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FAX Transrt�ittal �lerrmo No. of pogea Qday: at. ITIrno <br /> pram <br /> Company <br /> mpany <br /> Comment= octet ars <br /> SYSTEMS MONITORING DATA <br /> Date: Location: yg y <br /> Fief Technician: <br />;ccrt.-rtStatian <br /> No---±g—f 3 Jab No• 414S/e, Initial System Status: U own stern Type: C4i/c+r <br /> Tot. H O K/0: % Full, # of Full Drums, Propane: <br /> at: —L--24— /p-m. curren soreeo <br /> Pipe Size I.D.• " <br /> BEFORE ANY -.ADJUSTMENT: '�/�5�_ �'� 17a _ <br /> INITIAL Dilutior-tValves Position; o en closed o rccke Flow Mater: scfm <br /> INITIAL Vac: _" R dp: �� H20, AP: l,Z H2O, Ccic:" scfm, Calc: scfm <br /> j rd> before durst, efter dilut. T��rsp,` score as ut. a Tar ut <br /> INITIAL- Infl:`Ab <br /> before diiutPPm' lnflafta �d u pm, Eff1:l ppm,CD2---Z--,FSlo0 Z9s 7, Motor Amp": <br /> Initial Recirculation: or <br /> FINAL Dilution Valve Position: o en closed or cracked Flow Meter: ` <br /> FINAL Vac: _" scfm <br /> Hg, Op: O•�s •• }{ O, -- <br /> pH201 Calc: scfm, Carc: scfm <br /> FINAL: rnfl:•Zi7�o before dilut. . cfter dilut, be ore 1 ut. ricer r�u . <br /> PPn Infl: ppm, Effl:_ppm,C <br /> t t. <br /> 42 ,PILO / . , Motor Amps: <br /> before diluafter dilv <br /> Final Recirculation: opgrL or rinseri <br /> et Pf: `'�" <br /> Char„ber Temp: Exit Temp: ,Motor Amp Rating: <br /> STACK: Temperature: F, Magnehelic: Colc: scfm, H2O: <br /> Field Instrument: Last M'onitoring:� _ G�s y�-rcT�2 G7 <br /> ' 2 •�ws c� <br /> Manifold Bax Number: F _ Mani�ol�l Box Number-: <br /> Well r V cP 02 I CO2 I pplrrt Vale Well ;r� V cp C2 CD2Ppm Va1�ve <br /> Vw-LA 3 _ I <br /> ' ••• D � P a C- <br /> V k3-ZA <br /> r$ ep <br /> YvJ-3R7 Z AJ} oo. g p D d <br /> V w- Yfk A /Q.� ,� �rr, d o P-7 q <br /> . <br /> Date Det. Date Det. <br /> Influent Effluent AnaE zed Limit Lab lFacfor Influent' Effluent Analyzed Limit Lab Factor <br /> Benzene CH4 <br /> TPHg <br /> C3H� <br /> Alit— <br />