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1100 LAS FLORES; ; AS050184; Permit
3/12/24, 5:15 PM AS050184 Permit Data City of Carlsbad Sprinkler Permit 1100 LAS FLORES Job Address: DR Permit Type: SPRINK Parcel No: 1551803100 Lot #: 0 Reference No.: Permit No: AS050184 Status: APPROVED Applied 9/14/2005 Approved: 9/20/2005 Issued: 9/20/2005 PC #: Inspector: Project Title: BUENA VISTA VILLAGE FIRE SPRINKLER PLAN CHECK & INSPECTIONS Applicant: INNOVATIVE FIRE PROTECTION 405 VERNON WAY EL CAJON (619) 593-8200 Owner: PACIFIC LIBERTY INC 991 C LOMAS SANTA FE DR #441 SOLANA BEACH CA L Fees ($) Add'I Fees($) Total ($) Balance ($) L 1,150 F 0 -* 1,150 0 about:blank 1/1 05/11/2005 14:23 6195939133 INNOVATIVE FIRE PAGE @1 V... r"ry An\1ç 4cL Ler1 — Telephone numbJt'? •e' (i#) Fax Number '( Location of hydrants (address at other) static: - 1k • PSI Realduil _____ PSI PItol ________ P81 Flow 1ti. 3PM Oats, .__j ILj200 TIrnD of day: 1O .00 A.M Tsat.dby: 1PPi -IP. - fUI1! Do not wrft in this bar. Cross Street . 0f 3w. ar 4ep 44 Thomas 8rethers map page & grid ftQ '4 Draw an *ccur.ite map and .spnclty hydrant to (low (F) and hydrant to gauge (G). 4opa-nA WA fLoavo ¶L4 irt rr SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF J0B ITLE: -- ------- -------------- -. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL NODE PRESS. PRESS. @ PRESS. 0 DEMAND TAG (PSI) (PSI) (GPM) (PSI) (GPM) TEST 76.0 70.0 1181.0 74.5 559.2 AGGREGATE FLOW ANALYSIS: 07 REQ' D PRESS. 65.9 Aso4- TOTAL FLOW AT SOURCE 559.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 59.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 65.9 59.2 RP -1.0 - - - - 65.9 DA -1.0 - - - - 52.9 U.1 -1.0 - - - - 52.9 - - - BOR 0.5 - - - - 52.2 - - - TOR 7.5 - - - - 49.1 - - - 1 8.2 - - - - 48.7 - - - Bi 8.2 - - - - 39.8 - - - Cvi 15.5 - - - - 33.3 2 20.0 - - - - 29.2 - - - 3 31.0 - - - - 24.1 - - - 4 31.0 - - - - 22.4 - - - 5 41.0 - - - - 17.5 - - - 6 42.5 - - - - 15.8 - - - 6A 42.0 - - - - 16.0 - - - 7 41.0 - - - - 15.1 - - - 7A 42.0 - - - - 14.7 - - - 8 41.0 - - - - 14.7 - - - 9 31.0 - - - - 17.8 - - - 10 31.0 - - - - 14.2 - - - 11 32.5 - - - - 10.3 - - - hA 32.0 K= 4.90 10.2 15.7 12A 32.0 K= 4.90 9.7 15.3 13 32.5 - - - - 8.5 13A 32.0 K= 4.90 8.4 14.2 14A 32.0 K= 4.90 8.2 14.0 15 20.0 - - - - 23.8 - - - 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF ' JOB TITLE: BUENA VISTA BUILDING #1 -FOUR----HEAD -eALC - 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 59.2 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 65.9 (N/A) 0.7 150 FTG TLG PE 0.0 RP -1.0 0.0 65.9 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 65.9 0.0 13.0 psi, 59.2 gpm DA -1.0 0.0 52.9 0.0 Pipe: 3 59.2 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 52.9 0.0 0.7 150 ETG 3L PE 0.0 (3.1 -1.0 0.0 52.9 0.0 0.000 TL 138.71 PV Pipe: 4 59.2 6.000 PL 5.00 PF 0.0 (3.1 -1.0 0.0 52.9 0.0 0.7 150 FTG E PE -0.6 BOR 0.5 0.0 52.2 0.0 0.000 TL 25.07 PV Pipe: 5 59.2 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 52.2 0.0 1.5 120 FTG C PE -3.0 TOR 7.5 0.0 49.1 0.0 0.001 TL 28.50 PV Pipe: 6 59.2 4.000 PL 42.00 PF 0.1 TOR 7.5 0.0 49.1 0.0 1.5 120 FTG 3E PE -0.3 1 8.2 0.0 48.7 0.0 0.001 TL 72.00 PV Pipe: 7 59.2 1.442 PL 31.50 PF 8.9 1 8.2 0.0 48.7 0.0 11.6 120 FTG 2T PE 0.0 Bi 8.2 0.0 39.8 0.0 0.205 TL 43.50 PV Pipe: 8 59.2 1.442 PL 7.00 PF 3.3 Bi 8.2 0.0 39.8 0.0 11.6 120 FTG ET PE -3.1 Cvi 15.5 0.0 33.3 0.0 0.205 TL 16.00 PV Pipe: 9 59.2 1.400 PL 4.00 PF 2.2 Cvi 15.5 0.0 33.3 0.0 12.3 120 FTG EC PE -1.9 2 20.0 0.0 29.2 0.0 0.237 TL 9.29 PV Pipe: 10 12.9 1.400 PL 10.00 PF 0.3 2 20.0 0.0 29.2 0.0 2.7 120 FTG ETR PE -4.8 3 31.0 0.0 24.1 0.0 0.014 TL 19.26 PV Pipe: 11 12.9 1.101 PL 24.00 PF 1.7 3 31.0 0.0 24.1 0.0 4.4 120' FTG E3T PE 0.0 4 31.0 0.0 22.4 0.0 0.046 TL 37.24 PV Pipe: 12 12.9 1.101 PL 10.00 PF 0.6 4 31.0 0.0 22.4 0.0 4.4 120 FTG ER PE -4.3 5 41.0 0.0 17.5 0.0 0.046 TL 13.97 PV Pipe: 13 12.9 1.101 PL 4.00 PF 1.0 5 41.0 0.0 17.5 0.0 4.4 120 FTG 4ET2R PE -0.6 6 42.5 0.0 15.8 0.0 0.046 TL 21.87 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page-3 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOBTITLE: BUENAVISTABUILDING-#1FOUR HEAD CALC -- 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 1.101 PL 0.50 PF 0.0 6 42.5 0,0 15.8 0.0 0.0 120 FTG TR PE 0.2 6A 42.0 0.0 16.0 0.0 0.000 TL 4.47 PV Pipe: 15 12.9 1.101 PL 19.50 PF 1.4 6 42.5 0.0 15.8 0.0 4.4 120 FTG 2ETR PE 0.6 7 41.0 0.0 15.1 0.0 0.046 TL 30.09 PV Pipe: 16 0.0 1.101 PL 17.50 PF 0.0 7 41.0 0.0 15.1 0.0 0.0 120 FTG 4E2TR PE -0.4 7A 42.0 0.0 14.7 0.0 0.000 TL 38.02 PV Pipe: 17 12.9 1.101 PL 7.50 PF 0.3 7 41.0 0.0 15.1 0.0 4.4 120 FTG ---- PE 0.0 8 41.0 0.0 14.7 0.0 0.046 TL 7.50 PV Pipe: 18 12.9 1.101 PL 18.00 PF 1.3 8 41.0 0.0 14.7 0.0 4.4 120 FTG E2T PE 4.3 9 31.0 0.0 17.8 0.0 0.046 TL 27.93 PV Pipe: 19 . 59.2 1.400 PL 11.00 PF 3.6 9 31.0 0.0 17.8 0.0 12.3 120 FTG T PE 0.0 10 31.0 0.0 14.2 0.0 0.237 TL 14.97 PV Pipe: 20 30.9 1.101 PL 4.50 PF 3.3 10 31.0 0.0 14.2 0.0 10.4 120 FTG 2ET PE -0.6 11 32.5 0.0 10.3 0.0 0.230 TL 14.43 PV Pipe: 21 15.7 1.101 PL 0.50 PF 0.3 11 32.5 0.0 10.3 0.0 5.3 120 FTG TR PE 0.2 hA 32.0 4.9 10.2 15.7 0.065 TL 4.47 PV Pipe: 22 15.3 1.101 PL 8.50 PF 0.8 11 32.5 0.0 10.3 0.0 5.1 120 FTG ER PE 0.2 12A 32.0 4.9 9.7 15.3 0.062 TL 12.47 PV Pipe: 23 28.2 1.101 PL 16.50 PF 5.1 10 31.0 0.0 14.2 0.0 9.5 120 FTG 3E PE -0.6 13 32.5 0.0 8.5 0.0 0.195 TL 26.43 PV Pipe: 24 14.2 1.101 PL 0.50 PF 0.2 13 32.5 0.0 8.5 0.0 4.8 150 FTG TR PE 0.2 13A 32.0 4.9 8.4 14.2 0.036 TL 6.50 PV Pipe: 25 14.0 1.101 PL 8.50 PF 0.5 13 32.5 0.0 8.5 0.0 4.7 150 FTG ER PE 0.2 14A 32.0 4.9 8.2 14.0 0.035 TL 14.50 PV Pipe: 26 -46.2 1.400 PL 10.00 PF 1.2 9 31.0 0.0 17.8 0.0 9.6 150 FTG R PE 4.8 15 20.0 0.0 23.8 0.0 0.100 TL 12.00 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF 'JOB-TITLE:-BUENA VISTA BUILDING-#1 FOUR-HEAD-CALC - 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 -46.2 1.400 PL 26.50 PF 5.4 15 20.0 0.0 23.8 0.0 9.6 150 FTG E2T5R PE 0.0 2 20.0 0.0 29.2 0.0 0.100 TL 54.50 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.092 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.3 ft/sec at pipe 19. