Nickel-based catalysts frequently encounter significant challenges in achieving both high CO2 conversion and superior CO selectivity during reverse water gas shift (RWGS) reactions. To address this issue, we developed a facile strategy to prepare highly dispersed Ni/CeO2 catalysts by forming Ce1−xNixO2−y solid solutions. Under conditions of 300–600 °C, 0.1 MPa, and a gas hourly space velocity (GHSV) of 40,000 mL gcat−1 h−1, the 5Ni/CeO2-A catalyst exhibited outstanding selectivity, approaching 100 %. The RWGS reaction rate reached 1332 μmolCO gNi−1 s−1 and maintained stable for 50 h almost without deactivation. The formation of Ce1−xNixO2−y solid solution uniformly disperses numerous Ni species in the CeO2 lattice, effectively inhibiting Ni aggregation. This highly dispersed Ni weakens CO adsorption and facilitates its direct desorption without excessive hydrogenation. Moreover, the catalyst remains well-dispersed state even after reduction. The formed Ce1−xNixO2−y solid solution generates abundant oxygen vacancies on the catalyst surface, enhancing H2 dissociation. The catalyst’s pore size distribution is also modified, creating stacked pores that favor reactant diffusion and expose more active centers. In-situ DRIFTS experiments demonstrate that Ce-OH plays a pivotal role in CO2 adsorption on the 5Ni/CeO2-A catalyst, while the stabilization of bicarbonate and formate intermediates by the highly dispersed Ni further promotes catalytic performance. This study introduces a novel preparation method and provides valuable insights for designing Ni-based catalysts with exceptional CO selectivity.
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