Vapor-permeation (VP) aided esterification of oleic acid with ethanol and methanol was carried out at 383 K using both a pressurized vapor circulation system and a laboratory module of Zeolite membrane with excellent VP performance of dehydration of organic liquids. The combined process provided almost complete conversion in a short reaction time with the initial molar ratio of alcohol to oleic acid (m0) of 1.5. The reaction time, as for ethanol, was reduced by a factor of 1/3 as compared with the process carried out under the atmospheric pressure using a laboratory module of polyimide hollow fiber. The loss of alcohol by permeation was below 0.01% of the feed for ethanol and was only 0.16% for methanol. This indicates that the almost complete reaction can be achieved even if m0 goes down to unity. The Zeolite membrane worked effectively and stably for a long period, and is useful for achieving the highly efficient process of esterification.
'/%3e%3cuse xlink:href='%23a' transform='rotate(23.036 .093 25.536)'/%3e%3cuse xlink:href='%23a' transform='rotate(45.87 1.273 16.18)'/%3e%3cuse xlink:href='%23a' transform='rotate(69.945 .996 12.078)'/%3e%3cuse xlink:href='%23a' transform='rotate(20.66 -19.689 31.932)'/%3e%3c/svg%3e)
'/%3e%3c/defs%3e%3cpath fill='%23012169' d='M0 0h10080v5040H0z'/%3e%3cpath stroke='%23fff' stroke-width='.6' d='m0 0 6 3m0-3L0 3' clip-path='url(%23b)' transform='scale(840)'/%3e%3cpath stroke='%23e4002b' stroke-width='.4' d='m0 0 6 3m0-3L0 3' clip-path='url(%23c)' transform='scale(840)'/%3e%3cpath stroke='%23fff' stroke-width='840' d='M2520 0v2520M0 1260h5040'/%3e%3cpath stroke='%23e4002b' stroke-width='504' d='M2520 0v2520M0 1260h5040'/%3e%3cg fill='%23fff'%3e%3cuse xlink:href='%23d' x='2520' y='3780'/%3e%3cuse xlink:href='%23a' x='7560' y='4200'/%3e%3cuse xlink:href='%23a' x='6300' y='2205'/%3e%3cuse xlink:href='%23a' x='7560' y='840'/%3e%3cuse xlink:href='%23a' x='8680' y='1869'/%3e%3cuse xlink:href='%23e' x='8064' y='2730'/%3e%3c/g%3e%3c/svg%3e)
