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HomeMy WebLinkAbout2497 OCEAN ST; ; AS080040; Permit10/29/25, 2: 16 PM AS080040 Permit Data City of Carlsbad Sprinkler Permit Job Address: 2497 OCEAN ST Permit Type: SPRINK Parcel No: 2030210800 Lot#: 0 Reference No.: PC#: Permit No: AS080040 Status: ISSUED Applied 3/24/2008 Approved: Issued: Inspector: Project Title: DONALD RESIDENTIAL CONDO THREE FIRE SPRINKLER INSPECTIONS @ $65/EA Applicant: SOUTHLAND FIRE PROTECTION, INC 4733 PT. LOMAAV SAN DIEGO, CA 92107 619-523-1400 about:blank Fees($) 195 Add'I Fees ($) 0 Owner: DONALD FAMILY TRUST 03-19-99 PO BOX 1489 CARLSBAD CA Total($) 195 Balance($) 0 1/1 SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Donald Residential Condominimums 2497 Ocean Street Carlsbad, CA 92008 Unit A, Cale. FILE NUMBER: 07-147 DATE: MAR 11, 2008 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R-3 fu>!',t' plan!'> have ht:cn reviewed for apparent compham.:c with 1he curfl'lll applkahlc code!> and !>lundard!> in fon;c m thl' jun"l.11l'111111. Tilt' owner or t:nnlroctnr may ut,llll' 1h1-. 1,·, 1L"W 111 !>Uppon ofiln apphca11on for a huildi11g pnm11 1., 1th the l''<prt'!>~ understanding 1ha1 thl!> rcVll'W 1n 11" way rd11:,,cs lhc o.wner or <.·unlraclor or their pmkss1onal cnginter or an:hill.'CI for soJc rci.p,111-..,ihility for fuU compliance wilh said code,;. and siandards, including W huildin~ code nr for any r_csponsihihy for d"•licu~ni.:ics. errors. omili.),inns or ll(1lii,e-11ec in 1ht:se plans whcthl'r or nol no1cd in 1his review. Do": ~ ~/ 01!, Rovicwer: ,f:1,,/ □ Rf.COMMEND APPMOVAL fZI RECOMMEND APPROVAL. AS NOTED DENSITY: .05 gpm/sq. ft. AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: Master Bedroom 256 sq. ft. 2 sprinklers 26.1 gpm 31.1 gpm 26.1 gpm @ 23.6 psi 1/2 inch Southland Fire Protection, Inc Sorida Phan Carlsbad Fire Department C-16 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 TUCKER, GA 30084 CARLS ► a.. ~ c..:, lw..l __. -..... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 67.5 20.0 1100.0 67.4 31.1 40.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31. 1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 37.0 SOURCE 40.3 31.1 2 40.0 ----38.6 --- 3 40.0 ----31. 6 --- 3A 40.0 HOSE STREAM 31. 