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4016 PENINSULA DR; ; AS050085; Permit
11/21/25, 12:55 PM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: AS050085 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS050085 4016 PENINSULA DR Status: ISSUED SPRINK Applied 4/20/2005 1683400203 Approved: 6/21/2005 0 Issued: 6/21/2005 Inspector: MYSTIC PT. VILLAGE U, BLDG. 29 PLAN CHECK & INSPECTIONS (3 UNITS) Owner: INNOVATIVE FIRE PROTECTION 405 VERNON WAY EL CAJON (619) 593-8200 about:blank Fees($) 220 Add'I Fees ($) 0 Total ($) 220 Balance($) 0 1/1 MYSTIC POINT APARTMENTS PHASE 2 BLDG# ADDRESS PERMIT# 29 4016 PENINSULA DR AS050085 30 4024 PENINSULA DR AS050086 31 4038 PENINSULA DR AS050087 32 4060 PENINSULA DR AS050088 33 4074 PENINSULA DR AS050089 34 4082 PENINSULA DR AS050090 35 4088 PENINSULA DR AS050091 36 4104 PENINSULA DR AS050093 37 4124 KARST RD AS050099 38 4138 KARST RD AS050100 39 4146 KARST RD AS050101 40 4125 KARST RD AS050102 41 4109 KARST RD AS050103 42 4095 KARST RD AS050106 43 4087 KARST RD AS050107 44 4062 KARST RD AS050108 45 4076 KARST RD AS050109 46 4084 KARST RD AS050113 47 4100 KARST RD AS050114 48 4113 PENINSULA DR AS050115 49 4099 PENINSULA DR AS050120 50 4085 PENINSULA DR AS050121 51 4071 PENINSULA DR AS050122 52 4043 PENINSULA DR AS050123 53 4029 PENINSULA DR AS050124 54 4015 PENINSULA DR AS050125 SEE PERMIT AS050085 4016 PENINSULA DR FOR CALCS & PLANS Project: __ ....,!M~y~s..,,t...,,ic ...... P....,o=ino..:.:t!:.....-______ _ PROTECTION DESIGN & CONSULTING 4883 Ronson Court, Suite P San Diego, California 92111 (Phone) 858.751.2930 (Fax) 858.751.2933 Pennit No.: 043651 Review No.: 043651-1 Date: 5/12/05 By: SML Contractor: Innovative Fire Protection The above-referenced plans and calculations have been reviewed are recommended for approval to the Carlsbad Fire Department with the following comments: By 1. Include flow test data on plans and furnish written confirmation from testing or witnessing agency. 2. Furnish detail(s) of proposed fire-stop assembly for penetrations in 1-hour walls. 3. Relocate exterior alarm bells to address (front) side of buildings. 4. Calculations are acceptable, but contain discrepancies in equivalent fitting counts: Three-Plex Pipe 4, fittings should include a check and butterfly valve Pipe 22, fittings should include 2T Pipe 26, fittings should include E, 2T Pipe 28, fittings should include E, 2R Six-Plex Pipe 5, fittings should include a check and butterfly valve Pipe 6, fittings should include SE, 3T, 17R Pipe 15, fittings should include T, 2R Date SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 °DATE:'4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX GARAGE 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) s 93.0 87.0 1500.0 92. 9 161. 2 83.6 ~--< AGGREGATE FLOW ANALYSIS: 'J~ TOTAL FLOW AT SOURCE 161. 2 GPM ~ ,. TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM ~ OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 61.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) s 0.0 SOURCE 83.6 61. 2 RP 0.0 ----83.5 --- DA 0.0 70.5 --- C 0.0 ----67.5 --- BOR 0.6 62.8 --- TOR 3.6 55.8 --- 5 9.6 15.4 --- 6 9.6 ----9.0 --- 7 9.6 8.0 --- 7A 9.0 K= 5.60 7.8 15.6 BA 9.0 K= 5.60 7.6 15.5 9 9.6 ----8.5 --- 10 9.6 ----7.5 --- lOA 9.0 K= 5.60 7.3 15.2 llA 9.0 K= 5.60 7.2 15.0 12 9.6 8.5 --- 12A 9.0 ----8.7 --- 13 9.6 ----8.5 --- 14A 9.0 ----8.7 --- 15A 9.0 ----8.7 --- 16 19.6 11. 0 17 19.6 11. 0 --- 18 29.6 ----6.7 --- 19 29.6 6.7 --- 19A 29.0 ----7.0 --- 20A 29.0 7.0 --- -~---..,. ..... ·~•--• ___ ,, __ .. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 'DATE:· 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX GARAGE 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 61.2 3.990 PL 25.00 PF 0.1 s 0.0 SRCE 83.6 (N/A) 1. 6 150 FTG TG PE o.o RP 0.0 0.0 83.5 0.0 0.001 TL 58.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 83.5 0.0 13.0 psi, 61. 3 gpm DA 0.0 0.0 70.5 0.0 Pipe: 3 61. 3 2.440 PL 250.00 PF 3.0 DA 0.0 0.0 70.5 0.0 4. 2 150 FTG 4L PE 0.0 C 0.0 0.0 67.5 0.0 0.011 TL 270.00 PV Pipe: 4 61. 3 1.265 PL 10.00 PF 4.4 C 0.0 0.0 67.5 0.0 15.6 150 FTG 3L PE -0.3 BOR 0.6 0.0 62.8 0.0 0.275 TL 16.00 Py ~ Pipe: 5 61. 3 1.380 PL ~ 5.7 BOR 0.6 0.0 62.8 0.0 13.1 120 FTG E -1. 3 TOR 3.6 0.0 55.8 0.0 0.272 TL V 13~ ~f 3t.r 11 7/l. Pipe: 6 61. 3 1.400 PL TOR 3.6 0.0 55.8 0.0 12.8 150 FTG 7E8T PE -2.6 5 9.6 0.0 15.4 0.0 0.168 TL 226.00 PV Pipe: 7 61. 3 1.400 PL 22.00 PF 6.4 5 9.6 0.0 15.4 0.0 12.8 150 FTG 2T2R PE 0.0 6 9.6 0.0 9.0 0.0 0.168 TL 38.00 PV Pipe: 8 31.1 1.109 PL 1. 60 PF 1.0 6 9.6 0.0 9.0 0.0 10.3 150 FTG T PE 0.0 7 9.6 0.0 8.0 0.0 0.149 TL 6.60 PV Pipe: 9 15.6 0.874 PL 0.60 PF 0.5 7 9.6 0.0 8.0 0.0 8.4 150 FTG T PE 0.3 7A 9.0 5.6 7.8 15.6 0.133 TL 3.60 PV Pipe: 10 15.5 1.109 PL F 0.7 7 9.6 0.0 8.0 0.0 5.1 150 FT 0.3 BA 9.0 5.6 7.6 15.5 0.041 TL Pipe: 11 30.2 1. 400 PL 10.00 PF 0.5 6 9.6 0.0 9.0 0.0 6.3 150 FTG R PE 0.0 9 9.6 0.0 8.5 0.0 0.045 TL 12.00 PV Pipe: 12 30.2 1.109 PL 1. 60 PF 0.9 9 9.6 0.0 8.5 0.0 10.0 150 FTG T PE 0.0 10 9.6 0.0 7.5 0.0 0.140 TL 6.60 PV Pipe: 13 15.2 0.874 PL 0.60 PF 0.5 10 9.6 0.0 7.5 0.0 8. 1 150 FTG T PE 0.3 lOA 9.0 5.6 7.3 15.2 0.126 TL 3.60 PV •y·---•-•'-'""' ••+-•,-••• C ·• .. '--,--------..... