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HomeMy WebLinkAbout31400 CASINO DR_ 97-1130 (9)31400 CASINO DR. 97-1130 5/6 SPRINKLER SYSTEM HYDRAULIC ANALYSISt i JOB TITLE: LAKE CHEVROLET WATER SUPPLY CURVE Page 8 120+ i 110+ 0 100+\ i \ 90+ \\ i \ P 80+ \ R ; \ E ; \ 8 \ 8 70+ \ U ; \ R ; \ E 80+ \\ P ; 8 i \ 150+ \ 40X \ 30+ \ 20+ LEGEND • < -20.0 psi 0 8802 gpm" Flow Test Point" X = Required Water Supply 39.03 psi 0 404.2 gpm 10+ 0 = Availably Water Supply 104.72 pai 0 404.2 gpm s ' 32004800 8400 8000 .9800 11200 12800 14400 18000 FLOW (GPM) i e I 47 1,. f 1 t f r` f.r t, i7 tur a r e { 4 'a 4s- I SINGLETON FIRE PROTECTION r 22559 W. HICKORY PLACE SAUGUS, CALIF, 91350 S f MosT' PXM VM tea HYDRAULIC CALCULATIONS FOR JST REMOTE AREA JOB LAKE CHEVROLET - 31400 CASINO DRIVE DA'Z'E :10 -17 -97 DESIGN DATA - OCCUPANCY CLASSIFICATION: ORDINARY (GROUP II) DENSITY: ,40 AREA OF APPLICATION: 1500 SO. FT. COVERAGE PER SPRINKLER: 130 UP RIGHT - PENDENTS SPRINKLERS CALCULATED: 18 y SPRINKLER WATER FLOW REQUIRED: 431.5 gpm TOTAL WATER REQ.(including hose) 881.5 gpm FLOW \PRESSURE (at base of riser) 431.5 gpm 0 053.2 psi SPRINKLER ORIFICE SIZE: 1/2" NAME OF CONTRACTOR: SINGLETON FIRE PRO. DESIGN \LAYOUT BY: R.S. AUTHORITY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 887001 C•-18 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE N 9878Z 33 ) HRS SYSTEMS, INC. j ATLANTA, GA I mot r xa i F ate( f b / r F t j EQUIVALENT K- FACTOR CALCULATOR I Node Sprinkler Pipe dia. Total equiv. Pipe H -WK- factor (in) EquivalentNamelelength (ft) coef . K- factor t r CHEVY 5.E0 1.087 5.50 120 5.47 r xa i F s SINGLETON FIRE PROTECTION 22559 W. HICKORY PLACE SAUGUS, CALIF. 91350 r'. GISOUN fl.O*- / oAt.tc5 &.t 1. / j v AMA HYDRAULIC CALCULATIONS FOR MOST REMOTE AREA OB LAKE CHEVROLET - 31400 CASINO DRIVE DATE:10 -17 -97 DESIGN DATA - OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 AREA OF APPLICATION: 1500 SO. FT. COVERAGE PER SPRINKLER: 225 PENDENTS SPRINKLERS CALCULATED: 18 SPRINKLER WATER FLOW REQUIRED: 304.2 gpm TOTAL WATER REQ.(including hose) 404.2 gpm FLOW \PRESSURE (at base of riser) 304.2 gpm 0 027.9 psi SPRINKLER ORIFICE SIZE: 1/2" NAME OF CONTRACTOR: SINGLETON FIRE PRO. DESIGN \LAYOUT BY: R.S. AUTHORTIiY HAVING JURISDICTION: COUNTY OF RIVERSIDE CONTRACTOR CERTIFICATION NUMBER: 667001 C -16 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE M 9878Z 33 ) HRS SYSTEMS, INC. ATLANTA, GA 2 a,4 qty .. ,. .. \. 'r. -.. .. a . i 4 d EQUIVALENT K- FACTOR CALCULATOR Node Sprinkler Pipe d1a. Total equiv. Pipe H -W Equivalent Name K- factor (;n) length (ft) coef. K- factor CHEVY 5.60 1.087 5.50 120 5.47 a, a. r ( % %• P r t r «,3 fn _ i r II SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1Date: Oct 21, 1997IJOBTITLE: LAKE CHEVROLET CHEVY4 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'DNODEPRESS. PRESS. e " PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 105.0 20.0 8802.0 104.7 404.2 39.0 AGGREGATE FLOW ANALYSIS: I TOTAL FLOW AT SOURCE 4 TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM 4OTHERHOSESTREAMALLOWANCESiTOTALDISCHARGEFROMACTIVESPRINKLERS0.0 GPM 304.2 GPM NODE ANALYSIS DATAj NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 4FT) (PSI) (GPM) F 1 0.0 SOURCE 39.0 304.225.0 - - - - 38.7 r 3 5.0 - - - - 4 0.0 - - - - 27.7 - - - 29.2 8 19.0 - - - - 27.9 - - - 7 19.0 - - - - 20.9 - - - 8 12.0 K= 5.80 19.4 - - - 9 12.0 - - 7.2 15.A 0 7.5 7012K= 5 80 15.7 ' 12.0 - - - - .8 8.412 - - - ! 