# Revisiting organosolv strategies for sustainable extraction of valuable lignin

Marie E Vuillemin, María Catalina Quesada-Salas, Caroline Hadad, Jordane

Jasniewski, Eric Husson, Catherine Sarazin

► To cite this version:

Marie E Vuillemin, María Catalina Quesada-Salas, Caroline Hadad, Jordane Jasniewski, Eric Husson, et al.. Revisiting organosolv strategies for sustainable extraction of valuable lignin: the CoffeeCat process. RSC Sustainability, 2023, 4, 10.1039/d3su00050h. hal-04107140

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# Revisiting organosolv strategies for sustainable extraction of valuable lignin: the CoffeeCat process†

Marie E. Vuillemin, ID a María Catalina Quesada-Salas, a Caroline Hadad, bd
Jordane Jasniewski, ID c Eric Husson* a and Catherine Sarazin ID * a

An innovative and sustainable strategy for the selective extraction of lignin from lignocellulosic biomass has been designed, namely the CoffeeCat process, in which only green solvents and reagents are required: (i) water, (ii) 2-methyltetrahydrofuran-3-one (coffee furanone) recognized as a food grade ingredient and readily biodegradable and (iii) glutamic acid. Two fractions have been isolated from *Miscanthus x giganteus*, the delignified fraction (DL-glu) and the enriched-lignin fraction (L-glu). Competitive extraction yields of 27% and 43% of enriched-lignin fractions were respectively obtained at 140 °C (L-glu-140) and 180 °C (L-glu-180), based on the lignin content of the original biomass. The structural properties of these lignins were characterized by spectroscopic (FTIR and NMR), microscopic (SEM) and separative (SEC-MALLS) methods. Compared to other processes described in the literature, our strategy involved the isolation of lignin fractions with high purity (up to 84%). Both fractions have been valorized: (i) the DL-glu fractions have been subjected to ionic liquid pretreatment and subsequent enzymatic hydrolysis leading to a total depolymerization of the constitutive cellulose (99%) and to an efficient conversion of hemicellulose into xylose (70%); (ii) the L-glu fractions have been used to produce lignin nanoparticles (LNPs) in a mixture of 2-methyltetrahydrofuran-3-one/water (1/110 v/v). The size distribution (272 ± 9 nm and 472 ± 6 nm), charge (−29.2 ± 0.8 mV and −20.8 ± 0.4 mV) and regular spherical shape of these LNPs have been determined using Zetasizer-DLS measurements and SEM images of L-glu-140 and L-glu-180, respectively. In addition, the possibility of easy incorporation of the L-glu fraction into polylactic acid without requiring previous lignin modification has been preliminarily explored. The CoffeeCat process was thus demonstrated as a relevant eco-solution for an integrated lignocellulosic biorefinery.

Received 7th February 2023

Accepted 8th May 2023

DOI: 10.1039/d3su00050h

rsc.li/rscsus

## Sustainability spotlight

This work is based on the CoffeeCat process to design a sustainable strategy for a full-component refinery of lignocellulose. The strategy uses green solvents (the food approved 2-methyltetrahydrofuran-3-one and water) and reagents (glutamic acid) to selectively extract at 140 °C a nearly carbohydrate-free lignin with high β-O-4 linkage content. Synergistic ionic liquid pretreatment applied to the remaining delignified biomass led to total conversion of polysaccharides into platform sugars. The physico-chemical properties of the extracted lignin could open the way of designing biocompatible nanoparticles and facilitating the formulation of PLA-lignin biocomposites. Miscanthus is used as an example for potential biomass feedstock. This work is in line with points 12 and 13 of the UN's Sustainable Development Goals (combat climate change and ensure sustainable production patterns).

