P ropylene is one of the feedstocks in the petrochemical industries. It is commonly used as a precursor to producing important intermediates and products, such as isopropanol, polypropylene, propylene oxide, epichlorohydrin, and acrylonitrile [1,2]. Several researchers have investigated the challenges encountered in propylene production which includes searching ways of increasing catalyst selectivity for propylene and decreasing catalyst deactivations. In addressing this challenge, a density functional theory (DFT) calculation was employed by Yan et al. [3] to propose a radical mechanism for propane dehydrogenation over Ga 2 O 3 (100) where H abstraction by O(2) site was identified as a low energy barrier step. Ming et al. [4] employed DFT calculations to show that the introduction of tin into platinum catalyst lowers the energy barrier for propylene desorption and simultaneously increases the activation energy for propylene dehydrogenation, which has a positive effect on the selectivity of propylene production. Lauri et al. [5] also made related findings for the use of Pt-Sn catalyst, which lowered the coking rate while weakening the binding of propylene. Timothy [6] confirmed