Laserfiche WebLink
1 t <br /> Mr Kyle Christie Project 0905-114 04 <br /> December 6, 1995 <br /> Page 4 <br /> destruction efficiency, therefore, the was system was turned off The manufacturer is <br /> currently working to correct the problem Once the problem with the system is corrected, <br /> the unit will be restarted <br /> Percentage Uptime <br /> Due to a faulty hour meter, the operational time of the remediation system could not be <br /> accurately tracked However, based on the electricity used during the third quarter 1995, <br /> the system is estimated to have operated approxunateiy 40 percent of the time The low <br /> operational time Lan be attributed to the poor performance of the catalyst in the oxidizer <br /> Concentrations and Flow <br /> The average flow through the system was 92 cubic feet per minute (cfm) at an average <br /> applied vacuum of 25 inches of water column (see Table 4) Analytical reports and chain- <br /> of-custody documents are included in Appendix B Analytical results of influent and <br /> effluent samples collected on July 17, 1995, indicated that the system was not meeting the <br /> required destruction efficiency The manufacturer of the system was contacted to adjust the <br /> oxidation temperature in order to attain the required destruction efficiency Subsequently, <br /> the temperature was adjusted and a source test was conducted on August 10, 1995 The <br /> results of the source test indicated that the equipment was in compliance <br /> Influent and effluent air samples were also collected on August 29 and September 22, 1995 <br /> (see Table 3) Laboratory results indicate that the soil vapor concentrations have dropped <br /> from 11,000 milligrams per cubic meter (mg/m3) ui the second quarter to 4,600 rng/m3 <br /> Based on concentrations detected and an average flow rate of 92 Lfm, the amount of <br /> gasoline removed through the end of the third quarter 1995 is estimated to be <br /> approximately 16,748 pounds or 2,700 gallons <br /> The effect of the additional air sparge wells on dissolved phase hydrocarbon concentrations <br /> is not yet clear However, analytical results from the next quarter should demonstrate the <br /> effectiveness of the two additional air sparge wells <br /> Destruction Efficiency <br /> The remediation system has had an average TPHG destruction efficiency of 90 percent (see <br /> Table 4) This is lower than the permitted minimum required destruction efficiency of <br /> 95 percent But the system is in compliance with condition No 14, of the Permit to <br /> Operate, which states that the emission rate of volatile organic compounds to the <br /> atmosphere should not exceed 40 pounds per day The maximum errussions to the <br /> atmosphere during the third quarter has been 5 5 pounds per day Due to the low <br /> destruction efficiency, the system was shut off on October 6, 1995 The catalytic oxidizer <br /> SACW\PJCW8055080511404ES-951p s i <br />