3 5.0 4 40.0 ---29.9 4A 40.0 ---23.9 5 40.0 23.8 --- 6 35.0 ----25.1 --- 7 36.0 24.5 --- 8 36.0 24.3 --- BOR 37.0 ---23.6 TOR 47.0 17.1 --- 9 47.0 16.7 --- 10 47.0 15.9 --- 11 47.0 16.7 --- 12 47.0 16.6 --- 13 47.0 16.6 --- 14 47.0 16.0 --- 15 36.0 20.9 16 36.0 21. 2 --- 17 36.0 21. 2 --- 18 36.0 ---21. 2 --- 19 36.0 21. 2 --- 20 36.0 ---21. 3 --- 30 58.0 10.4 --- 31 58.0 9.9 --- 32 58.0 ---9.8 33 58.0 9.5 --- 34 58.0 ---8.6 --- 35 58.0 ---7.7 --- 36 58.0 7.2 --- 37 58.0 ---7.3 38 58.0 ---9.1 39 58.0 10.7 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI I (GPM) 40 58.0 10.9 --- 41 58.0 9. 3 --- 42 58.0 9. 3 --- 43 58.0 9.6 --- Sl 58.0 K= 4.90 7.0 13.0 S2 58.0 K= 4.90 7.1 13.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A PIPE DATA 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: 1 31.1 1.959 PL 21.33 PF 0.4 1 37.0 SRCE 40.3 (N/A) 3.3 150 FTG ETG PE -1. 3 2 40.0 0. 0 38.6 0.0 0.009 TL 40.33 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 40.0 0.0 38.6 0.0 7.0 psi, 31.1 gpm 3 40.0 0.0 31. 6 0.0 Pipe: 3 31.1 0.995 PL 1.00 PF 0. 4 3 40.0 0.0 31. 6 0.0 12.8 150 FTG C PE 0.0 3A 40.0 H.S. 31. 3 5.0 0.252 TL 1.50 PV Pipe: 3A 26.1 0.995 PL 1.00 PF 1. 3 3A 4 0. 0 H.S. 31. 3 5.0 10.8 120 FTG T PE 0.0 4 40.0 0.0 29.9 0.0 0.275 TL 4.87 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 4 40.0 0.0 29.9 0. 0 6.0 psi, 26.1 gpm 4A 40.0 0.0 23.9 0.0 Pipe: 4A 2 6. 1 1. 481 PL 1.00 PF 0.1 4A 40.0 0.0 23.9 0.0 4. 9 150 FTG E PE 0.0 5 40.0 0.0 23.8 0. 0 0.026 TL 5.00 PV Pipe: 5 2 6. 1 1.610 PL 42.58 PF 0.8 5 40.0 0.0 23.8 0.0 4. 1 150 FTG E PE 2.2 6 35.0 0.0 25.1 0.0 0.017 TL 48.62 PV Pipe: 6 26 .1 1.481 PL 4.00 PF 0.2 6 35.0 0.0 25.1 0.0 4. 9 150 FTG E PE -0.4 7 36.0 0. 0 24.5 0. 0 0.026 TL 8.00 PV Pipe: 7 2 6. 1 1.481 PL 1.00 PF 0.1 7 36.0 0.0 24.5 0.0 4. 9 150 FTG E PE 0.0 8 36.0 0.0 24.3 0.0 0.026 TL 5.00 PV Pipe: 8 26.1 1. 245 PL 1.00 PF 0. 2 8 36.0 0.0 24.3 0.0 6.9 150 FTG E PE -0.4 BOR 37.0 0.0 23.6 0.0 0.061 TL 4.00 PV Pipe: 9 26.1 1.101 PL 10.00 PF 2.2 BOR 37.0 0.0 23.6 0.0 8.8 150 FTG 10.0 PE -4.3 TOR 47.0 0. 0 17.1 0.0 0. 111 TL 20.00 PV Pipe: 10 15.1 1.101 PL 5.25 PF 0.4 TOR 4 7. 0 0. 0 17. 1 0.0 5 .1 150 FTG 5.0 PE 0.0 9 47.0 0.0 16.7 0. 0 0.040 TL 10.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 11 15.1 1.101 PL 13.25 PF 0.8 9 47.0 0.0 16.7 0.0 5.1 150 FTG 6.0 PE 0.0 10 47. 0 0.0 15.9 0.0 0.040 TL 19.25 PV Pipe: 12 15.1 1.101 PL 11. 00 PF 0. 7 10 47.0 0.0 15.9 0.0 5.1 150 FTG 7.0 PE -4. 8 30 58.0 0.0 10.4 0.0 0.040 TL 18.00 PV Pipe: 13 11. 