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SAX Transmittal Memo No el Pages Today pato I irn•
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<br /> u r rota
<br /> Campany Gampany
<br /> FAX # ILocasfan
<br /> Gomm�nts E
<br /> SYSTEMS MONITORING DATA
<br /> Date y5 ?-(oLacclian. S%� crcr.-J - �"�"�� Field Technicscn-
<br />;arf.-2Stcfion No 4' `f , lob No !�05/0, Initial System StctusU®/Dawn, Sysfern Type
<br /> Tot. Hrs•Ia14t,.4T� H 0 K/0•_Q_ % Full, __L of Full Drur^s, Prapcne:
<br /> at- 0.1 :ac) B/p m currenr s:orea Pipe Size I D • "
<br /> BEFORE ANY ADJUSTMENT:
<br /> INITIAL Dilution VQlve Posrian: open, GE�a or -crccued Fio.v Meter- scf„1
<br /> INITIAL Vac (07 " H-G, n-p D -5 " HZO, p " HZO, Ccic scfm, Ccic- scfm
<br /> N 5 t er dsiut. T,�,„A•�,__ erore auut. r.7-a'c 1Wt
<br /> INITIAL. Infl porrr, Inf€-"! porn, Effl 1 Ppm, CC2- H70-Z—O7., Motor Amos:
<br /> before dilutqq'arn- t•-f 1
<br /> Wl o V0O ` }l o Initial Recsrcula`,on or clQsad
<br /> F€NAL. Dilution Valve Position eoen, close or cracker, Flow Meer- L scfm
<br /> FIN."-,L Vac: bO " +rs; nip O u] " H20, eLp " HZ0, Ccic sc.,-n, Calc scfm
<br /> p �arar_ ailu#. c:ter c,lut baio-e ciut c: e�c�iut
<br /> FINAL: Inf€: p In'I[--Ppn-, Eff[. PPm, CO2 O ,X20 r'�, Mctor Amps
<br /> belora duut. o: cr dilut
<br /> Fina[ Rec,rculGtion
<br /> Set Pt• J Chcrnber Eemp' S�1 g- �, Exi e ,
<br /> O _ �
<br /> T mo ta09 Y Motor Amc Pcii�ng-
<br /> TACK Tempercfure r, Magnenelic to , Ccic
<br /> Tela Instrumr;enr: L cst Mor-i,cring tT:-�.Z. -30Z.(6-(o-
<br /> Manifold
<br /> CtF
<br /> Mani f old Box Numb---r Mcnl f ola Box Nurnber l
<br /> twiT,�rL .JeT�I ,..�.
<br /> Well r� Vac. 02 C0� ( ppm Valve Well �;' Vac 02 1 CO2 I pom IVefve
<br /> vw-I�4 7 119 51 1. z 111 IA, P-1 1 -79 1 Z1 10. 1 1 I to
<br /> VW-10, 1 7 118.°1 10. 9 I Zlo I0 P-z 178 I Z1 10- 0
<br /> Vw-22A I `7Z 19.5 1 0 5 1 Z90 -: 1 -7b I ZI 1 0. 1 ci 1=�j
<br /> v,,�_�r� 50 1 Zo, 51 0. 5 1 Z Z.0 0 F-�t I -1 to I Z1 I O o l 8 1
<br /> 130 I Z4 51 0 3 1 -5 c - r 1 -7 (,D I zt l o I I I�
<br /> % I ( Ll 1 O c, I -1 to I Z 1 I 0. 1
<br /> 1-1 -7 (o 1 2 1 I a 1
<br /> Zo•5I o• Z I 7e I zl I 0- 1 i 5
<br /> rw- 1 1 -1 Ll I Z) 10 3 1 (a G1 P-5 1 -75 1 2 ! 1 0- 1 1 F3
<br /> -15 I Z) 10. 5 1 10 0 I I I
<br /> J&4 w-3 1 `10 7-1 1 0 3 16 -�� � 1 `� �s �•�1 f
<br /> -7- I Z 1 1 00
<br /> w-5 -t U Z1 Z
<br /> cto D2(7 Det
<br /> 0 Influent l Cffluenf Anclv_ec'ILimrfl Lcb (Factor l lnfluen°I EtfIt e,^t Ancl ::- Ur-•i;l Leb Fec=es,
<br /> Benzene 1 I I CH I I 1
<br /> TPHg 1 I I 03N8 I I I
<br /> s — t---CA,,�c _� �'-
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