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 'DATE:· 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX GARAGE 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 15.0 1.109 F 0.6 10 9.6 0.0 7.5 0.0 5.0 150 0.3 llA 9.0 5.6 7.2 15.0 0.039 Pipe: 15 0.0 PF 0.0 9 9.6 0.0 8.5 0.0 0.0 PE 0.0 12 9.6 0.0 8.5 0.0 PV Pipe: 16 0.0 0.874 PL 3.60 PF 0.0 12 9.6 0.0 8.5 0.0 0.0 150 FTG ET PE 0.3 12A 9.0 0.0 8.7 0.0 0.000 TL 10.60 PV Pipe: 17 0.0 0.874 PL 7.00 PF 0.0 12 9.6 0.0 8.5 0.0 0.0 150 FTG R PE 0.0 13 9.6 0.0 8.5 0.0 0.000 TL 8.00 PV Pipe: 18 0.0 0.874 PL 4.60 PF 0.0 13 9.6 0.0 8.5 0.0 0.0 150 FTG ET PE 0.3 14A 9.0 0.0 8.7 0.0 0.000 TL 11. 60 PV Pipe: 19 0.0 0.874 PL 17.60 PF 0.0 13 9.6 0.0 8.5 0.0 0.0 150 FTG 2ET PE 0.3 15A 9.0 0.0 8.7 0.0 0.000 TL 28.60 PV Pipe: 22 0.0 1.109 PL 10.00 PF 0.0 5 9.6 0.0 15.4 0.0 0.0 150 FTG RT PE -4.3 16 19.6 0.0 11. 0 0.0 0.000 TL 16.00 PV Pipe: 23 0.0 0.874 PL 10.60 PF 0.0 16 19.6 0.0 11.0 0.0 0.0 150 FTG TR PE 0.0 17 19.6 0.0 11. 0 0.0 0.000 TL 14.60 PV Pipe: 24 0.0 0.874 PL 10.00 PF 0.0 17 19.6 0.0 11.0 0.0 0.0 150 FTG T PE -4.3 18 29.6 0.0 6.7 0.0 0.000 TL 13.00 PV Pipe: 25 0.0 0.874 PL 9.00 PF 0.0 18 29.6 0.0 6.7 0.0 0.0 150 FTG E2T PE 0.0 19 29.6 0.0 6.7 o.o 0.000 TL 19.00 PV Pipe: 26 0.0 0.874 PL 4.00 PF 0.0 19 29.6 0.0 6.7 0.0 0.0 150 FTG ET PE 0.3 19A 29.0 o.o 7.0 0.0 0.000 TL 11.00 PV Pipe: 27 0.0 0.874 PL 9.60 PF 0.0 19 29.6 0.0 6.7 0.0 0.0 150 FTG ER PE 0.3 20A 29. 0 0.0 7.0 0.0 0.000 TL 14. 60 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 'DATE:, 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX GARAGE CALC NOTES: (1) 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 (2) 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 0.097 gprn. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.6 ft/sec at pipe 4. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths ( in) E T L C B Ell Tee 1. 380 3.00 6.00 2.00 7.00 6.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths (in) E T R K C Ell Tee TEERUN COUPLG 0.874 4.00 3.00 1.00 0.00 1.00 1.109 5.00 5.00 1.00 0.00 1.00 1. 400 6.00 6.00 2.00 0.00 2.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths (in) E T L C B Ell Tee 1.265 5.00 9.00 2.00 11. 00 2.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths ( in) E T L C B Ell Tee 2.440 9.00 18.00 5.00 21. 00 11. 00 3.990 15.00 30.00 6.00 33.00 18.00 in Feet G 1.00 in Feet L EL45 1.00 1.00 2.00 in Feet G 2.00 in Feet G 2.00 3.00 A D 1.00 1.00 B L 0.00 1.00 0.00 1.00 0.00 2.00 A D 0.00 0.00 A D 0.00 0.00 0.00 0.00 G A u G E p R E s s u R E p s i 100.0 1 ~:::: 2 ~~ 80.0 60.0 - 40.0 - 20.0 - 0.0 B - -14.7 I I I I ' I I 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87.00 psi Flow: 1500.0 gpm LEGEND ~d I O):t 0:, 8 • Pl l 8 •• 1 1-1 - 8 ob, t-i, [1J ...... ; .. ,b, Available pressure 1 ~ 92.90 psi@ 161.2 gpm Required pressure ...... 3:N 1-( 0 tn 0 >-3 u, 2 ~ 83.56 psi@ 161.2 gpm A, Source Supply Curve 1-1 (') B. System Demand Curve .,, 0 1-1 tn z .,, 8 :,;, 1-1 m z "O :,:: t"" t< [1J [1J X :,;, G) tn ):t i-< ~ tn >-3 G) l'l t1'J 3: () ::c ):ll 1-( t"" 0 () ,, ):ll C t"" H (') ):t (') z •• ):,I /ta ::c i-< ):t tn tn 1-1 tn en ...,J ,b, ,,... X 1-( tn >-3 1-1 () .,, 0 1-1 z .,, >-3 fl) . <,Q tn Cl) 0 "1 u, I I I I I I I I 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 'DATE:, 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX GARAGE CALC WATER SUPPLY CURVE 96+ *\\\\\\\\\\\\ 10 \\\\\\\\\\\\\ I \\\\\\\\\\\\ 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point IX I 80+ I I I 72+ I I I P 64+ R I E I s I s 56+ u R E p s I ) I I I 48+ 1 I I 40+ I I I 32+ l I I 24+ I I 1============================== 16+ LEGEND I I X = Required Water Supply I 83.56 psi@ 161.2 gprn 8+ I 0 = Available Water Supply I 92.90 psi@ 161.2 gprn I " " " " " .. 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS 'DATE:, 4/14/2005 C:\HASS74\MYSTIC JOB TITLE: MYSTIC POINT 6PLEX THREE HEAD CALC WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ PRESS. @ TAG (PSI} (PSI) (GPM) (PSI) s 93.0 87.0 1500.0 92. 9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 146.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 46.9 GPM NODE NODE s RP DA C BOR TOR 5 6 7 7A BA 9 10 lOA llA 12 12A 13 14A lSA 16 17 18 19 19A 20A ANALYSIS DATA TAG ELEVATION (FT) 0.0 0.0 0.0 0.0 0.6 3.6 9.6 9.6 9.6 9.0 9.0 9.6 9.6 9.0 9.0 9.6 9.0 9.6 9.0 9.0 19.6 19.6 29.6 29.6 29.0 29.0 NODE TYPE SOURCE K= 4.90 K= 4.90 K= 4.90 PRESSURE (PSI) 71. 6 71. 6 58.6 56.8 53.8 49.0 23.3 19.4 19.4 19.7 19.7 18.2 18.2 18.5 18.5 14.4 12.9 11. 0 9.8 8.2 19.0 19.0 14.7 14.7 14.9 14.9 TOTAL REQ'D DEMAND PRESS. (GPM} (PSI} 146.9 71. 6 DISCHARGE (GPM} 46.9 --- --- --- --- ------ --- --- --- --- --- --- ------ --- 17. 6 --- 15.3 14.0 --- --- --- --- ------ Page 1 POINT.SDF --T•o• ... --,•• . --------.. - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 'DATE:• 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX THREE 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 46.9 3.990 PL 25.00 PF 0.0 s 0.0 SRCE 71. 6 (N/A) 1. 2 150 FTG TG PE 0.0 RP 0.0 0.0 71. 6 0.0 0.001 TL 58.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 71. 6 0.0 13.0 psi, 46.9 gpm DA 0.0 0.0 58.6 0.0 Pipe: 3 46.9 2.440 PL 250.00 PF 1. 8 DA 0.0 0.0 58.6 0.0 3.2 150 FTG 4L PE 0.0 C 0.0 0.0 56.8 0.0 0.007 TL 270.00 PV Pipe: 4 46.9 1.265 PL 10.00 PF 2.7 C 0.0 0.0 56.8 0.0 12.0 150 FTG 3L PE -0.3 BOR 0.6 0.0 53.8 0.0 0. 