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' �) � -��`~ -&«\ �) BASIC FIRE PROTECTION, INC' - K 940 N.E. LOMBARD ST. PORTLAND, OR. 97211 , HYDRAULIC CALCULATIONS FOR TIGARD CENTER BUILDING C - SHELL TIGARD, OREGON FILE NUMBER: BORDERS' ^ DATE: 6-18-96 --;DESIGN DATA- ///// OCCUPANCY CLASSIFICATION: Ordinary Hazard II DENSITY: '20 AREA OF APPLICATION: 1500 Sq. Ft. COVERAGE PER SPRINKLER: 122'5 NUMBER OF SPRINKLERS CALCULATED: 14 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 357.3 gpm TOTAL WATER REQUIRED (including hose): 607'3 gpm FLOW PRESSURE (at base of riser): 357-3 gpm 83.0 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: BASIC FIRE PROTECTION, INC. DESIGN/LAYOUT BY: Ken Kern AUTHORITY HAVING JURISDICTION: City of Tigard HYDRAULIC CALC'S PERFORMED BY: Ken Kern • ` � SPRINKLER SYSTEM HYDRAULIC ANALYSIS 2ame 1 Date: 06/18/96 O0RDERS1 JOB TITLE: BORDER51 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. ^ • TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 49 116'0 108'0 1591.0 114'7 607'3 90'7 , , AGGREGATE FLOW ANALYSIS: . . TOTAL FLOW AT SOURCE 607'3 GPM ` TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0'0 GPM OTHER HOSE STREAM ALLOWANCES 250.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 357.3 GPM NODE ANALYSIS DATA ' NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) ( PSI ) (GPM) ^ 1 15.2 - - - - 31.6 - - - 2 18'7 K= 5.60 19.9 25.0 3 18.7 K= 5.60 19.2 24'6 4 18'7 K= 5.60 19.2 ^ 24.5 �� 5 18.7 K= 5.60 1 24.6 6 16.7 K= 5.60 19.9 25.0 7 15.2 - - - - 31.9 - - - 8 15.2 - - - - 32.0 - - - 9 18.7 K= 5.60 20'2 25.2 lO 18.7 K= 5.60 19.6 24.8 11 18.7 K= 5.60 19'5 24.7 12 18.7 K= 6.60 19.6 24'8 17J 18.7 K= 5.60 20.2 25'2 14 15.2 - - - - 32.0 - - - 15 15.2 - - - - 33.1 - - - 16 18.7 K= 5.60 23.9 27.4 17 18.7 K= 5.60 23.5 272 _19 18'7 K= 5.60 23.5 27.2 99 18'7 K= 5.60 23.9 27.4 19 15'2 - - - - 33.1 - - - `O 15 2 - - - - �5 2 - - - �_ ' . 21 15.2 - - - - 35'2 - - - 22 i5'2 - - - - 37.3 - - - "23 15'2 - - - - 37'3 - - - 24 15'2 - - - - 39.3 - - - 25 15.2 - - - - 39.3 - - - 26 15.2 - - - - 41.4 - - - ' ` 27 15'2 - - - - 41.4 - - - 28 15.2 - - - - 43.4 - - - 29 15.2 - - - - 43.4 - - - ^ 30 15'2 - - - - 45'5 - - - 31 15.2 - - - - 45.4 - - - 32 15.2 - - - - 47.6 - - - 33 15.2 - - - - 