0 1.101 PL 6.33 PF 0. 4 TOR 47.0 0.0 1 7. 1 0.0 3. 7 150 FTG 12.0 PE 0.0 11 47.0 0.0 16.7 0.0 0.023 TL 18.33 PV Pipe: 14 4.6 1.101 PL 7.00 PF 0.1 11 47.0 0.0 16.7 0.0 1. 6 150 FTG 5.0 PE 0.0 12 47.0 0.0 16.6 0.0 0.004 TL 12.00 PV Pipe: 15 4.6 1.101 PL 11. 00 PF 0 .1 12 47.0 0.0 16.6 0.0 1. 6 150 FTG 6.0 PE 4. 8 20 36.0 0. 0 21. 3 0.0 0.004 TL 17.00 PV Pipe: 16 6.4 1.101 PL 9.33 PF 0. 1 11 47.0 0. 0 16.7 0.0 2.2 150 FTG 6.0 PE 0.0 13 4 7. 0 0.0 16.6 0.0 0.008 TL 15.33 PV Pipe: 17 6.4 1.101 PL 38.00 PF 0.5 13 4 7. 0 0.0 16.6 0.0 2.2 150 FTG 25.0 PE 0.0 14 47.0 0.0 16.0 0.0 0.008 TL 63.00 PV Pipe: 18 -4.6 1.101 PL 11. 00 PF 0.1 14 47.0 0.0 16.0 0.0 1. 6 150 FTG 5.0 PE 4. 8 15 36.0 0. 0 20.9 0.0 0.004 TL 16.00 PV Pipe: 19 -4.6 1.101 PL 45.09 PF 0.3 15 36.0 0. 0 20.9 0.0 1. 6 150 FTG 23.0 PE 0.0 16 36.0 0.0 21. 2 0.0 0.004 TL 68.09 PV Pipe: 20 -1. 6 1.101 PL 9.67 PF 0.0 16 36.0 0.0 21. 2 0.0 0. 5 150 FTG 6.0 PE 0.0 17 36.0 0.0 21. 2 0. 0 0.001 TL 15.67 PV Pipe: 21 -1. 6 1.101 PL 10.33 PF 0.0 17 36.0 0.0 21. 2 0.0 0. 5 150 FTG 5.0 PE 0.0 18 36.0 0.0 21. 2 0.0 0.001 TL 15.33 PV Pipe: 22 -1. 6 1.101 PL 9.67 PF 0.0 18 36.0 0.0 21. 2 0.0 0. 5 150 FTG 6.0 PE 0.0 19 36.0 0.0 21. 2 0.0 0.001 TL 15.67 PV Pipe: 23 -4.6 1.101 PL 4. 41 PF 0.1 19 36.0 0.0 21. 2 0.0 1. 6 150 FTG 20.0 PE 0.0 20 36.0 0.0 21. 3 0. 0 0.004 TL 24.41 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A 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: 23A -3.0 1.101 PL 10.33 PF 0.0 16 36.0 0. 0 21.2 0. 0 1.0 150 FTG 5.0 PE 0.0 19 36.0 0. 0 21. 2 0. 0 0.002 TL 15.33 PV Pipe: 24 11. 0 1. 101 PL 11. 00 PF 0.4 14 47.0 0. 0 16.0 0.0 3.7 150 FTG 5. 0 PE -4.8 40 58.0 0. 0 10.9 0.0 0.023 TL 16.00 PV Pipe: 25 15.1 1. 101 PL 7.83 PF 0.5 30 58.0 0.0 10.4 0.0 5.1 150 FTG 5. 0 PE 0.0 31 58.0 0.0 9. 9 0.0 0.040 TL 12.83 PV Pipe: 26 9.4 1.101 PL 3.08 PF 0.1 31 58.0 0.0 9. 9 0.0 3.2 150 FTG 5.0 PE 0.0 32 58.0 0.0 9. 8 0.0 0.017 TL 8.08 PV Pipe: 27 9.4 1.101 PL 9.83 PF 0. 2 32 58.0 0.0 9.8 0. 0 3.2 150 FTG 5. 0 PE 0. 0 33 58.0 0.0 9.5 0.0 0.017 TL 14.83 PV Pipe: 28 9.4 1.101 PL 43.50 PF 0.9 33 58.0 0.0 9. 5 0.0 3.2 150 FTG 11. 0 PE 0.0 34 58.0 0.0 8. 6 0.0 0.017 TL 54.50 PV Pipe: 29 9.4 1.101 PL 42.00 PF 0. 9 34 58.0 0.0 8.6 0.0 3.2 150 FTG 14.0 PE 0.0 35 58.0 0. 0 7.7 0.0 0.017 TL 56.00 PV Pipe: 30 9.4 1.101 PL 15.92 PF 0.5 35 58.0 0.0 7. 7 0.0 3.2 150 FTG 12.0 PE o.o 36 58.0 0.0 7.2 0.0 0.017 TL 27.92 PV Pipe: 31 13.0 1. 