发明名称 PROCESS FOR THE SEPARATION OF ISOBUTENE FROM NORMAL BUTENES
摘要 A process for the separation of isobutene, otherwise inseparable from butene -1 by fractionation, in high purity from butenes contained in a mixed hydrocarbon stream containing butene-1, butene- 2 and small amounts of butadiene in which the mixed hydrocarbon stream (107) is fed to distillation column reactor (40) containi ng an alumina supported palladium oxide catalyst. The column is operated to tend to exclude butene-2 from contact with the catalys t and to maintain butene-1 in contact with the catalyst to isomerize the butene-1 to butene-2. As butene-2 is produced it is distill ed away from the catalyst, upsetting the equilibrium and allowing for a greater than equilibrium amount of butene-2. The isobutene an d isobutane are concurrently separated from butene-2. Additionally, any butadiene in the feed is hydrogenated to butenes. The bottoms (108) is rich in butene-2.
申请公布号 CA2379348(C) 申请公布日期 2009.04.28
申请号 CA20002379348 申请日期 2000.05.11
申请人 CATALYTIC DISTILLATION TECHNOLOGIES 发明人 PODREBARAC, GARY G.;ADAMS, JOHN R.
分类号 B01D3/14;C07C7/163;B01D3/16;C07B61/00;C07C5/13;C07C5/25;C07C7/04;C07C7/148;C07C11/09 主分类号 B01D3/14
代理机构 代理人
主权项
地址