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 |