Ni@SiO2-yolk-shell catalyst was prepared by the method of etching Ni@SiO2-core-shell with hydrochloric acid, while the core-shell catalyst was prepared by the stober method. In comparison, Ni-SiO2-AE (without yolk-shell structure) was used to denote the catalyst prepared by the similar method as Ni@SiO2-yolk-shell but without fully encapsulation of Ni particles by SiO2. The catalytic performances of these three catalysts were investigated in carbon dioxide reforming of methane to syngas (CRM). The reaction was conducted under different conditions by varying GHSVs of reactants and reaction temperatures to further test the stability of the catalysts. The properties of the as-prepared and spent Ni@SiO2-yolk-shell, Ni@SiO2-core-shell and Ni-SiO2-AE catalysts were characterized by TEM/HRTEM, XRD, TG-DSC to measure the morphology, crystallinity and carbon deposition, etc. It was found that compared to Ni@SiO2-core-shell and Ni-SiO2-AE catalysts, Ni@SiO2-yolk-shell catalyst behaved remarkably stable performance at the temperature up to 1073 K, and the specific structure and carbon deposition-resisted behavior of the Ni@SiO2-yolk-shell catalyst may help to maintain the stability during the reaction. (C) 2015 Elsevier B.V. All rights reserved.