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880—B1.SDF JOB TITLE: BUENAVISTABUILDING #1---FOUR HEAD CALC - - a) 0) 0. 0.I41 ON a) 00 I-i (1.J 11) C'I 14 • >O U) It) U) IC) 0. in Z winus,o. 14 0 ( 0.I14)U) in 0. 0-rI-dOE '- - Iu)tsu)ow .0 0.0 0.114 '6 I-i U) -I 0 -d ON 0 >i -d IS) Cl ID Cl) Cl) (6 •0. . .. 0 LI) (6NDIXI 04 0 H co '-I '-I 0 H 114 -H U) 01 0 0 0 -o -H U) -.-1 U) 01 0 C/) w 1-4 -H EA 0 0 0 C.'.) 0 04 r1(9 0 i-1 0 0 N '-4 I 0 0 (6. lbi C) 0 c 0 o OD .-1 o 0 0 0 . • • r1 0 0 CD 0 I w (6' C'.) i wow 11I -(IU)-H----- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF --JOB-TITL-E-: -BUENA -VISTA BUILDING #1 -FOUR-H-E-AD-CALC WATER SUPPLY CURVE 84+ 77+ I \\\\\\\\ I \\\\\\\\ 70+ * <-70.0 psi @ 1181 gpm I Flow Test Point I X 63+ P 56+ R I E I S I S 49+ U I R I E I 42+ ( I P I S I I 35+ 28+ 21+ 14+ LEGEND I X = Required Water Supply I 65.89 psi @ 559.2 gpm 7+ I 0 = Available Water Supply I 74.50 psi @ 559.2 gpm 0++-+---+----+-----+ ------+ --------+ --------+---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOB-TITLE: BUENA-VISTA BUILDING -#1 TWO HEAD GA-LC- @-3:12-PITCH---• WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @. DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 74.6 529.4 49.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 529.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 29.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 49.3 29.4 RP -1.0 - - - - 49.3 - - - DA -1.0 - - - - 36.3 - - - U.1 -1.0 - - - - 36.3 - - - BOR 0.5 - - - - 35.7 TOR 7.5 - - - - 32.6 - - - 1 8.2 - - - - 32.3 - - - Bi 8.2 - - - - 29.8 - - - Cvi 15.5 - - - - 25.8 - - - 2 20.0 - - - - 23.2 - - - 3 31.0 - - - - 18.2 - - - 4 31.0 - - - - 16.5 - - - 5 41.0 - - - - 11.5 - - - 6 42.5 - - - - 9.9 - - - 6A 42.0 K= 4.90 9.8 15.4 7 41.0 - - - - 10.6 - - - 7A 42.0 K= 4.90 8.2 14.0 8 41.0 - - - - 11.2 - - - 9 31.0 - - - - 17.5 - - - 10 31.0 - - - - 17.5 ii 32.5 - - - - 16.8 - - - hA 32.0 - - - - 17.1 - - - 12A 32.0 - - - - 17.1 13 32.5 - - - - 16.8 - - - 13A 32.0 - - - - 17.1 - - - 14A 32.0 - - - - 17.1 - - - 15 20.0 - - - - 22.4 - - - V -. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOB-TITLE: BUENA VISTA-BUILDING-#1--TWO-HEAD-CALC @3:12 PITCH - 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 29.4 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 49.3 (N/A) 0.3 150 FTG TLG PE 0.0 RP -1.0 0.0 49.3 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 49.3 0.0 13.0 psi, 29.4 gpm DA -1.0 0.0 36.3 0.0 Pipe: 3 29.4 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 36.3 0.0 0.3 150 FTG 3L PE 0.0 U.1 -1.0 0.0 36.3 0.0 0.000 TL 138.71 PV Pipe: 4 29.4 6.000 PL 5.00 PF 0.0 LJ.1 -1.0 0.0 36.3 0.0 0.3 150 FTG E PE -0.6 BOR 0.5 0.0 35.7 0.0 0.000 TL 25.07 PV Pipe: 5 29.4 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 35.7 0.0 0.7 120 FTG C PE -3.0 TOR 7.5 0.0 32.6 0.0 0.000 TL 28.50 PV Pipe: 6 29.4 4.000 PL 42.00 PF 0.0 TOR 7.5 0.0 32.6 0.0 0.7 120 FTG 3E PE -0.3 1 8.2 0.0 32.3 0.0 0.000 TL 72.00 PV Pipe: 7 29.4 1.442 PL 31.50 PE' 2.4 1 8.2 0.0 32.3 0.0 5.8 120 FTG 2T PE 0.0 Bi 8.2 0.0 29.8 0.0 0.056 TL 43.50 PV Pipe: 8 29.4 1.442 PL 7.00 PF 0.9 Bi 8.2 0.0 29.8 0.0 5.8 120 FTG ET PE -3.1 Cvi 15.5 0.0 25.8 0.0 0.056 TL 16.00 PV Pipe: 9 29.4 1.400 PL 4.00 PF 0.6 Cvi 15.5 0.0 25.8 0.0 6.1 120 FTG EC PE -1.9 2 20.0 0.0 23.2 0.0 0.065 TL 9.29 PV Pipe: 10 12.9 1.400 PL 10.00 PF 0.3 2 20.0 0.0 23.2 0.0 2.7 120 FTG ETR PE -4.8 3 31.0 0.0 18.2 0.0 0.014 TL 19.26 PV Pipe: 11 12.9 1.101 PL 24.00 PF 1.7 3 31.0 0.0 18.2 0.0 4.3 120 FTG E3T PE 0.0 4 31.0 0.0 16.5 0.0 0.046 TL 37.24 PV Pipe: 12 12.9 1.101 PL 10.00 PF 0.6 4 31.0 0.0 16.5 0.0 4.3 120 FTG ER PE -4.3 5 41.0 0.0 11.5 0.0 0.046 TL 13.97 PV Pipe: 13 12.9 1.101 PL 4.00 PF 1.0 5 41.0 0.0 11.5 0.0 4.3 120 FTG 4ET2R PE -0.6 6 42.5 0.0 9.9 0.0 0.046 TL 21.87 PV 't I • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOB-TITLE:-BUENA VISTA BUILDING -#1 TWO HEAD-CALC @ 3:-1-2-PI-TCH---- 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 15.4 1.101 PL 0.50 PF 0.3 6 42.5 0.0 9.9 0.0 5.2 120 FTG TR PE 0.2 6A 42.0 4.9 9.8 15.4 0.063 TL 4.47 PV Pipe: 15 -2.5 1.101 PL 19.50 PF 0.1 6 42.5 0.0 9.9 0.0 0.8 120 FTG 2ETR PE 0.6 7 41.0 0.0 10.6 0.0 0.002 TL 30.09 PV Pipe: 16 14.0 1.101 PL 17.50 PF 2.0 7 41.0 0.0 10.6 0.0 4.7 120 FTG 4E2TR PE -0.4 7A 42.0 4.9 8.2 14.0 0.053 TL 38.02 PV Pipe: 17 -16.5 1.101 PL 7.50 PF 0.5 7 41.0 0.0 10.6 0.0 5.6 120 FTG ---- PE 0.0 8 41.0 0.0 11.2 0.0 0.072 TL 7.50 PV Pipe: 18 -16.5 1.101 PL 18.00 PF 2.0 8 41.0 0.0 11.2 0.0 5.6 120 FTG E2T PE 4.3 9 31.0 0.0 17.5 0.0 0.072 TL 27.93 PV Pipe: 19 0.0 1.400 PL 11.00 PF 0.0 9 31.0 0.0 17.5 0.0 0.0 120 FTG T PE 0.0 10 31.0 0.0 17.5 0.0 0.000 TL 14.97 PV Pipe: 20 0.0 1.101 PL 4.50 PF 0.0 10 31.0 0.0 17.5 0.0 0.0 120 FTG 2ET PE -0.6 11 32.5 0.0 16.8 0.0 0.000 TL 14.43 4PV Pipe: 21 0.0 1.101 PL 0.50 PF 0.0 11 32.5 0.0 16.8 0.0 0.0 120 FTG TR PE 0.2 hA 32.0 0.0 17.1 0.0 0.000 TL 4.47 PV Pipe: 22 0.0 1.101 PL 8.50 