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F:X TrQns4sitfei Memo Na. of Foges today's at. ,m• <br /> 0 <br /> From <br /> Gu rr�p any <br /> jr <br /> Company <br /> taecnan <br /> Canrnsnl= i <br /> i <br /> SYSTEMS MONITORING DATA <br /> Daae: -zZ -94 Location. Field Technician: lrJro/L <br /> -LrcStation No: 'y `3 '(, .lob No: 19ap� ip Initial Sysfen Status: �t7own, System Type: C't-%/ar <br /> Tot. Hrs: Zt 4 , H C K/C: Q % Full, # or Full Drums, Propane: <br /> at: 07 : fIp.m. current stared pipe Size I.D.- '• <br /> BEFORE ANY ADJUSTMENT: <br /> INITIAL Dilution Valve Position: ooen clos or cracked Flow Mater: scfm <br /> INITIAL Vac: S5 7' Hg. Qp: O•(o 91HZO, , Qp; " H2O, Ccic: scfm, Cola: scfm <br /> before CHUt, after dilut. 77,*-hA, erore auut• erten GiTu`t. <br /> INITIAL: Inf1: pprn, Infl:i+ e pm, Efrl:rv� d- pp�tt, C C2i•O ,H2O�za_o %as Motor Amps: <br /> before dilut. after dila . <br /> 4/0 ga -Lyb5,0 Initial Recirculation: 65M nr .crnr{ <br /> FINAL Dilution Vcr[ve PositiOn: open, closed or cracked , Flow Meter: scfm <br /> FINAL Vac: 64 " Hg, QP: 0.6 " HBO, ,gyp: " h20, Calc: scfrn, Calc: scfm <br /> before tiiuf, after dilut. berore arrest, arrer di u . <br /> FINAL: InfI:r pprr, Inf1: Ci S` ppm, Eff1:4d 40ppr;r, CO2 i, S— �g�0-If-R .i,, Motor Amps: <br /> before dilut, after dllut. <br /> A)10 2000 F'/D .90 Final Recirc�,Ietion: -n orf <br /> Set Pt: Chamber Tem Co60 - <br /> p: Exit Temp: &Z ,Motor Amp Rating: <br /> TACK: Te-rkpera;ure: 'F, Magn_l,elic: "�� Calc: scfn, HZ0: T <br /> Field Instrurnent: Last Monitoring: ��S Y-��Tc2 Zgo ZB S{F <br /> Manifold Box Number: Manifold Box Number: <br /> Well r Vac. O2 CO2 I ppm I Valve Well „'� Vac. 02 CO2 I ppm Va(�va <br /> Vw-IA i 1?/ I r9.z II Zloo <br /> 7120 I O S zC7 ° P-Z I S' z�•S I o I / S" <br /> V+'i-,2 A <br /> lvuj- 99Izv t I z•a 3soo a P-�r I g� �.y I o I 9 <br /> T.OM t 1 .(� I ! c P- 8'sm- zo.`� I za <br /> 3� I s o. v 20 � C q4 I zU.� <br /> v e..1- YrF I i Z,7 3, 0 I ¢'- 7 I S 3 Z0-'7 I o 13 0 C <br /> v,:, 70 20..0 /- 0 S O zo. 9 I o 3 O <br /> Zo.9 I p ( I[� t'Z G I 94 <br /> 7Y C5 I I <br /> M LI/-S 94- Z0.1 <br /> )Cie Det. Dofe Det. <br /> Influent Effluent Ancr zed Limit Lob Factor Influent I Effluent Ancl zed Limit Lela Factor <br /> Benzene I CHS <br /> TPHg I C3P8� I ! I <br /> l <br />