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    Catalytic partial oxidation of hydrocarbon fuels to hydrogen and carbon monoxide
    8.
    发明授权
    Catalytic partial oxidation of hydrocarbon fuels to hydrogen and carbon monoxide 失效
    烃燃料催化部分氧化成氢和一氧化碳

    公开(公告)号：US06221280B1

    公开(公告)日：2001-04-24

    申请号：US09175125

    申请日：1998-10-19

    申请人： Amarendra Anumakonda ,  Jean Yamanis ,  Joe Ferrall

    发明人： Amarendra Anumakonda ,  Jean Yamanis ,  Joe Ferrall

    IPC分类号： C07C102

    CPC分类号： H01M8/0612 ,  C01B3/386 ,  C01B2203/0261 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/1023 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1288 ,  C01B2203/169

    摘要： A method of processing sulfur-containing heavy hydrocarbon fuels in the substantial absence of steam through catalytic partial oxidation is described. The process comprises the steps of vaporizing a heavy hydrocarbon fuel and bringing the vaporized fuel and oxidizer mixture in contact with a noble metal catalyst supported on an open channel structure. The hydrocarbon fuel is considered to be a liquid hydrocarbon having at least six carbon atoms and a sulfur content of at least 50 ppm. The feed, containing only the vaporized fuel and oxygen in the oxidizer mixture, is subsequently routed through a reactor containing a noble metal catalyst (typically Rh/Alumina) at contact times of not more than about 500 milliseconds and a LHSV of not less than about 0.5 h−1. The feed is partially oxidized by a catalytic reaction occurring at a temperature of no less than about 1050° C., with the catalytic partial oxidation process producing essentially complete conversion of hydrocarbons present in the feed to hydrogen and carbon monoxide. The sulfur compounds in the feed are predominantly converted into hydrogen sulfide. The product gas consisting mainly of carbon monoxide and hydrogen can then be recovered or, alternatively, directed to a solid oxide fuel cell system.

    摘要翻译： 描述了通过催化部分氧化在基本上不存在蒸汽的情况下处理含硫重烃燃料的方法。 该方法包括蒸发重质烃燃料并使蒸发的燃料和氧化剂混合物与负载在开放通道结构上的贵金属催化剂接触的步骤。 烃燃料被认为是具有至少6个碳原子并且硫含量至少为50ppm的液态烃。 在氧化剂混合物中仅含有蒸发的燃料和氧气的进料随后在不大于约500毫秒的接触时间通过包含贵金属催化剂（通常为Rh /氧化铝）的反应器，并且LHSV不小于约 0.5 h-1。 进料通过在不低于约1050℃的温度下发生的催化反应被部分氧化，催化部分氧化过程产生进料中存在的烃基本上完全转化为氢气和一氧化碳。 进料中的硫化合物主要转化为硫化氢。 然后可以回收主要由一氧化碳和氢气组成的产物气体，或者替代地指向固体氧化物燃料电池系统。