4.8 Article

Fractionation of lignocellulosic biomass using the OrganoCat process

Journal

GREEN CHEMISTRY
Volume 17, Issue 6, Pages 3533-3539

Publisher

ROYAL SOC CHEMISTRY
DOI: 10.1039/c4gc02534b

Keywords

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Funding

  1. Excellence Initiative of the German Research Foundation
  2. Bioeconomy Science Center (BioSC)
  3. Ministry of Innovation, Science and Research within the framework of the NRW Strategieprojekt BioSC [313/323-400-002 13]

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The fractionation of lignocellulose in its three main components, hemicellulose, lignin and cellulose pulp can be achieved in a biphasic system comprising water and bio-based 2-methyltetrahydrofuran (2-MeTHF) as solvents and oxalic acid as catalyst at mild temperatures (up to 140 degrees C). This so-called Organo-Cat concept relies on selective hemicellulose depolymerization to form an aqueous stream of the corresponding carbohydrates, whereas solid cellulose pulp remains suspended and the disentangled lignin is to a large extent extracted in situ with the organic phase. In the present paper, it is demonstrated that biomass loadings of 100 g L-1 can be efficiently fractionated within 3 h whereby the mild conditions assure that no significant amounts of by-products (e.g. furans) are formed. Removing the solid pulp by filtration allows to re-use the water and organic phase without product separation in repetitive batch mode. In this way, (at least) 400 g L-1 biomass can be processed in 4 cycles, leading to greatly improved biomass-to-catalyst and biomass-to-solvent ratios. Economic analysis of the process reveals that the improved biomass loading significantly reduces capital and energy costs in the solvent recycle, indicating the importance of process integration for potential implementation. The procedure was successfully scaled-up from the screening on bench scale to 3 L reactor. The feedstock flexibility was assessed for biomasses containing moderate-to-high hemicellulose content.

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