发明名称 Process for the utilization of refinery C4 streams
摘要 A process is disclosed for preparing a C<SUB>4 </SUB>stream for feeding to an alkylation process which reacts isobutane with butene to produce isooctane. The C<SUB>4 </SUB>stream is treated in a first distillation column reactor to remove dienes and mercaptans and separate out any C<SUB>5</SUB>'s which might be present. The treated C<SUB>4</SUB>'s are then fed to a second distillation column reactor that concurrently isomerizes 1-butene to 2-butene and splits the normal C<SUB>4</SUB>'s from the iso C<SUB>4</SUB>'s. The iso C<SUB>4</SUB>'s are then fed to a third distillation column reactor where a portion of the isobutene is saturated to isobutane. The C<SUB>4</SUB>'s from the isomerization/splitter are combined with the C<SUB>4</SUB>'s from the hydrogenation unit and fed to a cold acid alkylation unit. The third distillation column may also oligomerize a portion of the isobutene to diisobutene in the upper end which is saturated in the bottom of the column to isooctane.
申请公布号 US6919016(B2) 申请公布日期 2005.07.19
申请号 US20040912253 申请日期 2004.08.05
申请人 CATALYTIC DISTILLATION TECHNOLOGIES 发明人 PODREBARAC GARY G.;MARASCHINO MARIO J.
分类号 C07C2/00;C07C2/58;C07C2/62;C07C4/00;C07C5/00;C07C6/00;C07C7/148;C07C9/21;C07C319/16;C07C319/18;C10G45/58;C10L1/04;(IPC1-7):C10L1/04 主分类号 C07C2/00
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