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 |
代理机构 |
|
代理人 |
|
主权项 |
|
地址 |
|