168 TL 16.00 PV Pipe: 5 46.9 1.380 PL 3.00 PF 3.5 BOR 0.6 0.0 53.8 0.0 10.1 120 FTG 2L2C PE -1. 3 TOR 3.6 0.0 49.0 0.0 0.166 TL 21. 00 PV Pipe: 6 46.9 1.400 PL 136.00 PF 23.1 TOR 3. 6 0.0 49.0 0.0 9.8 150 FTG 7E8T PE -2.6 5 9.6 0.0 23.3 0.0 0.102 TL 226.00 PV Pipe: 7 46.9 1.400 PL 22.00 PF 3.9 5 9.6 0.0 23.3 0.0 9.8 150 FTG 2T2R PE 0.0 6 9.6 0.0 19.4 0.0 0.102 TL 38.00 PV Pipe: 8 0.0 1.109 PL 1. 60 PF 0.0 6 9.6 0.0 19.4 0.0 0.0 150 FTG T PE 0.0 7 9.6 0.0 19.4 0.0 0.000 TL 6.60 PV Pipe: 9 0.0 0.874 PL 0.60 PF 0.0 7 9.6 0.0 19.4 0.0 0.0 150 FTG T PE 0.3 7A 9.0 0.0 19.7 0.0 0.000 TL 3.60 PV Pipe: 10 0.0 1.109 PL 11. 00 PF 0.0 7 9.6 o.o 19.4 0.0 0.0 150 FTG E PE 0.3 8A 9.0 0.0 19.7 0.0 0.000 TL 16.00 PV Pipe: 11 46.9 1. 400 PL 10.00 PF 1.2 6 9.6 0.0 19.4 0.0 9.8 150 FTG R PE 0.0 9 9.6 0.0 18.2 0.0 0.102 TL 12.00 PV Pipe: 12 o.o 1.109 PL 1. 60 PF 0.0 9 9.6 0.0 18.2 0.0 o.o 150 FTG T PE 0.0 10 9.6 0.0 18.2 0.0 0.000 TL 6.60 PV Pipe: 13 o.o 0.874 PL 0.60 PF o.o 10 9.6 0.0 18.2 0.0 0.0 150 FTG T PE 0.3 10A 9.0 0.0 18.5 0.0 0.000 TL 3.60 PV ,---~ ~-. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 • DATE:-4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX THREE 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 1.109 PL 11. 00 PF 0.0 10 9.6 0.0 18.2 0.0 0.0 150 FTG E PE 0.3 11A 9.0 0.0 18.5 0.0 0.000 TL 16.00 PV Pipe: 15 46.9 1.109 PL 10.00 PF 3.8 9 9.6 0.0 18.2 0.0 15.6 150 FTG 2R PE 0.0 12 9.6 0.0 14.4 0.0 0.318 TL 12.00 PV Pipe: 16 17.6 0.874 PL 3.60 PF 1. 8 12 9.6 0.0 14.4 0.0 9.4 150 FTG ET PE 0.3 12A 9.0 4.9 12.9 17. 6 0.165 TL 10.60 PV Pipe: 17 29.3 0.874 PL 7.00 PF 3.4 12 9.6 0.0 14.4 0.0 15.7 150 FTG R PE 0.0 13 9.6 0.0 11. 0 0.0 0.425 TL 8.00 PV Pipe: 18 15.3 0.874 PL 4.60 PF 1.5 13 9.6 0.0 11. 0 0.0 8.2 150 FTG ET PE 0.3 14A 9.0 4.9 9.8 15.3 0.128 TL 11.60 PV Pipe: 19 14.0 0.874 PL 17.60 PF 3.1 13 9.6 0.0 11. 0 0.0 7.5 150 FTG 2ET PE 0.3 15A 9.0 4.9 8.2 14.0 0.108 TL 28.60 PV Pipe: 22 0.0 1.109 PL 10. 00 PF 0.0 5 9.6 0.0 23.3 0.0 0.0 150 FTG RT PE -4.3 16 19.6 0.0 19.0 0.0 0.000 TL 16.00 PV Pipe: 23 0.0 0.874 PL 10.60 PF 0.0 16 19.6 0.0 19.0 0.0 0.0 150 FTG TR PE 0.0 17 19.6 0.0 19.0 0.0 0.000 TL 14.60 PV Pipe: 24 0.0 0.874 PL 10.00 PF 0.0 17 19.6 0.0 19.0 0.0 0.0 150 FTG T PE -4.3 18 29.6 0.0 14.7 a.a 0.000 TL 13.00 PV Pipe: 25 o.o 0.874 PL 9.00 PF 0.0 18 29.6 o.o 14.7 0.0 0.0 150 FTG E2T PE 0.0 19 29.6 0.0 14.7 0.0 0.000 TL 19.00 PV Pipe: 26 0.0 0.874 PL 4.00 PF 0.0 19 29.6 0.0 14.7 0.0 0.0 150 FTG ET PE 0.3 19A 2 9. 0 0.0 14.9 o.o 0.000 TL 11. 00 PV Pipe: 27 0.0 0.874 PL 9.60 PF 0.0 19 29.6 0.0 14.7 0.0 0.0 150 FTG ER PE 0.3 20A 29.0 0.0 14.9 0.0 0.000 TL 14.60 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 ·DATE:. 4/14/2005 C: \HASS74 \MYSTIC POINT. SDF JOB TITLE: MYSTIC POINT 6PLEX THREE HEAD CALC NOTES: (1) 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 (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 0.065 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.7 ft/sec at pipe 17. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths (in) E T L C B Ell Tee 1.380 3.00 6.00 2.00 7.00 6.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths (in) E T R K C Ell Tee TEERUN COUPLG 0.874 4.00 3.00 1.00 0.00 1.00 1. 109 5.00 5.00 1.00 0.00 1.00 1. 400 6.00 6.00 2.00 0.00 2.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths (in) E T L C B Ell Tee 1. 265 5.00 9.00 2.00 11.00 2.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths ( in) E T L C B Ell Tee 2.440 9.00 18.00 5.00 21. 00 11. 00 3.990 15.00 30.00 6.00 33.00 18.00 in Feet G 1.00 in Feet L EL45 1.00 1.00 2.00 in Feet G 2.00 in Feet G 2.00 3.00 A D 1.00 1.00 B L 0.00 1.00 0.00 1.00 0.00 2.00 A D 0.00 0.00 A D 0.00 0.00 0.00 0.00 G A u G E p R E s s u R E p s i 100.0 80.0 - 2H 60.0 - 40.0 - 20.0 _ o.o B - -14.7 ' ' I I 400 600 ' 800 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87,00 psi Flow: 1500.0 gpm I I I 1200 1400 FLOW {GPM) ' 1 LEGEND Available pressure 1 ~ 92.92 psi@ 146.9 gpm Required pressure 2 ~ 71.64 psi @ 146.9 gpm A. Source Supply Curve,--....1 B. System Demand Curve I 1600 1800 2000 c.io I 0 ):I tD >j [':I ! >-3 ·-· ! 1-1 >-3 ,Iii, t" ' [I] I-' •• ,Iii, ' 3:l'v >< 0 (/) 0 >-3 (JI 1-1 0 "ti 0 1-1 (/) z "ti >-3 ,, H 0\ z 'ti :,:: t" t" t'l [':I X ,, >-3 (/) :x: >< ,, tll t,rJ >-3 t,rJ [I] 3: :x: t'l :x: ):I >< 0 0 ,, 0 ):I ):I C t" t" (') H 0 )I oz .. )I / t" ::,: >< ):I tll tll 1-1 tll (/) -.J ,Iii, / 3: >< tll >-3 1-1 0 "ti 0 1-1 z 'tl >-3 Ill . o.Q (/) Cl) 0 .., (J1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 'DATE: 4/14/2005 JOB TITLE: MYSTIC POINT 6PLEX THREE HEAD CALC WATER SUPPLY CURVE 96+ *\\\\\\\\\\\\ 10 \\\\\\\\\\\\\ I \\\\\\\\\\\\ C:\HASS74\MYSTIC POINT.SDF 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point I I 80+ I I I 72+X I I I P 64+ R I E I s I S 56+ U I R I E l 48+ I P I s I I 40+ ) I I I 32+ I I I 24+ l I I============================== 16+ LEGEND I I X = Required Water Supply I 71.64 psi@ 146.9 gpm 8+ I O = Available Water Supply I 92.92 psi@ 146,9 gpm I " " " " " " " " O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX TWO HEAD CALC WATER SUPPLY DATA TOTAL SOURCE NODE TAG STATIC PRESS. (PSI) RESID. PRESS. (PSI) @ FLOW (GPM} 1500.0 AVAIL. PRESS. (PSI) @ DEMAND (GPM) s 93.0 87.0 92.