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FAX Transrr�itfal Memo No. of Page, odor's ate Ime <br /> 0 <br /> From <br /> Car„geny Company <br /> FAJC Location <br /> Comments <br /> SYSTEMS MONITORING DATA <br /> Date: �Z /7 Location: Field Technician: G� <br />,.att--(L5tation Job No• Za& � Initial System Status: Up ow System Type: C4' Vv <br /> Tot- Hrs: pQ7¢ , H2O KIO: % Full, 'u of Full Drums, Propane: <br /> at: _f +�� �p,rn- curren stored <br /> --- <br /> Pipe Size LD.: <br /> FEBIEFORE ANY ADJUSTMENT: _ <br /> ilution Valve Position: o en closed or cracked Flow Meter: scfm <br /> ac: " H.G. Qp: " H2O,. dp: V4.20, Calc: scfm, Calc: scfm <br /> be oar d iut, after dilut. 7whA, sercre ariut. 67-Fe r , ut. <br /> INITIAL- Infl- ppm, Infl: pm, Effi: ppm, CO2_.H20_7*, Motor Amps: <br /> before diluf. after diiu . <br /> Initial Recirculation: <br /> FINAL Dilution Valve Position: open, closed or cracked , Flow Meter: scfm <br /> FINAL Vac: „ Hg, Qp= , „ H2O, Calc: scfm ' <br /> H2O Op: , Coic: scfm ; <br /> bee o�rn diiut. after diluf. be are 3ut. atter i u . <br /> FINAL- Infl: pprry Infl: ppm, Effl: ppm, CO2 ,Moo %, Motor Amps: t <br /> before ditut. after diiut. <br /> Final Recirculation: ! <br /> �et Pt: <br /> - , Chomber Temp: Exit Temp: ,Motor Amp Rating: <br /> } STACK: Temperature: eF, Magnehelic: Calc: scfm, H'20: <br /> Field Instrument: Last Monitoring: t_)C_rt.2 SCF <br /> Manifold Box Number: Manifold Box Number-: <br /> Wel! Vc�c. OZ CO2 ppm Valve We{l , � Vac. 02 CO2 ppm � Val�ve` <br /> Vw-IAS P-I <br /> Vw-l13 p_Z <br /> V 1.x.3-2A P-3 <br /> V%,I-Z P-y <br /> V V'.,t-3A- ! r <br /> vw-3.9 _ P <br /> v ? k <br /> t'Iw- y <br /> &I La <br /> Date Det. Date Det_ <br /> Influent Effluent Analyzed Limit Lob Factor Influent Effluent Analyzed Limit Lob T-—CC}or <br /> Benzene CH4 <br /> TPHg <br /> C3H8 <br /> — A^.EJE�v2E—ii<.+T1 T14Ccr+1 W i K ,D ILvT, DJ A i/L <br />