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. a i • Page 1 of 2 <br /> Mike Infurna [EH] <br /> From: Matt Hanko[hanko@geoconinc.com] <br /> Sent: Wednesday, December 03, 2003 5:32 PM <br /> To: Mike Infurna [EH] <br /> Subject: Ranch Market <br /> Mike: <br /> RE: Ranch Market, 23569 South Santa Fe Road, Riverbank, CA <br /> I have attached two documents to assist you in following the discussion presented below. Attachment, Table 3 <br /> from 3Q-03 presents SVE performance data from when we surged the system and the O&M Tables depict the <br /> most current data for the SVE system performance. <br /> An SVE system and ozone sparge system are currently operated at the site. The SVE skid consists of a 300 <br /> scfm blower and knockout pot and uses GAC as the abatement media. The former SVE system consisted of a <br /> 500 scfm blower and used CAT/OX as the abatement media. <br /> As depicted in the attached Table 3 from 3Q-03, in April 2003 the SVE performance was poor with low vacuum <br /> and flow rates and low contaminant concentrations. We shut down the system in May for 18 days. The data in <br /> Table 3 Surge Performance demonstrates that contaminant concentrations did not rebound and supported the <br /> use of Granular Activated Carbon (GAG) as the abatement method. The surge performance and system switch <br /> were all discussed in our Second/Third Quarter report dated July 2003. The switch from CAT/OX to GAC was <br /> made in June 2003. <br /> Upon startup of the 300 scfm with GAC system in June 2003, greater vacuum and higher flow rates <br /> were achieved (refer to Table 3 of the O&M Tables)than those attained from the previous SVE system. As a <br /> result of the increased vacuum significantly higher contaminant influent concentrations were achieved. The <br /> contaminant concentrations in vapor well V-3 increased most notably than any other well (refer to Table 6 of the <br /> O&M tables)and the flow rate also increased most significantly. In fact, vapor well V-3 was the only well that <br /> exhibited a reversal in the decreasing contaminant trend (based on PID field readings- refer to Table 6 of the <br /> O&M Tables). No analytical data exists for individual vapor wells. <br /> The approximate O&M costs for the 500 scfm blower with CAT/OX was$5,600 per month. Currently the GAC is <br /> requiring change out every month at a cost of$6,100. The total O&M costs for the 300 scfm GAG system is <br /> approximately$8,300 per month. <br /> Geocon is proposing to mobilize a 300 scfm CAT/OX unit to the site to replace the 300 scfm GAC unit. The <br /> expected duration of operation for 300 scfm CAT/OX unit is unknown. However, Geocon proposes to extract from <br /> vapor wells V-3, V-5, and V-6 only for two months with the 300 scfm CAT/OX unit. The objective would be to <br /> reduce the mass load within the influence of those wells quickly and reduce concentrations so that GAC can be <br /> used economically at the site. If the influent concentrations have not been reduced to target levels(noted <br /> below), the 300 scfm CAT/OX system will remain in use until target levels are achieved. <br /> In order to make the switch, the SJUAPCD will require that a new Authority to Construct Application be submitted <br /> and processed (14 days to process). The units will switch out easily, in that, each is mounted on a trailer and can <br /> be rolled in and rolled out. Our total cost to make the switch will be under$1,000. <br /> O&M Cost Comparison between systems: <br /> Former 500 scfm CAT/OX(natural gas fired) _$5,600 per month <br /> Current 300 scfm GAG (with 4,000 Ib GAC change every 1 month) _ $8,300 <br /> 300 scfm CAT/OX(electrically fired) $4,900 <br /> 300 scfm GAG (with 4,000 Ib GAC change out every 2 months) =4,650 <br /> 300 scfm GAG (with 4,000 Ib GAC change out every 3 months) _$3,950 <br /> 12/8/2003 <br />