47.4 - - - • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 . JOB TITLE: BORDERS' NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 15.2 - - - - 49.7 - - - . .35 1 - - - - 49.3 - - - 36 15.2 -- - - - 52.1 - - - 37 15.2 - - - - 51.0 - - -- 38 15.2 - - -- - 64.7 -- - - 39 15.2 -- - - - 52.5 - - -- 40 15.2 - - - - 68.2 - - - 41 15.' -- _ _ 53.3 - - -- �'42 15 ..2 - - - - 72.9 - - - 4 3 15.2 - - - - 53.5 _ _ _- . BR 0.0 - - - - 83.0 - - - 4 6 0.0 - - - - 83.5 - - - 47 0.0 - - - - 89.5 - - - � 48 0.0 HOSE STREAM 89.5 250.0 49 0.0 SOURCE `a0.7 007.3 • • SPRINKLER SYSTEM HYDRAULIC ANALYSIS P.a.ge 3 JOB TITLE: BORDERS1 PIPE DATA PIPE TAG ((GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEI( FP6) HW( C) (FT) SUM. . NODES (FT) (K) (P8I) (GPM) F.L./FT (PSI) Pipe: 1 62.4 1.542 PL 46.50 PF 1.0.2 • • 1 15.2 0.0 31,6 0.0 1.0.7 120 FTG 2T 28 1,5 2 •F .9 25.0 (' I. -2 Pipe: 2 "37 1 1• , 54". "I.. 10.80 PF 0,7 2 18.7 5.6 1`a. 25,0 6 120 FTG - - - -- PE 0.0 •.J 3 18.7 5.6 19.2 2 24 6 0.063 TL 1.0 c.o 02 0.3 Pipe : 3 12.6 1 . 542 PI." 10.50 PF 0.1 .3 18.7 5.6 1.9.2 24.6 2.2 12.0 FTG ---- P8 0.0 4 18.7 5.6 19.2 24.5 0.009 TL 10.80 22 0.0 "5 4 2 3• 1 4 18.7 5.6 19.2 24.5 2.0 120 FTG ---- PE 0,0 - 8 18.7 5.6 19,2 24.6 0.007 TL_. 10..50 P2 0.0 Pipe: ` ; -36.2 L . 54? PL_ 10.50 PF 0.6 - 5 .1.,?,.-.7 S A I.• .2 24 .6 6 . 2 120 FTG ---- PE 0.0 18.7 5.6 19.9 25.0 0,060 TI.. 10.50 P2 0 . 3' i.F- -61.2 1.542 P1-. 46.80 PF 10.5 6 13.7 c 13- ._.,. 13... .L20 FTG 82T PE 1.5 7 15.2 0,0 31.9 0.0 0.188 TI.. 66, P2 0.7 Pipe: ,7 -62.4 2.227 P2 11,67 PF 0.3 1 15.2 0.0 31.6 0 ..) 5 . 1 120 FTG ---- PL=. 0.0 6 15.2 0. 0 32.0 0.0 0.027 TI... 11.67 P2 0.2 Pipe: 8 1. . 'i2 PL... 4• 0 PF 10..2 8 15.2 0.0 32.0 0.0 10.7 .1.20 FTG 2T PF 1.5 • : a 18.7 5 . - 20.2 . P . 0.163 1L. - 2 .. 50 PV 0.8 Pipe: "3 37.1 1,542 PL 10_50 PF 0.7 (.? 1%3 5.6 20.2 25.2 6.4 1.20 FTG -- -- PE 0.0 10 18.7 5.6 19.6 24.8 0.063 TI_ 1.0 ..'50 PV 0 P i.p 1.0 12.4 1,542 PI_. 1c PF 0.1 10 18_7 5.6 1.9.•6 24,8 2,1 120 (=TC, ---- PE 0.0 11 18.7 5,6 19.5 24.7 0.008 . . . . .1 . 0 . 8 0 ' P2 0.0 - 1.542 PI- 10.50 Pr: 0.1 11. 18.7 5.6 1.9.5 24.7 2.1 120 FTG ---- PF 0.0 12 18.7 5.6 19.6 24.8 0.008 TL. 10.50 P "..% 0,0 Pipe: 12 - 1.542 PL_. 