发明名称 Co-current catalyst flow with feed for fractionated feed recombined and sent to high temperature reforming reactors
摘要 A process is presented for the increasing the yields of aromatics from reforming a hydrocarbon feedstream. The process includes splitting a naphtha feedstream into a light hydrocarbon stream, and a heavier stream having a relatively rich concentration of naphthenes. The heavy stream is reformed to convert the naphthenes to aromatics and the resulting product stream is further reformed with the light hydrocarbon stream to increase the aromatics yields. The catalyst is passed through the reactors in a sequential manner.
申请公布号 US9024099(B2) 申请公布日期 2015.05.05
申请号 US201113327200 申请日期 2011.12.15
申请人 UOP LLC 发明人 Moser Mark D.;VandenBussche Kurt M.;Wegerer David A.;Gajda Gregory J.
分类号 C10G35/04;C07C5/02;C07C5/42;C10G59/02;C10G59/06;C10G69/08 主分类号 C10G35/04
代理机构 代理人
主权项 1. A process for reforming a hydrocarbon feedstream, comprising: passing the feedstream to a fractionation system to create a first overhead stream comprising n-hexane and lighter hydrocarbons, and a first bottoms stream comprising cyclohexane and heavier hydrocarbons; passing the first bottoms stream to a first reformer reactor, operated at a first set of reforming conditions, wherein the first set of reforming conditions include a temperature less than 540° C., to generate a first reactor effluent having an increased aromatic content; passing the first overhead stream and the first reactor effluent to a second reforming reactor system operated at a second set of reforming conditions, wherein the second set of reforming conditions include a temperature greater than or equal to 540° C., thereby generating a second effluent stream; passing a first regenerated catalyst stream to the first reformer reactor and generating a first reformer catalyst effluent stream; passing a second catalyst stream to the second reformer reactor system and generating a second reformer catalyst effluent stream; passing the second effluent stream to a reformate splitter to generate a second overhead stream comprising C7 and lighter aromatics, and a second bottoms stream comprising C8 and heavier aromatics; and passing the second overhead stream to an aromatics recovery unit, thereby generating an aromatics product stream comprising benzene and toluene, and a raffinate stream comprising non-aromatic hydrocarbons; wherein the catalyst for all the reforming reactors is the same.
地址 Des Plaines IL US