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<br />p'" :. ~ l ~l <br />t.' l.~ ". u :It . <br /> <br />salinity levels of the component flows would be monitored daily <br />and adjustments made accordingly. <br /> <br />Most of the excess Wellton-Mohawk drainage would need to be <br />bypassed along with the salt brine to the Santa Clara Slough. <br />The Wellton-Mohawk return. flow is currently returning about <br />125,000 acre-feet of irrigation drainage. This quantity of <br />drainage is well above the 108,000 acre-feet per year projected <br />and used for sizing the plant at 73 Mgaljd. If the Desalting <br />Plant were fully operational, about 97,300 acre-feet of this <br />drainage could be treated and some of the remaining 27,700 acre- <br />feet of drainage could be blended with the product water to meet <br />Minute 242. However, most of the untreated drainage water would <br />be bypassed along with the reject salt brine. <br /> <br />DESALTING PLANT PROBLEMS AND NEEDS <br />Desalting Plant problems and needs focus on reduqing the <br />operation and maintenance costs and on developing a replacement <br />water source to make up for the reject stream, operational bypass <br />and other unavoidable bypass. <br /> <br />Because power costs are a significant part of the operating <br />costs, and because power rates have been escalating in recent <br />years, Reclamation has been analyzing modifications to the <br />Desalting Plant to reduce energy costs. The annual Operations <br />Maintenance and Repair (OM&R) costs, including energy to run the <br />desalting plant, are projected to be in excess of $31 million <br />during years of operation. During years of surplus Colorado <br />River flows the Desalting Plant would not be operational, <br />however, the down time would allow needed maintenance activities <br />on the Reverse osmosis units. During these non-operating years <br />the OM&R costs are expected to be about $8.5 million. <br /> <br />I <br />- <br /> <br />In operating the Desalting Plant the united States will also <br />incur an obligation to replace the water lost through both the <br />salt brine that is rejected during the desalting process, and any <br />remaining Wellton-Mohawk return flow that cannot be discharged to <br />the Colorado River. <br /> <br />While the options to be discussed in this report will address the <br />need to defray the annual O&M costs, the options will not address <br />the Reclamation's need for replacement water. Following initial <br />analysis, it was determined that a unique opportunity could be <br />realized for making multiple use of the Desalting Plant by <br />treating water for the city of Yuma. While the options do <br />require that the city replace the operational bypass, the <br />treatment options do not develop new water for Reclamation. <br />other on-going studies, such as Vegetative Management, are <br />addressing the need for replacement water. <br /> <br />8 <br />