101 PL 0.50 PF 0.2 36 58.0 0. 0 7.2 0.0 4.4 150 FTG 5.0 PE 0.0 Sl 58.0 4. 9 7.0 13. 0 0.031 TL 5.50 PV Pipe: 32 -3.6 1.101 PL 17.00 PF 0.1 36 58.0 0. 0 7.2 0.0 1. 2 150 FTG 12.0 PE 0.0 37 58.0 0. 0 7.3 0.0 0.003 TL 29.00 PV Pipe: 33 13.1 1.101 PL 0.50 PF 0.2 37 58.0 0.0 7.3 0.0 4.4 150 FTG 5.0 PE 0.0 S2 58.0 4. 9 7.1 13.1 0.031 TL 5.50 PV Pipe: 34 -16.7 1.101 PL 28.25 PF 1. 8 37 58.0 0.0 7. 3 0.0 5.6 150 FTG 9.0 PE 0.0 38 58.0 0.0 9. 1 0. 0 0.049 TL 37.25 PV Pipe: 35 -11. 0 1.101 PL 41.59 PF 1. 6 38 58.0 0.0 9.1 0.0 3. 7 150 FTG 31. 0 PE 0.0 39 58.0 0.0 10.7 0.0 0.023 TL 72.59 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 3/11/2008 C:\HASS78\07-147.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT A PIPE TAG END NODES ELEV. (FT) 39 40 38 41 41 42 42 43 43 31 Pipe: 36 58.0 58.0 Pipe: 37 58.0 58.0 Pipe: 38 58.0 58.0 Pipe: 39 58.0 58.0 Pipe: 40 58.0 58.0 NOTES (HASS): NOZ. (Kl 0. 0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 PT (PSI) 10.7 10.9 9. 1 9.3 9. 3 9.3 9. 3 9. 6 9.6 9. 9 Q(GPM) DISC. VEL(FPS) (GPM) -11. 0 0.0 3.7 0. 0 -5.7 0.0 1.9 0.0 -5.7 0.0 1.9 0.0 -5.7 0.0 1.9 0.0 -5.7 0.0 1.9 0.0 DIA(IN) HW(C) FL/FT 1.101 PL 150 FTG 0.023 TL 1. 101 PL 150 FTG 0.007 TL 1.101 PL 150 FTG 0.007 TL 1.101 PL 150 FTG 0.007 TL 1.101 PL 150 FTG 0.007 TL LENGTH (FT) 1. 92 5. 0 6. 92 15.67 7.0 22.67 8.08 5.0 13.08 32.00 9. 0 41. 00 21. 58 20.0 41. 58 PRESS. SUM. (PSI) PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV 0.2 0.0 0.2 0.0 0.1 0. 0 0. 3 0.0 0.3 0.0 (11 Calculations were performed by the HASS 7.9 computer program under license no. 27091255 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 0.087 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.8 ft/sec at pipe 3. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 3/11/2008 JOB TITLE: DONALD C:\HASS78\07-147.SDF RESIDENTIAL CONDOMINIMUMS UNIT A 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 0.995 1. 55 3.87 1. 55 3.87 4.64 0. 77 7.73 7.73 3.87 1.101 2.53 6.33 2.53 6.33 7.59 1. 27 12.66 12.66 6.33 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C s G N Ell Tee 45-Ell TeeRun Couplg SwgChk GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.50 6.00 1.00 6.00 1. 