Abstract Dry reforming of methane (DRM) is a viable strategy for converting two potent greenhouse gases, CH 4 and CO 2 , into synthesis gas (H 2 and CO), which serves as a precursor for methanol, hydrogen, and Fischer–Tropsch fuels. However, catalyst deactivation due to carbon deposition and sintering remains a major challenge. This study examines Ni/γ-Al 2 O 3 catalysts individually promoted with Rh, La, Sm, or Au to evaluate their role in the DRM for syngas production. Detailed characterizations (BET, UV–Vis, TGA, SEM, TEM, XRD, XPS, and cyclic TPR-TPD-TPR) revealed that Rh and La improved Ni dispersion and reducibility. Rh-promoted catalysts showed the best catalytic performance, stability, and the least carbon accumulation, as confirmed by catalyst activity studies, CHN, TGA, and TPR data. Process optimization via central composite design predicted 98% CH 4 and 97% CO 2 conversion at 828.5 °C and an H 2 /CO ratio of 1.038, which was validated by experimental runs performed under these conditions depicting very good agreement with the results predicted by the model.
Bentalib et al. (Sat,) studied this question.