发明名称 Hydrocracking process for a hydrocarbon stream
摘要 A process for transalkylating a coal tar stream is described. A coal tar stream is provided, and is fractionated to provide at least one hydrocarbon stream having polycyclic aromatics. The hydrocarbon stream is hydrotreated in a hydrotreating zone, and then hydrocracked in a hydrocracking zone. A light aromatics stream is added to the hydrocracking zone. The light aromatics stream comprises one or more light aromatics having a ratio of methyl/aromatic available position that is lower than a ratio of methyl/aromatic available position for the hydrotreated stream. The hydrocracked stream is transalkylated in the hydrocracking zone.
申请公布号 US9073805(B2) 申请公布日期 2015.07.07
申请号 US201414472096 申请日期 2014.08.28
申请人 UOP LLC 发明人 Frey Stanley J.;Barger Paul T.;Bricker Maureen L.;Chen John Q.;Coughlin Peter K.;Johnson James A.;Kocal Joseph A.;Lippmann Matthew;Thakkar Vasant P.;Vanden Bussche Kurt M.
分类号 C07C6/12;C07C5/367;C10G47/00;C10G45/00;C07C6/06;C07C4/06;C07C5/10;C10G1/00;C07C7/12 主分类号 C07C6/12
代理机构 代理人
主权项 1. A process comprising: providing a coal tar stream; fractionating the coal tar stream to provide at least one hydrocarbon stream having polycyclic aromatics; hydrotreating the hydrocarbon stream in a hydrotreating zone in the presence of a catalyst containing at least one group VIII metal and at least one group VI metal to remove sulfur, nitrogen, and metals and to saturate hydrocarbon with double or triple bonds; hydrocracking the hydrotreated stream in the presence of catalyst comprising amorphous silica-alumina bases or low-level zeolite bases combined with one or more group VIII or group VIB metal hydrogenating metal in a hydrocracking zone to crack the polycyclic aromatics to mono-aromatics and saturate mono-aromatics to cycloparaffins; adding a light aromatics stream to the hydrocracking zone; transalkylating the polycyclic aromatic with the aromatics in the light aromatics stream in the hydrocracking zone to provide a greater portion of xylenes in the effluent of the hydrocracking zone; feeding the effluent from the hydrocracking zone to a dehydrogenation zone to convert cycloparaffins to aromatics in the presence of a catalyst containing platinum, Pt—Re or Pt—Sn and alumina or chloride alumina; recycling a portion of the effluent of the dehydrogenation zone to the hydrocracking zone; and wherein the light aromatics stream comprises one or more light aromatics having a ratio of methyl/aromatic available position that is lower than a ratio of methyl/aromatic available position for the hydrotreated stream.
地址 Des Plaines IL US