245 3.00 5.00 1.00 2.00 0.50 6.00 1.00 5.00 1.481 4.00 8.00 2.00 3.00 0.50 9.00 1.00 8.00 1.959 6.00 12.00 3.00 4.00 0.50 13.00 1.00 12.00 NOTES (USER) : 80.0 70.0 ;;I 1"" G A u G E p R E 60.0 50.0 S 4o.o2 s u R E 30.0 P 20.0 s i 10.0 0.0 -14.7 I B ~ 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 67.50 psi Resid: 20.00 psi Flow: 1100.0 gpm 1200 ~ 1400 FLOW (GPM) 1 ~ 2 ~ 1600 LEGEND Available pressure 67.44 psi @ 31. 1 gpm Required pressure 40.31 psi @ 31. 1 gpm A. Source Supply Curve 8. System Demand Curve 1800 Ca 0 o:,, t:Il >-l M >-l •• H >-l w t-< '---M c-' • • c-' '---ON oo zo :,, 00 t-< 0 :x, M U) U) CJ H :x, 0 H M z z ~ >-l t-< H M :,, ?;J t-< U) n >< 0 U) z >-l 0 M 0 3: 3: H ::c z >< H 0 3: :x, C :,, 3: C U) t-< H C n z H :,, >-l z :,, :,, t-< >< U) H () U) / ::c :,, U) U) -..J 00 / 0 -..J I c-' .c, CJ -..J u, cQ U) (D 0 "'~ ---j 2000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 3/11/2008 C:\HASS78\07-147.SDF RESIDENTIAL CONDOMINIMUMS UNIT A JOB TITLE: DONALD WATER SUPPLY CURVE 72+ I I 0 66\ I\ I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ I \ P 4 8+ \ R E s I \ I \ I \ S 42+ \ u R E p s X \ I \ I \ 36+ \ I \ I \ I \ I 30+ \ I I \ I \ I \ 24+ \ I \ I \ I * <-20.0 psi@ 1100 gprn 18+ Flow Test Point I I !==============-=============== 12+ LEGEND " I " I X Required Water Supply " I 40.31 psi @ 31.1 gprn " 6+ " I 0 = Available Water Supply " I 67.44 psi @ 31. 1 gprn " I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Donald Residential Condominimums 2497 Ocean Street Carlsbad, CA 92008 Unit B, Cale. FILE NUMBER: 07-147 DATE: MAR 11, 2008 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R-3 DENSITY: .05 gpm/sq. ft. AREA OF APPLICATION: Master Bedroom COVERAGE PER SPRINKLER: 256 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 26.1 gpm TOTAL WATER REQUIRED (including hose): 31.1 gpm FLOW AND PRESSURE (@ BOR): SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: 26.1 gpm@ 21.1 psi 1/2 inch Southland Fire Protection, Inc. Sorida Phan Carlsbad Fire Department C-16 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 TUCKER, GA 30084 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3/11/2008 JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ PRESS. @ TAG (PSI) I PSI) (GPM) (PSI) 1 67.5 20.0 1100. 0 67.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 2 6. 1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE (FT) (PSI) 1 37.0 SOURCE 37.7 2 40.0 ----36.0 3 40.0 ----29.0 3A 40.0 HOSE STREAM 28.7 4 40.0 ----27.4 4A 40.0 ----21. 4 5 4 0. 0 ----21. 2 6 35.0 ----22.6 7 36.0 ----21. 