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<br />e <br /> <br />e <br /> <br />PROCESS DESCRIPTION: <br /> <br />The facility will use air to strip the MCB from the contaminated ground- <br />water and spent caustic. The air laden with MCB will be charged to the <br />thermal oxidizer. The air will compromise part of the combustion air <br />for the thermal oxidizer. <br /> <br />V. <br /> <br />PLANT DRAINAGE IMPROVEMENT <br />Project No. W-16I <br /> <br />PURPOSE: <br /> <br />Corrosive and organic process waste will be kept segregated from storm- <br />water. <br /> <br />PROCESS DESCRIPTION: <br /> <br />Trenches, ditches and sumps containing corrosive and/or organic chemi- <br />cals will be pumped to the processing plant's process waste streams, <br />which are then transferred to the wastewater treatment facilities. The <br />remaining stormwater will be discharged in outfalls 002 and 003 after an <br />initial flush period. <br /> <br />FREEPORT FACILITIES <br /> <br />1. <br /> <br />COP COOLING WATER TOWER <br />Project No. W-150 <br /> <br />PURPOSE: <br /> <br />Remove possible contamination of the cooling water out falls from the <br />A-18 and A-24 Blocks by replacing the once-through seawater cooling <br />system with a closed-loop cooling tower system. <br /> <br />PROCESS DESCRIPTION: <br /> <br />The proposed system would consist of one or more cooling towers of <br />sufficient size to furnish noncontact cooling water to the production <br />plants in the A-18 and A-24 Blocks. Water from the tower(s) would be <br />pumped to heat exchangers in the various processes where the cooled <br />water would absorb process heat. The warm water would then return to <br /> <br />A-3 <br />