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 128.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 28.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION (FT) s 0.0 RP 0.0 DA 0.0 C 0.0 BOR 0.6 TOR 3.6 5 9.6 6 9.6 7 9.6 7A 9.0 8A 9.0 9 9.6 10 9.6 lOA 9.0 llA 9.0 12 9.6 12A 9.0 13 9.6 14A 9.0 15A 9.0 16 19.6 17 19.6 18 29.6 19 29.6 19A 29.0 20A 29.0 NODE TYPE SOURCE K= 4.90 K= 4.90 PRESSURE (PSI) 68.1 68.0 55.0 54.3 53.0 50.3 38.7 38.7 38.7 38.9 38.9 38.7 38.7 38.9 38.9 38.7 38.9 38.7 38.9 38.9 32.4 26.5 17.0 9.5 8.5 8.2 128.3 DISCHARGE (GPM) 28.3 --- --- --- --- --- --- --- --- --- --- --- --- --- --- ------ --------- --- --- --- --- 14.3 14.0 REQ'D PRESS. (PSI) 68.1 ----~--~-' ·--~~·- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 , DATE: 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX TWO 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 28.3 3.990 PL 25.00 PF 0.0 s 0.0 SRCE 68.1 (N/A) 0.7 150 FTG TG PE 0.0 RP 0.0 0.0 68.0 0.0 0.000 TL 58.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 68.0 0.0 13.0 psi, 28.3 gpm DA 0.0 0.0 55.0 0.0 Pipe: 3 28.3 2.440 PL 250.00 PF 0.7 DA 0.0 0.0 55.0 0.0 1. 9 150 FTG 4L PE 0.0 C 0.0 0.0 54.3 0.0 0.003 TL 270.00 PV Pipe: 4 28.3 1.265 PL 10.00 PF 1.1 C 0.0 0.0 54.3 0.0 7.2 150 FTG 3L PE -0.3 BOR 0.6 0.0 53.0 0.0 0.066 TL 16.00 PV Pipe: 5 28.3 1.380 PL 3.00 PF 1. 4 BOR 0.6 0.0 53.0 0.0 6.1 120 FTG 2L2C PE -1. 3 TOR 3.6 0.0 50.3 0.0 0.065 TL 21. 00 PV Pipe: 6 28.3 1.400 PL 136.00 PF 9. 1 TOR 3.6 0.0 50.3 0.0 5.9 150 FTG 7E8T PE -2.6 5 9. 6 0.0 38.7 0.0 0.040 TL 226.00 PV Pipe: 7 0.0 1.400 PL 22.00 PF 0.0 5 9.6 0.0 38.7 0.0 0.0 150 FTG 2T2R PE 0.0 6 9.6 0.0 38.7 0.0 0.000 TL 38.00 PV Pipe: 8 0.0 1.109 PL 1. 60 PF 0.0 6 9. 6 0.0 38.7 0.0 0.0 150 FTG T PE 0.0 7 9.6 0.0 38.7 0.0 0.000 TL 6.60 PV Pipe: 9 0.0 0.874 PL 0.60 PF 0.0 7 9.6 0.0 38.7 0.0 0.0 150 FTG T PE 0.3 7A 9.0 0.0 38.9 0.0 0.000 TL 3.60 PV Pipe: 10 0.0 1.109 PL 11. 00 PF 0.0 7 9.6 0.0 38.7 0.0 0.0 150 FTG E PE 0.3 BA 9.0 0.0 38.9 0.0 0.000 TL 16.00 PV Pipe: 11 0.0 1.400 PL 10.00 PF 0.0 6 9.6 0.0 38.7 0.0 0.0 150 FTG R PE 0.0 9 9.6 0.0 38.7 0.0 0.000 TL 12.00 PV Pipe: 12 0.0 1.109 PL 1. 60 PF 0.0 9 9.6 0.0 38.7 0.0 0.0 150 FTG T PE 0.0 10 9.6 0.0 38.7 0.0 0.000 TL 6.60 PV Pipe: 13 0.0 0.874 PL 0.60 PF 0.0 10 9.6 0.0 38.7 0.0 o.o 150 FTG T PE 0.3 lOA 9.0 0.0 38.9 0.0 0.000 TL 3.60 PV ---·--..... ____ ,,,.,,_..,.,,,.,.,. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 • DA'i'E: 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX TWO 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 1.109 PL 11. 00 PF 0.0 10 9.6 0.0 38.7 0.0 0.0 150 FTG E PE 0.3 llA 9.0 0.0 38.9 0.0 0.000 TL 16.00 PV Pipe: 15 0.0 1.109 PL 10.00 PF 0.0 9 9.6 0.0 38.7 0.0 0.0 150 FTG 2R PE 0.0 12 9.6 0.0 38.7 0.0 0.000 TL 12.00 PV Pipe: 16 0.0 0.874 PL 3.60 PF 0.0 12 9.6 0.0 38.7 0.0 0.0 150 FTG ET PE 0.3 12A 9.0 0.0 38.9 0.0 0.000 TL 10.60 PV Pipe: 17 0.0 0.874 PL 7.00 PF 0.0 12 9.6 0.0 38.7 0.0 0.0 150 FTG R PE 0.0 13 9.6 0.0 38.7 0.0 0.000 TL 8.00 PV Pipe: 18 0.0 0.874 PL 4. 60 PF 0.0 13 9.6 0.0 38.7 0.0 o.o 150 FTG ET PE 0.3 14A 9.0 0.0 38.9 0.0 0.000 TL 11,60 PV Pipe: 19 0.0 0.874 PL 17.60 PF 0.0 13 9.6 0.0 38.7 0.0 0.0 150 FTG 2ET PE 0.3 15A 9.0 0.0 38.9 0.0 0.000 TL 28.60 PV Pipe: 22 28.3 1.109 PL 10.00 PF 2.0 5 9.6 0.0 38.7 0.0 9.4 150 FTG RT PE -4.3 16 19.6 0.0 32.4 0.0 0.125 TL 16.00 PV Pipe: 23 28.3 0.874 PL 10.60 PF 5.8 16 19.6 0.0 32.4 a.a 15.1 150 FTG TR PE 0.0 17 19.6 0.0 26.5 0.0 0.398 TL 14.60 PV Pipe: 24 28.3 0.874 PL 10.00 PF 5.2 17 19.6 0.0 26.5 0.0 15.1 150 FTG T PE -4.3 18 29.6 0.0 17.0 0.0 0.398 TL 13.00 PV Pipe: 25 28.3 0.874 PL 9.00 PF 7. 6 18 29.6 0.0 17.0 o.o 15.1 150 FTG E2T PE 0.0 19 29.6 0.0 9.5 0.0 0.398 TL 19.00 PV Pipe: 26 14.3 0.874 PL 4.00 PF 1. 2 19 29.6 0.0 9.5 0.0 7.6 150 FTG ET PE 0.3 19A 29.0 4.9 8.5 14.3 0 .112 TL 11. 00 PV Pipe: 27 14.0 0.874 PL 9.60 PF 1. 6 19 29.6 0.0 9.5 0.0 7.5 150 FTG ER PE 0.3 20A 29.0 4. 9 8. 2 14.0 0.108 TL 14.60 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 'DA'i'E: 4/14/2005 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX TWO HEAD CALC NOTES: (1) 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 (2) 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 0.122 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.1 ft/sec at pipe 25. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A Diameter (in) 1. 380 PAGE: H Diameter ( in) 0.874 1.109 1.400 PAGE: I Diameter (in) 1. 2 65 PAGE: J Diameter (in) 2.440 3.990 MATERIAL: SCH40 HWC: 120 E Ell 3.00 Equivalent Fitting Lengths in Feet T L C B G Tee 6.00 2.00 7.00 6.00 1.00 MATERIAL: CPVC HWC: 150 E Ell 4.00 5.00 6.00 Equivalent Fitting Lengths in T R K C Tee TEERUN 3.00 1.00 5.00 1.00 6.00 2.00 COUPLG 0.00 1.00 0.00 1.00 0.00 2.00 Feet L EL45 1.00 1.00 2.00 MATERIAL: CPPR-L HWC: 150 E Ell 5.00 Equivalent Fitting Lengths in Feet T L C B G Tee 9.00 2.00 11.00 2.00 2.00 MATERIAL: S40PVC HWC: 150 E Ell 9.00 15.00 Equivalent Fitting Lengths in T L C B Tee 18.00 30.00 5.00 6.00 21.00 33.00 11. 