ASABE Technical Library - Abstract

Abstract.

The dry reforming of methane (DRM) with CO₂ has been widely studied due to its important applications in producing of syngas (CO + H₂), removal of two greenhouse gases, and upgrading of biogas (mainly composed of CH₂and CO₂) into value added chemicals. Compared to the noble metal catalysts, the nickel-based catalyst is suitable for industrial scaled-up DRM due to its high activity and low cost. However, nickel-based catalysts have been encountering a significant challenge that is the active metal sintering and coke deposition, leading to the catalyst deactivation and then the poor stability. Nevertheless, it has been reported that the deactivation of nickel catalysts can be suppressed by adding promoters like strong Lewis bases with the enhancement of chemisorb CO₂, and like lanthanide elements with the capacity of oxygen storage and release. Aluminum oxide is a commonly applied catalyst carrier own to its good pore size dispersion, high specific surface area and high mechanic strength. Herein, we report that the bimodal NiCeMgAl catalysts with different NiO-loading were synthesized by the refluxed co-precipitation method and were evaluated for DRM catalytic performance. The sample containing 15wt% NiO-loading (Ni₁₅CeMgAl) was found to be active enough at 750 °C with a high CH₄ conversion of 96.5%. Ni₁₅CeMgAl catalyst kept its bimodal porosity after reduction and DRM reaction. The evolution of the Ni₁₅CeMgAl catalyst before and after the DRM reaction was investigated by BET, XRD, TEM, and TGA techniques. A schema of the DRM reaction on the bimodal Ni₁₅CeMgAl catalyst was proposed, and the correlation between the structure evolution and catalytic performance change was also discussed.