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      Chemical Recovery of γ-Valerolactone/Water Biorefinery

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          Abstract

          We introduce the optimization of the pulping conditions and propose different chemical recovery options for a proven biorefinery concept based on γ-valerolactone (GVL)/water fractionation. The pulping process has been optimized whereby the liquor-to-wood (L:W) ratio could be reduced to 3 L/kg without compromising the pulp properties as raw material for textile fibers production. The recovery of the pulping solvent was performed through combinations of lignin precipitation by water addition, distillation at reduced pressure, and liquid CO 2 extraction. With a two-step lignin precipitation coupled with vacuum distillation, more than 90% of lignin and GVL could be recovered from the spent liquor. However, a significant part of GVL remained unrecoverable in the residue, which was a highly viscous liquid with complicated phase behavior. The recovery by lignin precipitation combined with liquid CO 2 extraction could recover more than 85% GVL and 90% lignin without forming any problematic residue as in the distillation process. The remaining GVL remained in the raffinate containing a low amount of lignin and other compounds, which can be further processed to isolate the GVL and improve the recovery rate.

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          Most cited references37

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          Synthesis of transportation fuels from biomass: chemistry, catalysts, and engineering.

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            γ-Valerolactone—a sustainable liquid for energy and carbon-based chemicals

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              Nonenzymatic sugar production from biomass using biomass-derived γ-valerolactone.

              Widespread production of biomass-derived fuels and chemicals will require cost-effective processes for breaking down cellulose and hemicellulose into their constituent sugars. Here, we report laboratory-scale production of soluble carbohydrates from corn stover, hardwood, and softwood at high yields (70 to 90%) in a solvent mixture of biomass-derived γ-valerolactone (GVL), water, and dilute acid (0.05 weight percent H2SO4). GVL promotes thermocatalytic saccharification through complete solubilization of the biomass, including the lignin fraction. The carbohydrates can be recovered and concentrated (up to 127 grams per liter) by extraction from GVL into an aqueous phase by addition of NaCl or liquid CO2. This strategy is well suited for catalytic upgrading to furans or fermentative upgrading to ethanol at high titers and near theoretical yield. We estimate through preliminary techno-economic modeling that the overall process could be cost-competitive for ethanol production, with biomass pretreatment followed by enzymatic hydrolysis.
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                Author and article information

                Journal
                Ind Eng Chem Res
                Ind Eng Chem Res
                ie
                iecred
                Industrial & Engineering Chemistry Research
                American Chemical Society
                0888-5885
                18 October 2018
                07 November 2018
                : 57
                : 44
                : 15147-15158
                Affiliations
                []Department of Bioproducts and Biosystems, Aalto University , Espoo, Finland
                []Department of Chemical and Metallurgical Engineering, Aalto University , Espoo, Finland
                [§ ]VTT Technical Research Centre of Finland, Ltd., Espoo, Finland
                Author notes
                Article
                10.1021/acs.iecr.8b03723
                6237546
                30449950
                b5df8790-ce0c-4e01-9474-7d7b1f005bde
                Copyright © 2018 American Chemical Society

                This is an open access article published under a Creative Commons Attribution (CC-BY) License, which permits unrestricted use, distribution and reproduction in any medium, provided the author and source are cited.

                History
                : 06 August 2018
                : 18 October 2018
                : 04 October 2018
                Categories
                Article
                Custom metadata
                ie8b03723
                ie-2018-03723r

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