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Catalytic distillation refining

机译:催化蒸馏精制

摘要

A process for hydrotreating petroleum fractions early in the refining process by employing catalyst prepared as components of distillation structures or as contained beds of catalyst in atmospheric distillation columns and or side draw columns. For example, a crude petroleum is hydrotreated by taking side streams from an atmospheric distillation column and the vacuum gas oil from a vacuum distillation column which are individually fed to separate desulfurizations, preferably in distillation column reactors containing a hydrodesulfurization catalyst. The overheads from each of the distillation column reactors is returned to the atmospheric column and the bottoms from each distillation column reactor is withdrawn as hydrotreated product. The process may also be used for upgrading the effluent from a fluid catalytic cracking unit, preferably operated as a catalytic distillation reactor.
机译:一种在精制过程中通过使用作为常压蒸馏塔和/或侧馏塔中的蒸馏结构组分或催化剂的床层制备的催化剂对石油馏分进行加氢处理的方法。例如,通过将来自常压蒸馏塔的支流和来自真空蒸馏塔的真空瓦斯油分别进料以进行单独的脱硫,优选在含有加氢脱硫催化剂的蒸馏塔反应器中,对粗石油进行加氢处理。将来自每个蒸馏塔反应器的塔顶馏出物返回至常压塔,并且将来自每个蒸馏塔反应器的塔底物作为加氢处理产物取出。该方法也可以用于提纯来自流化催化裂化单元的流出物,该流化催化裂化单元优选作为催化蒸馏反应器操作。

著录项

  • 公开/公告号US5837130A

    专利类型

  • 公开/公告日1998-11-17

    原文格式PDF

  • 申请/专利权人 CATALYTIC DISTILLATION TECHNOLOGIES;

    申请/专利号US19960735234

  • 发明设计人 CLIFFORD S. CROSSLAND;

    申请日1996-10-22

  • 分类号C10G25/00;

  • 国家 US

  • 入库时间 2022-08-22 02:09:41

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