Abstract
The production of synthesis gas by partial oxidation of methane and reforming of methane with carbon dioxide over supported Rh catalysts have been studied over a range of temperatures (550 -1000 K). Effect of support on catalytic activity for partial oxidation of methane over Rh catalysts was explained by Rh dispersion, where the activities and the dispersions were correlated. On the other hand, for reforming of methane with carbon dioxides, metal oxides used for support significantly influenced catalytic activity. Physical mixing of metal oxides such as AI2O3, TiO2, and MgO with Rh/SiO2 caused a marked improvement of the catalytic activity of Rh/SiO2
Published Version
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