12.0 K= 5.60 8.5 18.31312.0 - - - - 9.1 _ _ _ 14 12.0 K= 5.80 9.2 17.01512.0 - - - - 9.81612.0 K= 5.60 10.3 -18.01712.0 - - - - 11.01812.0 K= 5.6019 11.9 - - - 9.312.0 - - - - 1 12.7 j2012.0 - - - - 13.6 - - - 22 11.0 15.0 ' 23 12.0 K= 5.47 7.7 15.212.0 K= 5.47 8.4 15.82412.0 K= 5.60 10.7 1832512.0 - - - - . 11.212.0 K= 5.60 11.1 18.712.0 28 12.0 - - - - 11.7 - - - i <: 29 12.0 K= -5.60 9.4 16.6 ! ! 30 12.0 K= 5.60 9.5 17.2 yp , QQ1 12.0 9.93212.0 - - - - 13.3 - -- 33 11.0 - - - - 14.7 - - - 34 12.0 K= 5.47 7.7 - - - . 15.2 ia ':•.i•;),4" '! 4t,r " ? fir; t.. M twW'_ ts4 '4• 1 rt F i b4 r T sr' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: Oct 21, 1997 JOB TITLE: LAKE CHEVROLET WATER SU1DPLY DATA Page 1 CHEVY3 SOURCE STATIC RESID. FLOW AVAIL. TOTAL REO'DNODEPRESS. PRESS. 0 PRESS. A DEMAND PRESS. TAG (PSI) PSI) (GPM) PSI) GPM) PSI) 1 105.0 i 20.0 8802.0 104.3 681.5 85.2 r 65.2 431.5 2 5.0 AGGREGATEi FLOW ANALYSIS: 62.7 3 TOTAL FLOW AT SOURCE 681.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 431.5 GPM NODE ANALYSIS DATA NODE TYPE PRESSURE DISCHARGE NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 24.0 FT) 5.47 26.4 PSI) GPM) 1 0.0 SOURCE 65.2 431.5 2 5.0 62.7 3 5.0 53.7 4 0.0 54.8 5 3.0 53.2 8 19.0 46.1 7 19.0 43.4 8 23.0 39.1 b 23.0 33.2 10 23.0 37.7 11 23.0 33.2 12 23.0 36.6 13 23.0 33.1 14 23.0 35,8 15 23.0 33.0 16 23.0 35.2 17 23.0 32.9 18 23.0 34.5 19 23.0 32.7 20 23.0 34.0 21 23.0 32.4 22 23.0 33.5 23 23.0 32.2 24 23.0 33.1 25 23.0 31.8 26 23.0 32.7 27 23.0 31.4 28 23.0 32.4 29 23.0 30.9 30 31 23.0 24.0 32.2 26.3 32 24.0 K= 5,8C 24.7 27.8 33 24.0 K= 5.47 26.1 28.03424.0 K= 5.47 26.1 28.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE: LAKE CHEVROLET NODE ANALYSIS DATA (cont'd) NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 35 24.0 K= 5.47 26.4 28,1 36 23.0 30.3 37 23.0 32.1 38 24.0 21.8 39 24.0 K= 5.60 20.4 25.3 40 24.0 K= 5.60 20.2 25.2 41 24.0 21.7 42 24.0 K= 5.50 20.6 25.4 43 24.0 21.8 44 24.0 K= 5.80 20.7 25.5 AS 24.0 K= 5.47 22.1 25.7 46 24.0 K= 5.47 23.3 26.4 47 24.0 K= 5.60 23.8 27.3 48 24.0 26.4 49 23.0 30.0 50 23.0 32.0 51 24.0 K= 5.47 25.7 27,7 52 24.0 K= 5.47 25.5 27.6 53 24.0 K= 5.47 25.5 27.8 54 24.0 K= 5.47 25.9 27,8 55 24.0 K= 5.60 25.1 28.0 56 24.0 27.5 t f 57 23.0 30.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: LAKE CHEVROLET PIPE DATA. PIPE TAG END ELEV. NODES (FT) Pipe: 1 1 0.0 2 5.0 Pipe: 2 2 5.0 3 5.0 Pipe: 3 3 5.0 4 0.0 Pipe: 4 4 0.0 5 3.0 Pipe: 5 5 3.0 6 19.0 Pipe: 6 f6 19.0 7 19.0 Pipe: 7 7 19.0 8 23.0 Pipe: 8 8 23.0 9 23.0 Pipe: 9 9 23.0 11 23.0 Pipe: 10 8 23.0 10 23.0 Pipe: 11 10 23.0 11 23.0 Pipe: 12 11 23.0 13 23.0 Pipe: 13 10 23.0 12 23.0 Q(GPM) DIA(IN) LENGTH PRESS. