Hydrodeoxygenation of Furfural over Unsupported, SiO2‐supported or Metal‐promoted Mo Carbides: Tunning the Selectivity between 2‐Methylfuran and C10 Furoins Diesel Precursors

Author:

Sosa Letícia F.1,de Souza Priscilla M.2,Rafael Raphaela A.2,Wojcieszak Robert2,Marceau Eric2,Paul Sébastien2,Briois Valérie3,Noronha Fabio B.245,Toniolo Fabio S.1ORCID

Affiliation:

1. Chemical Engineering Program of COPPE/UFRJ Federal University of Rio de Janeiro P.O. Box 68502 CEP 21941-972 Rio de Janeiro Brazil

2. UCCS – Unité de Catalyse et Chimie du Solide Univ. Lille, CNRS, Centrale Lille, Univ. Artois, UMR 8181 F-59000 Lille France

3. Synchrotron SOLEIL L'Orme des Merisiers, Saint-Aubin, BP 48 91192 Gif-sur-Yvette Cedex France

4. Catalysis, Biocatalysis and Chemical Processes Division National Institute of Technology Av. Venezuela 82 20081-312 Rio de Janeiro, RJ Brazil

5. Chemical Engineering Department Military Institute of Engineering Praça Gal. Tibúrcio 80 22290-270 Rio de Janeiro, RJ Brazil

Abstract

AbstractThe 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.

Publisher

Wiley

Subject

Inorganic Chemistry,Organic Chemistry,Physical and Theoretical Chemistry,Catalysis

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