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- now- <br /> Wn <br /> 4 <br /> A <br /> 10 June 1991 <br /> Project F114.01 <br /> SYSTEM MONITORING SUMMARY <br /> EVAX TECHNOLOGIES, INC. <br /> Site: Exxon Station RS #7-1050 <br /> System Start Up: 3/8/91 <br /> 909 Test Hammer Lane <br /> Stockton, California <br /> Incinerator <br /> System Incinerator Incinerator 91 <br /> Test Date 6/5/91 5/21/91 4/25/ <br /> EXTRACTION <br /> VP TV8 VP TVH <br /> TVH <br /> POINT <br /> 56 C <br /> VP-1 12 110 0 64 C 48 <br /> VP-2 120 0 6� <br /> VP-3 120 0 100 0 68 a <br /> VP-4 -- 0 100 0 76 Q <br /> VP-5 130 0 100 0 82 (' r <br /> VP-6 100 C 940 0 1,100 b <br /> MW-3 760 0 160 0 160 0 2zb 0 <br /> MW-4 --- <br /> Detection1.0 1.0 1.0 <br /> Limit {ppm} TLV TLV TAY <br /> Method <br /> EXTRACTION POINT - Extraction Probe/well identt Hca' `a,.; is indicated or <br /> site plan. <br /> TVH - Total volatile <br /> ha <br /> hydrocarbons in parts per nilliot� �pPm) on a <br /> volume/volume <br /> TLV - Threshold Limit Values meter detects comblG+,lIs1� Qases by <br /> oxidation using a hexane standard. i <br /> VP - Manifold valve position. (O=Ope ) (C=Cl ='' ia <br /> a <br /> - 2 ` <br />