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<br />IV MULTISTAGE FLASH PROCESS <br /> <br />..... <br />c.o <br />.... <br />o <br /> <br />The multistage flash (MSF) distillation process is currently one <br /> <br />of the leading processes for the desalination of seawater because of <br /> <br />demonstrated performance and favorable economic projections. As a re- <br /> <br />suIt of the importance of the MSF process, a number of studies have been <br /> <br />done on the interrelations among design and operating variables, and <br /> <br />these reports provide a considerable body of useful information. <br /> <br />The two basic configurations of MSF that have received extensive <br /> <br />attention are: the single-effect multiple stage (SEMS) design and the <br />multieffect, multiple stage (MEMS) layout. Each design has certain ad- <br /> <br />vantages that may make it more favorable in specific applications. The <br /> <br />MEMS configuration has been described as a series of connected SEMS plants <br /> <br />and has the disadvantage of requiring pumps and more complicated piping <br /> <br />between each effect. The advantage of the MEMS design is operation with <br /> <br />either higher temperatures or a higher concentration factor, which re- <br /> <br />suIts in improved thermal efficiency, The SEMS process has the advantage <br /> <br />of design simplicity and proven performance in large-scale plants, while <br /> <br />a high capacity MEMS pilot plant has only recently been constructed. <br /> <br />Dual purpose power/seawater desalting plants are coming to the fore, <br /> <br />and as the capacity of these plants increases, the unit energy costs <br /> <br />will be reduced. The optimum design of these plants will then be toward <br /> <br />lower capital costs for the desalting unit at some sacrifice in thermal <br /> <br />efficiency, As a result, the SEMS design has been selected for most <br /> <br />large-scale plants now under consideration, and it was therefore selected <br /> <br />for this study. <br /> <br />9 <br /> <br />