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4 <br /> SYSTEMS MONITORING DATA <br /> 140 Date /'�l "tion: kA,10 WJQ r /?4.ek Field Technician J <br /> JobNo 36- 16Y , Initial ystem Status- U own Tot Hrs <br /> Knockout H20 drum . 96 full Drum Storage #of foil drums <br /> MAWOLD STATUS: <br /> INITIAL Manifold Dilution Vane Position open, clos "rk FINAL Position Qpen, clo <br /> WELLS ONLINE <br /> INITIAL Manifold Vac " H2O FINAL Manifold Vac=- H7O <br /> I INITIAL Flow @ Rtot ep_ s,XS' " HO, Calc Veloc QOes:,#pm, Calc Flow cfm <br /> FINAL Flow @ Pitot op •4-T' " H2O, Calc VelocZtO66 fpm, Calc Flow scfm <br /> (Flow = Veloci x 0 049 x O 91 <br /> Manifold PID OD O ppm <br /> NOTES <br /> TOX STATUS: <br /> INITIAL Auto Dilution Valve Position open. closed. r FINAL Position n. closedr I <br /> INITIAL Line Vac " H2O FI ane Vac H2O <br /> INITIAL Flow @ meter cfm FINAL Flow @ meter t cfm <br /> TE Intl , Chamber l yS1_ <br /> PID lrWWqW , Effluent {stack}_ /= <br /> ppm <br /> NOTES If It 1 t. I <br /> S F <br /> !r�j l�1VW1r Yes $b"�C{( kl ' OvrY 'AOT'2E*VW2 b Yes <br /> VW3 M Yes <br /> VW4 j4q Yes 6 <br /> VW5 106000 Yes V ('tvv ulsf-W't' <br /> VW$ StU Yes L'y'D Nt: <br /> Manifold 1.000 Yes <br /> Influent ,CW Ye No E ltJ �r't C <br /> Effluent no No <br /> I <br />` NOJES- <br /> Gas meter reading 9.1 <br /> Electric meter rea S <br /> Filter condition I IMagnehelic `�' H2O} <br /> OwU <br /> Chart condition I <br /> Maintenance conducted <br /> C - <br /> fMW*&.odm 002 <br />