00 18.00 Feet G 2.00 3.00 A 1.00 B 0.00 0.00 0.00 A 0.00 A 0.00 0.00 D 1.00 L 1.00 1.00 2.00 D 0.00 D 0.00 0.00 100.0 G 80.0 A u G E p R E s s u R E p s i 60.0 40.0 - - - 20.0 _ 0.0 B - -14.7 I I I ' I 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87.00 psi Flow: 1500.0 gpm I I I I 1200 1400 FLOW (GPM) LEGEND Available pressure 1 ~ 92.94 psi@ 128.3 gpm Required pressure 2-~~~-68.06 psi@ 128.3 gprn A. Source Supply Curve---...1 B. System Demand Curve I I I 1600 1800 2000 ~o g~ t'l >-,3 :, H >-,3 ..c::. t""'-t'l 1--' •• ..c::. ...... :3: N >< 0 C.I) 0 >-,3 u, H ('} "O 0 H C.I) z "O 8 :x, H O'I z "O :,,;: t"" t"" [z:l t'l X :x, en >< (/) >-,3 t'l J: ::c: >< 0 :x, :i:, C t"" H n ;t, ('} z .. :i:, /t"" ::c: >< :z:; en (/) H en en -..J .c. / :3: >< (.I) 8 H ('} "O 0 H z "C 8 fl) • IQ C.I) ro 0 "'I u, SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 • DATE.: 4 / 14 / 2 0 0 5 C:\HASS74\MYSTIC POINT.SDF JOB TITLE: MYSTIC POINT 6PLEX TWO HEAD CALC WATER SUPPLY CURVE p R E s s u R E p s I ) 96+ *\\\\\\\\\\\\ 0 \\\\\\\\\\\\\ I \\\\\\\\\\\\ 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point I I BO+ I I I 72+ I X I 64+ I I I 56+ I I I 48+ I I I 40+ I I I 32+ I I I 24+ I I I============================== 16+ LEGEND I I X = Required Water Supply I 68.06 psi@ 128.3 gpm 8+ I 0 = Available Water Supply I 92.94 psi@ 128.3 gpm I " " II " " II II 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE:· 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF uOB TITLE: THREE PLEX GARAGE CALC WATER SUPPLY DATA TOTAL SOURCE NODE TAG STATIC PRESS. (PSI) RESID. PRESS. (PSI) @ FLOW (GPM) 1500.0 AVAIL. PRESS. (PSI) @ DEMAND (GPM) s 93.0 87.0 92. 9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 165.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 65.9 GPM NODE ANALYSIS DATA NODE TAG ELEVATION (FT) s 0.0 RP 0.0 DA 0.0 C 0.0 BOR 0.6 TOR 3.6 5 9.6 6 9.6 7 9.6 7A 9.0 8A 9.0 9 9.6 10 9.6 lOA 9.0 llA 9.0 12 9.6 12A 9.0 13 9.6 14A 9.0 15A 9.0 16 9.6 17 19.6 18 19.6 19 28.6 20 28.6 20A 28.0 21A 28.0 NODE TYPE SOURCE K= 5.60 K= 5.60 K= 5.60 K= 5.60 PRESSURE (PSI) 62.9 62.B 49.8 46.4 41.1 34.5 17.0 13.3 10.7 10.3 8.7 11.1 8.8 8.6 7.2 11.1 11.3 11.1 11. 3 11. 3 17. 0 12.6 12.6 8.7 8.7 9.0 9.0 165.9 DISCHARGE (GPM) 65.9 --- --- --- --- --- --- --- --- 18.0 16.5 ------ 16.4 15.0 ------ --------- --- ------ ------ --- --- ~ .. ,.,._ •' , .... , .. ..,..,.. ___ ,..,,_~~- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF ·JOB TITLE: THREE PLEX GARAGE 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 65.9 3.990 PL 20.00 PF 0.1 s 0.0 SRCE 62.9 (N/A) 1. 7 150 FTG TG PE 0.0 RP 0.0 0.0 62.8 0.0 0.001 TL 53.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 62.8 0.0 13.0 psi, 65.9 gpm DA 0.0 0.0 49.8 0.0 Pipe: 3 65.9 2.440 PL 250.00 PF 3.5 DA 0.0 0.0 49.8 0.0 4.5 150 FTG 4L PE 0.0 C 0.0 0.0 46.4 0.0 0.013 TL 270.00 PV Pipe: 4 65.9 1. 265 PL 10.00 PF 5.0 C 0.0 0.0 46.4 0.0 16.8 150 FTG 3L PE -0.3 BOR 0.6 0.0 41.1 0.0 0.314 TL 16.00 PV 2V.3 Pipe: 5 65.9 1. 380 PL@~Vr BOR 0.6 0.0 41.1 0.0 14.1 120 FT 2C PE -1. 3 TOR 3.6 0.0 34.5 0.0 0.310 TL PV Pipe: 6 65.9 1.400 PL 46.00 PF 14.9 TOR 3.6 0.0 34.5 0.0 13.7 150 FTG 4E4R PE -2.6 5 9.6 0.0 17.0 0.0 0 .192 TL 78.00 PV Pipe: 7 65.9 1.400 PL 11.00 PF 3.6 5 9.6 0.0 17.0 0.0 13.7 150 FTG TR PE 0.0 6 9.6 0.0 13.3 0.0 0.192 TL 19.00 PV Pipe: 8 34.5 0.874 PL 1. 60 PF 2.6 6 9.6 0.0 13.3 0.0 18.4 150 FTG T PE 0.0 7 9.6 0.0 10.7 0.0 0.573 TL 4.60 PV Pipe: 9 18.0 0.874 PL 0.60 PF 0.6 7 9.6 0.0 10.7 0.0 9.6 150 FTG T PE 0.3 7A 9.0 5.6 10.3 18.0 0.172 TL 3.60 PV Pipe: 10 16.5 0.874 p F 2.3 7 9.6 0.0 10.7 0.0 8.8 150 0.3 8A 9.0 5.6 8.7 16.5 0.146 Pipe: 11 31. 4 1.109 PL PF 2.3 6 9.6 0.0 13.3 0.0 10.4 150 FTG T PE 0.0 9 9.6 0.0 11.1 0.0 0.151 TL 15.00 PV Pipe: 12 31. 4 0.874 PL 1. 60 PF 2.2 9 9.6 0.0 11.1 0.0 16.8 150 FTG T PE 0.0 10 9.6 0.0 8.8 0.0 0.482 TL 4.60 PV Pipe: 13 16.4 0.874 PL 0.60 PF 0.5 10 9.6 0.0 8.8 0.0 8.8 150 FTG T PE 0.3 10A 9.0 5.6 8.6 16.4 0.145 TL 3.60 PV .. -·---"•-.. _,_.,.,,~---w SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE:-4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SOP ,JOB TITLE: THREE PLEX GARAGE CALC PIPE TAG Q(GPM) DIA(IN) L]::NGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 15.0 0.874 PL 11.60 PF 1. 9 10 9.6 0.0 8.8 0.0 8.0 150 FTG E PE 0.3 llA 9.0 5.6 7.2 15.0 0.123 TL 15.60 PV Pipe: 15 0.0 1.109 PL 10.60 PF 0.0 9 9.6 0.0 11.1 o.o 0.0 150 FTG TR PE 0.0 12 9.6 0.0 11.1 0.0 0.000 TL 16.60 PV Pipe: 16 0.0 0.874 PL 3.00 PF 0.0 12 9.6 0.0 11.1 0.0 0.0 150 FTG ET PE 0.3 12A 9.0 0.0 11. 3 0.0 0.000 TL 10.00 PV Pipe: 17 0.0 0.874 PL 7.00 PF 0.0 12 9.6 0.0 11.1 0.0 0.0 150 FTG R PE 0.0 13 9.6 0.0 11.1 0.0 0.000 TL 8.00 PV Pipe: 19 0.0 0.874 PL 4.00 PF 0.0 13 9.6 0.0 11.1 0.0 0.0 150 FTG ET PE 0.3 14A 9.0 0.0 11. 3 0.0 0.000 TL 11. 00 PV Pipe: 21 0.0 0.874 PL PF 0.0 13 9.6 0.0 11.1 0.0 0.0 150 FTG PE 0.3 15A 9.0 0.0 11. 3 0.0 0.000 TL PV Pipe: 22 0.0 1.109 PL PF 0.0 5 9.6 0.0 17.0 0.0 0.0 150 FTG PE 0.0 16 9.6 0.0 17.0 0.0 0.000 TL PV Pipe: 23 0.0 1.109 PL 10.00 PF 0.0 16 9.6 0.0 17. 0 0.0 0.0 150 FTG T PE -4.3 17 19.6 0.0 12.6 0.0 0.000 TL 15.00 PV Pipe: 24 0.0 0.874 PL 13 .00 PF 0.0 17 19.6 0.0 12.6 0.0 0.0 150 FTG 2TR PE 0.0 18 19.6 0.0 12. 6 0.0 0.000 TL 20.00 PV Pipe: 25 0.0 0.874 PL 9.00 PF 0.0 18 19.6 0.0 12.6 0.0 0.0 150 FTG TR PE -3.9 19 28.6 0.0 8.7 0.0 0.000 TL 13.00 PV Pipe: 26 0.0 0.874 PL 9.00 PF 0.0 19 28.6 0.0 8.7 0.0 0.0 150 FTG ET PE 0.0 20 28.6 0.0 8.7 0.0 0.000 TL 16.00 PV Pipe: 27 0.0 0.874 PL 4.00 PF 0.0 20 28.6 0.0 8.7 0.0 0.0 150 FTG ET PE 0.3 20A 28.0 0.0 9.0 0.0 0.000 TL 11. 