The separation characteristics of the PVA-CS (polyvinyl alcohol-chitosan) b
lended composite membrane for dehydration of ethanol-water mixture are exam
ined. The relationships of flux and separation factor with the feed concent
ration and operation temperature are established. Using this correlated equ
ation, the continuous-flow pervaporation process about 500 kilolitres/year
dehydrated ethanol is designed. The numbers of stage and reheater are calcu
lated by stage-by-stage method for two kinds of cascades: one with equal me
mbrane area and the other with 10 degreesC of temperature decrement per sec
tion. The results show that when the numbers of stage and reheater are the
same, the cascade with 10 degreesC of temperature decrement has more advant
ages than that with equal membrane area. The influences of feed concentrati
on and flow rate on the numbers of stage and reheater in the cascades are d
iscussed.