Investigates the impact of support calcination on nickel accessibility and catalytic performance in titanium dioxide for dry methane reforming, highlighting its implications.
The influence of support calcination temperature on pore evolution, nickel (Ni) accessibility, and catalytic behavior was investigated using Ni-loaded titanium dioxide (TiO₂) catalysts for the dry reforming of methane (DRM). The TiO₂ supports calcined between 400°C and 1200°C showed a structural transition from a hierarchical mesoporous-macroporous framework to predominantly macroporous and eventually plate-like morphologies. Despite similar Ni loading (1.1-1.2 wt%), reducibility, and Ni particle size (∼60-86 nm), the accessibility of Ni sites varied significantly due to calcination-induced structural evolution. Notably, the most active catalyst, Ni/TiO₂-HR-C12, achieved a high initial CH₄ conversion of ∼93% and an H₂/CO ratio of ∼0.95 at 800°C. It also exhibited superior stability during 50 h at 700°C. Low-temperature-calcined support allowed Ni precursors to infiltrate mesopores, which collapsed during subsequent 900°C calcination, leading to Ni encapsulation and poor activity. In contrast, high-temperature-calcined supports (≥900°C) generated thermally stable structures that prevented Ni infiltration, preserving surface-exposed Ni sites. This high site accessibility is a decisive factor governing the enhanced DRM performance. These findings demonstrate that support thermal stability and Ni accessibility outweigh mesoporosity or Ni particle size, offering insights for designing thermally robust oxide-supported catalysts.
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Choi et al. (2026) studied this question.
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