Abstract
Reductive catalytic fractionation (RCF) is a promising lignin-first biorefining strategy that selectively extracts and depolymerizes lignin from whole biomass. Flow-through (FT)-RCF enables physical separation 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 subsequent 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 energy driver to enable this process at scale, can be reduced by recycling lignin oil between RCF reactions.
Original language | American English |
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Pages (from-to) | 1859-1875 |
Number of pages | 17 |
Journal | Joule |
Volume | 6 |
Issue number | 8 |
DOIs | |
State | Published - 17 Aug 2022 |
Bibliographical note
Publisher Copyright:© 2022 Elsevier Inc.
NREL Publication Number
- NREL/JA-2A00-81807
Keywords
- flow-through
- lignin valorization
- lignocellulosic biomass
- process intensification
- reaction engineering
- reductive catalytic fractionation
- solvent recycling
- solvent reduction