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 |