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. K) (PSI) (GPM) F.L. /FT (PSI) 431.5 6.010 PL 55.00 PF 0.3 SRCE 65.2 (N /A) 4.9 140 FTG - - -- PE 2.2 0.0 62.7 0.0 0.006 TL 55.00 PV 0.2 FIXED PRESSURE LOSS DEVICE 0.0 62.7 0.0 9.0 psi, 431.6 gpm 0.0 53.7 0.0 431.5 6.010 PL 201.00 PF 1.2 0.0 53.7 0.0 4.9 150 FTG 36.40 PE 2.2 0.0 54.6 0.0 0.005 TL 237.40 PV 0.2 431.5 6.010 PL 3.00 PF 0.1 0.0 54.6 0.0 4.9 140 FTG 18.20 PE 1.3 0.0 53.2 0.0 0.006 TL 21.20 PV 0.2 431.5 6.357 PL 19.00 PF 0.1 0.0 53.2 0.0 4.4 120 FTG - - -- PE 6.9 0.0 46.1 0.0 0.006 TL 19.00 PV 0.1 431.5 4.340 PL 53.50 PF 2.8 0.0 46.1 0.0 9.4 120 FTG 20.00 PE 0.0 0.0 43.4 0.0 0.038 TL 73.50 PV 0.6 431.5 4.340 PL 37.50 PF 2.6 0.0 43.4 0.0 9.4 120 FTG 30.00 PE 1,7 0.0 39.1 0.0 0.038 TL 67.50 PV 0.6 38.6 1.650 PL 90.00 PF 5.9 0.0 39.1 0.0 5.8 120 FTG 32.00 PE 0.0 0.0 33.2 0.0 0.048 TL 122.00 PV 0.2 38.6 3.340 PL 12.40 PF 0.0 0.0 33.2 0,0 1.4 120 FTG - - -- PE 0.0 0.0 33.2 0.0 0.002 TL 12.40 PV 0.0 393.0 3.340 PL 12.40 PF 1.4 O.0 39.1 0.0 14.4 120 FTG - - -- PE 0.0 0 37.7 0.0 0.114 TL 12.40 PV 1.4 33.3 1.650 PL 90.00 PF 4.5 0.0 37.7 0.0 5.0 120 FTG 32.00 PE 0.0 0.0 33.2 0.0 0.037 TL I 22,00 PV 0.2 71.9 3.340 PL 10.80 PF 0.1 0.0 33.2 0.0 2.6 120 FTG - - -- PE 0.0 0.0 33.1 0.0 0.005 TL 10.80 PV 0.0 359.7 3.340 PL 10.80 PF 1.0 0.0 37.7 0.0 13.2 120 FTG - - -- PE 0.0 0.0 36.6 0.0 0.097 TL 10.80 PV 1.2 l r ;{ fL'Fj j r fF ex i i >,f'r Fw' %4t:•'R4, d., Y r y . T,.: -. .rare:, . ' t•_ r. r i Y y f 9 1 ik t- I yy .. Y 4 •;{ 1 1FxR'rr .S.,,.,4.' "I r- 3',< IIII I r .. ,.. 4 :SC _,r ...: -.. :, .- ^.rte+,.. .. .•, yg ,ys.i'. y! `,, ?{ C "^ _ _ y .,t ,. E.. 1_r..`' -,rd -- x "Ra%!I.`- `r.- r;:tr. .'_" r ..ij:.`- ,i ber f.'$- '.O.P•?J`_ '!f..•+''3"d'Y -,' '' c soor J it r,. 0 c i is Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: LAKE CHEVROLET PIPE DATA f jPIPE TAG O(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 1 304.2 6.010 PL 59.00 PF 0.2 1 0.0 SRCE 39.0 (N /A) 3.4 140 FTG - - -- PE 2.2 2 5.0 0.0 36.7 0.0 0.003 TL 55.00 PV 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 36.7 0.0 9.0 psi, 304.2 gpm 12 .. ., ,. ripe: 3 3 5.0 4 0.0 Pipe: 4 4 0.0 5 3.0 Pipe: 5 5 3.0 8 19.0 Pipe: 6 6 19.0 7 19.0 Pipe: 7 7 19.0 21 11.0 Pipe: 8 8 .2.0 9 12.0 Pipe: 9 9 12.0 11 12.0 Pipe: 10 1C 12.0 11 12.0 Pipe: 11 11 12.0 13 12.0 Pipe: 12 12 12.0 13 12.0 Pipe: 13 13 12.0 15 12.0 304.2 6.010 PL 201.00 PF 0.6 0.0 27.7 0.0 3.4 150 FTG 38.40 PE 2.2 0.0 29.2 0.0 0.003 TL 237.40 PV 0.1 304.2 8.010 PL 3.00 PF 0.1 0.0 29.2 0.0 3.4 140 FTG 18.20 PE 1.3 0.0 27.9 0.0 0.003 TL 21.20 PV 0.1 304.2 6.357 PL 19.00 PF 0.1 0.0 27.9 0.0 3.1 120 FTG - - -- PE 6.9 0.0 20.9 0.0 0.003 TL 19.00 PV 0.1 304.2 4.340 PL 53.50 PF 1.5 0.0 20.9 0.0 6.6 120 FTG 20.00 PE 0.0 0.0 19.4 0.0 0.020 TL 73.50 PV 0.3 304.2 3.340 PL 89.50 PF 7.9 0.0 19.4 0.0 11.1 120 FTG 21.00 PE 3.5 0.0 15.0 0.0 0.071 TL 110.50 PV 0.8 15.0 1.087 PL 2.50 PF 0.3 5.6 7.2 15.0 5.2 120 FTG 2.00 PE 0.0 0.0 7.5 0.0 0.064 TL 4.50 PV 0.2 15.0 1.087 PL 14.00 PF 0.9 0.0 7.5 0.0 5.2 120 FTG - - -- PE 0.0 0.0 8.4 0.0 :,.064 TL 14.00 PV 0.2 15.7 1.087 PL 2.50 PF 0.5 5.6 7.8 15.7 5.4 120 FTG 5.00 PE 0.0 0.0 8.4 0.0 0.070 TL 1.50 PV 0.2 30.7 1.087 P' 3.03 PF 0.7 0.0 8.4 0.0 10.6 12C - - - -- PE 0.0 0.0 9.1 0.0 0.241 TL 3.00 PV 0.8 16.3 1.087 PL 3.50 PF 0.8 5.6 8.5 16.3 5.6 120 FTG 5.00 PE 0.0 0.0 9.1 0.0 0.075 TL 8.50 Pv 0.2 47.0 1 6'0 PL 10.00 PF 0.7 0.0 9.1 0.0 7.0 120 FTG - - -- PE 0.0 0.0 9.8 0.0 0.070 TL 0.00 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: LAKE CHEVROLET NODE ANALYSIS DATA (cont'd) 