Four catalysts, H2PtCl6-5SnCl(2)/gamma-Al2O3 (cat-1), {H2PtCl6-5SnCl(2
) + xLaCl(3)}/gamma-Al2O3 (cat-2), (Me4N)[Pt(SnCl3)(5)]/gamma- Al2O3 (
cat-3), and {(Me4N)[Pt(SnCl3)(5)] + xLaCl(3)}/gamma-Al2O3 (cat-4) were
prepared and their catalytic activities and stabilities in dehydrogen
ation of propane were investigated. It has been shown that the stabili
ties of the Pt-Sn bimetallic catalysts were improved by introducing la
nthanum into the catalysts either by the conventional impregnation met
hod with Pt-and Sn-containing salts or by using precursors derived fro
m Pt-Sn bimetallic clusters. Results from XPS analysis indicated that
addition of lanthanum could inhibit the reduction of tin in the cataly
sts, especially in cat-2. The distribution of pore capacity in a used
cat-2 was mainly in the large and medium size range, but in a used cat
-1 the distribution was mainly in the small to medium size range. Ther
mal gravimetric analysis (TGA) showed that weight loss in the used cat
-1 was much more than that in the used cat-2. The results suggested th
at introducing lanthanum into the Pt-Sn bimetallic catalysts could eff
ectively prevent them from coking.