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<br />The installed capacity of the desalting plant will produce up to 72.4 million <br />gallons of product water per day. The plant will produce an average of about <br />67,000 acre-feet of product water per year at about 300 milligrams per liter. <br />This flow will be blended with raw drainage waterto develop a total of73,000 <br />acre-feet per year of blended water to be delivered to the Colorado River. <br /> <br />Through various irrigation efficiency improvements to save water, including <br />the neutron probe, infrared thennometer, laser leveling of fields, and flash <br />irrigation. the drainage flow was reduced from 167,000 to 108,000 acre-feet <br />annually. The desalting plant is designed and constructed so capacity can be <br />increased to 96 million gallons per day of product water, jf necessary. <br /> <br />Lime Softening Pretreatment <br /> <br />The major process flows are highlighted in the Yuma Desalting Plant <br />Process Diagram & Mass Balance (next page). Feedwater is first diverted <br />from the drainage canal and conveyed to grit sedimentation basins for <br />removal of settleable solids and biomass. <br /> <br />The Bureau of Reclamation found that lime softening best met the feedwater <br />pretreatment requirements, and a design incorporating mixing, flocculation, <br />and clarification in a single vessel was chosen. Nearly all the feedwater <br />pretreatment needs (i.e., bicarbonate removal, iron and manganese removal, <br />and suspended solids reduction) are accomplished in the single-unit process. <br />Each of the three l85-foot-diameter Solids Contact Reactors (SCR) is <br />expected to use approximately 100 tons of lime per day at a dosage of 200 <br />milligrams per liter, <br /> <br />The calcium carbonate sludge produced by the lime softening process will <br />be piped to specially prepared evaporation ponds for disposal. Under nonnal <br />operation, 360 tons of sludge will be generated per day, which will fill about <br />6 acres per year. <br /> <br />The next pretreatment step following the SCRs is the Dual Media Filters, <br />consisting of anthracite coal over sand, which provides the final clarification <br />step. Sulfuric acid is added before filtration, and sodium hexametaphosphate, <br />as a calcium carbomate sulfate precipitate inhibitor, is added after filtration. <br /> <br />Reverse Osmosis Desalting <br />The heart of the desalting plant is the reverse osmosis desalting equipment. <br />One group of membrane-equipped pressure vessels can produce 22.4 mil- <br />lion gallons of desalted water per day. The desalting membrane element (7 <br />per pressure vessel) are installed in 8-inch-diameter and 20-foot-long pres- <br />sure vessels and are arranged in control blocks with a capacity of 1.5 million <br />gallons per day. The 1.5 million-gallons-per-day control block consists of 48 <br />pressure vessels, The 15 control blocks then contain a total of 5,040 elements. <br /> <br />2 <br />