3 EI ; NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 1 t FT) PSI) GPM) 35 12.0 K= 3.47 8.4 15.8 36 12.0 K= 5.60 10.4 18.0 37 12.0 - - 11.1 38 12.0 K= 5.60 10.8 18.4 39 12.0 - - 11.6 40 12.0 K= 5.60 8.8 16,6 41 12.0 - - 9.1 42 12.0 K= 5.60 9.3 17.0 43 12.0 - 9.9 44 12.0 - - 13.2 45 11.0 - - 14.6 c i is Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: LAKE CHEVROLET PIPE DATA f jPIPE TAG O(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 1 304.2 6.010 PL 59.00 PF 0.2 1 0.0 SRCE 39.0 (N /A) 3.4 140 FTG - - -- PE 2.2 2 5.0 0.0 36.7 0.0 0.003 TL 55.00 PV 0.1 Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 5.0 0.0 36.7 0.0 9.0 psi, 304.2 gpm 12 .. ., ,. ripe: 3 3 5.0 4 0.0 Pipe: 4 4 0.0 5 3.0 Pipe: 5 5 3.0 8 19.0 Pipe: 6 6 19.0 7 19.0 Pipe: 7 7 19.0 21 11.0 Pipe: 8 8 .2.0 9 12.0 Pipe: 9 9 12.0 11 12.0 Pipe: 10 1C 12.0 11 12.0 Pipe: 11 11 12.0 13 12.0 Pipe: 12 12 12.0 13 12.0 Pipe: 13 13 12.0 15 12.0 304.2 6.010 PL 201.00 PF 0.6 0.0 27.7 0.0 3.4 150 FTG 38.40 PE 2.2 0.0 29.2 0.0 0.003 TL 237.40 PV 0.1 304.2 8.010 PL 3.00 PF 0.1 0.0 29.2 0.0 3.4 140 FTG 18.20 PE 1.3 0.0 27.9 0.0 0.003 TL 21.20 PV 0.1 304.2 6.357 PL 19.00 PF 0.1 0.0 27.9 0.0 3.1 120 FTG - - -- PE 6.9 0.0 20.9 0.0 0.003 TL 19.00 PV 0.1 304.2 4.340 PL 53.50 PF 1.5 0.0 20.9 0.0 6.6 120 FTG 20.00 PE 0.0 0.0 19.4 0.0 0.020 TL 73.50 PV 0.3 304.2 3.340 PL 89.50 PF 7.9 0.0 19.4 0.0 11.1 120 FTG 21.00 PE 3.5 0.0 15.0 0.0 0.071 TL 110.50 PV 0.8 15.0 1.087 PL 2.50 PF 0.3 5.6 7.2 15.0 5.2 120 FTG 2.00 PE 0.0 0.0 7.5 0.0 0.064 TL 4.50 PV 0.2 15.0 1.087 PL 14.00 PF 0.9 0.0 7.5 0.0 5.2 120 FTG - - -- PE 0.0 0.0 8.4 0.0 :,.064 TL 14.00 PV 0.2 15.7 1.087 PL 2.50 PF 0.5 5.6 7.8 15.7 5.4 120 FTG 5.00 PE 0.0 0.0 8.4 0.0 0.070 TL 1.50 PV 0.2 30.7 1.087 P' 3.03 PF 0.7 0.0 8.4 0.0 10.6 12C - - - -- PE 0.0 0.0 9.1 0.0 0.241 TL 3.00 PV 0.8 16.3 1.087 PL 3.50 PF 0.8 5.6 8.5 16.3 5.6 120 FTG 5.00 PE 0.0 0.0 9.1 0.0 0.075 TL 8.50 Pv 0.2 47.0 1 6'0 PL 10.00 PF 0.7 0.0 9.1 0.0 7.0 120 FTG - - -- PE 0.0 0.0 9.8 0.0 0.070 TL 0.00 PV 0.3 tiro et _ r; h a r% f r J' f ; t 5.i Y i ii a 4 l h r{' I,^ f J 3 1 J.- 1 t t f f t .t ..: .. .rr •i. ".y ... :.i .,... •: .. . ... i„ l.ri` k. t -.3 l.G' 1. .y.7,. f.; i.• Ik ( +" J r," ..... .. ..: . y ... >„ :'.:i. ..,... -ter.. ,S. •y x'Y Y, ;rwE r i -l. i! .:5:' '# 1n : -,,, .. '.,.r..., :._ .. ... , <'., . >r ,,., y_:. ,;. y. :.4s d, •'..) ,•. ,. y .,.. <., , 1.. ,+. .,,+ ,•.j<t(` :..y ^fl ' i! £F /,}i. (w'4 ter {.:: .... ;... :x,yr.; +td. A >c: ,.9f.. ..''..- + J.' ,av.. jr(y !(, s:,'f+_ .••4` -. rs,, ys- ..rt +yj :5 _1.,.;, yy i.1%`f,'z44L t'GtatG', a A::. ,t. r .F 7,;: P4^° py. Q f 1'st'*lF ib' Y. w•: 4i.e^'''!1•:f''7.T.'4'ak: y}y .f_..- 4'' FJJ/ .'I k"i`.R.!Y..0 "F'97F 7.Y .s.',: 1 'f3'/": "EJ` rr'k Ris(1. -, tiro et _ r; h a r% f r J' f ; t 5.i Y i ii a 4 l h r{' I,^ w.i o y c q f f 4!. i y y s r, SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: LAKE CHEVROLET ii j PIPE DATA cont'd) PIPE TAG Q(aPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) FT) SUM. NODES FT) K) PSI) GPM) F.L. /FT PSI) 14 Pipe: 14 17.0 1.087 PL 2.50 PF 0.6 15 12.0 5.6 9.2 17.0 5.9 120 FTG 5.00 PE 0.012.0 0.0 9.8 0.0 0.081 TL 7.50 PV 0.2 15 Pipe: 15 63.9 1.650 PL 10.00 PF 1.2 17 12.0 0.0 9.8 0.0 9.6 120 