首页> 外文会议>4th International Natural Gas Conversion Symposium November 19-23, 1995 Kruger Park; South Africa >Catalytic Partial Oxidation of Methane to Synthesis Gas - Catalysis and Reaction Engineering
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Catalytic Partial Oxidation of Methane to Synthesis Gas - Catalysis and Reaction Engineering

机译:甲烷部分催化氧化制合成气-催化与反应工程

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Mechanistic studies on the partial oxidation of methane to synthesis gas have given strong indications that CO_2 is a primary product when using supported metal catalysts (Ru/gamma-Al_2O_3, Pd/gamma/Al_2O_3, Pt/gamma-Al_2O_3, Ni/gamma-Al_2O_3, Rh/gamma-Al_2O_3, Pt/MgO, Rh/MgO, Rh/ZrO_2) as well as Rh powder. CO_2 reacts in a reverse Boudouard reaction with carbon species resulting from methane dissociation to CO. The CO selectivity and the extent of carbon accumulation on the catalyst surface depends on metal-support interaction. CO and H_2 selectivity as well as carbon accumulation are also affected by hydrodynamics. Results of fluidized bed reactor operation are communicated.
机译:甲烷部分氧化为合成气的机理研究已强有力地表明,当使用负载型金属催化剂(Ru /γ-Al_2O_3,Pd /γ/ Al_2O_3,Pt /γ-Al_2O_3,Ni /γ-Al_2O_3时,CO_2是主要产物,Rh /γ-Al_2O_3,Pt / MgO,Rh / MgO,Rh / ZrO_2)和Rh粉末。 CO_2在逆向Boudouard反应中与甲烷分解成CO所产生的碳物种反应。CO的选择性和催化剂表面碳积聚的程度取决于金属与载体的相互作用。 CO和H_2的选择性以及碳的积累也受流体动力学的影响。传达了流化床反应器运行的结果。

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