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� s <br /> CONTINUED CONDITIONS FOR N-1133-2-1 Page: 2 <br /> 8 - For the thermal oxidizer, the influent hydrocarbon vapor,concentration into the remediation equipment <br /> shall not exceed 5200 ppm as gasoline and 27952 ppm as methane. <br /> 9 - For the thermal oxidizer the effluent hydrocarbon'concentration shall not exceed 259 ppm as gasoline <br /> and 1392 ppm as methane. <br /> 10 - For the carbon adsorption unit, the influent hydrocarbon concentration into the remediation equipment <br /> shall no exceed 500 ppm as gasoline and 3356 pprn as methane. <br /> 11 - For the carbon adsorption unit the effluent hydrocarbon concentration shall not exceed 32 ppm as <br /> gasoline and 168 ppm as methane. <br /> 12 - NOx emissions shall be limited to 2.4 pounds per,day and 2 tons per,year. <br /> 13 - A weekly log of running time and fuel usage shall be kept and made available for District inspection <br /> upon request. <br /> 14 - The overall hvdrocarbon destruction efficiency shall not-be less than 90% at any time. <br /> 15 - The total rate of soil ventilation shall not exceed 250 cfm for the thermal oxidizer and 200 cfm for <br /> the carbon adsorption sytem. <br /> 1' 61 <br /> fYl - <br /> CL i <br /> IGII <br /> _41- <br /> �� �.-�•,�- =„-���� '�v�`�`ate.� <br />