PF 0.0 11 32.5 0.0 16.8 0.0 0.0 120 FTG ER PE 0.2 12A 32.0 0.0 17.1 0.0 0.000 TL 12.47 PV Pipe: 23 0.0 1.101 PL 16.50 PF 0.0 10 31.0 0.0 17.5 0.0 0.0 120 FTG 3E PE -0.6 13 32.5 0.0 16.8 0.0 0.000 TL 26.43 PV Pipe: 24 0.0 1.101 PL 0.50 PF 0.0 13 32.5 0.0 16.8 0.0 0.0 150 FTG TR PE 0.2 13A 32.0 0.0 17.1 0.0 0.000 TL 6.50 PV Pipe: 25 0.0 1.101 PL 8.50 PF 0.0 13 32.5 0.0 16.8 0.0 0.0 150 FTG ER PE 0.2 14A 32.0 0.0 17.1 0.0 0.000 TL 14.50 PV Pipe: 26 -16.5 1.400 PL 10.00 PF 0.2 9 31.0 0.0 17.5 0.0 3.4 150 FTG R PE 4.8 15 20.0 0.0 22.4 0.0 0.015 TL 12.00 PV - -- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOB TITLE: BUENAVISTA-BU-I-LDING--#1TWO HEAD CALC @-3-12 PITCH-- PIPE TAG END ELEV. NOZ. NODES (FT) (K) Pipe: 27 15 20.0 0.0 2 20.0 0.0 Q(GPM) DIA(IN) LENGTH PRESS. PT DISC. VEL(FPS) HW(C) (FT) SUM. (PSI) (GPM) FL/FT (PSI) -16.5 1.400 PL 26.50 PF 0.8 22.4 0.0 3.4 150 FTG E2T5R PE 0.0 23.2 0.0 0.015 TL 54.50 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by 1IRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.005 gpm and a maximum imbalance at any node of 0.127 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.1 ft/sec at pipe 9. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERLJN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 0 0 0 0 0 CD '—I 0 0 '.D '-I 0 0 I-' 0 0 0 I 0 0 $ I - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880-B1.SDF JOBTITLE:BUENA VISTABUILDING -#i- TWO-HEAD CALC @ 3:12 P1-Pc-H-- o 0 00 00Cx] 0 0 0 0 •cj' 0 0 CD CD rr]U)U)Cr] Q..U)-d---- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/12/2005 C:\HA$S74\C2880-B1.SDF JOB TI.TLE:_BtJENA_V:ISTA_BUILDING #.1--TWO-HEAD CALC g3: 12_PITCH WATER SUPPLY CURVE 84+ 77+ I \\\\\\\\ 70+ * <-70.0 psi @ 1181 gpm I Flow Test Point 63+ P 56+ R I E I S I S 49+ X U I R I E 42+ ( I P I S I I 35+ ) I 28+ 21+ 14+ LEGEND I 'I I X = Required Water Supply I 49.34 psi @ 529.4 gpm 7+ I 0 = Available Water Supply I 74.64 psi @ 529.4 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB T1TLE: BUENA VISTA BUILDING #2-FOURHEAD-CALC - - WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 74.5 557.1 69.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 557.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 57.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 69.3 57.1 RP -1.0 - - - - 69.3 - - - DA -1.0 - - - - 56.3 - - - U.1 -1.0 - - - - 56.3 - - - BOR 0.5 - - - - 55.7 - - - TOR 7.5 - - - - 52.6 - - - 1 8.2 - - - - 52.2 - - - 2 8.2 - - - - 52.1 - - - 3 8.2 - - - - 52.0 - - - B2 8.2 - - - - 42.9 - - - CV2 15.5 - - - - 36.7 - - - 4 20.0 - - - - 32.5 - - - 5 31.0 - - - - 27.1 - - - 6 31.0 - - - - 23.7 - - - 7 41.0 - - - - 18.0 - - - 8 41.0 - - - - 16.9 - - - 8A 42.0 - - - - 16.5 - - - 9 41.0 - - - - 16.2 - - - 9A 42.0 - - - - 15.8 10 41.0 - - - - 13.1 - - - 11 31.0 - - - - 16.1 - - - 12 31.0 - - - - 12.0 13 32.5 - - - - 8.5 - - - 13A 32.0 K= 4.90 8.4 14.2 14A 32.0 K= 4.90 8.2 14.0 15 31.0 - - - - 12.2 - - - 16 32.5 - - - - 8.9 - - - 16A 32.0 K= 4.90 8.8 14.6 17A 32.0 K= 4.90 8.5 14.3 18 32.0 - - - - 14.7 - - - 19 20.0 - - - - 21.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB TITLE: BUENAVI-STABUILDING #2 FOUR HEAD- CALC- PIPE S 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 57.1 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 69.3 (N/A) 0.6 150 FTG TLG PE 0.0 RP -1.0 0.0 69.3 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 69.3 0.0 13.0 psi, 57.1 gpm DA -1.0 0.0 56.3 0.0 Pipe: 3 57.1 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 56.3 0.0 0.6 150 FTG 3L PE 0.0 U.1 -1.0 0.0 56.3 0.0 0.000 TL 138.71 PV Pipe: 4 57.1 6.000 PL 5.00 PF 0.0 U.1 -1.0 0.0 56.3 0.0 0.6 150 FTG E PE -0.6 BOR 0.5 0.0 55.7 0.0 0.000 TL 25.07 PV Pipe: 5 57.1 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 55.7 0.0 1.5 120 FTG C PE -3.0 TOR 7.5 0.0 52.6 0.0 0.001 TL 28.50 PV Pipe: 6 57.1 4.000 PL 42.00 PF 0.1 TOR 7.5 0.0 52.6 0.0 1.5 120 FTG 3E PE -0.3 1 8.2 0.0 52.2 0.0 0.001 TL 72.00 PV Pipe: 7 57.1 4.000 PL 81.50 PF 0.1 1 8.2 0.0 52.2 0.0 1.5 120 FTG ---- PE 0.0 2 8.2 0.0 52.1 0.0 0.001 TL 81.50 PV Pipe: 8 57.1 4.000 PL 10.50 PF 0.0 2 8.2 0.0 52.1 0.0 1.5 120 FTG ---- PE 0.0 3 8.2 0.0 52.0 0.0 0.001 TL 10.50 PV Pipe: 9 57.1 1.442 PL 35.50 PF 9.1 3 8.2 0.0 52.0 0.0 11.2 120 FTG 2T PE 0.0 B2 8.2 0.0 42.9 0.0 0.192 TL 47.50 PV Pipe: 10 57.1 1.442 PL 7.00 PF 3.1 B2 8.2 0.0 42.9 0.0 11.2 120 FTG ET PE -3.1 CV2 15.5 0.0 36.7 0.0 0.192 TL 16.00 PV Pipe: 11 57.1 1.400 PL 6.00 PF 2.2 CV2 15.5 0.0 36.7 0.0 11.9 120 FTG E PE -1.9 4 20.0 0.0 32.5 0.0 0.222 TL 9.97 PV Pipe: 12 19.3 1.400 PL 12.00 PF 0.6 4 20.0 0.0 32.5 0.0 4.0 120 FTG 2TR PE -4.8 5 31.0 0.0 27.1 0.0 0.030 TL 21.26 PV Pipe: 13 19.3 1.101 PL 22.00 PF 3.4 5 31.0 0.0 27.1 0.0 6.5 120 FTG E3T PE 0.0 6 31.0 0.0 23.7 0.0 0.096 TL 35.24 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB TITLE: BUENA -VISTA BUI-LDING-#2FOUR-HE-AD-CALC ------- --- - - 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 19.3 1.101 PL 10.00 PF 1.3 6 31.0 0.0 23.7 0.0 6.5 120 FTG ER PE -4.3 7 41.0 0.0 18.0 0.0 0.096 TL 13.97 PV Pipe: 15 19.3 1.101 PL 8.00 PF 1.1 7 41.0 0.0 18.0 0.0 6.5 120 FTG T PE 0.0 8 41.0 0.0 16.9 0.0 0.096 TL 11.31 PV Pipe: 16 0.0 1.101 PL 20.00 PF 0.0 8 41.0 0.0 16.9 0.0 0.0 120 FTG 3E3T PE -0.4 8A 42.0 0.0 16.5 0.0 0.000 TL 39.85 PV Pipe: 17 19.3 1.101 PL 4.00 PF 0.7 8 41.0 0.0 16.9 0.0 6.5 120 FTG E PE 0.0 9 41.0 0.0 16.2 0.0 0.096 TL 7.31 PV Pipe: 18 0.0 1.101 PL 12.00 PF 0.0 9 41.0 0.0 16.2 0.0 0.0 120 FTG 3ETR PE -0.4 9A 42.0 0.0 15.8 0.0 0.000 TL 25.90 PV Pipe: 19 19.3 1.101 PL 27.50 