Supported Vanadium Carbide Catalysts for Reverse Water Gas Shift and Methanol Steam Reforming: Activity, Stability, and Coking Pathways

A series of supported vanadium carbide (VC_<i>x</i>) catalysts were prepared, characterized, and tested for the carbon dioxide and methanol activation via the Reverse Water Gas Shift (RWGS) and Methanol Steam Reforming (MSR) reactions, respectively. Crystallite sizes of VC_<i>x</i> ranging from 9 to 36 nm were obtained depending on the support used (γ-Al₂O₃, SiO₂, CeO₂, ZrO₂ and TiO₂). In both reactions, the supported catalysts exhibited superior performance compared to the bulk VC_<i>x</i> sample. In the RWGS reaction, all catalysts showed high CO selectivity, with VC_<i>x</i>/Al₂O₃ demonstrating the best performance and no significant deactivation after 100 h at 873 K. Under MSR conditions, VC_<i>x</i>/ZrO₂ achieved the highest methanol conversion. However, all catalysts suffered from significant deactivation due to coke formation, with CH₄ as the main product instead of the desired H₂ and CO₂ from full steam reforming. Density Functional Theory (DFT) calculations revealed that methanol decomposition is more facile than CO₂ decomposition on both stoichiometric VC and carbon-deficient V₈C₇ surfaces, particularly in the presence of carbon vacancies, leading to coke formation in the form of partially hydrogenated C_<i>x</i>H_<i>y</i>* species. These findings indicate that VC_<i>x</i> catalysts are more susceptible to coking under MSR than RWGS conditions, in line with experimental observations, and highlight the critical role of the carbide surface structure and vacancy concentration in coke formation.