Dehydrogenation of propane to propene in the presence of carbon dioxide was carried out over unsupported (MoO3, CeO2, Al2O3, ZrO2, SiO2 and Yb2O3) and supported (MoO3/SiO2 and MoO3/Al2O3) oxide catalysts. The highest yield of propene (about 6,2%) with selectivity of above 63% was obtained using MoO3 catalyst. It was also found that the conversion and products distributions very depending on the catalyst and supports.
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