发明名称 Gas phase alkylation-liquid transalkylation process
摘要 An alkylation/transalkylation process involving vapor phase alkylation of a benzene feedstock in a multi-stage alkylation zone having a plurality of series connected catalyst beds containing a pentasil aromatic alkylation catalyst, such as silicalite, coupled with intermediate separation and recirculation steps and liquid phase transalkylation over a transalkylation catalyst comprising a molecular sieve having a pore size greater than the pore size of the silicalite. The benzene containing feedstock is supplied to the multi-stage alkylation reaction zone along with a C2-C4 alkylating agent operated under temperature and pressure conditions to maintain the benzene in the gas phase. Alkylated product is recovered from the alkylation zone and supplied to a benzene recovery zone for the separation of the benzene from the alkylation product. Benzene from the benzene recovery zone is recycled to the reaction zone. A higher boiling bottom fraction containing a mixture of monoalkylated and polyalkylated aromatic components is supplied to a secondary separation zone from which a monoalkylated aromatic component, e.g. ethylbenzene, is recovered overhead with a heavier polyalkylated aromatic recovered as a bottom fraction. The bottom fraction may be applied to a tertiary separation zone.
申请公布号 US5955642(A) 申请公布日期 1999.09.21
申请号 US19960739564 申请日期 1996.10.30
申请人 FINA TECHNOLOGY, INC. 发明人 MERRILL, JAMES T.;BUTLER, JAMES R.
分类号 B01J29/06;C07B61/00;C07C2/66;C07C5/13;C07C5/27;C07C6/12;C07C9/22;C07C15/02;C07C15/073;(IPC1-7):C07C1/00;C07C2/64;C07C2/68;C07C5/22 主分类号 B01J29/06
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