“…The most extensively investigated catalysts for PDH are supported Pt and bimetallic PtSn. , Previous studies have found that Pt is quite active for PDH but suffers from deactivation and poor selectivity. − However, the activity, propene selectivity, and stability of Pt improve with decreasing particle size and are best for isolated Pt atoms. , Both experimental and theoretical studies have shown that the addition of Sn increases the dispersion of Pt, enhances the rates of PDH, and reduces the rate of coke formation. − PtSn catalysts contain a variety of structures and Pt/Sn ratios, e.g., Pt particles, PtSn bimetallic alloys (e.g., Pt 3 Sn, PtSn), small, supported PtSn bimetallic particles, and isolated Pt atoms interacting with Sn, the nature of these structures depending on the catalyst preparation procedure, Pt/Sn ratios, and support composition. − Pt 3 Sn is often cited as the most active bulk alloy, although PtSn has also been shown to be active . The addition of hydrogen to the feed propane has been reported to enhance the rate of PDH by up to 4-fold, with an optimum propane-to-hydrogen ratio of 1:1. , Hydrogen addition also decreases the deactivation of PtSn catalysts due to coking by removal of coke precursors through the reaction with atomically adsorbed hydrogen, an interpretation supported by theoretical studies. , Hydrogen addition has also been found to cause restructuring of PtSn particles and increase Pt–Sn interactions. − …”