Abstract
We study the effect of variable permeabilities on the performance of a permeator employing a cellulose acetate type of membrane. The experiments were conducted using a CO 2 -N 2 mixture. The variation in the permeabilities of CO 2 and N 2 with the pressure and the feed composition has been measured experimentally, and statitical models have been fitted to the data. The experimental data have been compared with theoretical results obtained using a perfect mixing model which incorporated variable permeabilities.
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