发明名称 TWO-CATALYST HYDROCRACKING PROCESS
摘要 <p>TWO-CATALYST HYDROCRACKING PROCESS The process comprises contacting a hydrocarbon feedstock containing a substantial amount of organic nitrogen-containing compounds in a first reaction zone under hydrocracking conditions and in the presence of hydrogen with a first catalyst comprising nickel and molybdenum or nickel and tungsten, their oxides, and/or their sulfides on a co-catalytic acidic cracking support comprising ultrastable, large-pore crystalline aluminosilicate material and a silica-alumina matrix to produce a first hydrocracked effluent and contacting said first hydrocracked effluent in a second reaction zone under hydrocracking conditions and in the presence of hydrogen with a second catalyst comprising cobalt and molybdenum, their oxides, and/or their sulfides on a co-catalytic acidic cracking support comprising ultrastable, largepore crystalline aluminosilicate material and a silicaalumina matrix to produce a second hydrocracked effluent. Preferably, the first catalyst comprises nickel and tungsten deposed on the co-catalytic acidic cracking support. In one embodiment of the process, the second catalyst is a catalyst that has been deactivated and then regenerated prior to its use in the process.</p>
申请公布号 CA1128444(A) 申请公布日期 1982.07.27
申请号 CA19790339241 申请日期 1979.11.06
申请人 STANDARD OIL COMPANY 发明人 BERTOLACINI, RALPH J.;YU, ALBERT P.
分类号 C10G47/20;C10G65/10;(IPC1-7):10G65/10 主分类号 C10G47/20
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