posted on 2025-09-10, 05:30authored byHetong Wang, Wenyun Wang, Yunpeng Zhang, Jianyun Bao, Hongfei Wei, Guoli Fan, Feng Li
Presently, low-temperature methanation with high CO<sub>2</sub> conversion levels at atmospheric pressure possesses significant
energy efficiency and economic advantages. However, developing stable
and high-performance non-noble-metal catalysts for low-temperature
CO<sub>2</sub> methanation remains a formidable challenge. Herein,
a novel strategy for the fabrication of cerium-doped alumina-supported
Ni catalysts was developed via a facile one-step coprecipitation approach
facilitated by a microliquid-film reactor. The as-constructed Ni/Ce–Al<sub>2</sub>O<sub>3</sub> catalyst featuring a Ce/(Ce + Al) molar ratio
of 1:10 exhibited excellent low-temperature CO<sub>2</sub> methanation
activity, with ∼82% CO<sub>2</sub> conversion and 100% methane
selectivity at 250 °C and atmospheric pressure, as well as an
extremely high methane production rate of 5.48 g<sub>CH4</sub>·g<sub>cat</sub><sup>–1</sup>·h<sup>–1</sup>, suppressing
those over most previously reported Ni-based catalysts. It was revealed
that the introduction of a small amount of Ce favored the formation
of abundant interfacial Ni<sup>δ+</sup> sites and favorable
surface Ce<sup>3+</sup>–O–Al structures, which effectively
promoted the accommodation and migration of active hydrogen species
and activated adsorption of CO<sub>2</sub>, thereby facilitating the
generation of key formate and CO intermediates and subsequent conversions
to produce methane. This study provides a new approach for the construction
of high-performance Ni-based catalysts for low-temperature CO<sub>2</sub> methanation and gives deep insight into the critical roles
of surficial/interfacial active structures in boosting CO<sub>2</sub> hydrogenation to produce methane.