This work studies the behavior of a manganese dioxide catalyst during the total oxidation of methanethiol.
Modifications of the working γ-MnO2 catalyst were characterized by XPS, XRD, DRIFTS, and potentiometric
measurements after reactions at different durations and at different temperatures. At temperatures below 200
°C, sulfur adsorbs on γ-MnO2 in the form of sulfate species and poisons CH3SH adsorption sites. Accordingly,
the methanethiol conversion is strongly inhibited. At higher temperatures (260−280 °C), γ-MnO2 is strongly
reduced and is converted to a moderately active manganese sulfate phase while the reaction proceeds. This
contribution also shows that the activity and selectivity of the manganese sulfate phase formed in situ at high
temperature are comparable to those of a commercial manganese sulfate. The variation of the reaction
temperature between 280 and 150 °C controls the reversible hydration/dehydration of the manganese sulfate
phase and its associated activation/deactivation. This important change in activity is accompanied by a change
in the main byproduct formation. At 280 °C, the dehydrated manganese sulfate phase is fairly active and
favors the production of dimethyl disulfide. On the contrary, the hydrated phase that exists only in the lower-temperature region is much more reactive and promotes the production of methanol.