Laserfiche WebLink
FAX Transmittal Memo No. of pogem oday's ate Time <br /> Q <br /> From <br /> Company <br /> Company <br /> FAX <br /> Loc--tion <br /> COMM <br /> SYSTEMS MONITORING DATA <br /> �y� y " <br /> Date: (0-`3'9¢ Location: Si crc7'6-j �`*�`t Field Technician: <br />�rr.:.25tation No: !Y1 'f , Job NozL /d, Initial System Status:(12DDown, System Type:. C+7lun <br /> Tot. Hrs: !D•14 H O K/O: IO % Full, of Full Drums Propane: <br /> at: 1p : qp m, eurren s— oci <br /> •/P• Pipe Size 1.D.: <br /> BEFORE ANY ADJUSTMENT: <br /> INITIAL Dilution Valve Position:_ open, <12::;� or cracked , Flow Meter: scfm <br /> INITIAL Vac: 50 " Hg, Ap: 0-7 " H2O, gyp: " H2O, CCIc: scfm, Calc: scfm <br /> before dilut. after Out_ TtirhP, a ore ai ut. crTa' ilut. <br /> INITIAL: Infl: ppm, Inf1: ?490ppm, EffI: ppm, CC2 /-—3 ,N 0_,I--'7i3 %, Mator Amps: <br /> before dilut. after dila . <br /> Map 1,141 ZD b Initial Recirculation: qoa or- -closed <br /> FINAL Dilution Valve Position: open, closed or cracked , Flow Meter: scfm <br />,l FINAL Vac: 53 " Hg, Ap: 0.6 " H2O, n p: " H2O, Calc: scfm, Calc: scfm <br /> before diiut. after dilut. be or'i a d5uut. az ter di 7M. <br /> I.70 FINAL: Inf1: ppm, Inf1: 4) 2 Ppm, Effl: (TD Dpm' CO2/-0 ___,?1 0 _%, Motor Amps: <br /> before dilut. a er ��i,ut. <br /> .0p /rho 'V�0 Final RecWculction: open or -C-tosed <br /> Set Pt: Chamber Temp:- X00 , Exit Temp: O ,Motor Amp Rating: <br /> *Field <br /> STACK: Temperature: 'F, Mognehelic: " Calc: scfm, H2O:Instrument: Last Monitoring: SAS ►^-rCTE.2 Z977 / e SC,F <br /> Manifold Box Number: ,N , Manifold Box Number: <br /> Well ,�� Vac. 02 CO2 I ppm Vale Well 4, Vac. ( 02. CO2 ppm Va 'e` <br /> VWIA4 9' i•s �1 20 -( in !p <br /> vim,_► 1 7 1 . 1 . -3 .400 ° 0 e-z i '-1 t o <br /> vw--2,A 1 78r9' 7 I 45 21 0 .D �-3 k �� 20. 1 �b <br /> L�.l_213 O 1 Z0•Z f O - re 3c�U 0 D P-� I r 20.9 I -7 - G <br /> V w-SA 1 Z0,5– d.Z I za �� c P- S ZO•' D Z�e- " c <br /> V J- 39 q0 zo. 0 Ls G c �rc 4 zo `i' I v 50 6 <br /> vw- YA 11 . 4.0 70 35 c <br /> Vw -y t 5 <br /> r ("- 90 20. q v 9 <br /> r"iw-'L 70. 3 (9. 9- 15 G c 1 <br /> A�Iw-3 7& <br /> 90 <br /> Mw-5" 9-7 <br /> Date Det. Oafe Det_ <br /> Influent Effluent Anal zed Limit Lob Factor Influent Effluent Analyzed Lirnit Lob Factor <br /> Benzene CH <br /> TPH9 C3HB <br /> ,'fC -- rEh.tv�E•-EaTt T'•4Gc'r.! WlTrl ,9 �viOrl i� � ". . <br />