首页> 外国专利> FLUIDIZED CATALYST REGENERATION BY OXIDATION IN A DENSE PHASE BED AND A DILUTE PHASE TRANSPORT RISER

FLUIDIZED CATALYST REGENERATION BY OXIDATION IN A DENSE PHASE BED AND A DILUTE PHASE TRANSPORT RISER

机译:稠密相床中氧化流态化催化剂和稀相输运竖管

摘要

A process in which spent catalyst is regenerated with or without the complete combustion of CO in a regeneration zone comprising a first dense bed, a dilute phase transport riser and a second dense bed. Higher velocities and higher O2 concentrations employed within the regeneration zone result in shorter catalyst and gas residence time, reduced catalyst inventory, lower catalyst makeup rate, improved regeneration, and improved catalyst stability. The substantially complete combustion of CO eliminates CO pollution of the atmosphere without the need for a CO boiler and decreases feed preheat requirements.
机译:一种方法,其中在包括第一密相床,稀相传输提升管和第二密相床的再生区中,在有或没有CO完全燃烧的情况下再生用过的催化剂。在再生区内采用较高的速度和较高的O2浓度可缩短催化剂和气体的停留时间,减少催化剂的存量,降低催化剂的补充速率,改善再生,并提高催化剂的稳定性。一氧化碳的基本完全燃烧消除了对一氧化碳的污染,而无需一氧化碳锅炉,并降低了进料预热的要求。

著录项

  • 公开/公告号US3844973A

    专利类型

  • 公开/公告日1974-10-29

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PROD COUS;

    申请/专利号US19720258041

  • 发明设计人 STINE LUS;CONNER AUS;

    申请日1972-05-30

  • 分类号B01J11/70;B01J11/68;

  • 国家 US

  • 入库时间 2022-08-23 04:53:01

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