9 8 36.0 ---21. 8 BOR 37.0 ----21.1 TOR 47.0 ----14.6 9 47.0 ----12.4 10 47.0 ----10.3 11 47.0 9.0 12 47.0 8.8 13 47.0 7.2 14 47.0 ----7. 3 15 47.0 ----7. 8 16 47.0 8. 0 17 47.0 ----8.0 20 36.0 ---13.4 21 36.0 ----13.2 22 36.0 ----13.2 23 36.0 13. 1 24 36.0 13.0 25 36.0 ----13. 0 26 36.0 13.2 Sl 47.0 K-4.90 7. 0 S2 4 7. 0 K-4.90 7. 1 C:\HASS78\07-147 B.SDF TOTAL REQ'D DEMAND PRESS. (GPM) (PSI) 31.1 37.7 DISCHARGE (GPM) 31.1 --- --- 5.0 --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- 13.0 13.1 •--~#• ••W--••--~--~--- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 3/11/2008 C:\HASS78\07-147 B.SDF -JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT I PSI) Pipe: 1 31. 1 1. 959 PL 21. 33 PF 0.4 1 37.0 SRCE 37.7 (N/A) 3.3 150 FTG ETG PE -1. 3 2 40.0 0. 0 36.0 0.0 0.009 TL 40.33 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 40.0 0.0 36.0 0.0 7.0 psi, 31.1 gpm 3 40.0 0. 0 29.0 0.0 Pipe: 3 31. 1 0.995 PL 1. 00 PF 0.4 3 40.0 0.0 29.0 0.0 12.8 150 FTG C PE 0.0 3A 40.0 H.S. 28.7 5.0 0.252 TL 1. 50 PV Pipe: 4 2 6. 1 0.995 PL 1. 00 PF 1. 3 3A 40.0 H.S. 28.7 5.0 10.8 150 FTG T PE 0. 0 4 40.0 0.0 27.4 0.0 0.182 TL 7.00 PV Pipe: 5 FIXED PRESSURE LOSS DEVICE 4 40.0 0.0 27.4 0.0 6. 0 psi, 26.1 gpm 4A 40.0 0.0 21. 4 0.0 Pipe: 6 26.1 1. 4 81 PL 1. 00 PF 0.1 4A 40.0 0. 0 21. 4 0.0 4.9 150 FTG E PE 0.0 5 40.0 0.0 21. 2 0.0 0.026 TL 5.00 PV Pipe: 7 26.1 1. 610 PL 42.58 PF 0.8 5 40.0 0. 0 21. 2 0.0 4 .1 150 FTG E PE 2. 2 6 35.0 0.0 22.6 0. 0 0.017 TL 48.62 PV Pipe: 8 26.1 1. 4 81 PL 4.00 PF 0.2 6 35.0 0. 0 22.6 0.0 4. 9 150 FTG E PE -0.4 7 36.0 0.0 21. 9 0. 0 0.026 TL 8.00 PV Pipe: 9 26.1 1. 4 81 PL 1.00 PF 0.1 7 36.0 0. 0 21. 9 0. 0 4. 9 150 FTG E PE 0. 0 8 36.0 0. 0 21. 8 0.0 0.026 TL 5.00 PV Pipe: 10 26.1 1. 245 PL 1.00 PF 0.2 8 36.0 0.0 21. 8 0.0 6. 9 150 FTG E PE -0.4 BOR 37.0 0.0 21.1 0.0 0.061 TL 4.00 PV Pipe: 11 26.1 1.101 PL 10.00 PF 2. 2 BOR 37.0 0. 0 21. 1 0.0 8.8 150 FTG 10.0 PE -4.3 TOR 47.0 0.0 14.6 0.0 0. 111 TL 20.00 PV Pipe: 12 2 6. 1 1.101 PL 5.00 PF 2.1 TOR 47.0 0.0 14.6 0. 0 8.8 150 FTG 14.0 PE 0.0 9 47.0 0.0 12.4 0.0 0 .111 TL 19.00 PV ··•-·4-~- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/11/2008 C:\HASS78\07-147 B. SDF -JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B 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: 13 2 6. 1 1.101 PL 14.00 PF 2. 1 9 47.0 0.0 12.4 0.0 8.8 150 FTG 5.0 PE 0. 0 10 47.0 0. 