00 PV Pipe: 28 0.0 0.874 PL 9.60 PF 0.0 20 28.6 0.0 8.7 0.0 0.0 150 FTG ETR PE 0.3 21A 28.0 0.0 9.0 0.0 0.000 TL 17.60 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE:. 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF ,JOB TITLE: THREE PLEX GARAGE CALC NOTES: (1) 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 (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 0.076 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 18.4 ft/sec at pipe 8. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A Diameter (in) 1. 380 PAGE: H Diameter (in) 0.874 1.109 1.400 PAGE: I Diameter (in) 1. 265 PAGE: J Diameter (in) 2.440 3.990 MATERIAL: SCH40 HWC: 120 E Ell 3.00 Equivalent Fitting Lengths in Feet T L C B G Tee 6.00 2.00 7.00 6.00 1.00 MATERIAL: CPVC HWC: 150 E Ell 4.00 5.00 6.00 Equivalent Fitting Lengths in T R K C Tee TEERUN 3.00 1.00 5.00 1.00 6.00 2.00 COUPLG 0. 00 1. 00 0.00 1.00 0.00 2.00 Feet L EL45 1.00 1.00 2.00 MATERIAL: CPPR-L HWC: 150 E Ell 5.00 Equivalent Fitting Lengths in Feet T L C B G Tee 9.00 2.00 11.00 2.00 2.00 MATERIAL: S40PVC HWC: 150 E Ell 9.00 15.00 Equivalent Fitting Lengths in T L C B Tee 18.00 30.00 5.00 21.00 6.00 33.00 11. 00 18.00 Feet G 2.00 3.00 A 1.00 B 0.00 0.00 0.00 A 0.00 A 0.00 0.00 D 1.00 L 1.00 1.00 2.00 D 0.00 D 0.00 0.00 G A u G E p R E s s u R E p s i 100.0 80.0 - 2H 60.0 - 40.0 - 20.0 _ o.o B - -14.7 ' ' ' I I T 400 600 800 ' I 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87.00 psi Flow: 1500.0 gpm ' I ' I 1200 1400 FLOW (GPM) ' T LEGEND Available pressure 1 ~ 92.90 psi@ 165.9 gpm Required pressure -2:-~~~-62.87 psi@ 165.9 gpm A. Source Supply Curve--_J B. System Demand Curve I I 1600 1800 2000 <:.i C -o> CD >-3 tZJ >-3 ,. H >-3 ob t-t, t':I f-l •• ,I!,, ..... >-3 I\) ::r: 0 ,:i 0 tZJ u, tZJ re t'4 t':I :x SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE:. 4/14/2005 ,JOB TITLE: THREE PLEX GARAGE CALC WATER SUPPLY CURVE 96+ *\\\\\\\\\\\\ 10 \\\\\\\\\\\\\ C:\HASS74\3PLEX MYSTIC POINT.SDF I \\\\\\\\\\\\ 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point I I 80+ I I I 72+ I I I P 64+ R IX E I s I S 56+ U I R I E I 48+ I P I s I I 40+ l I I I 32+ I I I 24+ I I 1============================== 16+ LEGEND I I X = Required Water Supply I 62.87 psi@ 165.9 gprn 8+ I O = Available Water Supply I 92.90 psi@ 165.9 gpm I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS DATE: 4/14/2005 C:\HASS74\3PLEX .JOB TITLE: THREE PLEX THREE HEAD CALC WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ PRESS. @ TAG (PSI) (PSI} (GPM} (PSI) s 93.0 87.0 1500.0 92.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 146.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 46.9 GPM NODE ANALYSIS DATA TOTAL DEMAND (GPM} 146.9 MYSTIC REQ'D PRESS. (PSI) 58.9 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE s RP DA C BOR TOR 5 6 7 7A BA 9 10 10A llA 12 12A 13 14A 15A 16 17 18 19 20 20A 21A (FT) 0.0 0.0 0.0 0.0 0.6 3.6 9.6 9.6 9.6 9.0 9.0 9.6 9.6 9.0 9.0 9.6 9.0 9.6 9.0 9.0 9.6 19.6 19.6 28.6 28.6 28.0 28.0 SOURCE K= 4.90 K= 4.90 K= 4.90 (PSI) (GPM) 58.9 46.9 58.8 --- 45.8 --- 44.0 --- 41.1 --- 36.9 --- 26.3 --- 24.4 --- 24.4 --- 24.7 --- 24.7 --- 19.6 --- 19.6 --- 19.9 --- 19.9 14.3 --- 12.9 17.6 10.9 --- 9.8 15.3 8.2 14.0 26.3 --- 22.0 --- 22.0 --- 18.1 --- 18.1 --- 18.4 --- 18.4 --- Page 1 POINT.SDF '• --~"•T•-"'"-~-~ ... -~-~--·····-:·-> SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE; 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF .JOB TITLE: THREE PLEX THREE 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 46.9 3.990 PL 20.00 PF 0.0 s 0.0 SRCE 58.9 (N/A) 1.2 150 FTG TG PE 0.0 RP 0.0 0.0 58.8 0.0 0.001 TL 53.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 58.8 0.0 13.0 psi, 47.0 gprn DA 0.0 0.0 45.8 o.o Pipe: 3 47.0 2.440 PL 250.00 PF 1.8 DA 0.0 0.0 45.8 0.0 3.2 150 FTG 4L PE 0.0 C 0.0 0.0 44.0 0.0 0.007 TL 270.00 PV Pipe: 4 47.0 1. 265 PL 10.00 PF 2.7 C a.a 0.0 44.0 0.0 12.0 150 FTG 3L PE -0.3 BOR 0.6 0.0 41.1 0.0 0.168 TL 16.00 PV Pipe: 5 47.0 1. 380 PL 3.00 PF 2.8 SOR 0.6 0.0 41.1 0.0 10.1 120 FTG 2C PE -1. 3 TOR 3.6 0.0 36.9 0.0 0.166 TL 17. 00 PV Pipe: 6 47.0 1. 400 PL 46.00 PF 8.0 TOR 3.6 0.0 36.9 0.0 9.8 150 FTG 4E4R PE -2.6 5 9.6 0.0 26.3 0.0 0.102 TL 78.00 PV Pipe: 7 47.0 1.400 PL 11. 00 PF 1. 9 5 9.6 0.0 26.3 0.0 9.8 150 FTG TR PE 0.0 6 9.6 0.0 24.4 0.0 0.102 TL 19.00 PV Pipe: 8 0.0 0.874 PL 1. 60 PF 0.0 6 9.6 0.0 24.4 0.0 0.0 150 FTG T PE 0.0 7 9.6 0.0 24.4 0.0 0.000 TL 4.60 PV Pipe: 9 0.0 0.874 PL 0.60 PF 0.0 7 9.6 0.0 24.4 0.0 o.o 150 FTG T PE 0.3 ?A 9.0 0.0 24.7 0.0 0.000 TL 3. 60 PV Pipe: 10 0.0 0.874 PL 11. 60 PF 0.0 7 9.6 0.0 24.4 0.0 0.0 150 FTG E PE 0.3 BA 9.0 0.0 24.7 0.0 0.000 TL 15.60 PV Pipe: 11 47.0 1.109 PL 10.00 PF 4.8 6 9.6 0.0 24.4 0.0 15.6 150 FTG T PE 0.0 9 9.6 0.0 19.6 0.0 0.319 TL 15.00 PV Pipe: 12 0.0 0.874 PL 1. 60 PF 0.0 9 9.6 0.0 19.6 0.0 0.0 150 FTG T PE 0.0 10 9.6 0.0 19.6 0.0 0.000 TL 4.60 PV Pipe: 13 0.0 0.874 PL 0.60 PF 0.0 10 9.6 0.0 19.6 0.0 0.0 150 FTG T PE 0.3 10A 9.0 0.0 19.9 0.0 0.000 TL 3.60 PV ~ ..... _,..,. .... __ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF .JOB TITLE: THREE PLEX THREE 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 0.874 PL 11. 