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FAX Tronsmiffal Merno <br /> To Na, or Pages oday's ar. rrt• <br /> r rom <br /> ComFerty Cgmpany <br /> FAX occ7 on <br /> Comm*rtls <br /> SYSTEMS MONITORING DATA <br /> Location: s;� trc7's-+ - Field Technician- <br />�rr:rLStation No: 'Y9 "(, Job No-,Is�WQU, Initial System Status: J�/Down, System Type: Cor a0c <br /> Tot. Hrs: 7/07 .1 3 , H2O K/O: 805'0 % Full, 3•.� � of Full Drums, Propane: <br /> at: 0- 4( �1p.m. currenT' std' Pipe Size I.D.• •, <br /> BEFORE ANY ADJUSTMENT: <br /> INITIAL Dilution <br /> �l/alve Position:—open. IosecD or cracked , Flow Meter: scfrn <br /> INITIAL Vac: 45(2-7-' Hg, D . 8. " H 0, 2 scfm, Calc: scfm <br /> �yZv P' .5 2 p; „ H Q Calc• Z�Y <br /> before dilut. after dilut. T�rrtp,. a ore auut- cT•ar i ut. <br /> INITIAL: [nfl: ppm, Infl:a" pm, 1=ffl: iso ppm, CO2—LjE&,,H20e s% Motor Amps: <br /> before dilui. <br /> Initial Recirculation: <br /> FINAL Dilution Valve Position: open, closed �or cracked Flow Meter: scfm <br /> FINAL Vac: 046" " Hg, L1p: O.S " H2O, Qp: " H2O, Calc: scfm, CLIC: scfm <br /> before dllut. after cilut. before ai ut. arcer di u <br /> AFL <br /> ppm, Infl: i700 ppm, Eff I:IC'D opr , CO2 1,9t'o pi 0 % Motor Amps: <br /> before diiut. offer dilutes ' ' <br /> w1 �s _T:r lr�. ` 4/ S•C� Final Recirculction: An or r-In <br /> sed <br /> t czar-f�.rrro�S; <br /> Set P.: Chamb e r emp: -�, Exit Temp: !o% Z ,Motor Amp Rating: <br /> *STACK: Temperature: F, Magnehelic: Co IC: scfm, H 0: <br /> Field Instrument: P"/1) 2 z7� <br /> Last Monitoring: &S Y`'►c7G2. g LF- <br /> Manifold Box Number: Manifold Box Number: <br /> MIT,41,/�� ilJl'rA .14L <br /> WellT Vac. 02 1 CO2 ppm lValve Well -41 Vac. 02 COZ I ppm Valve <br /> i Vw-IA � E 19.0. 1 -2-v � 9O �° � P-1 7� zo.q p 7 L, <br /> vw-l13 jMr7zl zo.S- O 000 1, e-i 78 20.8 o <br /> Vw-2A 76 R. S' / 0 qs�t�. ° �?: gz zo, 0 7 c <br /> mow-�g 8& z0•s 0 Soo o P-y v a $ o IZ <br /> Z Vr -J-3Ar 7 1 14. /-0 /8 P- f 60 ZO.7 c <br /> 3 Yw- 33 8s- z0.7 v. / A 0 Z6.B p g <br /> S vw- 5'k $�. I r3•� Zj� E'-778 120.? I� C <br /> 4 74 Z-6-0 0. 3 /50 ;1: P-9 1630 20 O � <br /> Sv 20• 5 v 20.8 C7 G <br /> r-t w-z 77 8 .O /S G <br /> Mw-3 7Z Zo. 7 0, Z 27 <br /> ofw-� <br /> 77 W, g 0 i Z <br /> Date DetA Date Det. <br /> Influent Effluent Anal zed Limit Lob Factor Influent Effluent Analyzed Limit Lab Factor <br /> Benzene CH4 <br /> I <br /> TPHg C3H$ <br /> T04'C—e j WIT., 31av71 o,S A i/t— <br />