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Coal hydrogenation process with direct coal feed and improved residuum conversion

机译:直接加煤并提高残渣转化率的煤加氢工艺

摘要

A process for hydrogenation of coal to produce hydrocarbon liquids and gases, wherein the yield of liquid products is increased by feeding particulate coal at temperature below about 600° F. directly into a back-mixed reactor and preferably into an ebullated bed catalytic reaction zone containing coal-derived liquid and hydrogen for rapid heating and conversion. In the process, the coal is pressurized and fed without preheating directly into the reaction zone and additional heat needed in the reaction zone to maintain temperature therein at 750° - 900° F. is provided by heating recycle hydrogen and coal-derived liquid streams to temperatures above the desired reaction zone temperature. By using this process, the coal feed is heated quickly and hydrogenated in the catalytic reaction zone and undesired thermal reactions which usually occur in coal during preheating before its exposure to the catalytic hydrogenation reaction zone conditions are minimized, which results in increased yields of desirable light hydrocarbon liquids products and reduced production of undesirable asphaltenes and unconverted coal or char.
机译:煤加氢以生产烃类液体和气体的方法,其中通过将低于约600°F的温度下的颗粒状煤直接送入回混反应器,优选送入沸腾床催化反应区,以提高液体产物的产率,其中煤制液体和氢气,用于快速加热和转化。在该过程中,将煤加压并进料,而无需预热直接将其送入反应区,并通过将循环氢和煤衍生的液流加热到温度高于所需的反应区温度。通过使用该方法,煤进料被快速加热并在催化反应区中氢化,并且在将煤暴露于催化氢化反应区的条件降至最低之前,在预热期间通常发生在煤中的不期望的热反应被最小化,这导致所需光的产率提高。烃液体产品,减少不希望的沥青质和未转化的煤或焦炭的生产。

著录项

  • 公开/公告号US4437973A

    专利类型

  • 公开/公告日1984-03-20

    原文格式PDF

  • 申请/专利权人 HRI INC.;

    申请/专利号US19820365660

  • 发明设计人 PAUL H. KYDD;DERK T. A. HUIBERS;

    申请日1982-04-05

  • 分类号C10G1/08;

  • 国家 US

  • 入库时间 2022-08-22 08:39:19

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