发明名称 Catalytic cracking of coke producing hydrocarbons
摘要 A process for thermally and catalytically upgrading a heavy feed in a single riser reactor FCC unit is disclosed. A heavy feed is added to a blast zone in the base of the riser, and sufficient hot regenerated FCC catalyst is added to induce both thermal and catalytic cracking of the heavy feed. A reactive quench material, which cools the material discharged from the blast zone is added to a quench zone downstream of the blast zone, to reduce temperature at least in part by undergoing endothermic reactions in the riser. Quench liquids can be distillable FCC feeds such as gas oil, slack wax, or alcohols or ethers. The quench material is added in an amount equal to 100 to 1000 wt % of the non-distillable material in the heavy feed. A preferred catalyst, with a high zeolite content, is used which retains activity in the quench despite initial contact with the heavy feed, which tends to overwhelm conventional FCC catalysts.
申请公布号 US5271826(A) 申请公布日期 1993.12.21
申请号 US19900502008 申请日期 1990.03.30
申请人 MOBIL OIL CORPORATION 发明人 KRAMBECK, FREDERICK J.;NACE, DONALD M.;SCHIPPER, PAUL H.;SAPRE, AJIT V.
分类号 C10G11/00;C10G11/18;(IPC1-7):C10G11/00 主分类号 C10G11/00
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