发明名称 |
Upgrading naphtha in a single riser fluidized catalytic cracking operation employing a catalyst mixture |
摘要 |
The present invention discloses a catalytic cracking operation featuring a single riser in which a variety of hydrocarbon conversion reactions takes place, a stripping unit in which entrained hydrocarbon material is removed from catalyst and a regeneration zone in which spent cracking catalyst is regenerated, which comprises: (a) converting a relatively high boiling charge material introduced to the riser at a lower level thereof in the presence of a first catalyst component which is an amorphous cracking catalyst and/or a large pore crystalline silicate cracking catalyst to provide lighter products including significant quantities of naphtha; and, (b) converting a naphtha charge material introduced to the riser at a higher level thereof in the presence of a second catalyst componet which is a shape selective medium pore crystalline silicate zeolite catalyst to provide a relatively high octane gasoline product.
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申请公布号 |
US4892643(A) |
申请公布日期 |
1990.01.09 |
申请号 |
US19890336571 |
申请日期 |
1989.04.11 |
申请人 |
MOBIL OIL CORPORATION |
发明人 |
HERBST, JOSEPH A.;OWEN, HARTLEY;SCHIPPER, PAUL H. |
分类号 |
B01J8/00;B01J8/12;C10G11/18 |
主分类号 |
B01J8/00 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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