The catalytic dehydrogenation of propane has been studied over Pt and
Pt-Sn catalysts supported on gamma-Al2O3 and SiO2. Without the promote
r Pt shows the same initial specific activity (TOF) on both supports,
but deactivates rapidly due to coking. The effect of Sn as a promoter
depends on the support. On gamma-Al2O3 tin interacts with the support
and is stabilized in an oxidation state > 0. The result is an increase
in Pt dispersion and reduced deactivation without any change in the i
nitial specific activity in dehydrogenation. The selectivity to propen
e is strongly enhanced by tin, particularly due to blocking or poisoni
ng of acid sites on the support. On SiO2 the Sn is more readily reduce
d, and alloy formation is possible. This leads to a similar increase i
n Pt dispersion and improved catalytic stability, but also to a strong
reduction in the specific activity. The change in catalytic stability
on both supports is parallelled by a dramatic change in the hydrogen
adsorption properties, as seen from the TPD profiles after reduction.