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FAX Trarnsmiffal Memp Fie of t'ag.a �oaay': atr ,n. <br /> G I I <br /> tram <br /> Carrsperry 1 <br /> `AX Carnpeny <br /> Lor_-tan I <br /> GcmmmSs I <br /> _ I I <br /> I <br /> SYSTEMS MONITORING DATA <br /> Date: 34-k'S Location: S; c1c> o� - r'Z^•�, �r <br /> Feld Technician•, �_ RL (. <br /> ,zm-w2Station No 44 g 'f , Job Nofa Initial Sysfem Status Up/Down, System Type �r tA+d <br /> Tot. a . H70 K/O: O % Full, _ , 0 -11of Full Drurns, Propane: <br /> t+ 1 r <br /> --% 45—� a-n •/p.m. Curren s,orea <br /> Pipe Size I D • r <br /> BEFORE ANY ADJUSTMENT: <br /> INITIAL Dilution Valve Posaion: o en close or cracked Flow Meter: scfrn i <br /> INITIAL Vac. �, { _" HS, nLp. &­� J# HQp . $ " HBO, Ccic scfm, Calc scfm i <br /> Ware d,iut. after d1lut 7'<onA. etofs're auut. et;ar C�ut_ <br /> INITIAL: InfI- ppm, Infl:w/`S pm, E f f I7��Pprn, CC2 1.8 _,H2O % Motor Amps• <br /> before diluf. W (L.{ -y4 LL Z <br /> 3b c . \ -3 <br /> FINAL Dilution Valve Position: oxen, closed or crcck_d Flow Meter scfm <br /> FINAL Vac: -7 Z " Hg, ,Qp " H2O, Qp , q " H2O, Calc scfm, Calc scfm <br /> h afire dilut atter d1luf. be.ore eilut. aver dou . <br /> FINAL- Infl- r' ppn-, Infl•2, o ppm, Effl `'' 35 pprn, CO2�_(e __ l O i,, Mator Amos 3arncts <br /> be�ore dtEut. 6 0 �Z - <br /> 0 ��� <br /> Set Pt: , Chcmber Temp: EXIT Temp ,Motor Amp Rating-- <br /> STACK: Temperature: �F, Mogriehelic Calc scfm, H2O <br /> ' <br /> Field Instrument: Last Monitoring (SAS &ICT`2 <br /> Scr= <br /> Manifold Box Number: Manifold Box Number. <br /> �NIl1 <br /> Well _=1 Vac. OZ CO2 PPM Vae Wel( m� Vac OZ 1CO2 pp„n Val � <br /> 31 Vw-IA 11.,5 �.4 `d I ° P-I I S. o 10. 0 I 11 <br /> vw-13 11. 0 I X0. 5 q5 p-Z 18. 0 la. o t4 Io i <br /> Vw-aA f 1) 0 lo .(. I z&5 0.0 I (0 o <br /> * vUl_i.g 11. 0 o. 3 1 55 o P-� 8. o a.c� L $ �° I <br /> V 1.i-3k 11. 5 o. 5 $ o P-r 8.o D• 3 -I o <br /> 13. 0 1 (o <br /> ISO <br /> a. <br /> Wy <br /> p.aw-3 Ic.. a Io. a q O I I I P <br /> F►N W �o I <br /> 14 I'd S. 00 3 $ UA X05 1PP's` 1 f <br /> :f� <br /> Date Det -7Y to Det. <br /> Influent Effluent Anel zed Ltmtt Lab Factor Influent Effitsent Anal xedlLimit Lab lFc <br /> C 0 r, <br /> Benzene CH4 <br /> T PHg C3F�$ <br /> —IA-I C X1.1 Wt i r ,� ��v 7, 3A At <br />