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<br /> f"4X TransmitteiMemo Ne, Of Faga: odoys at. I Tim•
<br /> a
<br /> rrom
<br /> Compq„y
<br /> fAX Ir Company
<br /> *action
<br /> Ca n m+n!$
<br /> SYSTEMS MONITORING DATA
<br /> Date: 3-ZS-`]¢ Location: �i s crct�a - ��L�,G-mac t-,yf�
<br /> Fief Technician:-j�/( ,
<br />�rr�rcSta}ion No: �f 5 4 , Job No-tgcas, O, Initial Sysferz Status: tC>own, System Type:
<br /> Tat_ Hrs: 7l�3• 7, H2O K/0- '70 - %; Full. Tr of Full Drums, Propane:
<br /> at: �� a.rt-t_� - current S Tored Pipe Size I.D.•
<br /> BEFORE ANY ADJUSTMENT: -�—
<br /> INITIAL Dilution Valve Position: open, c1 s or cracked Flow Meter: scfm
<br /> INITIAL Vac:- �4 " t-I� Q �,q " H— ,�y�' p' i--'y.., 2o, p: " H2O, Colc: scfm, Calc: scfm
<br /> he one dilut. after Gldilut. -rtr*wP,,`„�- Sefora ai ut. ct,ar , ut.
<br /> INITIAL: lnfi- pp,r, lnfl: ! O pm, Effl:- 70 -ppm, COZ Z. 5- ,ftg ;,qo, Motor Amps:
<br /> before difut_ 0�
<br /> Initial Recirculation: one-L Or
<br /> 7, 7777777
<br /> FINAL Dilution Valve Position: open, closed or cracked Flow Meter:
<br /> scfm
<br /> FINAL �'ac:�`?}.lg, bp. U,g!�- „ HZO, gyp: 4y/A- " H2fl, Calc: r ' `' scfm, Calc: r✓;.�}- scfm
<br /> �» after diiut. btie�ert'
<br /> FINAL- lnf1: m
<br /> . pp , Inf1: 1700 ppm, Effl:_7D ppm, CO2 2 �O �p�„p . Motor Amps-.—itu _
<br /> 9;, atter
<br /> before dilut. after dilut. �4
<br /> Final Recirculation:
<br /> 'Wet Pt• a-L :�, .�� -�a cl, �_rj. pal
<br /> Chamber Temp: 4 on , Exit Temp:� Motor Amp Rating:
<br /> STACK: Temperature: F, Magnehelic: 32 _ Calc: scfm, HO:
<br /> Field Instrument: 2
<br /> Last Monitoring: 7z3�SCF
<br /> ETc2
<br /> Manifold Box Number: Manifold Box Number:
<br /> Well r{ Vac. 42 CO2 ppm Valve Well —;�� Vac. 02 CO2 ppm Va ve`
<br /> 3 Vw-IA ?Z Z.7 /2O ° P-1 0 /g
<br /> fob' 011 /zoo
<br /> 7 V w-2A 1 -70 z.0 5'600
<br /> S'
<br /> VV,-z- 7Z 0 1 G000 P-� 7Z 7
<br /> ! w-3F•- f 79 70 C
<br /> VW 1A- 70 -71
<br /> 4 ,o 75p a f0
<br /> 4. v -7 /,)- 3 ZO pa
<br /> P-� -7
<br /> Mw- � Q•S (� � lid � P—� 7Z � b
<br /> �•4 w'3 7 S --0
<br /> 0
<br /> S7 6 -T0 °
<br /> -
<br /> A4,.j-s S O Z S
<br /> date Det. Date Det.
<br /> Benzene CH
<br /> influent Effluent Anal zed Limit Lob Factor Influent Effluent AnaE zed Limit Lab Factor
<br /> 4
<br /> TPHg .
<br /> CAH$
<br />
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