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FAX Transrnitta! memo Ho. or PC odor's are ,,,,+ <br /> 0 <br /> r rom <br /> Core,�cny <br /> Company <br /> Fes( f <br /> Location <br /> Comm+nts <br /> SYSTEMS MONITORING DATA y <br /> Date: r� F 3 Location: .S; r_le ro - F't- _`"� Field Technician: Z� <br />;=:r-;,r4 Station No,• 4, 1 q , Job No--Lt"C-o'f <br /> �, initial System Status: own, System Type: e¢% <br /> Tot. Hrs:�_, H2O K/0: % Full, m of Full Drums, Propane: <br /> at: c_rn./p.m. Curren store <br /> Pipe Size I.D.• ' <br /> BEFORE ANY A©JUSTMENT: <br /> INITIAL Dilution Volvo Position: o e losed or cracked , Flow Meter: scfm <br /> INITIAL Vac: " Hg, ©p. ' H2O �P• " HZO, Calc: scfm, Ca c,-'-3y «+scfri�s) <br /> before diluf. After dilut. TAKr+p._ Sefore as ut. 6711 er + u <br /> t. <br /> INITIAL: Inti- ppm, Infl: i7Lo Rprn, Effl• oa ppm, CO2 ,H2O ��, Motor Amps: <br /> before diiut_ after dila .F <br /> Initial Recirculation: <br /> -; Z77 - <br /> FINAL Dilution Valve _Position: e , closed or cracked Flow Meter: scfm <br /> FINAL Vac: " Hg, Ap: " H2O, AP: " H2O, Calc: scfm, Calc: scfm <br /> before Flut. after dilut. be ore ai rut. atter <br /> FINAL: Infl: p m, lnflrl Qac <br /> Ppm, Effl: ppm, CO2 t z0 7., Motor Amps: <br /> before dilut offer dilut. � ' <br /> R F-,h Final Recirculction: <br /> Set Pt: �, �n�, a� fl 3S� �Q-, �A7 <br /> Chamber 'temp: Exit Temp: ,Motor Amp Roting: <br /> STACK: Temperature: �F, Magnehelic: Coic: scfm, H' 0: <br /> Field Instrument: 2 <br /> _ Last Monitoring: �� S N`•t�T�2 <br /> ' StF <br /> Manifold Box Number: Manifold Box Number-: <br /> WeII m VaC. 02 CO2 ppm valve` Wel! , 2 2 Ppm Va Ivo <br /> Vac. 0 Cp � - <br /> VW-1A <br /> V w-aA <br /> C_ <br /> _ vw- Yh c- <br /> �� <br /> h w:2- <br /> Date Det. Date <br /> Det. <br /> Influent Effluent Anal zed Limit Lob Factor Influent Effluent Ana! zed Limit Lob Factor <br /> 7;TPHg <br /> � <br /> C3H$ <br /> — r^4�IsvR.t~�EaTS T4 wtTrt <br />