------58 q= 32.5 K= 7.58 8.0 Pt 18.4 Pt 18.4 51 Q= 128.2 F= 0.0 C= 120 Pe 0.0 Pv -0.8 Vf/s= 10.8 D= 2.203 8.0 0.1100 Pf 0.9 Pn 17.6 ---------------------------59 q= 33.3 K= 7.58 8.0 Pt 19.3 Pt 19.3 52 Q= 161. 5 F= 0.0 C= 120 Pe 0.0 Pv -1. 2 Vf/s= 13.6 D= 2.203 8.0 0.1687 Pf 1. 3 Pn 18.0 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 18 CARLSBAD OAKS LOT 7, BLDG. D AREA 2: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3. 0-· 60 q= 34.4 K= 7.58 8.0 Pt 20.6 Pt 20.6 53 Q= 195.9 F= 0.0 C= 120 Pe 0.0 Pv -1.8 Vf/s= 16.5 D= 2.203 8.0 0.2413 Pf 1. 9 Pn 18.8 --------------------------~ 61 q= 36.0 K= 7.58 5.0 Pt 22.6 Pt 22.6 54 Q= 231.9 F=ET 20.5 C= 120 Pe 0.4 Pv -2.6 Vf/s= 19.5 D= 2.203 25.5 0.3298 Pf 8.4 Pn 20.0 62 Pt 31. 4 --------------------------------------GENERAL---------------------------------- 63 q= 32.1 K= 7.58 8.0 Pt 17.9 Pt 55 Q= 32.1 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 2.7 D= 2.203 8.0 0.0085 Pf 0.1 Pn ------------ 64 q= 32.1 K= 7.58 8.0 Pt 18.0 Pt 56 Q= 64.2 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 5.4 D= 2.203 8.0 0.0306 Pf 0.2 Pn ------------ 65 q= 32.3 K= 7.58 8.0 Pt 18.2 Pt 57 Q= 96.5 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 8.1 D= 2.203 8.0 0.0651 Pf 0.5 Pn ------------ 66 q= 32.8 K= 7.58 8.0 Pt 18.7 Pt 58 Q= 129.3 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 10.9 D= 2.203 8.0 0.1119 Pf 0.9 Pn ------------ 67 q= 33.6 K= 7.58 8.0 Pt 19.6 Pt 59 Q= 162.9 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 13.7 D= 2.203 8.0 0.1715 Pf 1. 4 Pn ------------ 68 q= 34.7 K= 7.58 8.0 Pt 21. 0 Pt 60 Q= 197.7 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 16.6 D= 2.203 8.0 0.2454 Pf 2.0 Pn ------------ 69 q= 36.3 K= 7.58 5.0 Pt 23.0 Pt 61 Q= 234.0 F=ET 20.5 C= 120 Pe 0.4 Pv Vf/s= 19.7 D= 2.203 25.5 0.3353 Pf 8.6 Pn 70 Pt 31.9 17.9 -0.0 17.8 18.0 -0.2 17.8 18.2 -0.4 17.8 18.7 -0.8 17.9 19.6 -1.3 18.4 21. 0 -1. 9 19.1 23.0 -2.6 20.3 --------------- --------------- --------------- --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 71 q= 32.7 K= 7.58 8.0 Pt 18.6 Pt 18.6 62 Q= 32.7 F= 0.0 C= 120 Pe 0.0 Pv -0.1 Vf/s= 2.7 D= 2.203 8.0 0.0088 Pf 0.1 Pn 18.5 --------------------------- 72 q= 32.7 K= 7.58 8.0 Pt 18.6 Pt 18.6 63 Q= 65.4 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.5 D= 2.203 8.0 0.0316 Pf 0.3 Pn 18.4 --------------------------- 73 q= 33.0 K= 7.58 8.0 Pt 18.9 Pt 18.9 64 Q= 98.4 F= 0.0 C= 120 Pe 0.0 Pv -0.5 Vf/s= 8.3 D= 2.203 8.0 0.0674 Pf 0.5 Pn 18.4 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 19 CARLSBAD OAKS LOT 7, BLDG. D AREA 2: .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 74 q= 33.4 K= 7.58 8.0 Pt 19.4 Pt 19.4 65 Q= 131.8 F= 0.0 C= 120 Pe 0.0 Pv -0.8 66 67 68 Vf/s= 11.l D= 2.203 8.0 0.1158 Pf 0.9 Pn 18.6 ------------ 75 q= 34.2 K= 7.58 8.0 Pt 20.4 Pt Q= 166.0 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 14.0 D= 2.203 8.0 0.1776 Pf 1.4 Pn ------------ 76 q= 35.4 K= 7.58 8.0 Pt 21. 8 Pt Q= 201. 4 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 16.9 D= 2.203 8.0 0.2540 Pf 2.0 Pn ------------ 77 q= 37.0 K= 7.58 5.0 Pt 23.8 Pt Q= 238.4 F=ET 20.5 C= 120 Pe 0.4 Pv Vf/s= 20.1 D= 2.203 25.5 0.3471 Pf 8.8 Pn 78 Pt 33.1 20. 4 -1. 