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Gasoline octane enhancement in fluid catalytic cracking process with split feed injection to riser reactor

机译:分流进料到提升管反应器中的流化催化裂化工艺中汽油辛烷值的提高

摘要

A fluid catalytic cracking unit equipped with multiple feed injection points along the length of the riser is operated such that portions of the same fresh feed are charged to different feed injection points. Preferably, the hydrocarbon fresh feed can be split into two or more non-distinct fractions, with one fraction charged to the bottom injection point along the length of the riser reactor, and the remaining fractions charged to injection points progressively higher up along the length of the riser reactor. Unconverted slurry oil boiling above 650°F can be recycled to one or more of the various injection points along the length of the riser. Steam in excess of levels typically employed for dispersion is used at the bottom of the riser to help lift the regenerated catalyst. Other inert gases can be used in place of, or in conjunction with, steam to accomplish lifting of the catalyst in the riser.
机译:沿着提升管的长度配备有多个进料注入点的流体催化裂化单元进行操作,以使相同新鲜进料的部分被装入不同的进料注入点。优选地,可以将烃新鲜进料分成两个或更多个不明显的馏分,其中一个馏分沿提升管反应器的长度注入底部注入点,而其余的馏分沿注入管的长度向上逐渐注入更高的注入点。立管反应堆。沸点高于650°F的未转化浆油可以沿立管的长度循环到各个注入点中的一个或多个。提升管底部使用的蒸汽通常超过用于分散的水平,以帮助提升再生的催化剂。可以使用其他惰性气体代替蒸汽或与蒸汽结合使用,以实现提升管中催化剂的提升。

著录项

  • 公开/公告号EP0232587B1

    专利类型

  • 公开/公告日1990-02-07

    原文格式PDF

  • 申请/专利权人 CHEVRON RESEARCH COMPANY;

    申请/专利号EP19860308420

  • 发明设计人 KRISHNA ASHOK S.;

    申请日1986-10-29

  • 分类号C10G11/14;C10G11/20;

  • 国家 EP

  • 入库时间 2022-08-22 06:14:27

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