## Introduction

In the current context of environmental issues of climate change, lignocellulosic biomass (LCB), one of the most substantial renewable feedstocks, is increasingly proposed as a promising alternative¹⁻³ to fossil resources. LCB offers potential to be converted by sustainable processing to clean energy biofuels, biomaterials and value-added chemicals,⁴⁻⁸ with the new value chain opening up to circular economy development.⁹ LCB contains mostly polymeric carbohydrates (hemicellulose, 20–30% w/w and cellulose, 30–40% w/w)¹⁰⁻¹²

<figure><img src="image_3.png" /></figure>

<footnote>aUnité de Génie Enzymatique et Cellulaire, UMR CNRS 7025, UFR des Sciences, Université de Picardie Jules Verne, 33 rue Saint Leu, 80039 Amiens Cedex 1, France.
E-mail: eric.husson@u-picardie.fr; catherine.sarazin@u-picardie.fr</footnote>

<footnote>bLaboratoire de Glycochimie, des Antimicrobiens et des Agroressources, UMR CNRS 7378, UFR des Sciences, Université de Picardie Jules Verne, 33 rue Saint Leu, 80039 Amiens Cedex 1, France</footnote>

<footnote>cLaboratoire d'Ingénierie des Biomolécules (LIBio), Université de Lorraine, 2 Avenue de la Forêt de Haye, TSA40602, 54518 Vandœuvre-lès-Nancy, France</footnote>

<footnote>dInstitut de Chimie de Picardie FR CNRS 3085, 80039 Amiens, France</footnote>

<footnote>† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3su00050h</footnote>
<figure><img src="image_4.png" /></figure>

and lignin, a polyphenolic polymer (15–40% w/w).¹¹⁻¹³ The use of cellulose and hemicellulose has been intensively studied for the production of paper, sugars, bioethanol, biobutanol and other fermentation products through various biological or thermochemical pathways.⁴,¹⁴⁻²² However, lignin is frequently considered as a by-product from LCB biorefining and is still currently under-valued.⁴ Only less than 2% of the 1.5–1.8 billion tons of industrial lignin waste is used in the world annually.⁴,²³,²⁴ Most of the lignin waste is dumped or burned as low-grade fuel, which not only causes wastage of resources, but also incurs serious environmental pollution.²³ Furthermore, the valorization of LCB is constrained by the highly ordered matrix of the raw material. The interactions between the LCB components are responsible for the recalcitrant properties of this biomass and considerably limit the accessibility to each compound.²⁵⁻²⁸ Different pretreatments (mechanical, chemical and biological) have been reported in the literature to fractionate the biomass, reduce its recalcitrance and access its components for further valorization.²⁹,³⁰ However, the implementation conditions of these strategies often generate uncontrolled depolymerization/repolymerization affecting the structural integrity of polymers, which limits the valorization potential, in particular for the lignin fraction. The complex, heterogeneous and variable structure of this is later related to the LCB source and is particularly sensitive to extraction processes (Kraft, lignosulfonate, soda, and organosolv processes).³¹⁻³⁴ The requirement for inorganic salts, a strong acid or base, or even some organic solvents, with questionable safety to implement these extractions, is well-known to considerably affect the chemical and structural properties of lignin (sulfur content, C–C bonds, and molecular weight) and its reactivity, thus offering fewer further possibilities for chemical or enzymatic transformations.³⁵⁻³⁸ A delignification process must allow the provision of a lignin extract for high value applications in the field of food, cosmetics and medicine.³⁹ For this kind of applications, eco-compatible conditions of implementation could be required to minimize intrinsic chemical modification and traces of incompatible solvents.

Among recent literature data, the selection of a green solvent for the development of organosolv processes has emerged. For instance, the OrganoCat strategy has been reported as an economically viable approach to co-valorize the three main constitutive fractions of LCB (xylose, cellulose pulp and lignin).⁴⁰⁻⁴⁹ It consists of a biphasic system with a reactive aqueous phase supplemented in oxalic acid that selectively depolymerizes the hemicellulose and an organic phase composed of 2-methyltetrahydrofuran (MeTHF) allowing lignin solubilization.⁴¹,⁴²,⁵⁰,⁵¹ Although the OrganoCat strategy can be considered as fully bio-based,⁵²,⁵³ some drawbacks could be identified in terms of environmental compatibility and restriction to some field of applications. For example, high oxalic acid concentrations are required, which are not compatible with food applications.⁵⁴ In addition, the recovery of highly viscous and adhesive lignin⁴³ requires additional purification steps including petroleum-based solvents and energy consumption before valorization.⁴³,⁴⁴,⁵⁵ Recently, other organosolv process studies reported the use of biobased solvents such as γ-

