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l � � <br /> a- of pages Today s DWo ur+• r <br /> FAX TransrnittCl Memo <br /> O From 1 <br /> Car*+peny <br /> 'ram—party I <br /> FAX f cwtors i <br /> carnments <br /> SYSTEMS MONITORING DATA y� � <br /> Date: 8 31 , Loc ��, crcr.- - r'"�` ,Field Technician: R�- <br />;ar.-2Stction No `+i g { , .fob No Q�/Q, Initial System Status Up Down, System Type Ji��"r <br /> Tot. Hrs:lo-715.5 , H O K/0•_ 0. 7. Full, 4 __ rTr of--'Pull Drums, Propane <br /> at. 01 : 30 �i /p m. current s:crea Pipe Size LID " <br /> BEFORE ANY ADJUSTMENT: <br /> INITIAL Dilution Valve Posi;ion: a enlose or crecked , Flow Meter- scfm <br /> INITIAL Vcc (01 "N�s Op 0. 5 ,. H20, ap '� t' H20, Ccic scfm, Ccic scfm <br /> tore abut after di iut Tc<hi.— erare auut c 'sCUM <br /> INlT1AL. Infl parr, Inrl.`'��y ppm. El f[ PPM, CC Z 0 5 �Q���, Motor Amps- <br /> — <br /> INITIAL. <br /> driut <br /> wA) 3Fj ]nrtic! Recirculation a r <br /> FINAL Dilution Valve Fosition. °oen, closed or cracked . Flow Meter sczrn I <br /> FINAL Vac: (o I " f-i� dp 0.5 " HZO, Ap H 0, Ccic scfr-:, Cc1c scfm <br /> I�Zi? bpra- r 1lut. c.ter etiut 3s�ore aiiut C-77-Ful <br /> FINAL: Int! pprr, ln`I ''�1 (o ppm. Effl'}�oPm, COz�_,°' 0�� ��', Mc{or Ames• <br /> Wore dtlut. � y1. 30 (•rnrl C.Crrcu c1hon �'+ • I A <br /> a 105o f <br /> O <br /> Set Pt Choriber Temp- 3"F_-, Exit Tema �aly _� ,Motor A;-ro Pcti.�g: <br /> TACK Ternperc;ure: 'F, Mcgnehelic Ccic scfm, H., T <br /> Field Instrument: L cst Mart-cring a$S T=2 30 1Z3 CcF <br /> Manifold Box Number <br /> Mani-Iola Box Number <br /> � "f'� 17 <br /> Well VQC. oZ I C0� I pprn Valve Well -� Vac 0Z I CO2 Ppm �Vel�ve <br /> VVj-1{� I �S tq 5 1 10 l Io BI I Z. 1 100 120 <br /> V,,,,-,r; -71 Z I l o b Zoo k P-z l 78 I Z I k 00 k tS k <br /> V w -ZA 1 -1 Z 10 t o to 1350 o p-: I -7 I Z 1 10 1 <br /> V 0 (a k ZS a o o l t o I <br /> 180 I Z ti I Z I 1 � I � - r I -7 G l -Z <br /> 3 91 1 Zl Io 5 Z- t l o l l 1Ll <br /> vw- 1, -78 1 1B 11 S k G �-7 11 L 1 1 0 1 1 C <br /> vw -moi -I I Zo l 0 -3 5 P-9 I Z I o 1 1 <br /> 7 y Z I l a Li C ft P'� I Z k Z-I I 0 1 14 G <br /> Z- 1 I o 5 1 11 C- <br /> -70 <br /> - <br /> -70 L I I o y 1 $ I <br /> ��• - � -7� 2 t loo °! <br /> �•-5 `70 7- 1 10 Z l to <br /> Dc`e Det Dcfe Det <br /> Influent Effluent Ancly_edUrnttlLib rector InfluentIEffluent Anelyzed Lsrit Lab Factari <br /> Benzene CH <br /> TPHg C3H8 t I 4 <br /> r.., ='A ,? is ' aj Wt rt Ji4vi 1n�P 0Z <br />