Since combustion starts at a temperature as low as 300˚C with iron oxides, one of the combustion catalysts, the evolution of toxic dioxins on the combustion is suppressed. 1,2 It has been reported that PdO microcrystals supported on χ-Al2O3 show a high catalytic activity in methane oxidation below 300˚C when CeO2 coexists altogether with PdO on the support (PdO/CeO2 catalysts). [3][4][5] Thus, PdO/CeO2 catalysts have the capability to ignite combustion at moderate temperatures as well as other advantages; colorless and transparent to visible light, which enables the catalyst to be utilized in various fields. We have reported that the Pd metal phase is observed in the X-ray absorption fine structure (XAFS) after treating the catalysts in an O2-deficient atmosphere at high temperature, and have suggested that a phase change between PdO and Pd takes place in the PdO/CeO2 catalysts. 4,5 In this work, in situ hightemperature measurements of XRD (in situ HTXRD) of the PdO/CeO2 catalysts and FT-IR (in situ HTFT-IR) of PdO microcrystals were made in order to verify the phase change in the temperature range where the catalysts work. The in situ high-temperature measurements allow us to have an accurate insight into the thermal change of the catalytic-active PdO under the condition of operation in which PdO catalyzes methane oxidation.
Experimental
ChemicalsThe synthesis of the PdO/CeO2 catalysts supported on χ-Al2O3 has been published. 4,5 In a small volume of an aqueous solution of Ce(NO3)3·6H2O, a weighed portion of Al(OH)3 (gibbsite) was suspended and admixed by vigorous stirring for 30 min. An aqueous solution of Pd((NO3)2 was added to the mixture in various atomic ratios of R = Ce/Pd. The mixture was stirred for 1 h, dried in air for 15 h and finally calcined at 500˚C in an electric furnace. The calcined solid was crushed, sieved to obtain a component of 10 -24 mesh in diameter, and was used in the measurements. In this experiment, we tested three kinds of catalysts with loading ratios of PdO and CeO2 vs. χ-Al2O3; 0.12 g/g and 0 g/g for the catalyst of R = 0, 0.18 g/g and 0.12 g/g for that of R = 1, 0.12 g/g and 0.84 g/g for that of R = 5, respectively. Three thermal events were observed in the thermogravimetry (TG) of a dried mixture of gibbsite, Ce(NO3)3·6H2O and Pd((NO3)2 below 500˚C: a large endotherm due to the formation of χ-Al2O3 located at 311˚C, an exotherm due to the formation of PdO at 240˚C, and that due to the formation of CeO2 at around 268˚C. Therefore, no other materials than χ-Al2O3, CeO2 and PdO are present in the PdO/CeO2 catalysts supported on χ-Al2O3 after calcination at 500˚C.
ApparatusThe catalytic activity was tested in a fix-bed continuous-flow quartz reactor operated at atmospheric pressure, where the details of the experimental condition and the reactor design have been described previously.4,5 A small portion (0.5 g) of the catalyst was loaded in the reactor through which the mixed reactive gas and helium gas were passed when the pressures of methane and oxygen were 3.4 kPa and 20.3 kPa, ...