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Nuel Henderson [EH] <br /> From: Timothy Cuellar[tcuellar@advgeoenv.com] <br /> Sent: Tuesday, November 04, 2003 12:07 PM <br /> To: Nuel Henderson [EH] <br /> Subject: Top Filling Station <br /> Nuel, <br /> I would like to make a modification to the I.R. work plan for Top Filling, <br /> & wanted to run it through you first. Due to the significant TPH-g/BTEX <br /> numbers in ground water, the manufacturers have suggested that we will (at <br /> least initially) be going through a lot of carbon, and they have made a <br /> recommendation to me that we pretreat with air stripper prior to running <br /> hydrocarbon-impacted water through the carbon media. Based on hydrocarbon <br /> concentrations encountered last quarter, we could anticipate 50-60 pounds <br /> of carbon exhaust per day if we were to run pump-treat extracted water <br /> directly through carbon media (or approximately 130-160 days of usage <br /> before a complete change-out is necessary) ; keep in mind that each change <br /> out will cost $10, 000. So AGE anticipates spending 25-$30, 000 per year for <br /> carbon. <br /> The manufacturers have stated to me that with an air stripper, I should <br /> achieve 90% reduction in ground water concentrations (pretreatment) , which <br /> could reduce the carbon usage significantly to 5-6 pounds carbon exhaust <br /> per day, and extend the life of the carbon to approximately 1,300-1, 600 <br /> days of usage before a complete carbon change-out would be necessary <br /> (basically 3 1/2 - 4 years) . <br /> One other factor to consider is the'sensitivity of the City of Stockton <br /> permit to discharge into the sanitary sewer; I cannot have anything in the <br /> effluent. If there is any hydrocarbons detected, they shut me down and <br /> start issueing notice of violations (fines?) . Having the air stripper gives <br /> me an element of added controls, not to mention the fact the TBA is a real <br /> booger and likes to channel through some of these ground water pump-treat <br /> systems. The air stripper will significantly reduce the potential of TBA to <br /> channel through the media. <br /> An air stripper would have a 1-time cost of $5, 000; and operates off one, <br /> regenerative blower which would cost about $100.00/month in electricity. <br /> Additionally, I already have the controls for air emmisions with the cat <br /> alytic oxidizer on the site. I could simply plumb the outgoing water from <br /> the air stripper to the carbon media vessels; I could plumb the outgoing <br /> air emmissions from the air stripper and to the catalytic oxidizer. <br /> Thanks for your time and if this is acceptable, I will prepare a short <br /> letter for your approval that explains the modification to the system. - <br /> Tim <br /> 1 <br />