4.8 Article

Purification and Fractionation of Lignin via ALPHA: Liquid-Liquid Equilibrium for the Lignin-Acetic Acid-Water System

Journal

CHEMSUSCHEM
Volume -, Issue -, Pages -

Publisher

WILEY-V C H VERLAG GMBH
DOI: 10.1002/cssc.202300989

Keywords

fractionation and purification; lignin; liquid-liquid equilibrium; renewable resources; sustainable chemistry

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The study focuses on identifying the regions of liquid-liquid equilibrium (LLE) for lignin purification and fractionation using the Aqueous Lignin Purification with Hot Agents (ALPHA) process. Pseudo-ternary phase diagrams were used to map out the lignin-acetic acid-water system at different temperatures and solvent: feed lignin mass ratios. The distribution of lignin and impurities between the two liquid phases was also measured.
In order to effectively practice the Aqueous Lignin Purification with Hot Agents (ALPHA) process for lignin purification and fractionation, the temperatures and feed compositions where regions of liquid-liquid equilibrium (LLE) exist must be identified. To this end, pseudo-ternary phase diagrams for the lignin-acetic acid-water system were mapped out at 45-95 degrees C and various solvent: feed lignin mass ratios (S : F). For a given temperature, the accompanying SL (solid-liquid), SLL (solid-liquid-liquid), and one-phase regions were also located. For the first time, ALPHA using acetic acid (AcOH)-water solution was applied to a lignin recovered via the commercial LignoBoost process. In addition to determining tie-line compositions for the two regions of LLE that were discovered, the distribution of lignin and key impurities (the latter can negatively impact lignin performance for materials applications) between the two liquid phases was also measured. As a representative example, lignin isolated in the lignin-rich phase was reduced 7x in metals and 4x in polysaccharides by using ALPHA with a feed solvent composition of 50-55 % AcOH and an S : F of 6 : 1, with said lignin being obtained at a yield of 50-70 % of the feed lignin and having a molecular weight triple that of the feed. Pseudo-ternary phase diagrams for the lignin-acetic acid-water system were mapped out at 45-95 degrees C and various solvent: feed lignin mass ratios (S : F), with the objective being to locate regions of liquid-liquid equilibrium (LLE) where lignin purification and fractionation could be practiced via the ALPHA process.image

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