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Microwave (MW) methodology has opened up new opportunities for chemical reactions by providing novel routes that are not practical by conventional heating. This paper reports on M–Mo bimetallic catalysts (M = Co or Cu) supported on TiO 2 for methane reforming, i.e., dry reforming of methane (DRM) and bi-reforming of methane under MW irradiation. Experimental results displayed outstanding activity of such M–Mo/TiO 2 catalysts, on which high reaction efficiency of methane reforming can be sustained at a much lower MW power of 100 W compared to literature results of 200 W. The molar ratio of M/Mo at 1.0 (CoMo1 and CuMo1) displayed the highest catalytic activity for MW-assisted methane reforming under all tested conditions. For DRM, about 81% CH 4 and 86% CO 2 were converted to syngas with a H 2 /CO ratio of 0.9 over the CoMo1 catalyst while the CuMo1 catalyst translated 76% CH 4 and 62% CO 2 into syngas with a H 2 /CO ratio of 0.8. In the presence of H 2 O (steam), the H 2 /CO ratio higher than 2, i.e., 2.2, could be obtained over the Co–Mo catalyst with an input steam-to-methane (S/C) molar ratio of 0.1, while the CuMo1 counterpart required an S/C of 0.2 introduced into the feed to produce such a syngas ratio (H 2 /CO) of 2.1. The reason behind the excellent performance of the Co–Mo/TiO 2 catalyst is the good exposure of the well-defined hexagonal MW absorber. Meanwhile, the formation of a high dielectric layer of MoO 2 surrounding active Cu 0 can promote the MW absorption of the Cu–Mo/TiO 2 catalyst and thereby enhance its catalytic performance. The Co–Mo catalyst exhibited better activity than the Cu–Mo samples given that the magnetic properties of Co particles led to a higher MW absorption ability. Both M–Mo/TiO 2 catalysts exhibited brilliant stability under MW irradiation.
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Nguyen et al. (2020) studied this question.
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