Catalytic reduction of NO by propene in the presence of oxygen was studied
over Sn-Al2O3 prepared by the sol-gel method. The maximum NO conversion did
not change much with Sri loading (1-5 wt%), although the effective tempera
ture window for NO reduction shifted to lower temperatures with increasing
Sri loading. X-ray diffraction (XRD), and X-ray absorption spectroscopy (XA
NES and EXAFS) revealed the formation of finely-divided SnO2 crystallites i
n Sn-Al2O3. It was deduced that not only the surface vicinity of supported
SnO2, which can be reduced at lower temperatures, but also alumina particip
ate in the reaction as catalytically active sites. The catalytic performanc
e of Sn-Al2O3 was markedly improved by an H2O treatment at 873 K. The H2O t
reatment did not affect the crystal structure of the catalysts and the disp
ersion state of supported SnO2, but promoted the removal of Cl- ions, which
originated from the SnCl4 precursor. The activity enhancement by the H2O t
reatment was accounted for by an increase in the surface SnO2 concentration
as active sites and by the modification of oxo-tin species as active sites
. Reaction kinetic studies suggested that NO reduction on the fresh and the
H2O-treated catalysts proceeds through the same reaction pathway in which
the surface NOx adspecies and C3H6-derived species play an important role f
or NO reduction.