Upon reducing sulfated zirconia (SZ) catalysts with hydrogen, roughly
50% of the sulfate groups are reduced to sulfur dioxide which is detec
ted mass spectrometrically; the other 50% are reduced to S-= ions that
are retained at the surface. The measured ratio H/S of consumed Ii at
oms to S atoms originally present as SO4= ions is thus H/S = 5. In the
presence of platinum, either deposited on the SZ, or as Pt/NaY in a p
hysical mixture with SZ, or downstream of SZ in a layered bed arrangem
ent, the SO2 is reduced further to H2S, which is detected chemically a
nd by MS. In this case H/S = 8. The TPR peak position is shifted to lo
wer temperature in PtSZ and in physical mixtures of SZ and Pt/NaY. Red
uction of sulfate groups lowers the Bronsted acidity of the catalysts,
as indicated by the intensity of the LR bands of adsorbed ammonia. Br
onsted acidity is almost totally eliminated by hydrogen reduction at 4
00 degrees C. The position of the band of ammonia on Lewis sites is no
t significantly affected by sulfate reduction, but the temperature at
which ammonia is desorbed from these sites is lowered. The H2S that is
formed in the presence of Pt partially poisons the Pt particles; thei
r catalytic signature in the isotope exchange of cyclopentane with D-2
indicates that large Pt ensembles are blocked by adsorbed S atoms eve
n after reduction up to 350 degrees C, but that isolated Pt atoms are
still acting as active sites. After complete reduction of the SO4= gro
ups, Pt in PtSZ loses its catalytic activity for the isotope exchange
reaction. (C) 1997 Academic Press.