Dry reforming of methane has received considerable interest as one of the most efficient thermocatalysis routes to coconvert two greenhouse gases (CO 2 and CH 4 ) into syngas (CO and H 2 ), requiring a robust catalyst for extensive application. CeO 2 with a honeycomb-lantern-like structure is fabricated by a facile template-free solvothermal process, followed by calcination, and the nickel-active component is confined on the surface of the honeycomb-lantern-like CeO 2 support (namely, Ni/CeO 2 -H) and employed in dry reforming of methane. The catalytic performance of the prepared sample is evaluated in a fixed-bed tubular reactor, and the CH 4 and CO 2 conversions could reach 83.94 and 82.81% at 800 °C, respectively. Meanwhile, the Ni/CeO 2 -H catalysts are thoroughly characterized using X-ray diffraction, N 2 adsorption− desorption, scanning electron microscopy, H 2 temperature-programmed reduction, CO 2 temperature-programmed desorption, X-ray photoelectron spectroscopy, thermogravimetric analysis, and CO 2 temperature-programmed oxidation (CO 2 -TPO), and the results demonstrate the enhancing effect of spatial confinement for the honeycomb-lantern-like structure. Moreover, the kinetics studies reveal that Ni/CeO 2 -H has the lowest activation energy (97.61 kJ/mol) among these Ni/CeO 2 catalyst samples, which can facilitate its excellent catalytic performance effectively. Based on the semiempirical power rate equation, the reaction orders of CH 4 and CO 2 for Ni/CeO 2 -H are 0.60 and 0.17, respectively. Furthermore, the activation energy of coke gasification for the spent Ni/CeO 2 -H catalyst is investigated and determined by the CO 2 -TPO technique on the basis of extrapolating the Wigner−Polanyi equation.