Pervaporation of a model flavor compound of concord grapes (methyl ant
hranilate) was evaluated with several membranes. Flux and selectivity
decreased linearly with increase in downstream pressure, and increased
with temperature. With a polydimethoxylsiloxane-polycarbonate membran
e, increasing the feed concentration from 20 to 200 ppm did not affect
the flux (55 g m(-2) h(-1)), but decreased the selectivity from 10 to
4. The presence of ethanol in the feed solution lowered separation fa
ctors and increased total flux. A polyether block amide membrane gener
ally gave higher flux and better selectivity. Experiments with commerc
ial grape essence confirmed the excellent potential of pervaporation f
or the production of highly enriched flavors.