10,50 PF 0.7 .12 18.7 5.6 19.6 24.8 6.4 .120 FTG ---- _ PE 0.0 13 18.7 5.6 20.2 28.2 0 .06 3 TL 10.50 PV 0,3 Pipe .13 - 62.3 1,542 PI-. 46.50 P;8 10.2 13 :18.7 5.6 20.2 25.2 10.7 1.20 FT;; _='T PE 1.5 14 15.2 0,0 32..0 0.0 0.163 TL 62.50 PV 0,6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 308 TITLE: BORDERS1 PIPE DATA (cont'd) PIPE TAG 0(GPM) DIA(T.N) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL( FP3) HW(C) (FT) SUM. - - NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI ) Pipe: 14 - 61.2 2.227 PL :3.79 PF 0.1 • • 7 15 , 2 0.0 31.9 0.0 5.0 120 FTG - - -- PE 0.0 14 15.2 0.0 32.0 0.0 0.025 TL 3.79 PV 0.2 Pipe: 15 -124.7 2.,227 PL. 11.67 PF 1.1 8 15.2 0.0 32.0 0.0 10.3 .120 FTG ---- . PF 0,0 15 15.2 0.0 33.1 0.0 0.098 TL 11.57 P0 0 . 7 Pipe: 15 53.7 1.542 PI-. 46.50 PF 7,7 15 15.2 0. 33,1 0.0 9.2 120 FTG 2T PF 1.5 15 18.7 5.6 23. 27.4 0,124 TL 62,50 20 0.6 Pipe 17 25.3 1.542 PL 1.0.50 PF 0.'3 16 18.7 5.6 23.9 27 .4 4.5 1.20 FTG ---- PE 0.0 - 17 18.7 5.5 23.5 27.2 0.033 TL 1.0.50 PV 0 . 1 F:' : 18 -0,9 1.542 PL .10.50 PF 0.0 - 17 18.7 5. 23,5 7 .2 0.1 120 FTG -- . -. -- __ PE 0.0 1.2 1 ' .6 2. - . c 27 . 2 (3 000 T 1 ._ 10 .. 50 PV 0 . 0 pi 1 --, '1 542 PI 10.50 PF 0.4 18 1.8.7 5.2 23 .5 27.2 4.a 120 FTG - - -- PE 0.0 ' 18.7 5.6 23.9 ._7 .4 0.037 TL 10,50 PV 0.2 Pipe: 20 -55.4 1.542 P1.. 46.50 PF 7.7 99 18.7 5.5 23,9 27.4 9.5 120 FTG ET PE 1.5 19 15.2 0.0 33.1 0.0 0.1.31 TL 58.50 PV 0.6 Pipe: 21 -123,5 2.227 PL.. .1.1_ .67 PF 1.1 1. 15.2 0.0 32.0 0.0 10.2 120 FTG - - - -- P1= 0.0 1.5..2 0.0 33.1 0.0 0.097 TL... 1.1..57 Pk/ 0.7 Pipe: 22 -178.4 2.227 PL 11.17 PF 2.1 15 15 0.0 7 . 1. 0.0 1.4 ... 120 FTC. - - - - -- 25 0.0 20 15.2 0.0 35.2 0.0 0.191. TL-. 11.1.7 PV I .5 Pipe: 23 0.,3 1..54: PL 135.00 PF 0.0 20 15.2 0,0 35 .2 0.0 0.0 120 FTG 4T PE 0.0 21. 15.2 0.0 35,2 0.0 0.000 TL 157.00 P0 0.0 • P i.p : ?,_i -178.9 2.227 PL_. 1 1 , 1 . % PF 2 . 1 1 ' " 1.5.2 0.0 33.1. 0.0 14.7 • 1.20 FTG - - - -- PE 0 ..0 21. 15.2 0.0 :35.2 0 .0 0.192 11 .... 1.1,1.7 2V 1 .5 P i. r : 25 - :1.78.6 2,227 PI-.. 