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
收藏
页数:11
相关论文
共 56 条
[31]   Molecular-level driving forces in lignocellulosic biomass deconstruction for bioenergy [J].
Petridis, Loukas ;
Smith, Jeremy C. .
NATURE REVIEWS CHEMISTRY, 2018, 2 (11) :382-389
[32]   Pretreatment and conversion of lignocellulose biomass into valuable chemicals [J].
Putro, Jindrayani Nyoo ;
Soetaredjo, Felycia Edi ;
Lin, Shi-Yow ;
Ju, Yi-Hsu ;
Ismadji, Suryadi .
RSC ADVANCES, 2016, 6 (52) :46834-46852
[33]   Effective interfacial area in agitated liquid-liquid continuous reactors [J].
Quadros, PA ;
Baptista, CMSG .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (17) :3935-3945
[34]  
Roy R., 2020, CURR RES GREEN SUSTA, V3, DOI [10.1016/j.crgsc.2020.100035, DOI 10.1016/J.CRGSC.2020.100035]
[35]   Chemicals from lignin: an interplay of lignocellulose fractionation, depolymerisation, and upgrading [J].
Schutyser, W. ;
Renders, T. ;
Van den Bosch, S. ;
Koelewijn, S. -F. ;
Beckham, G. T. ;
Sels, B. F. .
CHEMICAL SOCIETY REVIEWS, 2018, 47 (03) :852-908
[36]   Continuous chiral separation of amino acid derivatives by enantioselective liquid-liquid extraction in centrifugal contactor separators [J].
Schuur, Boelo ;
Floure, Joelle ;
Hallett, Andrew J. ;
Winkelman, Jozef G. M. ;
de Vries, Johannes G. ;
Heeres, Hero J. .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2008, 12 (05) :950-955
[37]   Green solvents for sustainable separation processes [J].
Schuur, Boelo ;
Brouwer, Thomas ;
Smink, Dion ;
Sprakel, Lisette M. J. .
CURRENT OPINION IN GREEN AND SUSTAINABLE CHEMISTRY, 2019, 18 :57-65
[38]   Scalable Enantioseparation of Amino Acid Derivatives Using Continuous Liquid-Liquid Extraction in a Cascade of Centrifugal Contactor Separators [J].
Schuur, Boelo ;
Hallet, Andrew J. ;
Winkelman, Jozef G. M. ;
de Vries, Johannes G. ;
Heeres, Hero J. .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2009, 13 (05) :911-914
[39]   Process development for biomass delignification using deep eutectic solvents. Conceptual design supported by experiments [J].
Smink, Dion ;
Kersten, Sascha R. A. ;
Schuur, Boelo .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2020, 164 :86-101
[40]   Comparing multistage liquid-liquid extraction with cold water precipitation for improvement of lignin recovery from deep eutectic solvents [J].
Smink, Dion ;
Kersten, Sascha R. A. ;
Schuur, Boelo .
SEPARATION AND PURIFICATION TECHNOLOGY, 2020, 252