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IIIPF FLtdJ
<br /> PIPE DAtro F^F+ tLi,WELL 004 .062 ORIFICE
<br /> Nn ITi-M H1 'J4-1 tla1, F'trtipn4inn�.,
<br /> }t ppa nr C' it
<br /> 0 ENTPG4JI- I 3 (I.0R 0.2E, 0,=.20 I.AH DIN A.0 LNG
<br /> 1 PIPE IA"' 0.0A 0.28 0.U:4 1.00 DIA 1.0 LNG
<br /> 0.1+0 0.28 0.IQ? 1.RR DIA X 2.0 LNG
<br /> 3 FIEF 1<. 0.012 0.2'� N,024 1.R6 DIA 12A.0 LNG
<br /> 4 CiRIFI(E l.r." 9,48 19.29 1@1.b1R 0.R6 DI+ >. 0.0 LNG
<br /> 5 F>IT 1.RR0 5.78 I'�.29 0.0"0 R.I+r UIF, x A.0 LNG
<br /> 71-1fAL HEF,D 9.5A it. FLOW 0.,Z, r+5
<br /> FIIIF rHP1jll,,H 1'IPE 7.38 min.
<br /> STAGE DISCHAGE CURIE
<br /> POINT ELFtJ,aEICIN
<br /> HIGHF`:•T WATFP 7073.5
<br /> TOP OF INLET 7070
<br /> NUTLET ItVIFRT 7064
<br /> OUTFLOW CONTROL 7064
<br /> No Ft E'J c.7AGF. FLOW CCIFITROL
<br /> I 7,117H.IR R,10 0. 17 PIPE
<br /> 2 7,R70.'A 0. N A.I'll PIPF
<br /> 4 7,0 I'll.'„ n.'0 R.18 PIPE
<br /> 4 7,y70,411 0.40 0.10 FIPF
<br /> H.',1, 0.50 0.18 PI F•F.
<br /> ,•,1t j•1 ,t, A.6R 0.18 PIPF
<br /> .:•I A.70 0.16 PIPE
<br /> !•s 0,:i1; R,t;O 0.to PIFF
<br /> -(1 0.9A 0.19 PIPE
<br /> 10 ,R71.1+0 1.0R 0. 19 PIPE
<br /> 11 "%,�71. Ill 1. 10 1). 1+ PIPE
<br /> 1.20 0.19 PI FIE
<br /> 1.:?R 0,19 PIPE
<br /> 14 ,R;"1.4ti 1.4R 0.19 PIPE
<br /> 1.':a 1.50 0.17 F•IPF
<br /> 1 H.'1. .1, 1.M i,.19 PIPE
<br /> 1; J1, 1.70 R.20 PIPF.
<br /> 1sc ;',a,'•I,f?1t I,RO R.h PIt•r
<br /> 1a I."F1 I.wO N.;R PIPE
<br /> 214 7 G,i:.MA 2.011 0.20 PIPF-
<br /> 21 ,',R7<, Ili ?.10 0.2R PIPE
<br /> C:• 7,11; ••,'N 2.?0 R.2y PIPL
<br /> ',o .z(1, 2.31A 0.20 Pi PE
<br /> 24 ,11T2.40 2.40 11.7R PIPE
<br /> ,072.`...r•1 2.50 0.21 PIPE
<br /> 26 77,A72,60 2.60 0.?I PIPF
<br /> 27 7,0'. ./A 2.70 0.21 PIPE
<br /> .i. ., 2,k?U 0,21 PIPE
<br /> ,•,u "•,v,1 90 0.21 PIPE
<br /> 3.00 0.21 PIPE
<br /> 10 0.21 PIPE
<br /> 2 7,0.'i.c0 3.20 0.21 PIPE
<br /> 3-4 -,R'i.-:0 3.30 0.22 PIPE
<br /> :4 7,H7-1.40 '1.40 0.22 PIPE
<br /> 35 7,07-.50 3.50 0.2? PIPE
<br /> STATE D14CHAP6E CUPUE DATA FILE: B:M34-6,DAT
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