Abstract:Lignocellulosic biomass as a potential alternative to fossil resource for the production of valuable chemicals and fuels has attracted substantial attention, while reducing the recalcitrance of lignocellulosic biomass is still challenging due to the complex and cross-linking structure of biomass. Solvent system plays important roles in the pretreatment of lignocellulose, enabling the transformation of solid biomass to liquid fluid with better mass and heat transfer, as well as in the selective formation of tar… Show more
“…In CELF, a high temperature (>150 °C) is still needed to remain outside the known miscibility gap (71.8 °C to 137.1 °C) [ 89 ] of the THF(tetrahydrofuran)/H 2 O mixture. Generally, approximately 85–90% lignin from plant biomass can be solubilized and fractionated, because the molecular weight of lignin is dramatically reduced and the cross-condensation reaction is also minimized under THF/H 2 O mixture treatment [ 90 ]. The nearly pure lignin product without sugar and ash can be precipitated after THF solvent evaporation, which is a potential feedstock for promoting the hydrolysis of cellulose [ 91 ].…”
Section: Recent Advances In Lignocellulosic Biomass Treatment Processesmentioning
Plant biomass is a highly abundant renewable resource that can be converted into several types of high-value-added products, including chemicals, biofuels and advanced materials. In the last few decades, an increasing number of biomass species and processing techniques have been developed to enhance the application of plant biomass followed by the industrial application of some of the products, during which varied technologies have been successfully developed. In this review, we summarize the different sources of plant biomass, the evolving technologies for treating it, and the various products derived from plant biomass. Moreover, the challenges inherent in the valorization of plant biomass used in high-value-added products are also discussed. Overall, with the increased use of plant biomass, the development of treatment technologies, and the solution of the challenges raised during plant biomass valorization, the value-added products derived from plant biomass will become greater in number and more valuable.
“…In CELF, a high temperature (>150 °C) is still needed to remain outside the known miscibility gap (71.8 °C to 137.1 °C) [ 89 ] of the THF(tetrahydrofuran)/H 2 O mixture. Generally, approximately 85–90% lignin from plant biomass can be solubilized and fractionated, because the molecular weight of lignin is dramatically reduced and the cross-condensation reaction is also minimized under THF/H 2 O mixture treatment [ 90 ]. The nearly pure lignin product without sugar and ash can be precipitated after THF solvent evaporation, which is a potential feedstock for promoting the hydrolysis of cellulose [ 91 ].…”
Section: Recent Advances In Lignocellulosic Biomass Treatment Processesmentioning
Plant biomass is a highly abundant renewable resource that can be converted into several types of high-value-added products, including chemicals, biofuels and advanced materials. In the last few decades, an increasing number of biomass species and processing techniques have been developed to enhance the application of plant biomass followed by the industrial application of some of the products, during which varied technologies have been successfully developed. In this review, we summarize the different sources of plant biomass, the evolving technologies for treating it, and the various products derived from plant biomass. Moreover, the challenges inherent in the valorization of plant biomass used in high-value-added products are also discussed. Overall, with the increased use of plant biomass, the development of treatment technologies, and the solution of the challenges raised during plant biomass valorization, the value-added products derived from plant biomass will become greater in number and more valuable.
