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Project 00760.02 11 'February 1991 <br /> SYSTEM MONITORING- SUMMARY <br /> EVAX TECHNOLOG.IES, INC. <br /> ,Site: Beacon Station #502 Combustor'.-Start Up: 10/11/89 <br /> 35-,North 'therokee Lane " <br /> Lodi. -:California <br /> System Combustor' ' Combustor Combustor <br /> Phase Final.' Test.. Source- Test Source Test' <br /> Test Date :11/8%89 10/25%89 -. - 10/11/89 . <br /> EXTRACTIONTVH NPI, .TVH VP` TVH VP <br /> POINT <br /> VW-4 55. "C 54.0,E O_ 19,000 0 <br /> VW-6 50 , _ C 65- . . C 5,0.00 0 . <br /> VW-:7 550 %0. .50. .. C 11,000 0- <br /> VW-5 57' C . 100' C 21,000 0 <br /> MW-1 31475 0150 ` :0` - 23,000 0 <br /> VW-9 -2;800 0 6,000 °. O ._- 20,000 <br /> 0 <br /> Detection -__ -- -- <br /> Limit (PPm) 1 .b 1:0 1.0 <br /> Method TLV TLV TLV <br /> Hours of Operation _ 24 24 24 . <br /> Vacuum �11Hg) 3.5 1.7 ND <br /> Flowrate (scfm) - 58 - 63:5: 23 <br /> Influent TVH- (ppm) 2.,500 1,520: '22,500 <br /> Detection Limit --- ---(Ppm) _,50_ 50 50 50 <br /> Method TLV TLV3 TLV <br /> EXTRACTION POINTExtraction- probe/well:, identification as J ndi`cated on <br /> :site :plan: <br /> TVH -: Total volatile. hydrocarbons7.in parts :per million (ppm) on ,a. <br /> volume/volume basis: <br /> TLV Threshold Limit Values, meter detects .fcombustible gases- by <br /> oxidation using ,a hexane standard:?. <br /> li UP Manifold' valve osi',tion. 0=0 en <br /> P ( p ) (C=Closed) , <br /> Vacuum -. System vacuum in inches of Mercury. <br /> scfm -- Standard cubi-c feet per minute <br /> NO Not detected <br />