首页> 外国专利> HYDROGENATION OF UNDISSOLVED COAL AND SUBSEQUENT LIQUEFACTION OF HYDROGENATED COAL

HYDROGENATION OF UNDISSOLVED COAL AND SUBSEQUENT LIQUEFACTION OF HYDROGENATED COAL

机译:未溶解煤的加氢和加氢煤的随后液化

摘要

HYDROGENATION OF UNDISSOLVED COAL AND SUBSEQUENT LIQUEFACTION OF HYDROGENATED COAL A staged process for hydrogenation of undissolved coal and subsequent liquefaction of the hydrogenated coal to provide useful hydrocarbon liquid products including naphtha, gasoline and diesel fuels. These low boiling hydrocarbon liquids are produced by the process comprising: (a) mixing solid coal particles with a hydrocarbon solvent oil in a solvent/coal ratio ranging from about 8/1 to about 1.5/1 to provide a flowable coal/oil slurry; (b) passing said coal/oil slurry and hydrogen upwardly through a first stage reaction zone containing a coal-derived liquid in a catalytic bed of particulate; catalyst maintained at a temperature ranging from about 400.degree. to about 700.degree.F and a hydrogen partial pressure of 100 to 2000 psig for a residence time sufficient to hydrogenate the solid coal particles; and (c) withdrawing the coal/oil slurry containing the hydrogenated coal particles from the first reaction zone and passing the coal/oil slurry to a second stage reaction zone containing a catalytic bed maintained at a temperature of between about 700.degree. and about 850.degree.F and a hydrogen partial pressure of 100 to 2000 psig to liquefy and convert the coal to useful hydrocarbon liquid fuel products. The first and second stage reaction zones may contain the same or different catalysts such as Co/Mo on a porous substrate such as alumina or silica. The process preferably uses a coal-derived slurrying oil and first stage temperature of 550-650.degree.F. and second stage temperature of 800-825.degree.F.
机译:未溶解的煤的加氢和加氢的煤的液化一种将未溶解的煤加氢和随后的加氢的煤液化的分阶段过程,以提供有用的烃类液体产品,包括石脑油,汽油和柴油。这些低沸点烃液体是通过以下方法生产的:(a)将固体煤颗粒与烃溶剂油以溶剂/煤比为约8/1至约1.5 / 1混合以提供可流动的煤/油浆; (b)使所述煤/油浆和氢气向上通过第一级反应区,该第一级反应区在颗粒的催化床上含有煤衍生的液体;催化剂保持在约400.degree温度范围内。至约700°F和100至2000 psig的氢分压,停留时间足以氢化固体煤颗粒; (c)从第一反应区中抽出含有氢化煤颗粒的煤/油浆,并使煤/油浆进入第二级反应区,该第二级反应区的催化床温度保持在约700℃。在大约850°F和100至2000 psig的氢分压下液化并将煤转化为有用的烃类液体燃料产品。第一级反应区和第二级反应区可在多孔基材如氧化铝或二氧化硅上包含相同或不同的催化剂如Co / Mo。该方法最好使用煤制浆油,第一阶段温度为550-650.F。第二阶段温度为800-825.F。

著录项

  • 公开/公告号ZA841630B

    专利类型

  • 公开/公告日1984-10-31

    原文格式PDF

  • 申请/专利权人 HRI INC.;

    申请/专利号ZA19840001630

  • 申请日1984-03-05

  • 分类号C10G;

  • 国家 ZA

  • 入库时间 2022-08-22 09:12:27

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号