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<br />VERTICAL TUBE EVAPORATOR <br /> <br />.... <br />roO <br />CJ1 <br />W <br /> <br />STEAM <br />O,2B6 . IO.lb/hr <br />2670 <br /> <br /> r" -t i1'f1 ~ <br /> r~ > <br /> -I--> r:: FIN <br /> r- > CON <br /> - -- ,,; f:- <br /> ~ <br /> Ir-+ <br /> - IT. OEA <br /> /' ;..,..;...~ <br />l -~ ~ <br />- <br /> <br />MU L TI STAGE FLASH <br /> <br />FIGURE 7 FLOW SHEET FOR lD-mgd VTE-MSF PROCESS <br /> <br />Table 8 <br /> <br />SEAWATER FEED <br />9,22. 1Q61b/h' 65"F <br /> <br />AL <br />OENSOR <br />HEAT REJECT <br />3,46 . 10. Ib/hr IOooF <br />ACID ADDITION <br />NONCONOENSABLES <br /> <br />ERATOR <br /> <br />PRODUCT WATER <br />3.47 . 10. Ibl hr 900F <br /> <br />BRINE BLOWDOWN <br />2,3. 10.lb/hr 92,soF <br /> <br />T8-190Z-3 <br /> <br />MASS AND ENERGY FLOWS IN 10 mgd VERTICAL TUBE EVAPORATOR-MSF PLANT <br /> <br /> HEAT CONTENT <br /> F'LOW RATE TEMPERATURE (3201" = 0 Enthalpy) <br /> 106 Ib/hr "F 106 Btu/hr <br />Input <br />Sea~ater Feed 9,22 65 285 <br />Ste:am to Heater 0,286 267 335 <br /> - <br /> 621 <br />Output <br />Product Water 3,46 90 201 <br />Brine Slowdown 2.30 92,8 122 <br />Heat Rej eel 3,46 100,0 228 <br />Condensate Return 0,286 267 70 <br /> - <br /> 620 <br /> <br />29 <br /> <br />"-,-" <br /> <br />