Reduction of Furfural to Furfuryl Alcohol in Liquid Phase over a Biochar-Supported Platinum Catalyst

被引:32
|
作者
Fuente-Hernandez, Ariadna [1 ]
Lee, Roland [1 ]
Beland, Nicolas [1 ]
Zamboni, Ingrid [1 ]
Lavoie, Jean-Michel [1 ]
机构
[1] Univ Sherbrooke, Dept Chem & Biotechnol Engn, Ind Res Chair Cellulos Ethanol & Biocommod CRIEC, Sherbrooke, PQ J1K 2R1, Canada
关键词
biochar; furfural; furfuryl alcohol (FA); hydrogenation; maple; platinum catalyst; SELECTIVE HYDROGENATION; ACID; CONVERSION; XYLOSE;
D O I
10.3390/en10030286
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
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 degrees C and 320 degrees 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 degrees 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.
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页数:10
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