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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />operation; (3) the Bypass Drain from Morelos Dam to the Slough to <br />dispose of reject stream from the Desalting Plant and other bypassed <br />water; (4) concrete lining of the first 49 miles of the Coachella Canal <br />in California to conserve water and, therefore, replace bypassed WMIDD <br />drainage flows during an interim period while the Desalting Plant was <br />under construction and prior to any required reductions in Colorado <br />River water deliveries to water users within the State of California; <br />and (5) a well field in Arizona known as the Protective and Regulatory <br />Pumping Unit (PRPU), which recovers ground water and combines it with <br />irrigation drainage flow to annually deliver up to 140,000 af of water <br />at the Southerly International Boundary with Mexico. <br /> <br />YUMA DESALTING PLANT <br /> <br />Location <br /> <br />The Desalting Plant, a central feature of the works authorized by <br />Title I, is located on a 60-acre tract of land 6 miles west of Yuma, <br />Arizona. <br /> <br />Sizing and Performance <br /> <br />Public Law 93-320 authorized construction of a desalting plant with a <br />129 million-gallon per day (Mgaljd) capacity. However, a 19772 sizing <br />study recommended construction of a 96 Mgaljd desalting plant with the <br />"operational characteristics for a reverse osmosis desalting process <br />'" calJable of recovering 70 percent of the plant feed water." Using <br />the criteria establishe~ in the 1977 study, contracts specifying a total <br />treatment capacity of about 96 Mgaljd were awarded to two manufacturers <br />of reverse osmosis desalting equipment. <br /> <br />However, by 1979, the WMIDD irrigation drainage reduction program was <br />proving so successful that irrigation drainage was projected to be <br />eventually reduced to 108,000 af per year. As a result, the required <br />capacity of the Desalting Plant was further reduced to 72.4 Mgaljd, and <br />a new plan was developed based on the premise of staged desalting plant <br />construction. That is, the 96 Mgal/d design was completed, but specific <br />increments of capacity (solids contact reactors (SCRs), filters, and <br />associated equipment) in construction were deleted. This approach was <br />less costly than redesigning the Desalting Plant. <br /> <br />Desalting Process <br /> <br />The Desalting Plant is divided into two distinct systems: (1) the <br />partial lime softening pretreatment system; and (2) the reverse osmosis <br />desalting system. <br /> <br />2 Colorado River Basin Salinity Control Project, Title I Division, <br />Desalting Complex Unit, Sizing Study, Yuma Desalting Plant, Arizona, <br />Interim Report, June 1977, Lower Colorado Region, Bureau of Reclamation. <br /> <br />5 <br />