Continuous liquid-liquid extraction to recover lignin and furanics from lactic acid: Choline chloride deep eutectic solvent after cooking of spruce

被引:4
作者
Gholami, Mahsa [1 ]
Tijburg, Jochem M. [1 ]
Schuur, Boelo [1 ]
机构
[1] Univ Twente, Fac Sci & Technol, Sustainable Proc Technol, POB 217, NL-7500 AE Enschede, Netherlands
关键词
Countercurrent LLX; Deep Eutectic Solvent (DES); Lignin recovery; Furanic recovery; CONTINUOUS CHIRAL SEPARATION; IONIC LIQUID; BIOMASS DELIGNIFICATION; PERFORMANCE; FRACTIONATION;
D O I
10.1016/j.seppur.2024.126526
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Lactic acid: choline chloride mixed in a 10:1 ratio is known to be a suitable delignification solvent. This deep eutectic solvent (DES) can produce lignin and hemicellulose derivatives as byproducts to cellulose. Hemicellulose byproducts include furanic compounds like furfural and 5-HMF. Sustainable and economically viable fractionation of lignin and furanics from the DES is required. After removing the larger lignin (>2500 Da) through water precipitation, non -precipitated molecules such as smaller lignin molecules and furanics can be retrieved through liquid-liquid extraction (LLX). In a previous investigation on solvent extraction conducted in a batch mode, 2MTHF and guaiacol have been identified as potential solvents. This study investigates the application of a continuous centrifugal contactor separator (CCCS) and Karr reciprocating plate column for LLX from aqueous DES -black liquor remaining after water -precipitation, was employed as the feed. Single stage CCCS operation exhibited extraction yields close to equilibrium yields, thus almost 100 % extraction efficiency. Performing a two -stage countercurrent LLX process via CCCS showed increased removal for furfural and 5-HMF extraction, while lignin extraction yield remained at about 90 %, comparable to single -stage extraction. Karr column countercurrent extraction with different solvent -to -feed ratios (0.5 and 1) yielded approximately 99 % furfural extraction. For 2-MTHF system, 5-HMF achieved 99 % extraction yield at a solvent -to -feed ratio of 1, while guaiacol yielded around 90 % at both solvent -to -feed ratios. However, 5-HMF extraction using 2-MTHF with a ratio of 0.5 required more stages. For guaiacol improvement of lignin extraction applying more stages was hindered by hydrophobic characteristic of residual lignin in raffinate. Conversely, 2-MTHF's multi -stage approach enhanced smaller lignin extraction influenced by increased lactic acid leaching into solvent. Both CCCS and Karr column methods proved viable for counter -current extraction with both solvents.
引用
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页数:11
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