FTG PE 0.0 r12.0 0.0 11.0 0.0 0.123 TL 10.00 PV 0.6 r - 18 Pipe: 16 18.0 1.087 PL 2.50 PF 0.7 17 12.0 5.6 10.3 18.0 6.2 120 FTG 5.00 PE 0.012.0 0.0 11.0 0.0 0.090 TL 7.50 PV 0.3I I 17 Pipe: 17 81.9 1.650 PL 5.50 PF 2.612.0 0.0 11.0 0.0 12.3 120 FTG 8.00 PE 0.02012.0 0.0 13.6 0.0 0.195 TL 13.50 PV 1.0 E 18 Pipe: 18 19.3 1.087 P12.0 5.6 11.9 19.3 8.7 120 FTG 5.00 PE 0.0 t Ij 19 12.0 0.0 12.7 0.0 0.103 TL 7.50 PV 0.3 Pipe: 19 19.3 1.087 PL 4.50 PF 1.0x`119 12.0 0.0 12.7 0.0 6.7 120 FTG 5.00 PE 0.02012.0 0.0 13.6 0.0 0.103 TL 9.50 PV 0.3 Pipe: 20 101.3 2.115 PL 1.00 PF 0.92012.0 0.0 13.6 0.0 9.2 120 FTG 10.00 PE 0.42111.0 0.0 15.0 0.0 0.086 TL 11.00 PV 0.6 21 Pipe: 21 203.0 3.340 PL 10.50 PF 0.4 i b11.0 0.0 15.0 0.0 7.4 120 FTG PE 0.03311.0 0.0 14.7 0.0 0.034 TL 10.50 PV 0.4 Pipe: 22 15.2 1.087 PL 10.00 PF 0.72212.0 5.5 7.7 15.2 5.3 120 FTG PE 0.02312.0 5.5 8.4 15.8 0.066 TL 10.00 PV 0.2 i 23 Pipe: 23 12.0 5.5 8.4 15.8 31.1 10.7 1.087 PL 11.50 PF 2.8 25 12.0 0.0 11.2 0.0 120 FTG 0.247 TL 11.50 PE PV 0.0 0.8 24 Pipe: 24 18.3 1.087 PL 1.00 PF 0.612.0 5.6 10.7 18.3 6.3 120 FTG 5.00 PE 0.02512.0 0.0 11.2 0.0 0.093 TL 6.00 PV 0.3 y I y Pipe: 25 49.4 1.650 PL 6.00 PF 0.52512.0 0.0 11.2 0.0 7.4 120 FTG PE 0.02712.0 0.0 11.7 0.0 0.076 TL 6.00 PV 0.4 26 Pipe: 20 18.7 1.087 PL 1.00 PF 0.612.0 5.6 11.1 18.7 5.5 120 FTG 5.00 PE 0.02712.0 0.0 11.7 0.0 0.098 TL 8.00 PV 0.3 tiro et _ r; h a r% f r J' f ; t 5.i Y i ii a 4 l h r{' I,^ SPRINKLER SYSTEM HYDRAULIC ANALYSIS P j SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6age5SPRINKLERSYSTEMHYDRAULICANALYSISPage4 JOB TITLE: LAKE CHEVROLETJOBTITLE: LAKE CHEVROLET JOB TITLE: LAKE CHEVROLET PIPE DATA (cont'd) PIPE DATA (cont'd) PIPE DATA (cont'd) .,') PIPE TAG Q(GPM) DIA(IN) LENGT4 PRESS. PIPE "AG O(GPM) DIA(IN) LENGTH PRESS. t_.p PIPE TAG 0(GPM) OIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) NODES (FT) (K) (PSI) (GPM) F.L. /FT (P8I) NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 40 171.5 3.340 PL 10.50 PF 0.3Pipe: 1 29.1 1.850 PL 90.00 PF 3.5 Pipe: 27 189.2 3.340 PL 9.70 PF 0.3 i 28 23.0 0.0 32.4 0.0 6.3 120 FTG - - -- PE 0.02123.0 0.0 32.4 0.0 6.9 120 FTG - - -- PE 0.0 30 23•.0 0.0 32.2 0.0 0.025 TL 10.50 PV 0.31213.0 0.0 36.6 0.0 4.4 120 FTG 32.00 PE 0.0 23 23.0 0.0 32.2 0.0 0.030 TL 9.70 PV 0.31323.0 0.0 33.1 0.0 0.029 TL 122.00 PV 0.1 ! Pipe: 41 54.1 1.850 PL 44.00 PF 6.4 i Pipe: 15 Pipe: 28 242.4 3.340 PL 9.70 PF 0.5 i 30 23.0 0.0 32.2 0.0 8.1 120 FTG 18.00 PE 0.4P101.0 3.340 PL 9.10 PF 0.1 20 23.0 0.0 34.0 0.0 8.9 120 FTG - - -- PE 0.0 F1323.0 0.0 33.1 0.0 3.7 120 FTG - - -- PE 0.0 31 24.0 0.0 26.3 0.0 0.090 TL 80.00 PV 0.41523.0 0.0 33.0 0.0 0.009 TL 9.10 PV 0.1 22 23.0 0.0 33.5 0.0 0.047 'iL 9.70 PV 0.5 Pipe: 16 330.8 3.340 PL 8.10 PF 0.8 23.0 0.0 33.5 0.0 2.6 120 FTG 32.00 PE 0.0 Pipe: 29 17.6 1.650 PL 90.00 PF 1.4 Pipe: 42 27.8 1.087 PL 3.00 PF 1.6 31 24.0 0.0 28.3 0.0 9.6 120 FTG 5.00 PE 0.022 9 12 23.0 0.0 35.8 0.0 12.1 120 FTG - --- PE 0.0 23 230 00 32.2 0.0 0.011 TL 122.00 PV 0.0 32 24.0 5.6 24.7 27.8 0.202 T!. 8.00 PV 0.8 14 23.0 0.0 35.8 0.0 0.083 TL 9.10 PV 1.0 Pipe: 43 28.2 1.650 PL 8.50 PF 0.2Pipe: 30 208.7 3.340 PL 10.10 PF 0.4Pipe: 17 25.9 1.850 PL 90.00 PF 2.8 23 2331 24.0 0.0 28.3 0.0 3.9 120 FTG - - -- PE 