In this work, two ZrO2-supported Fe2O3 catalysts were synthesized through the impregnation (Fe2O3/t-ZrO2) and the hydrothermal (Fe2O3/c-ZrO2) methods. The hydrothermal preparation improved the catalyst activity and propylene yield; propane conversion: 45.8 % vs. 31.2 %, propylene yield: 31.1 % vs. 23.2 %. This higher activity was attributed to the high specific surface area and thereby higher Fe dispersion that led to more formation of active Fe3 + sites. According to results, the t-ZrO2 surfaces were known to be more favorable for coke reaction compared to c-ZrO2. Adsorption energy of propane and propylene onto the most stable surfaces of ZrO2 was measured as a criterion for side reactions and coke deposits by DFT calculations. The results showed that propane and propylene are more adsorbed onto t-ZrO2 than onto c-ZrO2, which indicates more cracking of propane and propylene onto t-ZrO2. Finally, the experimental data were successfully fitted with the Deactivation Model with Residual Activity (DMRA). It was found that the Fe2O3/c-ZrO2 catalyst has a higher resistance against the deactivation by coke deposits compared to the Fe2O3/t-ZrO2 catalyst; activation energy of deactivation function: 83.64 vs. 70.09 kJ/mole.
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