3 19.1 21. 8 -1.9 19.9 23.8 -2.7 21.1 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 69 70 71 72 79 q= 40.8 K= 7.58 8.0 Pt 28.9 Pt 28.9 Q= 40.8 F= 0.0 C= 120 Pe 0.0 Pv -0.l Vf/s= 3.4 D= 2.203 8.0 0.0132 Pf 0.1 Pn 28.8 ------------ 80 q= 40.8 K= 7.58 8.0 Pt 29.0 Pt Q= 81.6 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 6.9 D= 2.203 8.0 0.0477 Pf 0.4 Pn ------------ 81 q= 41.1 K= 7.58 8.0 Pt 29.4 Pt Q= 122.7 F= 0.0 C= 120 Pe 0.0 Pv Vf/s= 10.3 D= 2.203 8.0 0.1015 Pf 0.8 Pn ------------ 82 q= 41.7 K= 7.58 5.0 Pt 30.2 Pt Q= 164.4 F=ET 20.5 C= 120 Pe 0.4 Pv Vf/s= 13.8 D= 2.203 25.5 0.1744 Pf 4.4 Pn 83 Pt 35 .1 29.0 -0.3 28.7 29.4 -0.7 28.7 30.2 -1. 3 28.9 --------------- --------------- --------------- --------------------------------------GENERAL---------------------------------- 54 q= 0.0 K= 0.00 12.0 Pt 31.3 Pt 31.3 80 Q= 231.3 F= 0.0 C= 120 Pe 0.0 Pv -0.2 Vf/s= 5.1 D= 4.310 12.0 0.0125 Pf 0.1 Pn 31.l --------------------------- 62 q= 0.0 K= 0.00 12.0 Pt 31.4 Pt 31".4 81 Q= 463.2 F= 0.0 C= 120 Pe 0.0 Pv -0.7 Vf/s= 10.2 D= 4.310 12.0 0.0452 Pf 0.5 Pn 30.7 --------------------------- 70 q= 0.0 K= 0.00 12.0 Pt 31. 9 Pt 31.9 82 Q= 697.2 F= 0.0 C= 120 Pe 0.0 Pv -1. 6 Vf/s= 15.3 D= 4.310 12.0 0.0964 Pf 1. 2 Pn 30.4 --------------------------- 78 q= 0.0 K= 0.00 12.0 Pt 33.1 Pt 33.l 83 Q= 935.6 F= 0.0 C= 120 Pe 0.0 Pv -2. 8 Vf/s= 20.6 D= 4.310 12.0 0.1662 Pf 2.0 Pn 30.3 --------------------------- GENERAL UNDERGROUND FIRE PROT., INC.714-632-8646 Date: 02-19-04 Sheet 20 CARLSBAD OAKS LOT 7, BLDG. D AREA 2 : .33/3000 PIPE FLOW K-FACTOR LENGTH FRICTION PRESSURE NO. NODE GPM FITTING TYPE FTG LOSS PSI NO. DIAMETER TOTAL PSI/FT NOTES --------------------------------------GENERAL---------------------VERSION 3.0-- 83 q= 0.0 K= 0.00 12.0 Pt 35.1 Pt 35.1 84 Q=ll00.0 F= 0.0 C= 120 Pe 0.0 Pv -3.9 Vf/s= 24.2 D= 4.310 12.0 0.2243 Pf 2.7 Pn 31. 2 --------------------------- 84 q= 0.0 K= 0.00 16.0 Pt 37.8 Pt 37.8 85 Q=ll00.0 F=L 8.4 C= 120 Pe 0.0 Pv -3.9 Vf/s= 24.2 D= 4.310 24.4 0.2240 Pf 5.5 Pn 33.9 --------------------------- 85 q= 0.0 K= 0.00 51. 0 Pt 43.3 Pt 43.3 86 Q=ll00.0 F=2L 16.7 C= 120 Pe 0.0 Pv -3.9 Vf/s= 24.2 D= 4.310 67.7 0.2244 Pf 15.2 Pn 39. 3 --------------------------- 86 q= 0.0 K= 0.00 24.0 Pt 58.4 Pt 58.4 87 Q=ll00.0 F=2L 23.1 C= 120 Pe 6.9 Pv -0.8 Vf/s= 11. 0 D= 6.385 47.1 0.0331 Pf 1.6 Pn 57.6 --------------------------- 87 q= 100.0 ADD HYD FLOW 85.0 Pt 66.9 Pt 66.9 88 Q=l200.0 F=2L 37.0 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.7 D= 7.970 122.0 0.0087 Pf 1.1 Pn 66.5 --------------------------- 88 q= 0.0 K= 0.00 15.0 Pt 68.0 Pt 68.0 89 Q=l200.0 F=LGT 73.9 C= 150 Pe 0.0 Pv -0.4 Vf/s= 7.7 D= 7.970 88.9 0.0087 Pf 0.8 Pn 67.6 --------------------------- 89 q= 400.0 ADD HYD FLOW 70.0 Pt 68.8 Pt 68.8 90 Q=l600.0 F=GT 80.2 C= 150 Pe 0.0 Pv -0.3 Vf/s= 6.8 D= 9.780 150.2 0.0055 Pf 0.8 Pn 68.5 90 <<<<<<<< Supply point >>>>>>>> Pt 69.6 --------------------------- FIXED DEVICE: Double Detector Check Valve Pf 8.0 NOTE: Fixed TOTAL REQUIRED INCLUDING FIXED PRESSURE LOSS Pt 77.6 pressure added. --------------------------------------GENERAL---------------------------------- Hydraulic Program by Beard Provencher & Associates, Incorporated (714) 283-1100