发明公开
EP1002778A1 Gas phase alkylation with split load of catalyst
有权
Verfahren zur Alkylierung in der Gasphase mit gespaltener Katalysatorbeladung
- 专利标题: Gas phase alkylation with split load of catalyst
- 专利标题(中): Verfahren zur Alkylierung in der Gasphase mit gespaltener Katalysatorbeladung
-
申请号: EP99122754.7申请日: 1999-11-16
-
公开(公告)号: EP1002778A1公开(公告)日: 2000-05-24
- 发明人: Merrill, James T. , Butler, James R. , Ghosh, Ashim K.
- 申请人: FINA TECHNOLOGY, INC.
- 申请人地址: 6000 Legacy Drive Plano, Texas 75024 US
- 专利权人: FINA TECHNOLOGY, INC.
- 当前专利权人: FINA TECHNOLOGY, INC.
- 当前专利权人地址: 6000 Legacy Drive Plano, Texas 75024 US
- 代理机构: Detrait, Jean-Claude
- 优先权: US193310 19981117
- 主分类号: C07C2/66
- IPC分类号: C07C2/66 ; C07C15/073
摘要:
Ethylbenzene is produced by alkylation over a split load of monoclinic silicalite alkylation catalysts having different silica/alumina ratios. A feedstock containing benzene and ethylene is applied to a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds. At least one catalyst bed contains a first monoclinic silicalite catalyst having a silica/alumina ratio of at least 275. At least one other catalyst bed contains a second monoclinic silicalite catalyst having a silica/alumina ratio of less than about 275. The alkylation reaction zone is operated at temperature and pressure conditions in which the benzene is in a gaseous phase to cause gas-phase alkylation of the aromatic substrate in the presence of the monoclinic silicalite catalysts to produce an alkylation product. The alkylation product is then withdrawn from the reaction zone for separation and recovery. The use of the split load of catalyst allows a higher purity ethylbenzene product to be produced at improved efficiencies than if only one of the catalysts were used by itself.
公开/授权文献
- EP1002778B1 Gas phase alkylation with split load of catalyst 公开/授权日:2003-04-02
信息查询