The hydrogenation of CO was carried out over Pd supported on MgO. The addit
ion of various lanthanide oxides increased the activity of Pd/MgO to produc
e methanol. CeO2 exhibited the highest promoting effect at a temperature as
low as of 250 degreesC and the optimum molar ratio of Ce/Pd was about unit
y. TPR experiment showed that CeO2 on MgO (without Pd) suffered less reduct
ion with hydrogen compared with that supported on Al2O3. Thus, the former r
etained the Ce(TV) state almost completely under the reducing condition, wh
ich was ascertained by XAFS measurement. XAFS analysis also indicated that
Pd in Pd/MgO suffered reduction extensively while that in Pd/CeO2/MgO partl
y retained the oxidized state owing to the reduction-resistant CeO2 on MgO.
The results of CO adsorption XPS, XAFS, and TEM measurement revealed that
addition of CeO2 increased the dispersion of Pd metal particles. It was con
cluded that the high active of the catalyst resulted from the combination o
f highly dispersed Pd metal and partly oxidized Pd component with a Pd-O bo
nd.