PF 3.2 9 41.0 0.0 16.2 0.0 6.5 120 FTG T3R PE 0.0 10 41.0 0.0 13.1 0.0 0.096 TL 32.79 PV Pipe: 20 19.3 1.101 PL 10.00 PF 1.3 10 41.0 0.0 13.1 0.0 6.5 120 FTG TR PE 4.3 11 31.0 0.0 16.1 0.0 0.096 TL 13.97 PV Pipe: 21 19.3 1.101 PL 25.00 PF 4.1 11 31.0 0.0 16.1 0.0 6.5 120 FTG 3E2TR PE 0.0 12 31.0 0.0 12.0 0.0 0.096 TL 42.21 PV Pipe: 22 28.2 1.101 PL 5.00 PF 2.9 12 31.0 0.0 12.0 0.0 9.5 120 FTG 2ET PE -0.6 13 32.5 0.0 8.5 0.0 0.194 TL 14.93 PV Pipe: 23 14.2 1.101 PL 0.50 PF 0.2 13 32.5 0.0 8.5 0.0 4.8 120 FTG TR PE 0.2 13A 32.0 4.9 8.4 14.2 0.055 TL 4.47 PV Pipe: 24 14.0 1.101 PL 8.50 PF 0.5 13 32.5 0.0 8.5 0.0 4.7 150 FTG ER PE 0.2 14A 32.0 4.9 8.2 14.0 0.035 TL 14.50 PV Pipe: 25 -8.9 1.101 PL 12.00 PF 0.2 12 31.0 0.0 12.0 0.0 3.0 150 FTG ---- PE 0.0 15 31.0 0.0 12.2 0.0 0.015 TL 12.00 PV Pipe: 26 28.9 1.101 PL 5.00 PF 2.7 15 31.0 0.0 12.2 0.0 9.7 150 FTG 2ET PE -0.6 16 32.5 0.0 8.9 0.0 0.134 TL 20.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS -- Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB TITLE: BUENA V-rSTA-BUILDING #2 FOUR HEAD CALC 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 14.6 1.101 PL 0.50 PF 0.2 16 32.5 0.0 8.9 0.0 4.9 150 FTG TR PE 0.2 16A 32.0 4.9 8.8 14.6 0.038 TL 6.50 PV Pipe: 28 14.3 1.101 PL 8.50 PF 0.5 16 32.5 0.0 8.9 0.0 4.8 150 FTG ER PE 0.2 17A 32.0 4.9 8.5 14.3 0.037 TL 14.50 PV Pipe: 29 -37.8 1.400 PL 21.00 PF 2.9 15 31.0 0.0 12.2 0.0 7.9 150 FTG 3E2R PE -0.4 18 32.0 0.0 14.7 0.0 0.069 TL 43.00 PV Pipe: 30 -37.8 1.400 PL 10.00 PF 1.2 18 32.0 0.0 14.7 0.0 7.9 150 FTG TR PE 5.2 19 20.0 0.0 21.1 0.0 0.069 TL 18.00 PV Pipe: 31 -37.8 1.400 PL 86.00 PF 11.4 19 20.0 0.0 21.1 0.0 7.9 150 FTG 8E5TR PE 0.0 4 20.0 0.0 32.5 0.0 0.069 TL 166.00 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.053 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 11.9 ft/sec at pipe 11. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 e - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB- TITLE:'- BUENA- VISTA--BUILD-iNG -#-2 FOUR- HE-AD- C-ALC-- - --- --- ------ PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 PAGE: H MATERIAL: CPVC HWC: 150 - Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 - SPRINKLER SYSTEM HYDRAULIC ANALYSIS - Page 6 DATE: 9/12/2005 , C:\HASS74\C2880-B2.SDF JOTITLEBUNAViSTAUILDING #2 FOUR HEAD ALC--- - - 0 0 0 C." E 0. .IIl 0) 00 S4HWr1 44 • >i Q Z U) U) U) In 0. ld win m Lo Q. 44 0) 0 Cr] 0. W-d-dO) 1.4 rlU)0U)U0) 0. a) QW) l 44 U) 0 >r -.1 It) C') U) U) oh -U'- ,..- w0 0 0 00 0 0 .0 H 0 0 N H 0 0 0 0 0 . . • • . o 0 0 0 0 a, w C'1 '-I 00r..1 0r)U)cflDrI —04U) -H-- -- - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB- TITLE: BUENA VISTA -BUT LDING-#2FOUR- HEAD CALC --- - -------------- WATER SUPPLY CURVE 84+ 77+ *\\\\\O\\ I \\\\\\\\ I \\\\\\\\ 70+ X * <-70.0 psi @ 1181 gpm I Flow Test Point 63+ P 56+ R I E I S I S 49+ U I R I E I 42+ I I P S I I 35+ 28+ 21+ 14+ LEGEND I U I X = Required Water Supply I 69.34 psi @ 557.1 gpm 7+ I 0 = Available Water Supply l 74.51 psi @ 557.1 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/12/2005 C:\HA$S74\C2880-B2.SDF JOB--TiTL-E:--BUE-NA--ViSTA-BUILDING #2-TWO HEAD CALC-@-3:1-2--PI-TCH-•--- - WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 74.6 528.6 51.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 528.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 28.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 51.2 28.6 RP -1.0 - - - - 51.2 DA -1.0 - - - - 38.2 U.1 -1.0 - - - - 38.2 - - - BOR 0.5 - - - - 37.5 TOR 7.5 - - - - 34.5 - - - 1 8.2 - - - - 34.1 - - - 2 8.2 - - - - 34.1 - - - 3 8.2 - - - - 34.1 - - - B2 8.2 - - - - 31.6 - - - CV2 15.5 - - - - 27.6 - - - 4 20.0 - - - - 25.0 5 31.0 - - - - 19.7 - - - 6 31.0 - - - - 17.0 - - - 7 41.0 - - - - 11.6 8 41.0 - - - - 10.7 - - - 8A 42.0 K= 4.90 8.2 14.0 9 41.0 - - - - 10.7 - - - 9A 42.0 K= 4.90 8.8 14.5 10 41.0 - - - - 11.9 - - - 11 31.0 - - - - 16.7 - - - 12 31.0 - - - - 18.2 - - - 13 32.5 - - - - 17.6 13A 32.0 - - - - 17.8 - - - 14A 32.0 - - - - 17.8 15 31.0 - - - - 18.5 - - - 16 32.5 - - - - 17.9 - - - 16A 32.0 - - - - 18.1 17A 32.0 - - - - 18.1 - - - 18 32.0 - - - - 18.4 - - - 19 20.0 - - - - 23.8 - - - - ---- - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Pàé 2 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB-TITLE: BUENA VISTA BUILD-ING 1-2-TWO -HE-AD CALC @ 3:12 P-ITCH - ----' --- - 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 28.6 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 51.2 (N/A) 0.3 150 FTG TLG PE 0.0 RP -1.0 0.0 51.2 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 51.2 0.0 13.0 psi, 28.5 gpm DA -1.0 0.0 38.2 0.0 Pipe: 3 28.5 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 38.2 0.0 0.3 150 FTG 3L PE 0.0 0.1 -1.0 0.0 38.2 0.0 0.000 TL 138.71 PV Pipe: 4 28.5 6.000 PL 5.00 PF 0.0 0.1 -1.0 0.0 38.2 0.0 0.3 150 FTC E PE -0.6 BOR 0.5 0.0 37.5 0.0 0.000 TL 25.07 PV Pipe: 5 28.5 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 37.5 0.0 0.7 120 FTC C PE -3.0 TOR 7.5 0.0 34.5 0.0 0.000 TL 28.50 PV Pipe: 6 28.5 4.000 PL 42.00 PF 0.0 TOR 7.5 0.0 34.5 0.0 0.7 120 FTC 3E PE -0.3 1 8.2 0.0 34.1 0.0 0.000 TL 72.00 PV Pipe: 7 28.5 4.000 PL 81.50 PF 0.0 1 8.2 0.0 34.1 0.0 0.7 120 FTG ---- PE 0.0 2 8.2 0.0 34.1 0.0 0.000 TL 81.50 PV Pipe: 8 28.5 4.000 PL 10.50 PF 0.0 2 8.2 0.0 34.1 0.0 0.7 120 FTC ---- PE 0.0 3 8.2 0.0 34.1 0.0 0.000 TL 10.50 PV Pipe: 9 28.5 1.442 PL 35.50 PF 2.5 3 8.2 0.0 34.1 0.0 5.6 120 FTC 2T PE 0.0 B2 8.2 0.0 31.6 0.0 0.053 TL 47.50 PV Pipe: 10 28.5 1.442 PL 7.00 PF 0.9 B2 8.2 0.0 31.6 0.0 5.6 