60 PF 0.0 10 9.6 0.0 19.6 0.0 0.0 150 FTG E PE 0.3 llA 9.0 0.0 19.9 0.0 0.000 TL 15.60 PV Pipe: 15 47.0 1.109 PL 10.60 PF 5.3 9 9.6 o.o 19.6 0.0 15.6 150 FTG TR PE 0.0 12 9.6 0.0 14.3 0.0 0.319 TL 16.60 PV Pipe: 16 17.6 0.874 PL 3.00 PF 1. 7 12 9.6 0.0 14. 3 0.0 9.4 150 FTG ET PE 0.3 12A 9.0 4. 9 12.9 17.6 0.166 TL 10.00 PV Pipe: 17 29.3 0.874 PL 7.00 PF 3.4 12 9.6 0.0 14.3 0.0 15.7 150 FTG R PE 0.0 13 9.6 0.0 10.9 0.0 0.425 TL 8.00 PV Pipe: 19 15.3 0.874 PL 4.00 PF 1. 4 13 9.6 0.0 10.9 0.0 8.2 150 FTG ET PE 0.3 14A 9.0 4. 9 9.8 15.3 0.128 TL 11. 00 PV Pipe: 21 14.0 0.874 PL 17.00 PF 3.0 13 9.6 0.0 10.9 0.0 7.5 150 FTG 2ET PE 0.3 15A 9.0 4.9 8.2 14.0 0.108 TL 28.00 PV Pipe: 22 0.0 1.109 PL 11. 60 PF 0.0 5 9.6 0.0 26.3 0.0 0.0 150 FTG TR PE 0.0 16 9.6 0.0 26.3 0.0 0.000 TL 17.60 PV Pipe: 23 0.0 1.109 PL 10.00 PF 0.0 16 9.6 0.0 26.3 0.0 0.0 150 FTG T PE -4.3 17 19.6 o.o 22.0 0.0 0.000 TL 15.00 PV Pipe: 24 0.0 0.874 PL 13.00 PF 0.0 17 19.6 0.0 22.0 0.0 0.0 150 FTG 2TR PE 0.0 18 19.6 0.0 22.0 0.0 0.000 TL 20.00 PV Pipe: 25 0.0 0.874 PL 9.00 PF 0.0 18 19.6 0.0 22.0 0.0 0.0 150 FTG TR PE -3.9 19 28.6 0.0 18.1 0.0 0.000 TL 13.00 PV Pipe: 26 0.0 0.874 PL 9.00 PF 0.0 19 28.6 0.0 18.1 o.o 0.0 150 FTG ET PE 0.0 20 28.6 0.0 18.1 0.0 0.000 TL 16.00 PV Pipe: 27 0.0 0.874 PL 4.00 PF 0.0 20 28.6 0.0 18.1 0.0 0.0 150 FTG ET PE 0.3 20A 28.0 0.0 18.4 0.0 0.000 TL 11. 00 PV Pipe: 28 0.0 0.874 PL 9.60 PF 0.0 20 28.6 0.0 18.1 0.0 0.0 150 FTG ETR PE 0.3 21A 28.0 0.0 18.4 0.0 0.000 TL 17.60 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE2 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF ,JOB TITLE: THREE PLEX THREE HEAD CALC NOTES: (1) 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 (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 0.063 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.7 ft/sec at pipe 17. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1. 380 3.00 6.00 2.00 7.00 6.00 1.00 1.00 1. 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 0.874 4.00 3.00 1.00 0.00 1.00 1.00 0.00 1.00 1.109 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 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G A D Ell Tee 1.265 5.00 9.00 2.00 11.00 2.00 2.00 0.00 0.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 2.440 9.00 18.00 5.00 21. 00 11. 00 2.00 0.00 0.00 3.990 15.00 30.00 6.00 33.00 18.00 3.00 0.00 0.00 100.0 G 80.0 A u G E 1 :,l~ - P 60. 0 2 :,~ R E s s u R E 40.0 p s i 20.0 0.0 - - B - -14.7 ' ' ' ' I I 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87.00 psi Flow: 1500.0 gpm I 1200 ' ' 1400 FLOW (GPM} 1 ~ 2 ~ ! 1600 LEGEND Available pressure 92.92 psi @ 146.9 gprn Required pressure 58.8B psi @ 146.9 gprn A. Source Supply Curve B. System Demand Curve ' I 1800 c..i 0 0 :i:,, ttl ➔ M ➔ •• H "'3.i,. t"'i...._ tlJ ~ •• .c. ...._ 1-3 N ::c 0 ::c 0 tlJ c.n t':I .,, t"'i tlJ X Cl'.l re ::c ➔ H ::c z ::c :::,:;: t':I t"'i tlJ t':I ::c ::c t':I en :i:,, i-< 0 Cl) ➔ () tlJ :i:,, :s:: t"'i () ::c i-< 0 ::c :r,, () c::: .. t"'i /H ::c () :r,, en :r,, enz -.J :r,, .i,. t"'i / i-< w Cl) "OH t"'i Cl) tlJ X :s:: i-< Cl) 1-3 H () re 0 H z re 1-'J Ill '° en (I) 0 "'l 0, 2000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 4/14/2005 ,JOB TITLE: THREE PLEX THREE HEAD CALC WATER SUPPLY CURVE 96+ *\\\\\\\\\\\\ 10 \\\\\\\\\\\\\ C:\HASS74\3PLEX MYSTIC POINT.SDF I \\\\\\\\\\\\ 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point I I 80+ I I I 72+ I I I P 64+ R I E I S IX s 56+ u l R I E I 48+ I P I s I I 40+ l I I I 32+ I I I 24+ I I I============================== 16+ LEGEND I I X = Required Water Supply I 58.88 psi@ 146.9 gpm 8+ I O = Available Water Supply I 92.92 psi@ 146.9 gpm I II " " .. " II 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE.: 4/14/2005 C: \HASS7 4 \3PLEX MYSTIC POINT. SOF .JOB TITLE: THREE PLEX TWO HEAD CALC WATER SUPPLY DATA SOURCE NODE TAG STATIC PRESS. (PSI} RES ID. FLOW AVAIL. TOTAL PRESS. @ PRESS. @ DEMAND (PSI) (GPM) (PSI) (GPM) s 93.0 87.0 1500.0 92.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 128.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 28.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION (FT) s 0.0 RP 0.0 DA 0.0 C 0.0 BOR 0.6 TOR 3. 6 5 9.6 6 9.6 7 9.6 7A 9.0 8A 9.0 9 9.6 10 9.6 lOA 9.0 llA 9.0 12 9.6 12A 9.0 13 9.6 14A 9.0 15A 9.0 16 9.6 17 19.6 18 19.6 19 28.6 20 28.6 20A 28.0 21A 28.0 NODE TYPE SOURCE K= 4.90 K= 4.90 PRESSURE (PSI) 65.2 65.2 52.2 51. 5 50.2 47.8 42.0 42.0 42.0 42.2 42.2 42.0 42.0 42.2 42.2 42.0 42.2 42.0 42.2 42.2 39.7 33.5 25.4 16.3 9.8 8.8 8.2 128.5 DISCHARGE (GPM) 28.5 --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- ------ 14.5 14.0 REQ'D PRESS. (PSI} 65.2 _____ , ______ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE.: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF ,JOB TITLE: THREE PLEX TWO HEAD CALC PIPE DATA PIPE TAG Q(GPM) DIA(IN) LE:NGTH PRESS. END ELEV. NOZ, PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 28.5 3.990 PL 20.00 PF 0.0 s 0.0 SRCE 65.2 (N/A) 0.7 150 FTG TG PE 0.0 RP 0.0 0.0 65.2 0.0 0.000 TL 53.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 0.0 0.0 65.2 0.0 13.0 psi, 28.5 gpm DA 0.0 0.0 52.2 0.0 Pipe: 3 28.5 2.440 PL 250.00 PF 0.7 DA 0.0 0.0 52.2 0.0 2.0 150 FTG 4L PE 0.0 C 0.0 0.0 51. 5 0.0 0.003 TL 270.00 PV Pipe: 4 28.5 1.265 PL 10.00 PF 1.1 C 0.0 0.0 51. 