CO2 reforming of tar reaction (CRT) is a promising method for simultaneous removal and conversion of CO2 and tar in syngas from the biomass gasification technology, which is essential for utilization and upgrading of syngas. However, the deactivation of supported Ni catalysts by sintering and carbon deposits remains the most challenging issue. In this study, (Mg, Al, Ce)Ox nanosheet-supported Ni-based catalysts with varying Ce/Ni ratios (0, 0.1, 0.2, 0.3) were constructed from freeze-dried Ni–Ce–Mg–Al LDH precursors with the thermally dried Ni–Ce0.2–Mg–Al LDH as a reference. The result suggested that freeze drying favored the achievement of loose nanosheets and highly dispersed metals. With the optimized Ce dosage (Ce/Ni = 0.2), the Ni–Ce0.2–F–R catalyst exhibited the most superior activity and stability over 40h time-on-stream. The possible reason is that Ni–Ce0.2–F–R catalyst possessed abundant and homogeneously distributed Ni–CeO2 interface, which accelerated the electron transfer from CeO2 to Ni via Ni–Ov–Ce structure (Ov, oxygen vacancy). An electron-rich state of Ni was thus achieved, which could effectively activate the C–H and C–C bonds. Furthermore, the abundant oxygen defects and stronger alkaline sites of the CeO2 support promoted the adsorption and activation of CO2, which was conducive to the elimination of coke adjacent Ni metal sites. In situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) suggested that the abundant surface-active oxygen species facilitated the deep oxidation and ring opening of the benzene ring.


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