0 10.3 0.0 0 .111 TL 19.00 PV Pipe: 14 16.1 1.101 PL 24.20 PF 1. 4 10 47.0 0.0 10.3 0.0 5. 4 150 FTG 6.0 PE 0. 0 11 47.0 0.0 9. 0 0.0 0.045 TL 30.20 PV Pipe: 15 6.8 1.101 PL 10.75 PF 0.2 11 47.0 0.0 9.0 0.0 2.3 150 FTG 13.0 PE 0.0 12 47.0 0.0 8.8 0.0 0.009 TL 23.75 PV Pipe: 16 9.3 1.101 PL 77. 32 PF 1. 7 11 47.0 0.0 9.0 0.0 3.1 150 FTG 29.0 PE 0. 0 13 47.0 0. 0 7.2 0.0 0.016 TL 106.32 PV Pipe: 16A 13.0 1.101 PL 1.00 PF 0. 2 13 47.0 0.0 7.2 0.0 4.4 150 FTG 5.0 PE 0. 0 Sl 4 7. 0 4. 9 7. 0 13. 0 0.031 TL 6.00 PV Pipe: 16B -3.7 1.101 PL 14.92 PF 0.1 13 47.0 0.0 7. 2 0.0 1. 3 150 FTG 12.0 PE 0.0 14 47.0 0.0 7.3 0.0 0.003 TL 26.92 PV Pipe: 17 13.1 1.101 PL 1. 17 PF 0.2 14 47.0 0.0 7.3 0.0 4.4 150 FTG 5.0 PE 0.0 S2 47.0 4.9 7. 1 13.1 0.031 TL 6.17 PV Pipe: 18 -16.8 1.101 PL 6.00 PF 0.5 14 47.0 0. 0 7. 3 0.0 5.7 150 FTG 5.0 PE 0.0 15 47.0 0. 0 7. 8 0.0 0.049 TL 11. 00 PV Pipe: 18A -6.8 1.101 PL 7.42 PF 0.1 15 47.0 0.0 7. 8 0.0 2.3 150 FTG 6.0 PE 0.0 16 47.0 0.0 8. 0 0.0 0.009 TL 13.42 PV Pipe: 18B -6.8 1.101 PL 1.00 PF 0.1 16 47.0 0.0 8.0 0.0 2.3 150 FTG 5.0 PE 0.0 17 47.0 0.0 8.0 0.0 0.009 TL 6.00 PV Pipe: 19 -10.0 1.101 PL 82.74 PF 2.5 15 4 7. 0 0.0 7. 8 0.0 3.4 150 FTG 49.0 PE 0.0 10 47.0 0.0 10.3 0. 0 0.019 TL 131.74 PV Pipe: 20 6.8 1.101 PL 11. 00 PF 0.2 12 47.0 0.0 8. 8 0. 0 2.3 150 FTG 7.0 PE 4.8 20 36.0 0.0 13.4 0. 0 0.009 TL 18.00 PV Pipe: 21 -6.8 1.101 PL 11. 00 PF 0.2 17 47.0 0.0 8.0 0. 0 2.3 150 FTG 7. 0 PE 4. 8 25 36.0 0.0 13.0 0.0 0.009 TL 18.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/11/2008 C:\HASS78\07-147 B.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B PIPE TAG END NODES ELEV. (FT) 20 21 21 22 22 23 23 24 24 25 25 26 26 21 Pipe: 21A 36.0 36.0 Pipe: 22 36.0 36.0 Pipe: 23 36.0 36.0 Pipe: 24 36.0 36.0 Pipe: 25 36.0 36.0 Pipe: 26 36.0 36.0 Pipe: 27 36.0 36.0 NOTES (HASS): NOZ. (K) 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 0.0 PT ( PSI) 13.4 13.2 13.2 13. 2 13.2 13.1 13.1 13.0 13.0 13.0 13.0 13.2 13.2 13.2 Q(GPM) DISC. VEL(FPS) (GPM) 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 0.0 6.8 2.3 2.2 0.8 2.2 0.8 2.2 0.8 2.2 0.8 -4.5 1.5 -4.5 1. 5 DIA(IN) HW(C) FL/FT 1.101 PL 150 FTG 0.009 TL 1.101 PL 150 FTG 0.001 TL 1.101 PL 150 FTG 0.001 TL 1.101 PL 150 FTG 0.001 TL 1.101 PL 120 FTG 0.002 TL 1. 101 PL 150 FTG 0.004 TL 1. 101 PL 150 FTG 0.004 TL LENGTH (FT) 5.00 7.0 12.00 38.34 31. 