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
C3H8,0 = 25 kgcat·s·mol–1 and P
C3H8,0 = 5 kPa at a total pressure of 101.3 kPa). XRD patterns
taken during temperature-programmed reduction in 5% H2/He
and isothermal reduction/oxidation cycling between 5% H2/He and 20% O2/N2 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/Ga2O3 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/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.