发明名称 Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production
摘要 A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
申请公布号 US9024097(B2) 申请公布日期 2015.05.05
申请号 US201113327192 申请日期 2011.12.15
申请人 UOP LLC 发明人 Serban Manuela;VandenBussche Kurt M.;Moser Mark D.;Wegerer David A.
分类号 C10G35/04;C07C5/02;C07C5/41;C07C15/04;C07C15/06;C10G35/085;C10G35/095;C10G35/24;C10G59/02 主分类号 C10G35/04
代理机构 代理人
主权项 1. A process for producing aromatic compounds from a hydrocarbon feedstream, comprising: passing the hydrocarbon feedstream to a hydrogenation/dehydrogenation reactor system and contacting with a hydrogenation/dehydrogenation catalyst consisting of a noble metal on a support thereby generating a first stream with reduced naphthene and olefin content, wherein the hydrogenation/dehydrogenation reactor system is operated at a temperature between 420° C. and 460° C.; passing the first stream to a fractionation unit to generate an overhead stream comprising C7 and lighter paraffins, and a bottoms stream comprising heavier hydrocarbons; passing the overhead stream to a high temperature reforming reactor system thereby generating a reformate product stream, wherein the high temperature reforming reactor system is operated at a temperature between 540° C. and 580° C.; and passing the bottoms stream to a second reforming reactor system, thereby generating a second effluent stream; and passing the second effluent stream to the high temperature reforming reactor system.
地址 Des Plaines IL US