This study reports the synthesis, characterization, and catalytic performance of a series of catalysts of Ru supported on CeO
2-Y
2O
3 composites (Ru/CeYX; X = 0, 33, 66, and 100 wt.% Y
2O
3) for CO
2 hydrogenation. Supported material modification (Y
2O
3-CeO
2), by the Y
2O
3 incorporation, allowed a change in selectivity from methane to RWGS of the CO
2 hydrogenation reaction. This change in selectivity is correlated with the variation in the physicochemical properties caused by Y
2O
3 addition. X-ray diffraction (XRD) analysis confirmed the formation of crystalline fluorite-phase CeO
2 and α-Y
2O
3. High-resolution transmission electron microscopy (HR-TEM) and energy-dispersive X-ray spectroscopy (EDS) elemental mapping revealed the formation of a homogeneous CeO
2-Y
2O
3 nanocomposite. As the Y
2O
3 content increased, the specific surface area, measured by BET, showed a decreasing trend from 106.3 to 51.7 m
2 g
−1. X-ray photoelectron spectroscopy (XPS) of Ce3d indicated a similar Ce
3+/Ce
4+ ratio across all CeO
2-containing materials, while the O1s spectra showed a reduction in oxygen vacancies with increasing Y
2O
3 content, which is attributed to the decreased surface area upon composite formation. Catalytically, the addition of Y
2O
3 influenced both conversion and selectivity. CO
2 conversion decreased with increasing Y
2O
3 content, with the lowest conversion observed for Ru/CeY100. Regarding selectivity, methane was the dominant product for Ru/CeY0 (pure CeO
2), while CO was the main product for Ru/CeY33, Ru/CeY66, and Ru/CeY100, indicating a shift towards the reverse water–gas shift (RWGS) reaction. The highest RWGS reaction rate was observed with the Ru/CeY33 catalyst under all tested conditions. The observed differences in conversion and selectivity are attributed to a reduction in active sites due to the decrease in surface area and oxygen vacancies, both of which are important for CO
2 adsorption. In order to verify the surface species catalytically active for RWGS, the samples were characterized by FTIR spectroscopy under reaction conditions.
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