120 FTG ET PE -3.1 CV2 15.5 0.0 27.6 0.0 0.053 TL 16.00 PV Pipe: 11 28.5 1.400 PL 6.00 PF 0.6 CV2 15.5 0.0 27.6 0.0 5.9 120 FTC E PE -1.9 4 20.0 0.0 25.0 0.0 0.062 TL 9.97 PV Pipe: 12 17.1 1.400 PL 12.00 PF 0.5 4 20.0 0.0 25.0 0.0 3.6 120 FTG 2TR PE -4.8 5 31.0 0.0 19.7 0.0 0.024 TL 21.26 PV Pipe: 13 17.1 1.101 PL 22.00 PF 2.7 5 31.0 0.0 19.7 0.0 5.8 120 FTC E3T PE 0.0 6 31.0 0.0 17.0 0.0 0.077 TL 35.24 PV V SPRINKLER SYSTEM HYDRAULIC-ANALYSIS . Page 3 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB--TITLE:-BUENA VISTA --BUILDING #2--TWO--HEAD-C-ALC-@--3:12 PITCH 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 17.1 1.101 PL 10.00 PF 1.1 6 31.0 0.0 17.0 0.0 5.8 120 FTG ER PE -4.3 7 41.0 0.0 11.6 0.0 0.077 TL 13.97 PV Pipe: 15 17.1 1.101 PL 8.00 PF 0.9 7 41.0 0.0 11.6 0.0 5.8 120 FTG T PE 0.0 8 41.0 0.0 10.7 0.0 0.077 TL 11.31 PV Pipe: 16 14.0 1.101 PL 20.00 PF 2.1 8 41.0 0.0 10.7 0.0 4.7 120 FTG 3E3T PE -0.4 8A 42.0 4.9 8.2 14.0 0.053 TL 39.85 PV Pipe: 17 3.1 1.101 PL 4.00 PF 0.0 8 41.0 0.0 10.7 0.0 1.1 120 FTG E PE 0.0 9 41.0 0.0 10.7 0.0 0.003 TL 7.31 PV Pipe: 18 14.5 1.101 PL 12.00 PF 1.5 9 41.0 0.0 10.7 0.0 4.9 120 FTG 3ETR PE -0.4 9A 42.0 4.9 8.8 14.5 0.057 TL 25.90 PV Pipe: 19 -11.4 1.101 PL 27.50 PF 1.2 9 41.0 0.0 10.7 0.0 3.8 120 FTG T3R PE 0.0 10 41.0 0.0 11.9 0.0 0.036 TL 32.79 PV Pipe: 20 -11.4 1.101 PL 10.00 PF 0.5 10 41.0 0.0 11.9 0.0 3.8 120 FTG TR PE 4.3 11 31.0 0.0 16.7 0.0 0.036 TL 13.97 PV Pipe: 21 -11.4 1.101 PL 25.00 PF 1.5 11 31.0 0.0 16.7 0.0 3.8 120 FTG 3E2TR PE 0.0 12 31.0 0.0 18.2 0.0 0.036 TL 42.21 PV Pipe: 22 0.0 1.101 PL 5.00 PE' 0.0 12 31.0 0.0 18.2 0.0 0.0 120 FTG 2ET PE -0.6 13 32.5 0.0 17.6 0.0 0.000 TL 14.93 PV Pipe: 23 0.0 1.101 PL 0.50 PF 0.0 13 32.5 0.0 17.6 0.0 0.0 120 FTG TR PE 0.2 13A 32.0 0.0 17.8 0.0 . 0.000 TL 4.47 PV Pipe: 24 0.0 1.101 PL 8.50 PF 0.0 13 32.5 0.0 17.6 0.0 0.0 150 FTG ER PE 0.2 14A 32.0 0.0 17.8 0.0 0.000 TL 14.50 PV Pipe: 25 -11.4 1.101 PL 12.00 PF 0.3 12 31.0 0.0 18.2 0.0 3.8 150 FTG ---- PE 0.0 15 31.0 0.0 18.5 0.0 0.024 TL 12.00 PV Pipe: 26 0.0 1.101 PL 5.00 PF 0.0 15 31.0 0.0 18.5 0.0 0.0 150 FTG 2ET PE -0.6 16 32.5 0.0 17.9 0.0 0.000 TL 20.00 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B2..SDF JOB--TITLE:--BUENA V-I-STA--BU-I-LDI-NG #2---TWO HE-AD CALC @ --- 3:1-2-P-I-TCH 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 1.101 PL 0.50 PF 0.0 16 32.5 0.0 17.9 0.0 0.0 150 FTG TR PE 0.2 16A 32.0 0.0 18.1 0.0 0.000 TL 6.50 PV Pipe: 28 0.0 1.101 PL 8.50 PF 0.0 16 32.5 0.0 17.9 0.0 0.0 150 FTG ER PE 0.2 17A 32.0 0.0 18.1 0.0 0.000 TL 14.50 PV Pipe: 29 -11.4 1.400 PL 21.00 PF 0.3 15 31.0 0.0 18.5 0.0 2.4 150 FTG 3E2R PE -0.4 18 32.0 0.0 18.4 0.0 0.007 TL 43.00 PV Pipe: 30 -11.4 1.400 PL 10.00 PF 0.1 18 32.0 0.0 18.4 0.0 2.4 150 FTG TR PE 5.2 19 20.0 0.0 23.8 0.0 0.007 TL 18.00 PV Pipe: 31 -11.4 1.400 PL 86.00 PF 1.2 19 20.0 0.0 23.8 0.0 2.4 150 FTG 8E5TR PE 0.0 4 20.0 0.0 25.0 0.0 0.007 TL 166.00 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.117 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 5.9 ft/sec at pipe 11. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB TITLE: BUENAVISTA BUILDING#2-TWO HEAD C'ALC @ 3:12-PITCH- PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 0 0 0 C..) 0 0 OD SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/12/2005 C:\HASS74\C2880-B2.SDF JOB-TITLE:—BUE-NA-VISTA BUILDING #2 TWO HEAD CALC-@--3:-12--PVFCH- 0 0 0 0 Co 0 . • • • • 0 0 0 0 0 OD w V C-.-) r1 * oru DruU)U)ru '-0115)-H---- a 01 co H H H 0 H rzi -H U) Q. 0 0 0 N '0 -H U) w -d U) 01 U) 0 Id 0 w zo -H >•- 4-1 11 U) -Y -ø - - SPRINKr.ERSYSTgMHYDRAuLIC ANALYSIS Pagê7 DATE:. 9/12/2005 C:\HASS74\C28807B2.SDF -JOB TITLE:-BUENA VISTA -BUI-LDI-NG--#-2—TWO—HEAD-CALC--@---3:-12- -PITCH - ------- -- WATER SUPPLY CURVE 84+ 77+ I \\\\\\\\ I \\\\\\\\ 70+ * <-70.0 psi @ 1181 gpm I Flow Test Point 63+ P 56+ R E I S I X S 49+ U I R I E I 42+ ( I P S I I 35+ ) I 28+ 21+ 14+ LEGEND I U I X = Required Water Supply I 51.17 psi 0 528.6 gpm 7+ I 0 = Available Water Supply " I 74.64 psi 0 528.6 gpm 0++-+---+----+-----+ ------+ --------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS - Page 1 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOBTITLE:BUENAVISTABUILDINGit3 FOUR HEAD CALC - WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 74.5 557.8 69.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 557.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 57.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 69.7 57.8 RP -1.0 - - - - 69.7 DA -1.0 - - - - 56.7 - - - U.1 -1.0 - - - - 56.7 - - - BOR 0.5 - - - - 56.0 - - - TOR 7.5 - - - - 53.0 1 8.2 - - - - 52.5 - - - 2 8.2 - - - - 52.4 - - - 3 8.2 - - - - 52.4 - - - 4 8.2 - - - - 52.4 - - - 5 8.2 - - - - 52.4 - - - B3 8.2 - - - - 43.4 - - - CV3 15.5 - - - - 37.1 - - - 6 20.0 - - - - 32.9 - - - 7 20.0 - - - - 29.7 - - - 8 31.0 - - - - 23.9 - - - 9 31.0 - - - - 15.7 - - - 10 31.0 - - - - 15.7 - - - bA 32.0 - - - - 15.3 - - - hA 32.0 - - - - 15.3 - - - 12 20.0 - - - - 18.9 13 20.0 - - - - 13.2 - - - 14 20.0 - - - - 10.0 - - - 14A 21.0 K= 4.90 9.3 14.9 15A 21.0 K= 4.90 9.0 14.7 16 20.0 - - - - 9.1 - - - 16A 21.0 K= 4.90 8.4 14.2 17A 21.0 K= 4.90 8.2 14.0 - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/12/2005 C:\HASS74\C2880-83.SDF JOBTITLETBUENAVISTA BUILDING #3 FOUR HEAD CALC 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 57.8 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 69.7 (N/A) 0.7 150 FTG TLG PE 0.0 RP -1.0 0.0 69.7 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 69.7 0.0 