0.000.0 32.2 0.0 7.6 120 FTG - - -- PE 0.0 33 24.0 5.5 26.1 28.0 0.024 TL 8.60 PV 0.11423.0 0.0 35.8 0.0 3.9 120 FTG 32.00 PE 0.0 25 23.0 0.0 31.8 0.0 0.035 TL 10.10 PV 0.41523.0 0.0 33.0 0.0 0.023 TL 122.00 PV 0.1 Pipe: 31 224.8 3.340 PL 10.10 PF 0.4 Pipe: 44 -1.7 1.650 PL 10.00 PF 0.0Pipe: 18 128.9 3.340 PL 9.70 PF 0.1 33 24.0 5.5 26.1 28.0 0.3 120 FTG - - -- PE 0.02223.0 0.0 33.5 0.0 8.2 120 FTG - - -- PE 0.01523.0 0.0 33.0 0.0 4.5 120 FTG - - -- PE 0.0 24 23.0 0.0 33.1 0.0 0.041 TL 10.10 PV 0.5 34 24.0 5.5 28.1 28.0 0.000 TL 10.00 PV 0.0 17 23.0 0.0 32.9 0.0 0.014 TL 9.70 PV 0.1 Pipe: 45 -29.7 1.850 PL 10.00 PF 0.3 Pipe: 19 304,8 3.340 PL 9.70 PF 0.7 Pipe: 32 17.1 1.850 PL 90.00 PF 1.3 34 24.0 5.5 28.1 28.0 4.5 120 FTG - - -- PE 0.0 : 14 23.0 0.0 35.8 0.0 11.2 120 FTG - - -- PE 0.0 i 24 23.0 0.0 33.1 0.0 2.8 120 FTG 32.00 PE 0.0 3 35 24.0 5.5 26.4 9.8.1 0.030 TL 10.00 PV 0.1c2523.0 0.0 31.8 0.0 0.011 TL 122.00 PV 0.01e23.0 0.0 35.2 0.0 0.071 TL 9.70 PV 0.8 Pipe: 48 -57.8 1.850 PL 18.00 PF 3.5Pipe: 20 23.1 1.850 PL 90.00 PF 2.3 Pipe: 33 223.9 3.340 PL 10.50 PF 0.4 35 24.0 5.5 25.4 28.1 8.7 120 FTG 18.00 PE 0.42523.0 0.0 31.8 0,0 8.2 120 FTG - --- PE 0.0le23.0 0.0 35.2 0.0 3.5 120 FTG 32.00 PE 0.0 27 23.0 0.0 31.4 0.0 0.040 TL 10.50 PV 0.5 36 23.0 0.0 30.3 0.0 0.102 TL 34.00 PV 0.5172300.0 32.9 0.0 0.019 TL 122.00 PV 0.1 Pipe: 47 202.3 3.340 PL 9.00 PF 0.3 Pipe: 21 150.0 3.340 PL 10.40 PF 0.2 Pipe: 34 207.7 3.340 PL 10.50 PF 0.4 36 23.0 0.0 30.3 0.0 7.4 120 FTG - - -- PE 0.02423.0 0.0 33.1 O.0 7.8 120 FTG - - -- PE 0.01723.0 0.0 32.9 0.0 5.5 120 FTG - - -- PE 0.0 49 23.0 0.0 30.0 0.0 0.033 TL 9.00 PV 0.42823.0 0.0 32.7 0.0 0.035 TL 10.50 PV 0.41923.0 0.0 32.7 0.0 0.019 TL 10.40 PV 0.2 Pipe: 48 117.4 3.340 PL 9.50 PF 0.1Pipe: 35 17.5 1.850 PL 90.00 PF 1.4 30 23.0 0.0 32.2 0.0 4.3 120 FTG - - -- PE 0.0Pipe: 22 261.8 3.340 PL 10.40 PF 0.8 28 23.0 0.0 32.7 0.0 2.8 120 FTG 32.00 PE 0.0 37 23.0 0.0 32.1 0.0 0.012 TL 9.50 PV 0.11823.0 0.0 35.2 0.0 10.3 120 FTG - - -- PE 0.0 27 23.0 0.0 31.4 0.0 0.011 TL 122.00 PV 0.0 l1823.0 0.0 34.5 0.0 0.082 TL 10.40 PV 0.7 t Pipe: 49 67.0 1.650 PL 49.00 PF P.0Pipe: 36 241.4 3.340 PL 10.50 PF 0.5 ! 18 G 24.00 PE 0.4Pipe: 23 20.5 1.650 PL 90.00 PF 1.8 27 23.0 0.0 31.4 0.0 8.8 120 FTG - - -- PE 0.0 37 23.0 0.0 32.1 0.0 10.0 12C 23.0 0.0 34.5 0.0 3.1 120 FTG 32.00 PE 0.0 29 23.0 0.0 30.9 0.0 0.046 TL 10.50 PY 0.5 38 24.0 0.0 21.8 0.0 0.134 73.00 PV 0.7 FTG 19 23.0 0.0 32.7 0.0 0.015 TL 122.00 PV 0.1 Pipe: 50 25.3 1.087 PL 3.50 PF 1.4Pipe: 37 190.1 3.340 PL 10.50 PF 0.3 ` 38 24.0 0.0 21.8 0.0 8.7 120 FTG 5.00 PE 0.0Pipe: 24 170.5 3.340 PL 10.10 PF 0.2 26 23.0 0.0 32.7 0.0 7.0 120 FTG - - -- PE 0.0 39 24.0 5.8 20.4 25.3 0.189 TL 8.50 PV 0.51923.0 0.0 32.7 0.0 6.2 120 FTG - - -- PE 0.0 28 23.0 0.0 32.4 0.0 0.030 TL 10.50 PV 0.32123.0 0.0 32.4 0.0 0.024 TL 10,10 PV 0.3 lPipe: 51 25.2 1.087 PL 4.50 PF 1.6Pipe: 38 18.7 1.850 PL 90.00 PI 1.5 ! 38 24.0 0.0 21.8 0.0 8.7 120 FTG 5.00 PE 0.0 rPipe: 25 261. 6 3. 