The alloying of Pt with Ga delivered from a hydrotalcite-like support was investigated as a strategy to produce bimetallic catalysts for propane dehydrogenation. A series of Pt/Mg(Al,Ga)O x catalysts (2–3 wt % Pt, Ga/Pt molar ratios between 0 and 10) and a model Pt/Ga 2 O 3 catalyst (4 wt % Pt, Ga/Pt molar ratio of 50) were characterized by means of X-ray diffraction (XRD), transmission electron microscopy, and activity measurements (873 K, W cat / F C 3 H 8,0 = 25 kg cat ·s·mol –1 and P C 3 H 8,0 = 5 kPa at a total pressure of 101.3 kPa). XRD patterns taken during temperature-programmed reduction in 5% H 2 /He and isothermal reduction/oxidation cycling between 5% H 2 /He and 20% O 2 /N 2 at 873 K revealed dynamic alloy formation and segregation that depended upon the gas environment and Ga content. Alloying on the Pt/Mg(Al,Ga)O x catalyst with a Ga/Pt ratio of 2 could not be observed by XRD. For a Ga/Pt ratio of 10, an alloy with a diffraction peak at 40.2° was formed during the initial reduction. After subsequent reduction/oxidation treatments, this catalyst evolved toward a stable periodic cycling between pure Pt and one or more Pt–Ga alloys with characteristic peaks at 40.2° and 46.5°. The exact composition of the Pt–Ga alloy(s) could not be identified. On the model Pt/Ga 2 O 3 catalyst, an alloy was formed with the same characteristic peak at 40.2° as on the Ga-rich Pt/Mg(Al,Ga)O x . In addition, another Pt–Ga alloy appeared on the Pt/Ga 2 O 3 catalyst, which was identified as a stoichiometric PtGa phase. These alloys were formed on Pt/Ga 2 O 3 at a lower temperature than on Pt/Mg(Al,Ga)O x and they were stable during the reduction/oxidation cycling. Catalytic activity measurements demonstrated that the formation of Pt–Ga alloys on the Pt/Mg(Al,Ga)O x sample with a Ga/Pt ratio of 10 and on the Pt/Ga 2 O 3 catalyst led to pronounced enhancement of the initial selectivity toward propylene, but lower activity per exposed Pt atom.
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Redekop et al. (2014) studied this question.
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