13.0 psi, 57.8 gpm DA -1.0 0.0 56.7 0.0 Pipe: 3 57.8 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 56.7 0.0 0.7 150 FTG 3L PE 0.0 U.1 -1.0 0.0 56.7 0.0 0.000 TL 138.71 PV Pipe: 4 57.8 6.000 PL 5.00 PF 0.0 U.1 -1.0 0.0 56.7 0.0 0.7 150 FTG E PE -0.6 BOR 0.5 0.0 56.0 0.0 0.000 TL 25.07 PV Pipe: 5 57.8 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 56.0 0.0 1.5 120 FTG C PE -3.0 TOR 7.5 0.0 53.0 0.0 0.001 TL 28.50 PV Pipe: 6 57.8 4.000 PL 42.00 PF 0.1 TOR 7.5 0.0 53.0 0.0 1.5 120 FTG 3E PE -0.3 1 8.2 0.0 52.5 0.0 0.001 TL 72.00 PV Pipe: 7 57.8 4.000 PL 81.50 PE 0.1 1 8.2 0.0 52.5 0.0 1.5 120 FTG ---- PE 0.0 2 8.2 0.0 52.4 0.0 0.001 TL 81.50 PV Pipe: 8 57.8 4.000 PL 10.50 PF 0.0 2 8.2 0.0 52.4 0.0 1.5 120 FTG ---- PE 0.0 3 8.2 0.0 52.4 0.0 0.001 TL 10.50 PV Pipe: 9 57.8 4.000 PL 10.00 PE 0.0 3 8.2 0.0 52.4 0.0 1.5 120 FTG ---- PE 0.0 4 8.2 0.0 52.4 0.0 0.001 TL 10.00 PV Pipe: 10 57.8 4.000 PL 10.50 PF 0.0 4 8.2 0.0 52.4 0.0 1.5 120 FTG ---- PE 0.0 5 8.2 0.0 52.4 0.0 0.001 TL 10.50 PV Pipe: 11 57.8 1.442 PL 33.50 PF 9.0 5 8.2 0.0 52.4 0.0 11.4 120 FTG 2T PE 0.0 B3 8.2 0.0 43.4 0.0 0.197 TL 45.50 PV Pipe: 12 57.8 1.442 Pb 7.00 PF 3.1 B3 8.2 0.0 43.4 0.0 11.4 120 FTG ET PE -3.1 CV3 15.5 0.0 37.1 0.0 0.197 TL 16.00 PV Pipe: 13 57.8 1.400 Pb 5.00 PF 2.3 CV3 15.5 0.0 37.1 0.0 12.0 120 FTG EC PE -1.9 6 20.0 0.0 32.9 0.0 0.227 TL 10.29 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS - Page 3 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOBTITijE:-BUENA-VISTABU1LD1NG #3 FOUR HEAD CALC 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 17.1 1.101 PL 29.00 PF 3.1 6 20.0 0.0 32.9 0.0 5.8 120 FTG E2T3R PE 0.0 7 20.0 0.0 29.7 0.0 0.077 TL 40.91 PV Pipe: 15 17.1 1.101 PL 10.00 PF 1.1 7 20.0 0.0 29.7 0.0 5.8 120 FTG ER PE -4.8 8 31.0 0.0 23.9 0.0 0.077 TL 13.97 PV Pipe: 16 17.1 1.101 PL 83.00 PF 8.2 8 31.0 0.0 23.9 0.0 5.8 120 FTG 2E5T PE 0.0 9 31.0 0.0 15.7 0.0 0.077 TL 106.16 PV Pipe: 17 0.0 1.101 PL 7.00 PF 0.0 9 31.0 0.0 15.7 0.0 0.0 120 FTG T PE 0.0 10 31.0 0.0 15.7 0.0 0.000 TL 10.31 PV Pipe: 18 0.0 1.101 PL 19.50 PF 0.0 10 31.0 0.0 15.7 0.0 0.0 120 FTG 3E3T PE -0.4 bA 32.0 0.0 15.3 0.0 0.000 TL 39.35 PV Pipe: 19 0.0 1.101 PL 16.50 PF 0.0 10 31.0 0.0 15.7 0.0 0.0 120 FTG 4ETR PE -0.4 hA 32.0 0.0 15.3 0.0 0.000 TL 33.71 PV Pipe: 20 17.1 1.101 PL 13.50 PF 1.6 9 31.0 0.0 15.7 0.0 5.8 120 FTG ETR PE 4.8 12 20.0 0.0 18.9 0.0 0.077 TL 20.78 PV Pipe: 21 57.8 1.400 PL 17.00 PF 5.7 12 20.0 0.0 18.9 0.0 12.0 120 FTG ET PE 0.0 13 20.0 0.0 13.2 0.0 0.227 TL 24.94 PV Pipe: 22 29.6 1.101 PL 5.50 PF 3.3 13 20.0 0.0 13.2 0.0 10.0 120 FTG 2ET PE 0.0 14 20.0 0.0 10.0 0.0 0.212 TL 15.43 PV Pipe: 23 14.9 1.101 PL 0.50 PF 0.3 14 20.0 0.0 10.0 0.0 5.0 120 FTG TR PE -0.4 14A 21.0 4.9 9.3 14.9 0.060 TL 4.47 PV Pipe: 24 14.7 1.101 PL 8.50 PF 0.6 14 20.0 0.0 10.0 0.0 4.9 150 FTG ER PE -0.4 15A 21.0 4.9 9.0 14.7 0.038 TL 14.50 PV Pipe: 25 28.2 1.101 PL 17.00 PF 4.1 13 20.0 0.0 13.2 0.0 9.5 150 FTC 3E PE 0.0 16 20.0 0.0 9.1 0.0 0.129 TL 32.00 PV Pipe: 26 14.2 1.101 PL 0.50 PF 0.2 16 20.0 0.0 9.1 0.0 4.8 150 FTG TR PE -0.4 16A 21.0 4.9 8.4 14.2 0.036 TL 6.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOBTITLE:-BUENAV-ISTA BUILDING #3-FOUR-HEAD -CALC------- - ----- - 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 14.0 1.101 PL . 8.50 PF 0.5 16 20.0 0.0 9.1 0.0 4.7 150 FTG ER PE -0.4 17A 21.0 4.9 8.2 14.0 0.035 TL 14.50 PV Pipe: 28 -40.7 1.400 PL 81.50 PF 14.0 12 20.0 0.0 18.9 0.0 8.5 150 FTG 9E7T PE 0.0 6 20.0 0.0 32.9 0.0 0.079 TL 177.50 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.066 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.0 ft/sec at pipe 13. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 6.065 . 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOBTITLE:UENAVFSTA UILDTNG#3 FOUR HEAD'CALC PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 - DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOBTiTLE:BUENAVISTABUILING#3FOUIti1EADCALC 0 0 c.,J 0 0 OD '—I 0 I C" I I - I I I ml - C) 0 c 0 C) a, H o 0 CD 0 . . • 0 0 0 0 I '.0 . (. o4rz1cocJ)rz] — QIU)d- --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS - Page 1 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOB -TITLE:-BUENA-VISTA BUILDING#3 TWO HEAD CAL-C-@-3:12 PITCH -. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 0 PRESS. 0 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 74.6 528.2 48.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 528.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 28.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 48.3 28.2 RP -1.0 - - - - 48.3 - - - DA -1.0 - - - - 35.3 U.1 -1.0 - - - - 35.3 - - - BOR 0.5 - - - - 34.6 - - - TOR 7.5 - - - - 31.6 - - - 1 8.2 - - - - 31.2 - - - 2 8.2 - - - - 31.2 - - - 3 8.2 - - - - 31.2 - - - 4 8.2 - - - - 31.2 - - - 5 8.2 - - - - 31.2 - - - B3 8.2 - - - - 28.8 CV3 15.5 - - - - 24.8 - - - 6 20.0 - - - - 22.3 7 20.0 - - - - 21.0 - - - 8 31.0 - - - - 15.9 - - - 9 31.0 - - - - 12.7 - - - 10 31.0 - - - - 10.7 - - - 10A 32.0 K= 4.90 8.2 14.0 hA 32.0 K= 4.90 8.4 14.2 12 20.0 - - - - 19.2 - - - 13 20.0 - - - - 19.2 - - - 14 20.0 - - - - 19.2 - - - 14A 21.0 - - - - 18.8 - - - 15A 21.0 - - - - 18.8 - - - 16 20.0 - - - - 19.2 - - - 16A 21.0 - - - - 18.8 - - - 17A 21.0 - - - - 18.8 - - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS -- Page 2 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOB-TITLE: BUENA VISTA-BUILDINGit3 TWO HEAD CALC @-3:12 PITCH 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 28.2 6.000 PL 45.00 PF 0.0 TEST -1.0 SRCE 48.3 (N/A) 