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Two stage process for the conversion of synthesis gas using a cobalt catalyst the first stage and a supported ruthenium in the second stage

机译:在第一步中使用钴催化剂进行合成气转化的两步工艺,在第二步中使用负载型钌进行转化

摘要

A process is described for the conversion of synthesis gas into hydrocarbons comprising the steps of; (i) passing a synthesis gas comprising hydrogen and carbon monoxide over a cobalt catalyst at elevated temperature and pressure to produce a first reaction product mixture comprising hydrocarbons, steam, carbon monoxide and hydrogen, (ii) condensing and separating water from the first reaction product mixture to produce a de-watered first reaction product mixture, (iii) passing the de-watered first reaction product mixture over a supported ruthenium catalyst at elevated temperature and pressure to produce a second reaction product mixture containing hydrocarbons, and (iv) recovering the hydrocarbons from the second reaction product mixture.
机译:描述了一种用于将合成气转化为烃的方法,该方法包括以下步骤: (i)在升高的温度和压力下使包含氢和一氧化碳的合成气在钴催化剂上通过以产生包含烃,蒸汽,一氧化碳和氢的第一反应产物混合物,(ii)从第一反应产物中冷凝和分离水混合物以产生脱水的第一反应产物混合物,(iii)将脱水的第一反应产物混合物在升高的温度和压力下通过负载的钌催化剂,以产生包含烃的第二反应产物混合物,和(iv)回收来自第二反应产物混合物的烃。

著录项

  • 公开/公告号GB2489362A

    专利类型

  • 公开/公告日2012-09-26

    原文格式PDF

  • 申请/专利权人 JOHNSON MATTHEY PUBLIC LIMITED COMPANY;

    申请/专利号GB20120012273

  • 发明设计人 MARK MCKENNA;

    申请日2010-12-16

  • 分类号C10G2/00;B27K3/10;

  • 国家 GB

  • 入库时间 2022-08-21 17:03:19

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