Three nickel-based catalyst systems, Ni/c-Al 2 O 3 , Ni/BaTiO 3 , and Ni-0.75wt%La-BaTiO 3 , were investigated for the CO 2 reforming of CH 4 . The temperature of CH 4 decomposition on catalyst Ni/c-Al 2 O 3 is the lowest and the relative content of H 2 is the highest; but the temperature of CH 4 decomposition on catalyst Ni-0.75 wt%La-BaTiO 3 is the highest and the relative content of H 2 is the lowest. The amount of carbon deposition via CH 4 decomposition decreases with the increase of rare earth La and the temperature of decomposition also declines gradually. Different active coke species were formed on different catalysts. The higher activity of coke species is, the easier the reaction with activated CO 2 is. The coke species were investigated by the XPS technique. Several surface coke species existed on catalysts after the reaction. The surface species with the binding energy near 282 and 286 ev are the main coke species. These species resulted in the catalyst deactivation. By analyzing the coke on catalyst, it was found the catalyst Ni-0.75wt% La-BaTiO 3 suppressed the formation of coke species whose binding energy is near 282 and 286 ev.