0.3 150 FTG TLG PE 0.0 RP -1.0 0.0 48.3 0.0 0.000 TL 105.22 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP -1.0 0.0 48.3 0.0 13.0 psi, 28.2 gpm DA -1.0 0.0 35.3 0.0 Pipe: 3 28.2 6.000 PL 100.00 PF 0.0 DA -1.0 0.0 35.3 0.0 0.3 150 FTG 3L PE 0.0 U.1 -1.0 0.0 35.3 0.0 0.000 TL 138.71 PV Pipe: 4 28.2 6.000 PL 5.00 PF 0.0 U.1 -1.0 0.0 35.3 0.0 0.3 150 FTG E PE -0.6 BOR 0.5 0.0 34.6 0.0 0.000 TL 25.07 PV Pipe: 5 28.2 4.000 PL 6.50 PF 0.0 BOR 0.5 0.0 34.6 0.0 0.7 120 FTG C PE -3.0 TOR 7.5 0.0 31.6 0.0 0.000 TL 28.50 PV Pipe: 6 28.2 4.000 PL 42.00 PF 0.0 TOR 7.5 0.0 31.6 0.0 0.7 120 FTG 3E PE -0.3 1 8.2 0.0 31.2 0.0 0.000 TL 72.00 PV Pipe: 7 28.2 4.000 PL 81.50 PF 0.0 1 8.2 0.0 31.2 0.0 0.7 120 FTG ---- PE 0.0 2 8.2 0.0 31.2 0.0 0.000 TL 81.50 PV Pipe: 8 28.2 4.000 PL 10.50 PF 0.0 2 8.2 0.0 31.2 0.0 0.7 120 FTG ---- PE 0.0 3 8.2 0.0 31.2 0.0 0.000 TL 10.50 PV Pipe: 9 28.2 4.000 PL 10.00 PF 0.0 3 8.2 0.0 31.2 0.0 0.7 120 FTG ---- PE 0.0 4 8.2 0.0 31.2 0.0 0.000 TL 10.00 PV Pipe: 10 28.2 4.000 PL 10.50 PF 0.0 4 8.2 0.0 31.2 0.0 0.7 120 FTG ---- PE 0.0 5 8.2 0.0 31.2 0.0 0.000 TL 10.50 PV Pipe: 11 28.2 1.442 PL 33.50 PF 2.4 5 8.2 0.0 31.2 0.0 5.5 120 FTG 2T PE 0.0 B3 8.2 0.0 28.8 0.0 0.052 TL 45.50 PV Pipe: 12 28.2 1.442 PL 7.00 PF 0.8 B3 8.2 0.0 28.8 0.0 5.5 120 FTG ET PE -3.1 CV3 15.5 0.0 24.8 0.0 0.052 TL 16.00 PV Pipe: 13 28.2 1.400 PL 5.00 PF 0.6 CV3 15.5 0.0 24.8 0.0 5.9 120 FTG EC FE -1.9 6 20.0 0.0 22.3 0.0 0.060 TL 10.29 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOTITLE-:-BUENAVISTA BUILDING i3 TWO HEADCALC @ 3d2:P-ITCH - -- 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 10.3 1.101 PL 29.00 PF 1.2 6 20.0 0.0 22.3 0.0 3.5 120 FTG E2T3R PE 0.0 7 20.0 0.0 21.0 0.0 0.030 TL 40.91 PV Pipe: 15 10.3 .1.101 PL 10.00 PF 0.4 7 20.0 0.0 21.0 0.0 3.5 120 FTC ER PE -4.8 8 31.0 0.0 15.9 0.0 0.030 TL 13.97 PV Pipe: 16 10.3 1.101 PL 83.00 PF 3.2 8 31.0 0.0 15.9 0.0 3.5 120 FTG 2E5T PE 0.0 9 31.0 0.0 12.7 0.0 0.030 TL 106.16 PV Pipe: 17 28.2 1.101 PL 7.00 PF 2.0 9 31.0 0.0 12.7 0.0 9.5 120 FTC T PE 0.0 10 31.0 0.0 10.7 0.0 0.194 TL 10.31 PV Pipe: 18 14.0 1.101 PL 19.50 PF 2.1 10 31.0 0.0 10.7 0.0 4.7 120 FTG 3E3T PE -0.4 10A 32.0 4.9 8.2 14.0 0.053 TL 39.35 PV Pipe: 19 14.2 1.101 PL 16.50 PF 1.8 10 31.0 0.0 10.7 0.0 4.8 120 FTC 4ETR PE -0.4 hA 32.0 4.9 8.4 14.2 0.055 TL 33.71 PV Pipe: 20 -18.0 1.101 PL 13.50 PF 1.7 9 31.0 0.0 12.7 0.0 6.0 120 FTC ETR PE 4.8 12 20.0 0.0 19.2 0.0 0.084 TL 20.78 PV Pipe: 21 0.0 1.400 PL 17.00 PF 0.0 12 20.0 0.0 19.2 0.0 0.0 120 FTG ET PE 0.0 13 20.0 0.0 19.2 0.0 0.000 TL 24.94 PV Pipe: 22 0.0 1.101 PL 5.50 PF 0.0 13 20.0 0.0 19.2 0.0 0.0 120 FTC 2ET PE 0.0 14 20.0 0.0 19.2 0.0 0.000 TL 15.43 PV Pipe: 23 0.0 1.101 PL 0.50 PF 0.0 14 20.0 0.0 19.2 0.0 0.0 120 FTG TR PE -0.4 14A 21.0 0.0 18.8 0.0 0.000 TL 4.47 PV Pipe: 24 0.0 1.101 PL 8.50 PF 0.0 14 20.0 0.0 19.2 0.0 0.0 150 FTG ER PE -0.4 15A 21.0 0.0 18.8 0.0 0.000 TL 14.50 PV Pipe: 25 0.0 1.101 PL 17.00 PF 0.0 13 20.0 0.0 19.2 0.0 0.0 150 FTG 3E PE 0.0 16 20.0 0.0 19.2 0.0 0.000 TL 32.00 PV Pipe: 26 0.0 1.101 PL 0.50 PF 0.0 16 20.0 0.0 19.2 0.0 0.0 150 FTG TR PE -0.4 16A 21.0 0.0 18.8 0.0 0.000 TL 6.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/12/2005 C:\HASS74\C2880-B3.SDF JOB TITLE: BUENA VISTA -BUILDING --#3 -TWO HEADCALC @3:12 PITCH---- - ----- -- 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 1.101 PL 8.50 PF 0.0 16 20.0 0.0 19.2 0.0 0.0 150 FTG ER PE -0.4 17A 21.0 0.0 18.8 0.0 0.000 TL 14.50 PV Pipe: 28 -18.0 1.400 PL 81.50 PF 3.1 12 20.0 0.0 19.2 0.0 3.7 150 FTG 9E7T PE 0.0 6 20.0 0.0 22.3 0.0 0.017 TL 177.50 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.089 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 9.5 ft/sec at pipe 17. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkViv BfyViv GatVlv AlmChk DPVlv NPTee 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.442 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 4.000 10.00 20.00 6.00 22.00 12.00 2.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/12/2005 C:\HASS74\C2880-83.SDF JOB TITLE:BUENA VISTA- BUILDING#3TWO HEADCALC @ 3:12--PITCH PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 5.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.400 6.00 6.00 2.00 0.00 2.00 2.00 0.00 2.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/12/2005 C:\HASS74\C2880-3.sDF JOB-TITLE:-BUENA-VISTA-BU-ILDING #3 -TWO -HEAD -CALC-@- -3:-I2- PITCH---- - 0 0 I0 I tC'4 R o U 00 14C'1 UN 14 • O Z U) N U) ('4 0116 111 WLOU)IflQ.E 14 (i w 0 ri Q Q.0 0.141.' 'U II U -4 Lfl _I O 0 >i -14 W ::1 N U) U) 'U 0 r1 00 r-I '-4 0 114 U) 04 0 0 0 N U) 0) --1 U) 04 U)° C,)W z r 0 0 U) r-I DO I- 0 0 0 0 0 0 0 0 0 0 0 Q 0 CD W r1 001z 04111C0C/)X1 '-04U)-d--. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/28/2005 C:\HASS74\C2880-PG.SDF JOB-TITLE:--BUENA VIST PARKINGGARAGE-ORDTNARY HAZARD, GROUP I WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) TEST 76.0 70.0 1181.0 73.2 775.8 43.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 775.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 275.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) TEST -1.0 SOURCE 43.9 275.8 RP -1.0 - - - - 43.7 - - - DA -1.0 - - - - 32.7 - - - U.1 -1.0 - - - - 32.4 - - - BOR 0.5 - - - - 31.7 - - - TOR 7.5 - - - - 28.0 - - - 1 8.2 - - - - 26.2 - - - 2 8.2 - - - - 24.8 - - - 3 8.2 - - - - 24.6 - - - 4 8.2 - - - - 24.4 - - - 5 8.2 - - - - 24.2 - - - 6 8.2 - - - - 24.1 - - - 7 8.2 - - - - 23.8 - - - 8 8.2 - - - - 23.8 - - - B3 8.2 - - - - 22.0 101 8.5 K= 5.60 21.3 25.8 102 8.5 K= 5.60 16.3 22.6 103 8.5 K= 5.60 13.7 20.8 104 8.5 K= 5.60 12.6 19.9 105 8.5 K= 5.60 12.3 19.6 106 8.5 K= 5.60 16.1 22.5 107 8.5 K= 5.60 13.6 20.6 108 8.5 K= 5.60 12.4 19.7 109 8.5 K= 5.60 12.1 19.5 110 8.5 K= 5.60 16.2 22.5 111 8.5 K= 5.60 14.4 21.3 112 8.5 K= 5.60 13.6 20.6 113 8.5 K= 5.60 13.2 20.