首页> 外国专利> The process still several steps to increase the octane and yield of liquid hydrocarbons, a process still several steps to produce liquid hydrocarbons.The system of fluidized bed reactor catalitico still in various stages and process for catalytic cracking unit to integrate stock catalitico fluidised

The process still several steps to increase the octane and yield of liquid hydrocarbons, a process still several steps to produce liquid hydrocarbons.The system of fluidized bed reactor catalitico still in various stages and process for catalytic cracking unit to integrate stock catalitico fluidised

机译:该过程仍然需要数步以增加辛烷值和液态烃的收率,该过程仍然需要数步以生产液态烃。流化床反应器催化系统仍处于各个阶段,催化裂化装置将流化的催化反应器集成到一起的过程

摘要

An improvement in gasoline octane without substantial decrease in overall yield is obtained in an integrated process combining a fluidized catalytic cracking reaction and a fluidized catalyst olefin oligomerization reaction when crystalline medium pore shape selective zeolite catalyst particles are withdrawn in partially deactivated form from the oligomerization reaction stage and added as part of the active catalyst in the FCC reaction.
机译:当从低聚反应阶段中以部分失活的形式抽出结晶介质孔型选择性沸石催化剂颗粒时,将流化催化裂化反应和流化催化剂烯烃低聚反应结合在一起的综合方法获得了汽油辛烷的改善,而总收率没有实质性降低。并在FCC反应中作为活性催化剂的一部分添加。

著录项

  • 公开/公告号BR8802823A

    专利类型

  • 公开/公告日1989-01-03

    原文格式PDF

  • 申请/专利权人 MOBIL OIL CORPORATION;

    申请/专利号BR19888802823

  • 发明设计人 AMOS ANDREW AVIDAN;TAI-SHENG CHOU;

    申请日1988-06-09

  • 分类号C07C2/10;C10G11/18;

  • 国家 BR

  • 入库时间 2022-08-22 06:40:31

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