Kinetic and mechanistic insights into hydrogenolysis of lignin to monomers in a continuous flow reactor

被引:68
作者
Li, Yanding [1 ,2 ]
Demir, Benginur [2 ,3 ]
Ramos, Leida M. Vazquez [2 ,3 ]
Chen, Mingjie [2 ]
Dumesice, James A. [2 ,3 ]
Ralph, John [1 ,2 ,4 ]
机构
[1] Univ Wisconsin, Dept Biol Syst Engn, Madison, WI 53706 USA
[2] Univ Wisconsin, DOE Great Lakes Bioenergy Res Ctr, Madison, WI 53706 USA
[3] Univ Wisconsin, Dept Chem & Biol Engn, Madison, WI 53706 USA
[4] Univ Wisconsin, Dept Biochem, Madison, WI 53706 USA
关键词
REDUCTIVE CATALYTIC FRACTIONATION; MODEL COMPOUNDS; LIGNOCELLULOSE FRACTIONATION; DELIGNIFICATION MECHANISM; DEPOLYMERIZATION; OXIDATION; CLEAVAGE; HYDROLYSIS; REACTIVITY; CONVERSION;
D O I
10.1039/c9gc00986h
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Industrial biorefineries remain limited due to inefficient valorization of their lignin streams. Rarely can a lignin depolymerization method be combined with a current polysaccharide-centric biorefinery process. Hydrogenolysis is among the more promising methods for depolymerizing lignin on an industrial scale. We performed reaction kinetics and mechanistic studies on lignin model compounds to understand lignin hydrogenolysis pathways, demonstrating that lignin end-units and internal units react significantly differently. Understanding the reaction mechanism and its sensitivity to variables helped us establish a continuous lignin upgrading process from various fractionated lignins. Near-theoretical yields of lignin platform monomers with > 80% overall product selectivity were obtained in a continuous hydrogenolysis process using a Pd/C catalyst.
引用
收藏
页码:3561 / 3572
页数:12
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