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 1. D4TE: 9/28/2005 C\HASS74\C2880-PG.SDF JOBTITLE: BUENA VISTA PARKING GARAGE-ORDINARYHAZARD, GROUP I 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: 1 275.8 6.357 PL 45.00 PF 0.2 TEST -1.0 SRCE 43.9 (N/A) 2.8 150 FTG TLG PE 0.0 RP -1.0 0.0 43.7 0.0 0.002 TL 125.09 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE .RP -1.0 0.0 43.7 0.0 11.0 psi, 275.8 gpm DA -1.0 0.0 32.7 0.0 Pipe: 3 275.8 6.357 PL 100.00 PF 0.3 DA -1.0 0.0 32.7 0.0 2.8 150 FTG 3L PE 0.0 U.1 -1.0 0.0 32.4 0.0 0.002 TL 149.87 PV Pipe: 4 275.8 6.357 PL 5.00 PF 0.1 U.1 -1.0 0.0 32.4 0.0 2.8 150 FTG E PE -0.6 BOR 0.5 0.0 31.7 0.0 0.002 TL 32.20 PV Pipe: 5 275.8 4.260 PL 7.00 PF 0.7 BOR 0.5 0.0 31.7 0.0 6.2 120 FTG C PE -3.0 TOR 7.5 0.0 28.0 0.0 0.018 TL 36.00 PV Pipe: 6 275.8 4.260 PL 42.00 PF 1.5 TOR 7.5 0.0 28.0 0.0 6.2 120 FTG 3E PE -0.3 1 8.2 0.0 26.2 0.0 0.018 TL 81.00 PV Pipe: 7 275.8 4.260 PL 81.50 PF 1.5 1 8.2 0.0 26.2 0.0 6.2 120 FTG ---- PE 0.0 2 8.2 0.0 24.8 0.0 0.018 TL 81.50 PV Pipe: 8 275.8 4.260 PL 10.50 PF 0.2 2 8.2 0.0 24.8 0.0 6.2 120 FTG ---- PE 0.0 3 8.2 0.0 24.6 0.0 0.018 TL 10.50 PV Pipe: 9 275.8 4.260 PL 10.00 PF 0.2 3 8.2 0.0 24.6 0.0 6.2 120 FTG ---- PE 0.0 4 8.2 0.0 24.4 0.0 0.018 TL 10.00 PV Pipe: 10 275.8 4.260 PL 10.50 PF 0.2 4 8.2 0.0 24.4 0.0 6.2 120 FTG ---- PE 0.0 5 8.2 0.0 24.2 0.0 0.018 TL 10.50 PV Pipe: 11 250.0 4.260 PL 10.00 PF 0.2 5 8.2 0.0 24.2 0.0 5.6 120 FTG ---- PE 0.0 6 8.2 0.0 24.1 0.0 0.015 TL 10.00 PV Pipe: 12 167.2 4.260 PL 10.50 PF 0.3 6 8.2 0.0 24.1 0.0 3.8 120 FTG T PE 0.0 7 8.2 0.0 23.8 0.0 0.007 TL 36.50 PV Pipe: 13 84.8 4.260 PL 10.00 PF 0.0 7 8.2 0.0 23.8 0.0 1.9 120 FTG ---- PE 0.0 8 8.2 0.0 23.8 0.0 0.002 TL 10.00 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/28/2005 . C:\HASS74\C2880-PG.SDF ..JOB "T-I-TL-E-:-BUENA VISTA PARKING GARAE---RAG -NARY-HAZARDj -GROUP- I ...... PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. MODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 25.8 1.442 PL 33.00 PF 2.2 5 8.2 0.0 24.2 0.0 5.1 120 FTG 2T PE 0.0 B3 8.2 0.0 22.0 0.0 0.044 TL 49.00 PV Pipe: 15 25.8 1.442 PL 6.50 PF 0.6 B3 8.2 0.0 22.0 0.0 5.1 120 FTG T PE -0.1 101 8.5 5.6 21.3 25.8 0.044 TL 14.50 PV Pipe: 16 82.8 1.442 PL 4.00 PF 7.7 6 8.2 0.0 24.1 0.0 16.3 120 FTG 2T PE -0.1 102 8.5 5.6 16.3 22.6 0.383 TL 20.00 PV Pipe: 17 60.2 1.442 PL 12.00 FE' 2.5 102 8.5 5.6 16.3 22.6 11.8 120 FTG ---- PE 0.0 103 8.5 5.6 13.7 20.8 0.212 TL 12.00 PV Pipe: 18 39.5 1.442 FL 12.00 PF 1.2 103 8.5 5.6 13.7 20.8 7.8 120 FTG ---- FE 0.0 104 8.5 5.6 12.6 19.9 0.097 TL 12.00 PV Pipe: 19 19.6 1.442 PL 11.50 FE' 0.3 104 8.5 5.6 12.6 19.9 3.9 120 FTG ---- FE 0.0 105 8.5 5.6 12.3 19.6 0.027 TL 11.50 PV Pipe: 20 .82.4 1.442 FL 4.00 PP 7.6 7 8.2 0.0 23.8 0.0 16.2 120 FTG 2T PE -0.1 106 8.5 5.6 16..1 22.5 0.379 TL 20.00 PV Pipe: 21 59.9 1.442 PL 12.00 PP 2.5 106 8.5 5.6 16.1 22.5 11.8 120 FTG ---- PE 0.0 107 8.5 5.6 13.6 20.6 0.210 TL 12.00 PV Pipe: 22 39.2 1.442 PL 12.00 PP 1.2 107 8.5 5.6 13.6 20.6 7.7 120 FTG ---- FE 0.0 108 8.5 5.6 12.4 19.7 0.096 TL 12.00 PV Pipe: 23 19.5 1.442 PL 11.50 PP 0.3 108 8.5 5.6 12.4 19.7 3.8 120 FTG ---- PE 0.0 109 8.5 5.6 12.1 19.5 0.026 TL 11.50 PV Pipe: 24 . 84.8 1.442 FL 4.00 PF 7.5 8 8.2 0.0 23.8 0.0 16.7 150 FTG 2T FE -0.1 110 8.5 5.6 16.2 22.5 0.265 TL 28.18 PV Pipe: 25 62.3 1.442 FL 12.00 PF 1.8 110 8.5 5.6 16.2 22.5 12.2 150 FTG ---- FE 0.0 111 8.5 5.6 14.4 21.3 0.149 TL 12.00 PV Pipe: 26 41.0 1.442 PL 12.00 PF 0.8 111 8.5 5.6 14.4 21.3 8.1 150 FTG ---- FE 0.0 112 8.5 5.6 13.6 20.6 0.069 TL 12;00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/28/2005 C:\HASS74\C2880-PG.SDF JOB- 1I E:-BtJENA VISTA PARKING GARAGE ORbiNARYHAZ-ARD, GROUP 1 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 27 20.4 1.442 PL 11.50 PF 0.3 112 8.5 5.6 13.6 20.6 4.0 120 FTG ---- PE 0.0 113 8.5 5.6 13.2 20.4 0.029 TL 11.50 PV NOTES: Calculations were performed by the HASS 7.6 computer program under license no. 16080621 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.064 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 16.7 ft/sec at pipe 24. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: B MATERIAL.: THNWL f-{WC: 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 1.442 4.00 8.00 3.00 9.00 8.00 1.00 12.00 12.00 8.00 4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00 6.357 18.00 38.00 11.00 40.00 13.00 4.00 35.00 35.00 38.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DA1: 9/28/2005 C:\HASS74\C2880-PG.SDF , JOB-TITLE: BUENA-VISTA-PARKING GARAGE- ORDINARY HAZARD, GROUP I - * 0 0 0 C'.) 0 0 '-I 0 0 0 '-I 0 - 0. 0 0 0 N r-1 0 0 0 r1 0 0 0 0 o 0 ) 0 0 0 . • • o• o 0 0 0 0 C> OD W 1w C'.) ,-1 ct rz1 —QU)-d-- SPRINKLER SYSTEM HYDRAULIC-ANALYSIS - Page 6 'DAL'E: 9/28/200.5 C:\HASS74\C2880-PG.SDF JOB-TITLE:-BUENA--VIS-TA PARKINGGARAGE---ORDINARY HAZARD, -GROUP-. I .. - WATER SUPPLY CURVE 84+ 77+ I \\0\\\\\ I \\\\\\\\ 70+ * <-70.0 psi 8 1181 gpm I . Flow Test Point 63+ P 56+ R I E I S I S 49+ U. I R I E I X 42+ ( I P I S I 35+ ) I 28+ 21+ 14+ LEGEND I X = Required Water Supply I 43.90 psi 8 775.8 gpm 7+ I 0 = Available Water Supply " I 73.24 psi 8 775.8 gpm I Vt + ------+--------+--------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)