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FAX Transmittal Memo NO Of Pagss oday's ate I ern• I
<br /> 0
<br /> rrom I
<br /> Company !Camyany 1
<br /> FAX f 1 ot�,lan
<br /> •
<br /> Comments
<br /> I
<br /> SYSTEMS MONITORING DATA
<br /> Date: 31131-1S , Location S� arcr..� - F��C �F el� Technician: V RC•�
<br /> ,arr.-a-Station No `4g '( , Jab No 04��0� Initial System Status. Up/Down, System Type- c►°Rk>�
<br /> Tot. Hrs: Ito-1._3 , H2O K/0 O % Full, O J1 of Full Drums, Propane:
<br /> at: 13 :Socurrent s;orea „
<br /> a_rn./� Pipe Size I D
<br /> BEFORE ANY ADJUSTMENT:
<br /> INITIAL Dilution Valve Posrion:_coen, closed or cracked Flow Meter scfm
<br /> INITIAL Vac " Hg, !Ar'] " H20, gyp. " H2O, Calc scf rn, CCIC: scfm
<br /> be,are dilut after d,2ut 71f"A. cror_ auut e,--e�ut.
<br /> INITIAL. Infl pprr, Infl:c;t�r pm, Effl• ppm, CO2-,H2O7, Motor Amps:
<br /> before Q,Iert. dduf.
<br /> Initial Recirculation s mn" or clauLl
<br /> FINAL Dilution Valve Position. oven, close or cracked , Flow Mesar: scfrn
<br /> FINAL Vac. `1 3 " Hg, Ap ____ " H2O, Ap. 1 3 " H2O, Calc scfm, Calc- scfm
<br /> *halos a,]ut. erter chit C.ors cuz.t c 7 er 7uu
<br /> FINAL. Infl ppr, in fl: (oto ppm, Effl 0 cpm, COz ,�O i,, Mctcr Amps:
<br /> 6 e,t artar c�ifut C,1-GZ SCJ ...
<br /> Final Rec,rc�etion QP-- er cicsen
<br /> Set Pt: Chamber Ternp- Exit Temp , Motor A+mo Pc-,Ing:
<br /> STACK. Temperature: 'F, Mcgnehel,c Calc scfm, H2G-
<br /> Field Instrument: Last Moni,onng &i (Z-
<br /> Mani
<br /> Manifold Box Number Mcnlfold fox Number T�
<br /> Well 14_=� Vac. O2 C4� ppmValve Well „'� Vac D2 CO2 ppm � Vai�z
<br /> Vw-IA
<br /> ,
<br /> VC
<br /> V w-2-,i 7f I I
<br /> \/w-zri
<br /> vw-3A-
<br /> Rf- m--34 P►•r. 11
<br /> P1 I P-s 1 I I
<br /> Iq -oo
<br /> I 114 01 I
<br /> Mw
<br /> 1 1 1
<br /> Dcte Det Date De;.
<br /> Influent Effluent Anal .ed L,rnit Lab Factor I lInfluent Effluent�AnalYZedlL,rnitl Lab Facto
<br /> Benzene CH4 I 1
<br /> TPHg f C3H8L 1 I
<br /> , ' — f^CA. ,e?C— ., Tdt s Wim Zvi ] 1 1} ,�
<br />
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