“…In addition, H2O was revealed to be a nucleophile agent to break the linkages between lignin and hemicellulose (e.g., hydrogen bonds, ether and ester bonds) owing to its higher hydrogen bond acceptor ability compared to THF. 37 For pretreatment using DMI/H2O at lower ratio e.g., 4:1, decreased lignin removal efficiency was observed which was echoed by findings for THF/H2O 37 and GVL/H2O 38 co-solvent systems. This is probably due to the reduced cleavage activity of sulfuric acid and the decreased dissolving ability of solvent due to the presence of water at a higher percentage.…”
Section: Fig 1 Schematic Diagram Of Dmi/h2o Co-solvent Pretreatmentmentioning
confidence: 82%
“…Similar phenomena were reported for deep eutectic solvent (DES) and THF. 36,37 H2O in these cosolvents (e.g., THF/H2O) is considered as an efficient plasticizer favoring organic solvent diffusion into the compact lignin complexes, leading to the solubilization of lignin in solvent-water mixture.…”
Section: Fig 1 Schematic Diagram Of Dmi/h2o Co-solvent Pretreatmentmentioning
confidence: 99%
“…For example, MeTHF, EAC and GVL dissolved S-and G-type lignin, while THF solvent showed high selectivity to fractionate and solubilize lignin with G and H units. 37 Table 1. Semi-quantitative information for subunits and interunit linkage in lignin before and after DMI/H2O co-solvent pretreatment.…”
An efficient and sustainable pretreatment, such as organosolv pretreatment that produces high-quality lignin and highly digestible carbohydrates, could enable the potential complete utilization of lignocellulosic biomass. Demand for bio-based solvents with a high boiling point, low viscosity, and negligible toxicity is increasing. Herein, we report the use of dimethyl isosorbide (DMI) as a solvent to fractionate lignocellulosic biomass into its main components for the first time. High lignin removal efficiency (91.2%) with good cellulose retention (around 80%) could be achieved during the pretreatment of Eucalyptus by DMI/H2O co-solvents under a mild condition. A near-complete cellulose conversion to its monosaccharide could be realized at a relatively low enzyme loading of 20 FPU g−1 glucan. The addition of water could suppress the condensation of lignin, yielding high-quality lignin with a good fraction of β-O-4 linkages reserved (24.8%) and homogeneous molecular weight (Đ<2) suitable for depolymerization to mono-aromatic chemicals. Besides its highly digestible nature, the high quality of the cellulose-rich residue is also demonstrated from a material perspective. A more efficient fibrillation of obtained pulp to nanocellulose was developed, leading to a promising potential of energy saving compared to the traditional bleaching pathway. Overall, this work developed a mild pretreatment technology as a potential basis for a green and closed-loop biorefinery concept for converting lignocellulosic biomass to multiple products (high-quality lignin, fermentable sugars, or functional materials).
“…Especially, the H 2 O-THF consisted biphasic system is frequently employed as reaction media for conversion of cellulose with impressive HMF yields (Cao et al, 2019;Jing et al, 2018;Shen et al, 2020;Shi et al, 2013;Yang et al, 2012). Compared with other O-contained organic solvents, the boiling point of THF was only 66 ℃, so THF could be easily separated with products for recycling (Li et al, 2020). Besides, THF can be synthesized from biomass-based derivatives, such as furfural and 1,4-butanediol (Lange & Wadman, 2020), thus is a promising renewable and green solvent.…”
A simple and efficient biphasic system consisting of H2O, tetrahydrofuran (THF), cyclohexane (CHX) and Al2(SO4)3 was employed to convert cellulose into 5-hydroxymethylfurfural (HMF) with high yield of 71.2%. The real volumes of organic phase (Vorg) and aqueous phase (Vaque) of the biphasic system at reaction temperature were measured to found out that over 80% of the added H2O was dissolved into the organic phase at reaction temperature, leading to high Vorg/Vaque (over 44/1) and high concentration of Al2(SO4)3 (over 0.34 g/mL) in aqueous phase. The high concentration of Al2(SO4)3 in aqueous phase could efficiently catalyze the conversion of cellulose into HMF, while the high Vorg/Vaque could protect the formed HMF from rehydration, all of which are responsible for the high efficiency of the system on conversion of cellulose into HMF. The addition of CHX into reaction mixture could decrease the solubility of Al2(SO4)3 and H2O in the organic phase, which could improve the stability of HMF in the reaction system, resulting higher yield of HMF from cellulose. Because of the high Vorg/Vaque of the reaction system, one microemulsion-like system and liquid film catalytic model are proposed for the cellulose-to-HMF process.
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