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Hydrogen production in steam reforming of methane at low reaction temperature over nickel catalysts

机译:镍催化剂上低反应温度下甲烷水蒸气重整制氢

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Effects of supports to nickel catalysts have been studied for the steam reforming of methane at 773 K. The activity of nickel supported on silica reduced with hydrogen at 773 K decreases with oxidation of nickel particles by steam during the reaction. Nickel supported on alumina is scarcely reduced with hydrogen at 773 K and inactive in the reforming at 773 K. However, the catalyst reduced at 973 K is fairly active while nickel is partially oxidized during the reaction. In absence of steam, surface hydroxyl groups on these catalysts react with methane at 773 K to produce hydrogen and carbon dioxide, suggesting that the hydroxyl groups play an important role in the low temperature reforming. In the case of zirconia-supported nickel, water accumulated on the surface at 773 K involves in the reaction with methane and the catalyst is the most effective in the stream reforming at 773 K.
机译:对于在773 K下甲烷的蒸汽重整,已经研究了载体对镍催化剂的影响。在反应过程中,随着蒸汽对镍颗粒的氧化,在773 K上氢还原的负载在二氧化硅上的镍的活性降低。负载在氧化铝上的镍在773 K时几乎不会被氢还原,而在773 K时在重整中没有活性。但是,在973 K时还原的催化剂相当活泼,而镍在反应过程中被部分氧化。在没有蒸汽的情况下,这些催化剂上的表面羟基在773 K下与甲烷反应生成氢和二氧化碳,这表明羟基在低温重整中起着重要作用。在氧化锆负载的镍的情况下,在773 K时积聚在表面上的水会与甲烷发生反应,并且催化剂在773 K的料流重整中最有效。

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