Hydrodeoxygenation of Furfural over Unsupported, SiO2‐supported or Metal‐promoted Mo Carbides: Tunning the Selectivity between 2‐Methylfuran and C10 …
LF Sosa, PM de Souza, RA Rafael… - …, 2024 - Wiley Online Library
ChemCatChem, 2024•Wiley Online Library
The hydrodeoxygenation of furfural (FF) over Mo carbides in liquid phase at 200° C, 30 bar
of H2 for 4 h in 2‐butanol was investigated. Unsupported and SiO2‐supported Mo carbide
with different crystallographic phases (β‐Mo2C/SiO2 and α‐MoC/SiO2), and in the presence
of Cu and Ni as promoters were studied. The reactivation treatment under H2 atmosphere of
the passivated Mo carbides was investigated by XAS. The results show that Mo is present in
different states of oxidation in the passivated catalysts, with more severe oxidation in the …
of H2 for 4 h in 2‐butanol was investigated. Unsupported and SiO2‐supported Mo carbide
with different crystallographic phases (β‐Mo2C/SiO2 and α‐MoC/SiO2), and in the presence
of Cu and Ni as promoters were studied. The reactivation treatment under H2 atmosphere of
the passivated Mo carbides was investigated by XAS. The results show that Mo is present in
different states of oxidation in the passivated catalysts, with more severe oxidation in the …
Abstract
The hydrodeoxygenation of furfural (FF) over Mo carbides in liquid phase at 200 °C, 30 bar of H2 for 4 h in 2‐butanol was investigated. Unsupported and SiO2‐supported Mo carbide with different crystallographic phases (β‐Mo2C/SiO2 and α‐MoC/SiO2), and in the presence of Cu and Ni as promoters were studied. The reactivation treatment under H2 atmosphere of the passivated Mo carbides was investigated by XAS. The results show that Mo is present in different states of oxidation in the passivated catalysts, with more severe oxidation in the bimetallic systems, in which the original carbides are not restored after reactivation. Finally, the product distribution in the HDO of furfural is modified as a function of catalyst oxidation degree. Using the less oxidized Mo carbide (β‐Mo2C), a higher yield to 2‐methylfuran is obtained, while C10 condensation products are formed for the more oxidized catalysts.
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