Reduction of Furfural to Furfuryl Alcohol in Liquid Phase over a Biochar-Supported Platinum Catalyst
Ariadna Fuente-Hernández,
Roland Lee,
Nicolas Béland,
Ingrid Zamboni,
Jean-Michel Lavoie
Affiliations
Ariadna Fuente-Hernández
Industrial Research Chair on Cellulosic Ethanol and Biocommodities (CRIEC-B), Department of Chemical & Biotechnological Engineering, Université de Sherbrooke, Sherbrooke, QC J1K2R1, Canada
Roland Lee
Industrial Research Chair on Cellulosic Ethanol and Biocommodities (CRIEC-B), Department of Chemical & Biotechnological Engineering, Université de Sherbrooke, Sherbrooke, QC J1K2R1, Canada
Nicolas Béland
Industrial Research Chair on Cellulosic Ethanol and Biocommodities (CRIEC-B), Department of Chemical & Biotechnological Engineering, Université de Sherbrooke, Sherbrooke, QC J1K2R1, Canada
Ingrid Zamboni
Industrial Research Chair on Cellulosic Ethanol and Biocommodities (CRIEC-B), Department of Chemical & Biotechnological Engineering, Université de Sherbrooke, Sherbrooke, QC J1K2R1, Canada
Jean-Michel Lavoie
Industrial Research Chair on Cellulosic Ethanol and Biocommodities (CRIEC-B), Department of Chemical & Biotechnological Engineering, Université de Sherbrooke, Sherbrooke, QC J1K2R1, Canada
In this work, the liquid phase hydrogenation of furfural has been studied using a biochar-supported platinum catalyst in a batch reactor. Reactions were performed between 170 °C and 320 °C, using 3 wt % and 5 wt % of Pt supported on a maple-based biochar under hydrogen pressure varying from 500 psi to 1500 psi for reaction times between 1 h and 6 h in various solvents. Under all reactive conditions, furfural conversion was significant, whilst under specific conditions furfuryl alcohol (FA) was obtained in most cases as the main product showing a selectivity around 80%. Other products as methylfuran (MF), furan, and trace of tetrahydrofuran (THF) were detected. Results showed that the most efficient reaction conditions involved a 3% Pt load on biochar and operations for 2 h at 210 °C and 1500 psi using toluene as solvent. When used repetitively, the catalyst showed deactivation although only a slight variation in selectivity toward FA at the optimal experimental conditions was observed.