10.67 PF 2.0 20 15.2 0.0 35.2 0.0 14,7 120 FTG ---- PE 0.0 00 15,2 0.0 37 3 0 0,191 TL.. 10.87 P0 l..5 Pipe: 28 0.0 1.542 PL 135.00 PF 0.0 22 15.2 0.0 37.3 0.0 0.0 120 FTG 4T PF 0.0 :3 15.2 0.0 37.3 0.0 0.000 TL 167.00 P0 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 • JOB TITLE: BORDERS1 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL( FPS) HW( c2) (FT) SUM. . , NODES (FT) (K) (PSI) (GPM) F.L. /FT (PSI) Pipe: 27 -17a.7 .227 PL 10.67 PF 2.0 . • 21 15.2 0.0 35.2 0.0 14.7 120 FTG - - - -- PE 0.0 23 15.2 0.0 37.3 0.0 0.191 TL 10.67 PV 1.5 Pipe: 28 -178.6 2.227 P1-. 10.67 PF 2.0 22 15.2 0.0 37.3 0.0 14.7 120 FTG - - -- PE 0.0 24 15.2 0.0 39.3 0.0 0.191 TL 10.67 PV 1.5 Pipe: 29 0.0 1.542 PL 135.00 PF 0.0 24 15.2 0.0 39.3 0.0 0 .0 120 FTG 41" PE 0.0 25 15.2 0.0 32.3 0.0 0.000 TL 167.00 PV 0.0 Pipe: :30 -1 2.227 PL 10 . PF 2.0 23 15.2 0.0 37.3 0.0 14.7 120 FTG - - -- PF 0.0 25 15.2 0.0 9.3 0.0 0.191 TL :1.0.67 PV 1.5 Pipe: 31 1. 7 8 . 7 2.227 PL 10.67 PF 2.0 ' 24 1.5.2 0.0 32.3 0.0 1.4.7 120 FTG - - - - -- PE 0.0 26 15.2 0.0 41..4 0.0 0.191 TL-. i0,67 `='.., 1.5 c., .. 0.2 _ 1.542 P1... 135.00 PF 0.0 26 15.2. 0.0 41.4 0.0 0.0 120 FTG 4T PE 0,0 27 15.2 0,0 4 1 . 4 0.0 0.000 TL 167.00 PV 0,0 Pipe: 33 -178. _ 2.227 PL 10.67 PF 2.0 25 15.2 0.0 39.3 0.0. 1.4 . - 1.20 FIG ° - - -- - 1-'1- 0.0 27 15.2 0.0 41.4 0.0 0.19:1 TL 10.67 PV 1.5 Pipe: 34 -1/'. 2.227 P1... 1.0 .67 PF 2.0 26 15.2' 0.0 4.1.4 0.0 14.7 120 FTG -- - - -- PE 0.0 28 15.2 0.0 43.4 0.0 0.191 TL 10.67 PV 1.5 P.i;.pe : :35 0 .. .L .. 542 Pt_ 1.35.00 PF 0.0 ? 3 1.5.2 0 . 0 43.4 0.0 0 . 1. 120 FT(i 4T P5 0 .0 29 15 .2 0 .0 43.4 •=4 (: 0.000 TL- 1. H 7 . 00 2V 0.0 Pipe: 36 -178.5 2..227 P1... 10.7 PF 2.0 27 15.2 0.0 4 1 . 4-4 0.0 14.7 120 FTc:, -- - - - - -- PE 0.0 9 15.2 0.0 43.4 0.0 0.191 TL_. 10..67 PV 1.5 Pipe: 37 -179.6 2.227 PL 1.0 .7 PF 2,1 28 15.2 0,0 43.4 0.0 14 i 120 FTG ---- - PF 0.0 30 15.2 0.0 45.5 0.0 0.193 TL 10.67 PV 1 . 5 Pipe: 38 2.0 1.542 PL 135.00 PF 0.0 30 15 ..2 0 , 0 45.5 0 .0 0 . 0 1.20 FTG 4T PF 0.0 31 15.2 0,0 45 ..4 0.0 0.000 TL .1.57.00 PV 0.0 Pipe: 39 - 177.7 2227 PL 1.0.67 PF 2.0 29 15.2 0.0 43.4 . 0.0 14.6 120 FTC, - - - - -- PE 0.0 31 1 5 .3 0.0 45.4 0.0 0.18 TL 10.57 PV 1.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page h .30B TITLE: BORDERS1 PIPE DATA (r_ont 'd ) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ . PT DISC. VEL( FPS) HW(C) (FT) SUM. . NODES (FT) (K) (PSI) (GPM) F.L./FT (Pr I ) Pipe: 40 -181.5 2.227 PL_ 10.67 PF ' . 1 . 