Copper and nickel catalysts supported on praseodymium-doped ceria (PDC) for the water-gas shift reaction

• Doping ceria catalyst support with 5 wt% of Pr increased the reducibilty of sample.
• The OSC and catalytic results in WGS reaction showed the same trend for CePr supports.
• Ni catalysts showed higher activity (due to WGS and methanation) than Cu ones.
• Cu in bimetallic catalysts lowered the reduction temperature of nickel (II).
• Cu-Ni catalysts presented a good selectivity towards WGS.

The aim of this work is to study the behavior of Cu and Ni catalysts supported on praseodymium-doped ceria (PDC) for the WGS reaction. Samples were prepared by impregnation of several PDC supports (praseodymium content in the range 0–50 wt%) synthesized by the urea thermal decomposition method. Bare support and catalysts were characterized by BET, XRD, oxygen storage capacity and TPR. The activity tests were carried out in an atmospheric fixed bed reactor, using a CO/H2O/H2/N2 mixture as the feed stream. Doping of ceria with small loading of Pr increases the surface reducibility and the oxygen storage capacity of ceria. Nickel catalysts are more active than copper ones. In both cases, catalysts supported on PDC with 5 Pr wt% are more active than samples supported on pure ceria. Methanation, which is likely to occur on Ni catalysts, is moderated in samples supported on praseodymium-doped ceria.

Figure optionsDownload high-quality image (146 K)Download as PowerPoint slide