5 o.o 7.3 150 FTG 3L PE -0.3 BOR 0.6 0.0 50.2 0.0 0.067 TL 16.00 PV Pipe: 5 28.5 1. 380 PL 3.00 PF 1. 1 BOR 0.6 0.0 50.2 0.0 6.1 120 FTG 2C PE -1. 3 TOR 3.6 0.0 47.8 0.0 0.066 TL 17.00 PV Pipe: 6 28.5 1. 400 PL 46.00 PF 3.2 TOR 3.6 0.0 47.8 0.0 5.9 150 FTG 4E4R PE -2.6 5 9.6 0.0 42.0 0.0 0.041 TL 78.00 PV Pipe: 7 0.0 1.400 PL 11. 00 PF 0.0 5 9.6 0.0 42.0 0.0 0.0 150 FTG TR PE 0.0 6 9.6 0.0 42.0 0.0 0.000 TL 19.00 PV Pipe: 8 0.0 0.874 PL 1. 60 PF 0.0 6 9.6 0.0 42.0 0.0 0.0 150 FTG T PE 0.0 7 9.6 0.0 42.0 0.0 0.000 TL 4.60 PV Pipe: 9 0.0 0.874 PL 0.60 PF 0.0 7 9.6 0.0 42.0 0.0 0.0 150 FTG T PE 0.3 7A 9.0 0.0 42.2 0.0 0.000 TL 3.60 PV Pipe: 10 0.0 0.874 PL 11. 60 PF 0.0 7 9.6 0.0 42.0 0.0 0.0 150 FTG E PE 0.3 BA 9.0 0.0 42.2 0.0 0.000 TL 15.60 PV Pipe: 11 0.0 1.109 PL 10.00 PF 0.0 6 9.6 0.0 42.0 0.0 0.0 150 FTG T PE 0.0 9 9.6 0.0 42.0 0.0 0.000 TL 15.00 PV Pipe: 12 0.0 0.874 PL 1. 60 PF 0.0 9 9.6 0.0 42.0 0.0 0.0 150 FTG T PE 0.0 10 9.6 0.0 42.0 0.0 0.000 TL 4.60 PV Pipe: 13 0.0 0.874 PL 0.60 PF 0.0 10 9.6 0.0 42.0 0.0 0.0 150 FTG T PE 0.3 10A 9.0 0.0 42.2 0.0 0.000 TL 3.60 PV ---··---.. -........... ---.. --,.-,.-········· •·••-~-r..., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF JOB TITLE: THREE PLEX TWO 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 0.874 PL 11. 60 PF 0.0 10 9.6 0.0 42.0 0.0 0.0 150 FTG E PE 0.3 llA 9.0 0.0 42.2 0.0 0.000 TL 15.60 PV Pipe: 15 0.0 1.109 PL 10.60 PF 0.0 9 9.6 o.o 42.0 0.0 o.o 150 FTG TR PE 0.0 12 9.6 0.0 42.0 0.0 0.000 TL 16.60 PV Pipe: 16 0.0 0.874 PL 3.00 PF 0.0 12 9.6 0.0 42.0 0.0 0.0 150 FTG ET PE 0.3 12A 9.0 0.0 42.2 0.0 0.000 TL 10.00 PV Pipe: 17 0.0 0.874 PL 7.00 PF 0.0 12 9.6 0.0 42.0 0.0 0.0 150 FTG R PE 0.0 13 9.6 0.0 42.0 0.0 0.000 TL 8.00 PV Pipe: 19 0.0 0.874 PL 4.00 PF 0.0 13 9.6 0.0 42.0 0.0 0.0 150 FTG ET PE 0.3 14A 9.0 0.0 42.2 0.0 0.000 TL 11. 00 PV Pipe: 21 0.0 0.874 PL 17.00 PF 0.0 13 9.6 0.0 42.0 0.0 0.0 150 FTG 2ET PE 0.3 15A 9.0 0.0 42.2 0.0 0.000 TL 28.00 PV Pipe: 22 28.5 1.109 PL 11.60 PF 2.2 5 9.6 0.0 42.0 0.0 9.5 150 FTG TR PE 0.0 16 9.6 0.0 39.7 0.0 0.127 TL 17.60 PV Pipe: 23 28.5 1.109 PL 10.00 PF 1. 9 16 9.6 0.0 39.7 0.0 9.5 150 FTG T PE -4.3 17 19.6 0.0 33.5 0.0 0.127 TL 15.00 PV Pipe: 24 28.5 0.874 PL 13.00 PF 8. 1 17 19.6 0.0 33.5 0.0 15.3 150 FTG 2TR PE 0.0 18 19.6 0.0 25.4 0.0 0.404 TL 20.00 PV Pipe: 25 28.5 0.874 PL 9.00 PF 5.3 18 19.6 0.0 25.4 0.0 15.3 150 FTG TR PE -3.9 19 28.6 0.0 16.3 0.0 0.404 TL 13.00 PV i: Pipe: 26 28.5 0.874 PL ~ ~1,i·s • 19 28.6 0.0 16.3 0.0 15.3 150 FTG PE 0.0 20 28.6 0.0 9.8 0.0 0.404 TL 1 PV Pipe: 27 14.5 0.874 PL 4.00 PF 1. 3 20 28.6 0.0 9.8 0.0 7.8 150 FTG ET PE 0.3 20A 28.0 4.9 8.8 14.5 0 .116 TL 11.00 PV ~ Pipe: 28 14.0 0.874 PL ~¢~~ 20 28.6 0.0 9.8 0.0 7.5 150 FTG 21A 28.0 4. 9 8.2 14.0 0.108 TL V SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DAT&: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF JOB TITLE: THREE PLEX TWO HEAD CALC NOTES: (1) 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 (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 0.050 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.3 ft/sec at pipe 25. (4) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A Diameter (in) 1.3B0 PAGE: H Diameter (in) O.B74 1.109 1.400 PAGE: I Diameter (in) 1. 2 65 PAGE: J Diameter (in) 2.440 3.990 MATERIAL: SCH40 HWC: 120 E Ell 3.00 Equivalent Fitting Lengths in Feet T L C B G Tee 6.00 2.00 7.00 6.00 1.00 MATERIAL: CPVC HWC: 150 E Ell 4.00 5.00 6.00 Equivalent Fitting Lengths in T R K C Tee TEERUN 3.00 1.00 5.00 6.00 1.00 2.00 COUPLG 0.00 1.00 0.00 0.00 1.00 2.00 Feet L EL45 1.00 1.00 2.00 MATERIAL: CPPR-L HWC: 150 E Ell 5.00 Equivalent Fitting Lengths in Feet T L C B G Tee 9.00 2.00 11.00 2.00 2.00 MATERIAL: S40PVC HWC: 150 E Ell 9.00 15.00 Equivalent Fitting Lengths in Feet T L C B G Tee 18.00 30.00 5.00 21.00 6.00 33.00 11. 00 18.00 2.00 3.00 A 1.00 B 0.00 0.00 0.00 A 0.00 A 0.00 0.00 D 1.00 L 1.00 1.00 2.00 D 0.00 D 0.00 0.00 G A u G E p R E s s u R E p s i 100.0 1 ~ ~ 80.0 - 2 ~ 60.0 - 40.0 - 20.0 - o.o 8 - -14.7 I I ' I 1 I I 400 600 800 1000 WATER SUPPLY ANALYSIS Static: 93.00 psi Resid: 87.00 psi Flow: 1500.0 gpm ' 1200 I 1400 FLOW (GPM) - 1 ~ 2 ~ I I 1600 LEGEND Available pressure 92.94 psi@ 128.5 gpm Required pressure 65.25 psi@ 128.5 gpm A. Source Supply Curve- B. System Demand Curve ' ' 1800 ~~ trl 8 ~ t-3" ., , H i-,3.i::,, t-+ ...... trl I-' .. .i::,, ...... 8 I\) :r 0 :;., 0 t"l 0, trl 'O t-+ trl :>< C/l 'ti ,, 8 H :e:: z 0 ::,;: t" :r trl trl ,, ):I t:I C/l 1-( n C/l ):i 8 t-' t'l () 3: :t: 1-( C ~ nc •• t" /H :t: n ):i ~~ -.J ):i .i::,, t-+ /1-( w {fl 'O H t" C/l trl :>< 3: 1-( {/.l 8 H () 'O 0 H z "O 8 Ill . I.Cl {fl (T) t:l I'll 0, 2000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 4/14/2005 C:\HASS74\3PLEX MYSTIC POINT.SDF JOB TITLE: THREE PLEX TWO HEAD CALC WATER SUPPLY CURVE 96+ *\\\\\\\\\\\\ 0 \\\\\\\\\\\\\ I \\\\\\\\\\\\ 88+ * <-87.0 psi@ 1500 gpm I Flow Test Point I I 80+ I I I 72+ I I X P 64+ R I E I s I s 56+ u l R I E I 48+ I P I s l I 40+ ) I I I 32+ I I I 24+ I I !============================== 16+ LEGEND " I " IX= Required Water Supply II I 65.25 psi@ 128.5 gpm .. 8+ " I O = Available Water Supply It I 92.94 psi@ 128.5 gpm ff I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)