[Study on CuO-CeO2 catalysts doped with alkali and alkaline earth metal oxides by in-situ DRIFTS].

CuO-CeO2 series catalysts are the effective catalysts for the selective CO oxidation in hydrogen-rich gas. The adsorption species on the CuO-CeO2 catalysts doped with alkali and alkaline earth metal oxides were investigated with in situ diffuse reflectance FTIR spectroscopy (in-situ DRIFTS) technique. The results showed that a bane at 2 106 cm(-1), due to the carbonyl species, appeared on the CuO-CeO2 catalysts. In the reaction atmosphere, the intensity of this band increased first and then decreased with increasing the temperatures. It was noted that the main active adsorption sites of the CuO-CeO2 catalysts were Cu+ species. At lower temperatures, the carbonyl species were desorbed from the surface of CuO-CeO2 catalysts in the reversible form, while they were desorbed mainly in the irreversible form at the higher temperatures. A sharp peak at 3 660 cm(-1), attributed to the geminal Ce(OH)2 group, was also apparent on the surface of reduced CuO-CeO2 catalyst. The peaks at 1 568, 2 838 and 2 948 cm(-1) were attributed to formate species and the peaks centered at 1 257 and 1 633 cm(-1) were assigned to carbonate species. CO could react with the active hydroxyl species and generate formate species. At higher temperatures, the C-H bond of formate species could break and form carbonate species. These two species would decrease the performance of CuO-CeO2 catalysts at higher temperatures. The stronger IR peaks attributed to CO2 and formate species were observed, moreover there was still a weak IR peak assigned to carbonyl species for Cu1 Li1 Ce9Odelta catalyst when the temperature was above 180 degrees C. It was shown that as the electron donor, the doping of Li2 O on CuO-CeO2 catalyst could contribute to the irreversible desorption of CO at lower temperatures and inhibit the adsorption of H2 on the catalytic surface, and benefit the formation of formate species as well. Although the amounts of CO adsorption on Cu1 Mg1 Ce9 Odelta and Cu1 Ba1 Ce9 Odelta catalysts were much more than other catalysts at lower temperatures, they were mainly desorbed in the reversible form, which had no contribution to the selective CO oxidation.