30 15,2 0.0 45,5 0.0 15.0 120 FTG - - - -- PE 0.0 15.2 0.0 47.6 0.0 0.197 TL 1.0.67 PV 1.5 Pipe: 41 4.0 1.542 PL 135.00 PF 22 .15.2 0.0 47.6 0.0 0.7 120 FTC; 4T PE 0.0 33 15.2 0.0 47.4 0.0 0.001 TL... 167.00 PV 0.0 Pipe: 42 -175. 2.22 PL. 10.57 P1= 2.0 3:1. 15.2 0.0 45.4 0.0 14.5 120 FTG - - -- PE 0.0 33 15.2 0.0 47.4 0 ,0 0.185 TL 10,67 PV 1.4 Pipe: 40 - 195 2.227 P1.... 10.67 PF 2.2 :3 := 15.2 0.0 47.6 0.0 15.:3 120 FTG - - - - -- PE 0.0 .34 15.2 0.0 49.7 0.0 0.205 TI.... 10,67 PV 1.6 Pipe: a4 6.9 1.542 P1... 17 PF 0,5 34 15,2 0.0 49.7 0.0 .I.. 2 120 FTG 4T PE 0.0 35 15.2 O 0 49.3 0.0 0.002 TL. 167,00 PV 0.0 P i - 1. 1. .. PI... 1. l',7 0E 1.." :3:3 .15.2 0.0 47.4 0.0 :14.1 120 FTC, ---- PE 0.0 35 15.2 0 .. 0 49.3 0,0 0, "17 9 TL 10.57 PV 1. Pip 46 -192.5 2.227 P1.. 10.57 PF 2.3 34 15,2 0.0 49.7 0 0 15.9 120 FTG -- -- PE 0.0 6 1.5.2 0.0 52.1 0..0 0,219 TL 10.67 PV 1.7 Pip.;-.: Cl: 1.0,7 1.542 PI.... 135,00 PF 1.1. 36 15.2 0.0 5 2 . 1. 0.0 1..5 120 FT'::, 4T P5 0.0 37 15..2 0.0 5:1..0 0.0 0..006 TI.. 167_00 PV 0.0 Pipe: 48 -154,8 2.227 P1._ 10.67 PF 1.8 35 15.2 0.0 4. 9 0 131: 120 F T G _- '- ..- .- PE 0.0 :37 1 5 0.0 51.0 0 .0 0.165 TL 10.67 PV [ _ _ P i. 49 -203.2 2 .227 21._ 42.17 OF 12.7 36 15.2 0.0 t _ . 1 0.0 :15. 1.2(3 FTG 25 PE 0.0 3 15.2 0.0 64.7 0.0 0..243 TL 52,17 PV L.. Pipe: 50 45.3 IL .542 PL .103.00 PF 12.2 :3:3 15,2 0.0 54.7 0.0 7 , 3 120 FTG 4T Pi-. 0.0 39 1S.7 52.5 0,0 0.09.1 TL.. 1.33.00 PV 0.4 Pipe: 51 -154.1 2 '727 PI._ 10.17 PF 1.5 37 15.2 0.0 51,0 0 , 0 1 : .7 120 FTG - - --- PE 0 .0 :39 15.2 0.,0 52.5 .. .0 0..145 2.... 10,17 PV 1.1 Pipe: 52 -248.6 .- .227 P1._ 9.67 Pi . 3 .4 38 15.2 0.0 64.7 0.0 20,5 120 FTG ---- PE 0.0 40 15.2 0.0 66.2 0.0 0.352 52 rL 9.67 PV 2.3 >PR ENI'.LE'=.' `;YSTEM HYDRAULIC ANALYSIS Page .JOB TITLE: BORDERS1 PIPE DATA (cont'd) PIPE TAG O(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC . V51.( FPS) HW(C) (FT) SUM. . NODES (FT) (K) (PS.I) (GPM) F.L./FT (PSI ) Pipe: : 5:3 50.4 1..542 PL 103.00 PF 14.2 - • 40 15.2 0.0 68,2 0.0 8.7 120 FIG G 4 i• PE 0.0 41 15.2 0 .0 53 0.0 0.110 T1... 1 5 .. 00 PV 0.5 Pipe: 54 -108.7 2.227 PL.. 2.67 RE 3 15.2 0.0 52.5 0.0 9.0 120 FTG -- - - - - PE 0.0 41 15. 0.0 53.3 0. 0 0,076 TL 9.67 P' 0.5 Pipe: 55 -299.0 2.227 PO 9,67 PF '1 . . 40 15.2 0.0 68.2 0.0 24.6 120 FTG - - - -- 25 0..0 42 15.2 0.0 72.9 0.0 0.496 TL 9,67 PV 4 . 