The CO
2 storage–regeneration (CO
2-SR) process represents a promising strategy for integrating CO
2 capture and catalytic conversion within a single cyclic operation using multifunctional catalysts. In this concept, CO
2 is first stored on basic sites and subsequently converted through
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The CO
2 storage–regeneration (CO
2-SR) process represents a promising strategy for integrating CO
2 capture and catalytic conversion within a single cyclic operation using multifunctional catalysts. In this concept, CO
2 is first stored on basic sites and subsequently converted through methane activation, enabling the coupling of CO
2 capture and reforming reactions in a single reactor. In this work, a series of unsupported Ni–Ba catalysts were investigated as model multifunctional materials for the CO
2-SR process. Catalysts with different Ni/Ba ratios were prepared to analyze how the distribution of storage and catalytic sites influences the cyclic CO
2 capture–conversion behavior. In addition, Rh was introduced as a promoter either during synthesis by co-precipitation or ex situ by impregnation, allowing to evaluate the influence of Rh location and surface enrichment on the catalytic properties. Rh incorporation in the NiBa catalyst (Ni/Ba = 10/1 and Ni/Rh = 100/1) increased the specific surface area (BET area 64 m
2·g
−1 vs. 55 m
2·g
−1 for NiBa) and reduced the NiO crystallite size from 250.4 Å to 231.5 Å, indicating improved dispersion of the metallic phase. XPS analysis revealed the coexistence of Rh
0 and Rh
3+ species, suggesting that Rh acts as a redox mediator that facilitates hydrogen activation and promotes hydrogen spillover to neighboring Ni sites. Raman and CO
2-TPD results show that Ba-derived domains stabilize carbonate species responsible for CO
2 storage, while Rh enhances catalyst reducibility and modifies the kinetics of carbonate decomposition during the regeneration stage. Transient CO
2–CH
4 pulse experiments demonstrate that the CO
2-SR process proceeds through a dynamic surface cycle involving reversible carbonate formation on Ba-derived basic sites coupled with methane activation on Ni-containing interfacial sites. The results indicate that catalyst performance is governed by a hierarchical surface architecture composed of Ni–O–Ba interfacial domains, reversible Ba–O–Ba carbonate storage sites, and more stable Ba-rich domains. The distribution of these domains, controlled by the Ni/Ba ratio and the dispersion of the metallic phase, determines the reversibility of carbonate formation and the efficiency of the cyclic CO
2 storage–regeneration process.
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