This study aimed to investigate the effect of carbon derived from glucose (C) on the physicochemical characteristics and catalytic activity of Ni, supported over SiO₂, ZSM-5, and TiO₂ in methane dry reforming. Among the Ni catalysts without C, Ni/SiO₂ exhibited the highest CH₄-CO₂ conversion and stability at all experimented temperatures. On the other hand, the C-incorporated catalysts prepared by glucose impregnation, followed by pyrolysis, showed dissimilar performances. C improved the stability of Ni/SiO₂ in the reforming at 650 °C and 750 °C and increased the CH₄ and CO₂ conversion to the level close to the thermodynamic equilibrium at 850 °C. However, this element did not substantially affect the activity of Ni/ZSM-5 and exerted a retarding effect on Ni/TiO₂. Characterizations with H₂-TPD, XRD, EXAFS, and STEM-EDS revealed that the different influences of C by the supports were attributed to the extent of metal dispersion and metal-support interaction.