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Catalytic Partial Oxidation of Methane to Synthesis Gas - Catalysis and Reaction Engineering

机译:甲烷催化部分氧化合成气 - 催化和反应工程

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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:对合成气体的部分氧化的机械研究具有强烈的指示,即在使用负载金属催化剂时CO_2是初级产品(Ru / Gamma-Al_2O_3,Pd /γ-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)以及Rh粉末。 CO_2在反向Boudouard反应中与碳物质反应,由甲烷解离与CO.CO.CO选择性和碳积聚在催化剂表面上的碳积累的程度取决于金属载体相互作用。 CO和H_2选择性以及碳积累也受水动力学的影响。 传达流化床反应器操作的结果。

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