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FAX 7ransmitfic1 Memo No, or PagesToday's ai■ im•
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<br /> Gamperty Company
<br /> • FAX � acct ort
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<br /> SYSTEMS MONITORING DATA
<br /> Date: 'z9 �.,�-2 y5 f
<br /> Location: S;� c�ct��+ - Field Technician- A-11 _
<br />-�,r:r-;r{Station No: 'f 1 `f , ,lobNom/D, Initial System Status: Down, System Type: C47/rxr
<br /> Tot. Hrs; Q :7-7 , H2O K/Q: ZO q; Pull, � of Full Drums, Propane:
<br /> at: l? -0:2 a.m./ Curren Stored ..
<br /> � Pipe Size I.D.-
<br /> BEFORE ANY ADJUSTMENT:
<br /> INITIAL Dilution Valve Position: o
<br /> INITIAL Vac--$3 en las or cracked , Flow Mater: scfm
<br /> '" "
<br /> �, �p: Q H2O, gyp; " H2O, Cafc: S" - scfm, Calc: scfm
<br /> A .�ore dilut. after diiut. Ta-nP, a b i re oiiuf- ct;er ut.
<br /> INITIAL: Infl• Ppm, Infi: /ooa ppm, Eff1:_ 00 ppm, CO2 S o ,H2O , Motor Amps:
<br /> before dilut, at#oar dile
<br /> — -I
<br /> W 026/Qcv— �W +'
<br /> 3S fni�ial Recirculation:
<br /> FINAL Dilution Valve Position: open, closed or cracked , Flow Meter: scfm
<br /> FINAL Vac: $_ " Hg, Ap- 0'!9a " H2O, AP: " H2O, Ccic: ?ti's-- scfm, Caic: scfm
<br /> before COO. after dilut, before afiut. after di u .
<br /> FINAL: lnfl: ppn^, lnfl: 1300 ppm, Effl: Ido ppm, CO2 s0 I.8 ,P10 i9.r 9;, Motor Amps:
<br /> before dilut, after c'ilu#.
<br /> �Prr ; { r. - Final Recirculcfion: r, o r ciD s p
<br /> Set Pt- - Cry' C �-•-cr -.�� � 1:� - .� zc. -r.•-�.;h
<br /> Chamber Temp:_ lfla0 Exit Ternp: 5 , Motor Amp Rating:
<br /> .STACK: Temperature: 'F, Magnehelic: " Cafc: scfm, H 0:
<br /> Field Instrument: r Monitoring:. Lost Moni�orin9: raA.S' V-►i=TG2 Z703-Zr:;; SAF
<br /> Manifold Box Number: ,M�, Manifold Box Number:
<br /> $?J'T-A�
<br /> Well Tar' � Vac. 02 CO2 i ppm Valve Well fi l Vac. 02 CO2 ppm Valve
<br /> f Vw-IA � oz- v �� o P-I � b8 � 209 � fz c
<br /> Z ZO. 0 700 96
<br /> 7 VLJ-2A .J 19.2, Z-0 400024;0
<br /> V%I/ 90 20. 1 0 . 2- 5vQ 4C-0 0 0 �d S 20. 9 f 4 , t- c
<br /> z
<br /> S 20. 9 0
<br /> 3 YvJ- 39 Zo.Sa.l
<br /> 4 vw- Yk 94 ro,s -Z 120 V o
<br /> P--� $4 za• 9 � a IS
<br /> -�P> 70 zv.. 1 1 v• z gs P-'S
<br /> rfw- 1 q9z za v � 1z ° P-� � �3 zo-9 0 is-
<br /> 4
<br /> Mw-y 90 2v, 3 o iS o
<br /> Cc
<br /> 100 zo. $ 0 5-
<br /> Date
<br /> Dale Det. Date Det.
<br /> Influent Effluent Analyzed Limit Lab Factor Influent Effluent Analyzed,Limit Lob Factor
<br /> Benzene CH
<br /> TPHg C11 3HB I
<br /> 1 ^Sv2�.•i6.t"CS t fk�Lka W J-1 rt ILv i i a,J A lZ
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