120 FT 10.10 PF 0.5 28 23.0 0.0 32.4 0.0 2.8 120 FTG 32.00 Pc: 0.01823.0 0.0 34.5 0.0 9.8 120 F1'G - - -- PE 0.0 r - 40 24.0 5.8 20.2 25.2 0.188 TL 9.50 PV 0.5 s2023.0 0.0 34.0 0,0 0.054 TL 10.10 PV 0.6 I l. 29 23.0 0.0 30.9 0.0 0.013 TL 122.00 PV 0.1 Pipe: 52 18.5 1.650 PL 9.50 PF 0.1 iPipe: 28 18.7 1.850 PL 80.00 PF 1.5 Pipe: 39 280.1 3.340 PL 10.50 ff 38 24.0 0.0 21.8 0.0 2.5 120 FTG - - -- PE 0.02923.0 0.0 30.9 0.0 9.5 12C FTG - - -- FIE 0.0 41 24.0 0.0 21.7 0.0 0.010 TL 9.50 PV 0.02023.0 0.0 34.0 0.0 2.8 120 FTG 32.00 PE 0.0 i .... 0.62123.0 0.0 32.4 0.0 36 23.0 0.0 303 00 0053 TL 1050 PV0.013 TL 122.00 PV 0.1 I a ate, ::rk?sr+ n :. ' .. .mac }i , , -. •; , -y 3 i i 'ia ., r t 1 a ,. ... . x .. .. .. .. fit, .i ..,.. r sY+'`K °£1.,- • :y ., _ e- - .- .w,E'• x srt .. .< ,,,, _ a ,. . . _ .•_..... dy• M. . .. ..r - .. +M ,.., ie. -... 4 „L Tw a,'.l- .. .. .: .i., , ,. ,: .. , ... .. : t llr .. , . ..s 1 [ _ .. Jam.. . ... ,. .. -r . -. :. ., .. .. V i o - i 5 i r . r Y: 1 - -.. .. , .,.. .. , ... ... -. - .. ,.'.. .. -' ,., ' ... :. , ., . , , r' f., y. r .1 i - ` i. , k>yOK•M ?M';' ifF ,. ':.. _ ;. : - ,... ..: J .. -. _ ..: , :• ... ... .r ._ .`..: .. ,.. - ,y,, ,p,,, ,z ,. x 7t'!'`'f.iii-J. +!.'"t31. 751 ".<..,r' :.'9#?t..w..- R',:iN K ^ >_ K .• .. ; .:;i r- .Y .; ,,., , . .. i =.• . ,..::.; S, =;f' 9.,±'r z- >' "r. ,fr'<£. 'c: >`<;?'r"i+'i r • "3srz": d T! c :M+e- .li':re iw a?F.R a; v. L r. v h rt. 3,'S Si a..,• I C` tqY P p }l LT90 r "n I I k_? r l, f j 4f, S I f SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 i JOB TITLE: LAKE CHEVROLET j PIPE DATA ( cont'd) PIPE TAG ELEV. NOZ. PT DISC. VEL(FPS)DHW(C)) LENGTH PRESS. H END SUM. NODES (FT) (K) (r81) (GPM) F.L. /FT (PSI) Pipe: 27 -68.0 1.850 PL 3.50 PF 1.6 27 12.0 0.0 11.7 0.0 10.2 120 FTG 8.00 PE 0.0 32 12.0 0.0 13.3 0.0 0.138 TL 11.50 PV 0.7 Pipe: 28 -18.6 1.087 PL 2.50 PF 0.8 28 12.0 5.6 8.8 16.6 5.6 120 FTG 5.00 PE 0.0 29 12.0 0.0 9.4 0.0 0.078 TL 7.50 PV 0.2 Pipe: 29 -16.6 1.087 PL 7.00 PF 0.5 29 12.0 0.0 9.4 0.0 5.8 120 FTG - - -- PE 0.0 31 12.0 0.0 9.9 0.0 0.078 TL 7.00 PV 0.2 Pipe: 30 -17.2 1.087 PL 1.00 PF 0.5 30 12.0 5.6 9.5 17.2 6.0 120 FTG 5.00 PE 0.0 31 12.0 0.0 9.9 0.0 0.083 TL 8.00 PV 0.2 Pipe: 31 -33.8 1.087 PL 6.50 PF 3.3 1 12.0 0.0 9.9 0.0 11.7 120 FTG 5.00 PE 0.0 32 12.0 0.0 13.3 0.0 0.290 TL 11.50 PV 0.9 Pipe: 32 -101.9 2.115 PL 1.00 PF 1.0 C) C) 32 12.0 0.0 13.3 0.0 9.3 120 FTG 10.00 PE 0.4 33 11.0 0.0 14.7 0.0 0.087 TL 11.00 PV 0.6 Pipe: 33 101.1 3.340 PL 10.10 PF 0.1 33 11.0 0.0 14.7 0.0 3.7 120 FTG - - -- PE 0.0 45 11.0 0.0 14.6 0.0 0.009 TL 10.10 PV 0.1 Pipe: 34 -15.2 1.087 PL 10.00 PF 0.7 34 12.0 5.5 7.7 15.2 5.3 120 FTG - - -- PE O.G 35 12.0 5.5 8.4 15.8 0.068 TL 10.00 PV 0.2 Pipe: 35 -31.0 1.087 PL 11.00 PF 2.7 35 12.0 5.5 8.4 15.8 i0.7 120 FTG - - -- PE 0.0 37 12.0 0.0 11.1 0.0 0.246 TL 11.00 PV 0.8 Pipe: 36 -18.0 1.087 PL 3.00 PF 0.7 36 12.0 e.0 10.4 18.0 6.2 120 FTG 5.00 PE 0.0 37 12.0 0.0 11.1 0.0 0.090 TL 8.00 PV 0.3 Pipe: 37 -49.0 1.650 PL 6.50 PF 0.5 37 12.0 0.0 11.1 0.0 7.4 120 FTG - PE 0.0 i 39 12.0 0.0 11.6 0.0 0.075 TL 6.50 PV 0.4 Pipe: 38 -18.4 1.087 PL 3.00 PF 0.8 38 12.0 5.6 10.8 18.4 6.4 120 FTG 5.00 PE 0.0 i 39 12.0 0.0 11.6 0.0 0.094 TL 8.00 PV 0.3 Pipe: 39 -67.5 1.650 PL 4.00 PF 1.6 39 12.0 0.0 11.6 0.0 10.1 120 FTG 8.00 PE 0.0 44 12.0 0.0 13.2 0.0 0.138 TL 12.00 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 JOB TITLE: LAKE CHEVROLET PIPE DATA (cont'd) PIPE TAG