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PIPE FLC441
<br /> PIPF DATta 1„R t1A'x WELL 00'3 9PILLW,4, .14 OF<IFIfE
<br /> No ITHI k+ H1 /el Man DtmFnston=
<br /> t t +ps or C' f t
<br /> 0 F1.I1Pf.NC I.639 0,04 1.26 0.t•10 1.00 DIA X 0.0 LNG
<br /> 1 PIP[. u.V17 O.R0 1.26 0.0?4 1.00 DIA 1.0 LNG
<br /> 2 ELPv" 1.256 0.03 1.26 0.11i4 1.00 DIA X 2.0 LNG
<br /> 3 PIPF. I..7:3Q 0.32 1.76 0.024 1.00 cliA K 1?0.0 LNG
<br /> 4 t.-iF;I910E. 1„'2q' 6.58 16.12 0.A10 0.14 DIA x 0.0 LNG
<br /> 5 Ell[ I Otul 4.04 16.12 0.000 0.14 DIA X 0.0 LNG
<br /> TUT AL HEAD 7.00 ft FLOW 0.59 rfs
<br /> TIME THRulJCH PIPE 1.62 min.
<br /> STAGE UISCHAGE CURVE
<br /> PnitiT ELEVATION
<br /> Hl',HFSI H1,TEk 7115
<br /> Tt_,P uF INLET 711t
<br /> O(ITt FT ItP;1'S+T ?IAA
<br /> OLITfLCW COWP,iL 'J08
<br /> No F11,1 THGE Fl,%q Gi1Pll RnL
<br /> 1 7,111. 1a 0.10 0.30 WE1P
<br /> 7,111.:A 0.20 0.E•6 PIPE
<br /> 7,111.40 0.3a 0,67 PIPE
<br /> 4 ?,l11.JN a.40 f,.t8 PIPE'
<br /> :, 7, 111.`i 0.50 O.b9 PIPE
<br /> 7,111.A14 0.60 0.',a P1rlF
<br /> 7, II).;7t1 0.7e 0.71 PIPF.
<br /> 7,111.st, a,RN 0.72 PIPF:
<br /> 7, Itt,90 N,9a 0.7 3 PJPF
<br /> I a 7,11_.0t+ 1.00 0.74 PIPF
<br /> 11 ',11..1a 1. it) 0.75 PIPF
<br /> 12 7. 11_.2N 1.20 N.:'6 PIPF
<br /> 14 . 112.4ti 1.40 PIPE
<br /> 15 r,11: I,r, I.50 Ef.,'� PIPE
<br /> 1� 112'.m I. A a.SO PIPF
<br /> !' 7, 1t. .'rN.fI PIPF
<br /> 1:i 7,I I .act 1.80 0.81 PIPF
<br /> l9 7,I I?.'-ti 1.516 0.112 PIPE
<br /> 21i ',113.00 2.00 U.H3 PIPE
<br /> L1 7, 11 In 2.10 0.84 PIPE
<br /> [. 7,113.20 2.20 O.E,'J PIPE
<br /> 7,113.3N 2,30 0.R6 PIPE
<br /> 24 ?,1 ''.JN 2.46 8.a7 PIPE
<br /> 25 l,tf�.C.N 2.50 a.P7 PIPE
<br /> l6 7,113.11+0 2.60 0.103 PIPE
<br /> 7.113.7Q 7...70 0. ^> PIPE
<br /> 211 7,11;.r)b 2.80 0.Q0 PIPE
<br /> [? 7,11< 9tj 7.90 $3 r1 PIPE
<br /> 30 7.114.(it) 3.00 0,91 PIPE
<br /> 31 114. i0 3.IO 0.92 PIPF
<br /> 114._t, 3.20 0.93 PIPE
<br /> 3i 114,cO 3.30 A.94 PIPE
<br /> 34 7,114.4t, 3.40 0.94 PiPL
<br /> 3F "7,114.50 3.50 0.95 PIPE
<br /> +� 14, .N j.r,0 it.1,6 PIPF
<br /> ', 114,70 3.76 0.97 PIPE
<br /> d8 7,114.f0 3.80 F4,97 PIPE
<br /> 7,114.40 3.40 0.9g PIPF
<br /> 40 7, 115.00 4.00 0.0;� PIPE
<br /> ST"GE DISCHAkGE iUR�)E DATA FILE: Ft:MS3-7.GAT
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