Abstract

Abstract VMCM-41 catalysts, prepared at different hydrothermal ageing times, were applied for the selective oxidation of methane to formaldehyde. An increase in hydrothermal ageing time leads to higher V content as well as higher content of oligomeric VOx species in the fresh catalysts. The VMCM-41 catalysts undergo structural changes on stream at 650 °C, positively affecting the catalytic performance. A formaldehyde selectivity up to 38% at methane conversion of about 4% was achieved over a catalyst synthesized with hydrothermal ageing time of 3 h, which corresponds to a high formaldehyde production rate of rCH2O = 829 h−1. In contrast, V/MCM-41 prepared via a surface sensitive grafting method showed only a rCH2O of about 323 h−1 under the same conditions. Factors for the superior behavior of VMCM-41 are i) the generation of monomeric VOx on stream which promote formaldehyde formation as well as ii) lower acidities of the restructured catalysts reducing further formaldehyde decomposition.

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