0 69.34 65.25 28.0 93.25 34.58 34.0 68.58 4.75 5.0 9.75 41.91 19.0 60.91 1. 25 5. 0 6.25 PRESS. SUM. (PSI) PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV 0.1 0.0 0.1 0.0 0.1 0. 0 0. 1 0. 0 0. 0 0.0 0.3 0.0 0.0 0.0 (1) Calculations were performed by the HASS 7.9 computer program under license no. 27091255 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 0.006 gpm and a maximum imbalance at any node of 0.165 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.8 ft/sec at pipe 3. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/11/2008 C:\HASS78\07-147 B.SDF JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B (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 1.101 2.53 6.33 2.53 6.33 7.59 l. 27 12.66 12.66 6.33 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C s G N Ell Tee 45-Ell TeeRun Couplg SwgChk GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.50 6.00 1.00 6.00 l. 245 3.00 5.00 l. 00 2.00 0.50 6.00 l. 00 5.00 1. 4 81 4.00 8.00 2.00 3.00 0.50 9.00 1.00 8.00 1.959 6.00 12.00 3.00 4.00 0.50 13. 00 1.00 12.00 NOTES (USER) : 80.0 70.01 ~ G A 60.0 u G E p R E 50.0 S 40.0 s 2 u R E 30.0 p 20.0 s i 10.0 0.0 -14.7 B ' 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 67.50 psi Resid: 20.00 psi Flow: 1100.0 gpm 1200 1400 FLOW (GPM) 1 2 1600 ~ ~ LEGEND Available pressure 67.44 psi @ 31.l gpm Required pressure 37.70 psi @ 31.l gpm A. Source Supply Curve B. System Demand Curve 1800 ----i 2000 Ca tJ 0 :i, tJJ >'l M >'l •• H >cl w t--< '--M f--' •• f--' '--tJ N oo zo :i, 0) t--< tJ ::0 M UJ UJ H 'U tJ ::0 M H z z >'l ~ H t--< :i, M t--< ::0 0 UJ 0 >-< z UJ tJ >'l 0 M 3: 3: H z :i: H >-< 3: tJ C ::0 3: :i, UJ C t--< C H z 0 H >'l :i, z tJJ >' t--< >-< 0 UJ H /UJ :i: :i, UJ UJ ._.J 0) / 0 ._.J I f--' "" ._.J I 'U tJJ '" "" UJ 11) tJ "'] ._.J SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 3/11/2008 JOB TITLE: DONALD RESIDENTIAL CONDOMINIMUMS UNIT B WATER SUPPLY CURVE 72+ I I 0 66\ I\ I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ I \ P 48+ \ R I \ E I \ s I \ S 42+ \ u I \ R I \ E X \ 36+ \ I \ P I \ s I \ I 30+ \ ) I \ I \ I \ 24+ \ I \ I \ I * <-20.0 psi@ 1100 gprn 18+ Flow Test Point I I I============================== 12+ LEGEND " I " I X = Required Water Supply " I 37.70 psi @ 31. 1 gprn " 6+ " I 0 = Available Water Supply " I 67.44 psi @ 31. 1 gprn " I " C:\HASS78\07-147 B.SDF 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)