C1%3PM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) MW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 40 -16.6 1.087 PL 3.00 PF 0.4 40 12.0 5.6 8.8 18.6 5.7 120 FTG 2.00 PE 0.0 41 12.0 0.0 9.1 0.0 0.077 TL 5.00 PV 0.2 Pipe: 41 -16.6 1.087 PL 10.00 PF 0.8 41 12.0 0.0 9.1 0.0 5.7 120 FTG - - -- PE 0.0 43 12.0 0.0 9.9 0.0 0.077 TL 10.00 PV 0.2 Pipe: 42 -17.0 1.087 PL 3.00 PF 0.7 42 12.0 5.6 9.3 17.0 5.9 120 FTG 5.00 PE 0.0 43 12.0 0.0 9.9 0.0 0.081 TL 8.00 PV 0.2 Pipe: 43 -33.6 1.087 PL 6.50 PF 3.3 43 12.0 0.0 9.9 0.0 11.8 120 FTG 5.00 PE 0.0 44 12.0 0.0 13.2 0.0 0.288 TL 11.50 PV 0.9 Pipe: 44 -101.1 2.115 PL 1.00 PF 0.9 44 12.0 0.0 13.2 0.0 9.2 120 FTG 10.00 PE 0.4 45 11.0 0.0 14.6 0.0 0.086 TL 11.00 PV 0.8 NOTES: 1) Calculations were performed by the HASS 8.0.0 computer programll9878Z33grantedby MRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 2) The system has been balanced to provide an average imbalance at each node of 0.005 gpm and a maximum imbalance at any Bode of 0.119 gpm. 3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 12.3 ft /sec. JJ 1 , Y i t PF 1'j '.}'°' ^G S r ti ! •, t y f bi i p. rl '... ` C ay ."M•' sl!' i >.'Yd +f J i''S f i7 Ly r iL ca -! kF P ' p, f Y'Y` ! }>lZ f a• a t - z4yg f J 1 Q ti .f `ar y i S*' i i^,'' t( q. 2' 14j 1`k yy, p%` 1 •• xV. X. F V !> T .Z• ' 'f i} S ' ,ty °l 1..y ' " i y SKy W tiy " : 1 Y'n .may 1 j {..,. / ..Y G'^ tL•/ 1 a y!.1 F { : - f'Fa 1 •f x'C.F 7. / +.4-r -Q. ' Y t 1 I 4, > 1 ' 1 ti f 1/ ij } _ .t '. ! 4 ia4gy +t"!i•i'!L'V,M 9',.._}?Fj?M. y oW. h• :1wM•`h.3f'y,.!'f"'+ r* 6 / r h r F. l b3L. Y.F'r :.•: f f r. 1 f rdi*v s 1 f I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 f JOB TITLE: LAKE CHEVROLET PIPE FITTINGS TABLE 1, -)Pipe !Pipe Table Name: STANDARD.PIP Nominal Equivalent Fitting Lengths in Feet C =120) Diameter in) E T L C B G A D 1.00 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 1.25 3.00 8.00 2.00 7.00 6.00 1.00 10.00 10.00 1.50 4.00 8.00 2.00 9.00 8.00 1.00 10.00 10.00 2.00 5.00 10.00 3.00 11.00 5.00 1.00 10.00 10.00 2.50 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10.00 3.00 7.00 15.00 5.00 16.00 10.00 1.00 13.00 10.00 3.50 8.00 17.00 5.00 19.00 11.00 1.00 14.00 10.00 4.00 10.00 20.00 8.00 22.00 12.00 2.00 20.00 10.00 5.00 12.00 25.00 8.00 27.00 9.00 2.00 21.00 15.00 6.00 14.00 30.00 9.00 32.00 10.00 3.00 28.00 19.00 8.00 18.00 35.00 13.00 45.00 12.Ov 4.00 35.00 27.00 10.00 22.00 50.00 16.00 55.00 19.00 5.00 40.00 29.00 ii+ 12.00 27.00 80.00 18.00 65.00 21.90 8.00 49.00 35.00 A16.00 35.00 70.00 28.00 86.00 22.00 7.00 63.00 45.00 18.00 39.00 85.00 33.00 98.00 39.00 8.00 70.00 50.00% Fitting Code Letters: E =standard all Tatee L =long turn all Cacheck valve B= butterfly valve Gagats valve A =alarm check valve Dadry pipe valve Y i t PF 1'j '.}'°' ^G S r ti ! •, t y f bi i p. rl '... ` C ay ."M•' sl!' i >.'Yd +f J i''S f i7 Ly r iL ca -! kF P ' p, f Y'Y` ! }>lZ f a• a t - z4yg f J 1 Q ti .f `ar y i S*' i i^,'' t( q. 2' 14j 1`k yy, p%` 1 •• xV. X. F V !> T .Z• ' 'f i} S ' ,ty °l 1..y ' " i y SKy W tiy " : 1 Y'n .may 1 j {..,. / ..Y G'^ tL•/ 1 a y!.1 F { : - f'Fa 1 •f x'C.F 7. / +.4-r -Q. ' Y t 1 I 4, > 1 ' 1 ti f 1/ ij } _ .t '. ! 4 ia4gy +t"!i•i'!L'V,M 9',.._}?Fj?M. y oW. h• :1wM•`h.3f'y,.!'f"'+ r* 6 / r h r F. b3L. Y.F'r :.•: f f