Deactivation and Regeneration Study of a Co-Promoted MoO3 Catalyst in Hydrogenolysis of Dibenzofuran

MoO3 Nanobelt-Modified HMCM-49 Zeolite with Enhanced Dispersion of Mo Species and Catalytic Performance for Methane Dehydro-Aromatization

The methane dehydro-aromatization reaction (MDA) is a promising methane valorization process due to the conversion of methane to value-added aromatics (benzene, toluene and naphthalene). However, one of the major disadvantages of utilizing zeolite in MDA is that the catalyst is rapidly inactivated due to coke formation, which eventually causes the activity and aromatic selectivity to decrease. Consequently, the process is not conducive to large-scale industrial applications. The reasonable control of Mo site distribution on the zeolite surface is the key factor for partially inhibiting the coking of the catalyst and improving stability. Here, MoO₃ nanobelts can be used for alternative Mo precursors to prepare MDA catalysts. Catalysts modified with MoO₃ nanobelts present higher activity (13.4%) and benzene yield (9.2%) than those catalysts loaded with commercial MoO₃.