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DIRECT COAL LIQUEFACTION PROCESS AND SYSTEM

机译:直接煤液化工艺及系统

摘要

A direct coal liquefaction process and system is provided that utilizes a dispersed catalyst and recycle of atmospheric and vacuum fractionator bottoms to produce a maximum yield of jet fuel/diesel or chemical plant feedstock while eliminating all slurry heat exchangers and a slurry preheat furnace. Process hydrogen is preheated in a heat exchanger and, if necessary, in a hydrogen furnace, and mixed with the recycled atmospheric and vacuum fractionator bottoms being fed to the input of the direct liquefaction reactor. Heat for the hydrogen heat exchanger is provided by the overhead from the hot separator receiving the effluent from the direct liquefaction reactor. Product selectivity is controlled by operating conditions.
机译:提供了一种直接的煤液化方法和系统,其利用分散的催化剂以及大气和真空分馏塔底物的再循环来产生最大的喷气燃料/柴油或化工厂原料的产率,同时消除了所有浆料热交换器和浆料预热炉。在热交换器中,如有必要,在氢气炉中将工艺氢气进行预热,并与循环的常压和减压分馏塔底馏出物混合,然后将其送入直接液化反应器的输入端。氢气热交换器的热量由热分离器的塔顶馏出物提供,热分离器从直接液化反应器接收流出物。产品的选择性由操作条件控制。

著录项

  • 公开/公告号US2016340592A1

    专利类型

  • 公开/公告日2016-11-24

    原文格式PDF

  • 申请/专利权人 ACCELERGY CORPORATION;

    申请/专利号US201615162385

  • 申请日2016-05-23

  • 分类号C10G1/06;C10G7/06;C10G7/00;C10G1/00;

  • 国家 US

  • 入库时间 2022-08-21 13:47:14

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