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<br />,... <br />co <br />w::.. <br />t\.) <br /> <br />STEAM <br />0,299 x 10. Ib/hr <br />2550F <br /> <br />CONDENSATE <br />RETURN <br /> <br />aRINE <br />HEATER <br /> <br />DEAERATOR <br />~ <br />MAKEUP FEED <br />6,94 x 10. Ib/hr---: <br /> <br />NONCONDENSABLES <br />ACID AODITION <br />HEAT REJECT 5,06 x 10. Ib/hr 90. F <br />SEAWATER FEED 12 x 10. Ib/hr 65. F <br />PRODUCT WATER 3.47 x 10. Ib/hr SS.F <br />BRINE RECYCLE 24,3 x 10. Ib/hr <br />aRINE BLOWDOWN 3,47 x 10. Ib/hr <br />900F <br /> <br /> <br />MULTISTAGE FLASH EVAPORATOR <br />(42 STAGES HEAT RECOVERY, <br />2 STAGES HEAT REJECTION) <br /> <br />TC-7902.1 <br /> <br />FIGURE 1 <br /> <br />FLOW SHEET FOR THE lD-mgd MSF PROCESS <br /> <br />Table 4 <br /> <br />MASS AND ENERGY FLOWS IN 10 mgd MULTISTAGE FLASH DISTILLATION PLANT <br /> <br /> FLOW RATE TEMP""ATURE HEAT CONTENT <br /> (320r = 0 Enthalpy) <br /> 106 Ih/hr F 106 Btu/hr <br />Input <br />Seawater Feed 12 65 372 <br />Brine From Heater 24,3 250 12ll <br /> 5353 <br />Output <br />-----pro~uct Water 3,46 88 195 <br />Brine Blowdown 3,46 90 181 <br />Heat Reject 5,06 90 278 <br />Brine to Heater 24, 3 238,6 4699 <br /> 5353 <br />Steflm to Heater 0,299 255 348 <br />Con~ensate Return 0,299 255 .22. <br /> 282 <br /> <br />11 <br /> <br />