发明名称 |
Use of swing preliminary alkylation reactors |
摘要 |
Alkylation systems and processes are described herein. The alkylation system generally includes a preliminary alkylation system containing a preliminary alkylation catalyst therein and adapted to contact an aromatic compound and an alkylating agent with the preliminary alkylation catalyst so as to alkylate the aromatic compound and form a preliminary output stream, wherein the preliminary alkylation system includes a first preliminary alkylation reactor and a second preliminary alkylation reactor connected in parallel to the first preliminary alkylation reactor and a primary alkylation system adapted to receive the preliminary output stream and contact the preliminary output stream and the alkylating agent with a primary alkylation catalyst disposed therein so as to form a primary output stream. |
申请公布号 |
US9375706(B2) |
申请公布日期 |
2016.06.28 |
申请号 |
US201113028381 |
申请日期 |
2011.02.16 |
申请人 |
FINA TECHNOLOGY, INC. |
发明人 |
Butler James |
分类号 |
B01J29/04;B01J29/06;B01J29/70;B01J29/90;C07C2/54;C07C2/64;C07C2/66;C07C6/08;C07C6/12;C07C7/12;C07C15/073;B01J19/00;B01J19/24;C07C15/02;C07C15/067 |
主分类号 |
B01J29/04 |
代理机构 |
|
代理人 |
Shung Albert |
主权项 |
1. An alkylation system comprising:
a preliminary alkylation system comprising a first preliminary alkylation reactor and a second preliminary alkylation reactor, wherein the second preliminary alkylation reactor is connected in parallel to the first preliminary alkylation reactor, wherein each preliminary alkylation reactor contains a preliminary alkylation catalyst therein, and wherein each preliminary alkylation catalyst in the preliminary alkylation system has a silica to alumina molar ratio ranging from 10 to 200; wherein the preliminary alkylation system is adapted to contact an aromatic compound and an alkylating agent with the preliminary alkylation catalyst so as to alkylate the aromatic compound and form a preliminary output stream, wherein the preliminary alkylation system is adapted to operate under liquid phase conditions at a temperature of from about 160° C. to about 270° C.; and a primary alkylation system adapted to receive the preliminary output stream and contact the preliminary output stream and an alkylating agent with a primary alkylation catalyst disposed therein so as to form a primary output stream, wherein the preliminary alkylation system is located upstream of the primary alkylation system. |
地址 |
Houston TX US |