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Lodi Chrome <br />Chrome plating tanks pumped out by PSC Company (Attachment A, Quotations). The <br />cost estimate to remove the liquid from the plating tanks is approximately $26,195. <br />Mr. Mason explained that the quotation did not include the cost of removing <br />contaminated debris or the tanks themselves. In addition, Mr. Mason provided me with <br />a cost estimate from Dockter Environmental Consulting to provide a closure plan, <br />sampling and closure documentation. The cost for these services was listed as $4,465. <br />I asked how Lodi Chrome plan to finance the cleanup since Mr. Mason's letter dated <br />August 30, 2006, indicated that Lodi Chrome was in extreme financial hardship and <br />could not fulfill the Department of Toxic Substances Control's (DTSC), Stipulation and <br />Order. Mr. Mason replied that he had some friends who were willing to help him with <br />the money in order to cleanup the facility. Mr. Mason informed me that he had been ill <br />which had prevented him from starting cleanup sooner. Mr. Mason explained that he <br />started some cleanup activities earlier today, January 10, 2007. According to Mr. <br />Mason, he and his friend, Mr. Rushin, had swept up buffing dust from the buffing room <br />floor and then placed the dust into a sack container. During the inspection, I observed <br />an unlabeled sack container that was open and that held a gray colored dust. Mr. <br />Mason identified the gray dust as buffing dust removed from the floor. I asked if the <br />dust was a hazardous waste. Mr. Mason said that he thought it was hazardous waste <br />due to metals but had not tested it. <br />Mr. Mason indicated that he wanted to clean up the facility and remove hazardous <br />waste from the plating tanks. Mr. Mason said that he would make arrangements to <br />have the plating tanks pumped out within the next week. However, when DTSC staff <br />returned to the site on January 18, 2007, the plating tank still contained plating liquids. <br />Inspection Rep <br />Mr. Mason showed me the plating area, which contains plating baths, cleaning baths, <br />rinse tanks, and a sludge storage tank. The size of tanks utilized in the plating area <br />ranged from 55 -gallon containers to large tanks greater than 500 gallons. I asked Mr. <br />Mason is he knew the concentrations of plating baths. Mr. Mason informed me that he <br />periodically had the plating baths tested. Mr. Mason provided me with analytical reports <br />for the bright acid copper tank, chromic acid tank, copper cyanide tank, bright nickel and <br />dry acid salts. (see Attachment B, Analytical Report) The analytical report indicates that <br />the plating baths contains, chrome, copper, nickel and zinc. <br />(See Photograph below) <br />3of11 <br />