发明名称 PROCESS AND APPARATUS FOR THE CONVERSION OF HYDROCARBONS
摘要 A hydrocarbon conversion process is described. The process includes contacting in a reactor an inert gas with one or more catalyst compositions suitable for methylation of toluene and hydrogenation of phenol; contacting a reducing agent with the one or more catalyst compositions under conditions suitable for reducing metal oxide content of the catalyst composition; contacting at least part of toluene and/or benzene-containing with a oxygenate in the presence of the one or more catalyst compositions and under conditions effective to convert toluene to xylenes and produce a reactor effluent stream comprising para-xylene and having a lower concentration of phenol than the toluene-containing stream; separating at least one para-xylene-enriched stream from the reactor effluent stream; and separating from the at least one para-xylene enriched stream at least one toluene-enriched stream and at least one para-xylene-product stream. An apparatus for carrying out such a process is also described.
申请公布号 US2016115094(A1) 申请公布日期 2016.04.28
申请号 US201514872388 申请日期 2015.10.01
申请人 Dakka Jihad M.;Tinger Robert G. 发明人 Dakka Jihad M.;Tinger Robert G.
分类号 C07C2/86;C07C51/265;C07C5/27 主分类号 C07C2/86
代理机构 代理人
主权项 1. A hydrocarbon conversion, comprising: a) contacting in at least a first reactor an inert gas with one or more catalyst compositions suitable for methylation of toluene and/or hydrogenation of phenol; b) contacting a reducing agent with the one or more catalyst compositions under conditions suitable for reducing metal oxide content of the first catalyst composition; c) contacting at least part of an aromatic hydrocarbon stream comprising ≧5.0 wt % toluene and/or benzene with a oxygenate in the presence of the first catalyst composition and under conditions effective to convert toluene to xylenes and produce a reactor effluent stream comprising para-xylene and having a lower concentration of phenol than the aromatic hydrocarbon stream; d) separating in a first separator at least one para-xylene-enriched stream from the reactor effluent stream; and e) separating in a second separator from the at least one para-xylene enriched stream at least one toluene-enriched stream and at least one para-xylene-product stream.
地址 Whitehouse Station NJ US