Multi-pass flow-through reductive catalytic fractionation

被引:37
作者
Jang, Jun Hee [1 ,2 ]
Brandner, David G. [1 ,2 ]
Dreiling, Reagan J. [1 ,2 ]
Ringsby, Arik J. [1 ]
Bussard, Jeremy R. [1 ]
Stanley, Lisa M. [1 ]
Happs, Renee M. [1 ]
Kovvali, Anjaneya S. [3 ]
Cutler, Joshua I. [4 ]
Renders, Tom [5 ]
Bielenberg, James R. [3 ]
Roman-Leshkov, Yuriy [6 ]
Beckham, Gregg T. [1 ,2 ,3 ]
机构
[1] Natl Renewable Energy Lab, Renewable Resources & Enabling Sci Ctr, Golden, CO 80401 USA
[2] Oak Ridge Natl Lab, Ctr Bioenergy Innovat, Oak Ridge, TN 37830 USA
[3] ExxonMobil Res & Engn Co, Clinton, NJ 08809 USA
[4] ExxonMobil Chem Co, Baytown, TX 77520 USA
[5] Katholieke Univ Leuven, Ctr Sustainable Catalysis & Engn, Heverlee, Belgium
[6] MIT, Dept Chem Engn, Cambridge, MA 02139 USA
关键词
LIGNOCELLULOSE FRACTIONATION; LIGNIN DEPOLYMERIZATION; VALORIZATION; CHEMICALS; PLATFORM; BIOMASS;
D O I
10.1016/j.joule.2022.06.016
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Reductive catalytic fractionation (RCF) is a promising lignin-first bio-refining strategy that selectively extracts and depolymerizes lignin from whole biomass. Flow-through (FT)-RCF enables physical sepa-ration of the biomass and catalyst, but this process configuration typically operates at high solvent-to-biomass ratios. Here, we demonstrate multi-pass FT-RCF, wherein the lignin-enriched solvent obtained after an initial FT-RCF step is recycled and used in subse-quent FT-RCF without intermediate lignin recovery. Multi-pass FT-RCF reduces the solvent-to-biomass ratio from 48 to 1.9 L/kg, which is a lower solvent loading than is accessible in batch reactors, without negative impacts on delignification and monomer yield with up to 12 wt % lignin in the solvent. Overall, this work demonstrates that solvent demand in RCF processes, which is a key cost and en-ergy driver to enable this process at scale, can be reduced by recy-cling lignin oil between RCF reactions.
引用
收藏
页码:1859 / 1875
页数:18
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