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Fluid cat cracking heavy using stripped catalyst for feed preheat and regenerator temperature control

机译:使用汽提催化剂对流化床催化裂化重质,用于进料预热和再生器温度控制

摘要

A fluid cat cracking process for catalytically cracking a feed containing vanadium into lower boiling products, includes a cat cracker and a regenerator, with the feed entering the catalytic cracking zone preheated by indirect heat exchange with spent, stripped catalyst particles being recycled from the cracking reactor to the regenerator. Operating the regenerator at a temperature no higher than about 1150. degree. F. permits the amount of vanadium in the feed to be substantially increased with no loss of catalytic activity due to vanadium poisoning of the catalyst, when compared to a higher regenerator temperature of 1365. degree. F. Using the stripped, spent catalyst for heating the feed reduces feed coking and heat exchanger fouling, compared to using the hotter regenerated catalyst for feed preheat.
机译:用于将含钒的进料催化裂化成较低沸点产物的流化催化裂化方法,包括催化裂化器和再生器,进入催化裂化区的进料通过与废的汽提的催化剂颗粒间接换热而预热,然后从裂化反应器中回收到再生器。在不高于约1150度的温度下运行再生器。与较高的再生器温度(1365度)相比,F。允许进料中的钒含量大大增加,而不会因催化剂的钒中毒而失去催化活性。 F.与使用较热的再生催化剂进行进料预热相比,使用汽提的废催化剂加热进料可减少进料结焦和热交换器结垢。

著录项

  • 公开/公告号US5853568A

    专利类型

  • 公开/公告日1998-12-29

    原文格式PDF

  • 申请/专利权人 EXXON RESEARCH AND ENGINEERING COMPANY;

    申请/专利号US19970903425

  • 发明设计人 JOHN F. R. BRANDER;

    申请日1997-07-30

  • 分类号C10G11/00;C10G35/10;

  • 国家 US

  • 入库时间 2022-08-22 02:09:05

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