Managing hydrogen and carbon monoxide in a gas to liquid plant to control the H2/CO ratio in the Fischer-Tropsch reactor feed
    2.
    发明申请
    Managing hydrogen and carbon monoxide in a gas to liquid plant to control the H2/CO ratio in the Fischer-Tropsch reactor feed 失效
    管理气体到液体设备中的氢气和一氧化碳,以控制费 - 托反应堆进料中的H2 / CO比

    公开(公告)号:US20040102532A1

    公开(公告)日:2004-05-27

    申请号:US10388843

    申请日:2003-03-15

    Abstract: The present invention provides a process for controlling the ratio of hydrogen to carbon monoxide in feed streams to reactors that convert syngas to hydrocarbon liquids. The process includes primary syngas production process for converting hydrocarbon gas to syngas comprising hydrogen and carbon monoxide. The process further includes introducing a hydrogen rich stream, a carbon monoxide rich stream, or both produced by an auxiliary source to a feed stream being passed to a reactor for converting the syngas to hydrocarbon liquid, thereby adjusting the H2/CO ratio in the feed stream. Examples of reactors that may be used to convert syngas to hydrocarbon liquids are FT reactors staged in series and oxygenate producing reactors staged in series.

    Abstract translation: 本发明提供了一种控制进料流中的氢气与一氧化碳与将合成气转化为烃液体的反应器的比例的方法。 该方法包括用于将烃气转化成包含氢气和一氧化碳的合成气的初级合成气生产方法。 该方法还包括将富氢流,一氧化碳浓缩物流或由辅助源产生的二者引入进料流中,将其转化为反应器以将合成气转化为烃液体,由此调节进料中的H 2 / CO比 流。 可用于将合成气转化为烃类液体的反应器的实例是分级式的FT反应器和串联的含氧化合物反应器。

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