Catalytic oxidation of methane over ZrO2-supported Pd catalysts

The catalytic oxidation of methane has been examined in an integral reactor over Pd/ZrO2 catalysts in this study in order to determine how various pre paration pretreatment and reaction variables influence activity. The conver sion of methane versus temperature data indicate that mild oxidative and re ductive treatments enhance the activity of a 5 wt% Pd/ZrO2 catalyst while a higher-temperature reductive pretreatment produces a less efficient cataly st. Increasing the Pd loading from 0.1 to 10 wt% improves catalytic perform ance while higher loadings yield negligible improvement. Decay studies were performed on a 5 wt% Pd/ZrO2 catalyst and compared to those of an optimize d Pd/Al2O3 catalyst. Under the conditions used in this study, the activity of the Pd/ZrO2 catalyst remains fairly constant over a 50-hr period while t he Pd/Al2O3 catalyst initially exhibits an increase in activity but then a decrease after approximately 16 hr. At 250 degrees C the Pd/ZrO2 converts 5 6% of the methane to CO2 and H2O after approximately 45 hr while the Pd/Al2 O3 catalytically oxidizes only 32% of the methane under the same conditions . An optimized Pd/ZrO2 catalyst achieves a methane conversion of 100% below 300 degrees C, which is 40 degrees C lower than that obtained using the op timized Pd/Al2O3 catalyst. The 5 wt% Pd/ZrO2 CH4-oxidation catalyst also was characterized using X-ray photoelectron spectroscopy before and during heating in vacuum at 180 degr ees C and after treatment in a 2:1 mixture of O-2 and CH4 at 180 degrees C and 100 Torr for 45 min. The near-surface region of the as-entered catalyst consists mostly of ZrO2 and PdO along with some Pd metal. Some of the PdO is reduced to Pd metal at 180 degrees C, which is near the onset temperatur e for methane oxidation, and the Pd signal is diminished probably due to ag glomeration of the Pd. Exposure of the catalyst to a 100 Torr mixture of 2: 1 O-2 and CH4 at 180 degrees C for 45 min results in the formation of adsor bed CHx, CO and CO3= and/or HCO3- species. These data suggest that the CH4 hydrogen bonds are first broken to form an adsorbed carbon species, which r eacts with surface oxygen to form an adsorbed CO. This CO then reacts to fo rm a surface carbonate or bicarbonate species which decomposes to form CO2. (C) 1999 Academic Press.