The batch fermentation combined with the removal of ethanol from the broth
by means of membrane distillation process (MD) has been investigated. The p
orous capillary polypropylene membranes were used for the separation of vol
atile compounds from the feed (broth), formed as a result of fermentation.
The elimination of these compounds allows increase in the productivity and
the rate of conversion of sugar to ethanol, since they act as inhibitors. I
n the case of fermentation combined with the MD, the efficiency of 0.4-0.51
(g EtOH)/(g of sugar) and the production rate of 2.5-4 (g EtOH)/dm(3) h wa
s achieved in relation to 0.35-0.45 (g EtOH)/(g of sugar) and 0.8-2 (g EtOH
)/dm(3) h obtained in:the classical batch fermentation. The ethanol Aux obt
ained in membrane distillation varied in the range of 1-4 (kg EtOH)/m(2) pe
r day and was dependent on the temperature and the feed composition. (C) 20
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