1 Rip: S6 58.3 1.542 PL. 103.00 PF 19,5 42 15.2 0 .0 72.9 0,0 10.0 120 FTG 4T PE 0.0 - 4:3 15.2 0.0 53.5 0,0 0 ..144 TL. 135.00 PV 0.7 Pipe: 57 -58.3 2 .• 22 PL 9.67 PF 0.2 41. 1 0 , 0 53.3 0.0 4 .8 1.20 FTG - - - -- PE. 0.0 43 15.2 0.0 53,5 0.0 0,024 TL 9.67 PV 0.2 Pipe: 58 -357.3 3.352 ,1 20.00 PF 3.5 42 15 0.0 72 9 0.0 t .. .0 120 FTG 2513 PF_ 6.6 RR 0 .,0 0 ) .a .0 0 0 (1 c., 9,4 I.... 37.00 PV 1 . 1. Pipe :: 59 -357.3 6.:100 PL_ 65.00 PF 0.5 BR 0 .0 0.0 83.0 0.0 3.9 140 FTG 35 PF 0,0 46 0.0 0.0 93.5 0,0 0.004 TL.. 120.86 PV 0,1 1. Pipe: 60 5 ED PRE5502F LOSS DEVICE 47 0,0 0.0 2 . > 0.0 6.0 psi, 357.3 gpm 4 0.0 0.0 83,5 0. Pipe: 61 -357.3 8.270 PI... 10.00 PF 0.1 47 0.0 0.0 82,5 0 0 _..1 140 ETC', ET P1= 0,0 49 0.0 H.5. 89.5 250.0 0.001 'TI. 80,49 PV 0.0 _ • Pipe: 62 -607. 9.270 PO 475.00 PF 1. . 2 p 48 0.0 H.5 99.5 250.0 3.6 140 FTG -20 PE 0.0 49 0.0 52125 90.7 (WA) 0.00 :) Ti... 509.58 PV 0.1 ' NOTES: - t:J_ons were performed by the HASS 5. •,0 computer program under license no. R -27 grantee; to Basic Fire Prot. '440 N .5 . Lombard `:: `., t :. Portland, OR 97211 c (,) The system ;em ha been balanced to provide an average imbalance at each node of 0.002 ,;prn ::3nd a rna;Y'.;Warn imbalance at an; node of 0.068 gprn _ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 . . 308 TITLE: BORDERS1 (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 24.6 ft/sec. ° (4) e. System remote area HAS been proven or 'peaked'. b. Minimum pressure at any sprinkle/: 19'152 psi , . o. Minimum pressure with /emote area shifted • one sprinkler space toward left cross main: 1 poi d. Remote area is located adjacent to right cross main (5) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PlP PAGE: A MATERIAL: Steel HAC: 120 Diameter Equivalent Fitting Lengths in Feet (in) 8 Ell Tee LngEl ChkVi BfyVl 6atV1 AlmCk DPVlv ° ? SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 06/18/96 BORDERS1 JOB TITLE: BORDERS1 WATER SUPPLY CURVE . LiATEP SUPPLY A1'ALYSIS Static: 11,00 psi 5sid:109.00 psi Flaw: 191.0 gpm 10,0 LEGEND 1 1m Available pressure 11165 psi 607.3 gpm 100.0 Pe uir ed pressure .� 90.2 psi C� �U?13 ��p �a - w - czt2 Euj -/ z0.0� . 0,0 - -14,7 . . " " 400 b00 909 1990 1200 1400 100 1900 iu09 FLOW (gpm)