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/Ga2O3 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-C3Hg,F-0 = 25 kg(cat).s.mol(-1) and P-C3Hg,P-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 degrees 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 degrees and 46.5 degrees. The exact composition of the Pt-Ga alloy(s) could not be identified. On the model Pt/Ga2O3 catalyst, an alloy was formed with the same characteristic peak at 40.2 degrees as on the Ga-rich Pt/Mg(AI,Ga)O-x. In addition, another Pt-Ga alloy appeared on the Pt/Ga2O3 catalyst, which was identified as a stoichiometric PtGa phase. These alloys were formed on Pt/Ga2O3 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/Ga2O3 catalyst led to pronounced enhancement of the initial selectivity toward propylene, but lower activity per exposed Pt atom.