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FAX Trans,,ittal Mers�o He. of Pog•: odcy'x at. „r. <br /> 0 <br /> C <br /> r forn crnRc„y i <br /> FAX Ccmpony <br /> Comrss•n1s oearlan <br /> SYSTEMS MONITORING DATA y <br /> Dote: 4 93 , Location: Si crcr•a - '��•-1C-'� Feed Technician: <br /> 17 <br /> crx.-25tation IVQ. �f g of, Job No-/ Initial Systern Status: U own. S stem T CQ-r crc- <br /> Tot. Hr-s= HZO K/O: % Ful{, y- ype:,��_ <br /> rr of uI! rums, Propane: <br /> at: _ Q_m-/p.rn. tartan $wed Pipe Size 1.D. <br /> ANY ADJUSTMENT: y y�� � f <br /> FE3EE:FC)REE <br /> NITIAL Dilution Valve Position: o en closed or cracke�N{TIAL Vac- :7rs� " !{ Flow Meter: scfm <br /> 9' gyp' s, H2O �P: ter " H2O, Caic: r�si-r scfm, Calc: scfm <br /> INITIAL: (rig!-'-moi Tse be are dilut. flet dilut. hc.y p,.��- a ore atut. atter � ut_ <br /> PPS lnf1: ppm, Effl: •`Epprri, CO2--- 'H20`�7� Motor Amps: <br /> before dila#, after iluf. <br /> Initial Recirculation: <br /> FINAL Dilution Valve Position: open, closed or cracked , Flow Mefer: <br /> s c f rrs <br /> FINAL Vac: _ - <br /> Hg, ,Lp be ogre dile"H2O' AP' " H2O, Calc: scfm, Calc: scfm <br /> FINAL- "Infl: rr Infl: after dilut. berore itut. atter i _ <br /> PP ppm, Effi:� _ppm, CO2 ,KZO 7-, Motor Amps: <br /> before di[ut. oflar c�ilut. I <br /> Fina! IZecirc�ation: <br /> et Pt-- Chamber Temp: Exit Tem <br /> ' p: �Motor Amp Rating: <br /> *TACK: Tamperature. F, Magnehelic: Calc: scfm, H2Q; <br /> Field ! <br /> nst'rurrient: Last Monitoring:� <br /> ' tads' r"+ETc2 StF <br /> Manifold Box Number: Manifold Box Number: <br /> WeII Vac. 02 CO2 ppm Valve' Well mVac. 02 CO2 ppm Vatfve` <br /> Vw-IA �.- P-I <br /> V+"-113 i <br /> V LQ-2JA <br /> M- Y 7 <br /> ea <br /> Mw-� ' E <br /> Date Det. Date Det_ <br /> Influent Effluent Anal zed Limit Lob Factor 18 -- <br /> LT_P_H_�L <br /> fluent Effluent Analyzed Limit Lob Factor <br /> Benzene CH4 <br /> .................. G3H <br /> - '� — r--E+lSv2E-t�.aTS T"�4�Cc,•s Wi i rt .D �LvT� C,a �},I` _ �� <br />