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FAX Transrn[tfal Memo <br /> 0 Na. of Pages odaya oFr <br /> ram <br /> Company <br /> _ Company <br /> oeai an <br /> Comments <br /> SYSTEMS MONITORING DATA <br /> Dare: %? y Location: .�; crc r•� -�'�'��^� Field Technician: <br /> gr_r.rtStation No: 'l S 'f, Job No:e:Y.� Initial System Status: ow System Type: S'Q-i/cxc <br /> Tat_ Hrs: o a. H2O K/0: r- % Full, --- of Fu rums, Propane: <br /> at: Lz1Z 'a-m./p.m. Curren sore <br /> Pipe Size 1.D.• <br /> BEFORE ANY ADJUSTMENT: 1 <br /> INITIAL Dilution Valve Position: o en closed or cracked Flow Meter: scfm <br /> INITIAL Vac: " Hg, a " H2O, Calc: scfm, Calc: scfm <br /> p�before TirtH2O� after dilut. T4<,1P,. sore aiuf. a ler l Int. <br /> INITIAL: Infl• ppm, lnfl: pm, Effl: ppm, CO H O Motor <br /> before dilui. a{ter difu . 2 a 2 'a Amps: <br /> Initial Recirculation: <br /> FINAL Dilution Valve Position: open, closed or cracked , Flow Meter: <br /> scfm <br /> FINAL Vac: <-S" 39Hg, .gyp: �•� H2O AP: 2,� �{ p, Calc: scfm, Cafr. scfm <br /> before Out. offer difut_ be rore aZt. ar er I nu <br /> FINAL: Inff:��.r► pp+r„ Infl: ppm, Effl: _ppm, CO 17i,+ <br /> before Hut. after difuf_ p Z �So 0 —�, Motor Artlps: <br /> fid✓ Final Recirculation: p <br /> '��� <br /> Set Pt: -- Chamber Temp: Exit Temp: %-K Motor Amp Rating: <br /> STACK: Temperature: �F, Magnehelic: 11Calc: scfm, H2O: <br /> Field Instrument: Last Monitoring:` 64S' wr�Tc2 ,�( 7/ao>o <br /> ' SCF <br /> Manifold Box Number: Manifold Box Number: <br /> We!! 7r Vac. OZ j CO2 ppm Valve Well Trrl VaC. 02 CO2 i ppm Valve` <br /> Vw-IA <br /> 11w,►�3 I I P_z I <br /> Vw--2A I 3 <br /> vs„/_z g I P^-f ! <br /> 1r w-3Ar <br /> ! <br /> Date Det. Date Det. <br /> influent Effluent Anal zed Limit Lob Factor Influent Effluent Analyzed Limit Lab Factor <br /> Benzene CH¢ <br /> TPHg <br /> it C3118, <br /> "" W t x w i i ��.,] <br />