valerolactone,⁵⁶ dihydrolevoglucosenone⁵⁷ or dimethyl isosorbide⁵⁸ to improve the sustainability of LCB fractioning. However, the use of these solvents was often combined with sulfuric acid affecting the structure of polymers.

Therefore, in this study, we proposed to design a new organosolv process to both improve the sustainability of the extraction of an enriched-lignin fraction without residual sulfur or carbohydrate and preserve its structural integrity as much as possible. To this end, we rationally selected a food-grade and easily biodegradable solvent together with natural amino acids (i.e. proteinogenic amino acids). 2-Methyltetrahydrofuran-3-one (MeTHF-3-one) is listed as generally recognized as safe (GRAS) and readily biodegradable in agreement with the Organization for Economic Co-operation and Development (OECD) standards⁵⁹ and used in food industries to mimic flavors.⁶⁰ GRAS amino acids were chosen (glutamic acid and aspartic acid)⁶¹ to replace the usually used oxalic acid in the OrganoCat process, also tested for comparison. The use of these natural materials could deserve some applications requiring a “nature” label, for example, in cosmetics applications. The targeted LCB was *Miscanthus x giganteus* (Mxg), a dedicated crop and recognized feedstock in circular and local biorefineries.⁶²⁻⁶⁵ The ability of our proposed strategy to selectively extract lignin while improving the accessibility of structural polysaccharides was investigated. The generated fractions were characterized by quantitative and structural analytical techniques (FTIR, NMR, SEM, and SEC-MALLS). Possible ways of valorization for each fraction were explored: (i) the enzymatic conversion of polysaccharides into platform monomeric sugars, (ii) the conception of lignin-based nanoparticles, and (iii) the design of polylactic acid (PLA)-lignin-based composites. A flowchart of the entire process is presented in Chart 1.

<figure><img src="image_5.png" /><figcaption>Chart 1 Schematic of the overall CoffeeCat process.</figcaption></figure>
<figure><img src="image_6.png" /></figure>

# Experimental

## Materials

MeTHF-3-one (>97%) was supplied by Alfa Aesar (Thermo Fisher Scientific, Heysham) and L-aspartic acid (>99%), L-glutamic acid (>99%), oxalic acid (>99%) and commercial alkali lignin (Kraft low sulfonate content, 4% sulfur, $M_w$ ~10 000 Da) were purchased from Sigma-Aldrich (Germany). *Miscanthus x giganteus* (*Mxg*) was provided by INRAe (France). 1-Ethyl-3-methylimidazolium acetate ([Emim][OAc], >98%) was purchased from Solvionic S.A (Verniolle, France). Anhydrous sodium acetate (99%) was from Fluka Sigma-Aldrich (Steinheim, Germany), sodium hydroxide aqueous solution (46/48%) from Fisher Scientific (Illkirch, France), acetic acid (99%) from Carl Roth (Lauterbourg, France) and sulfuric acid 72% w/w from VWR. HPLC grade trifluoroacetic acid (99%) was purchased from Sigma-Aldrich (Germany), HPLC grade acetonitrile (>99%) was obtained from Merck (Darmstadt) and dimethyl sulfoxide D6 (99.80%) was obtained from VWR. Absolute ethanol (>99.8%) and methanol (>99.9%); standard glucose (99.5%) and xylose (99%) were purchased from Sigma-Aldrich (Steinheim, Germany). A Cellic CTec2 enzymatic cocktail including both cellulolytic and hemicellulolytic activities (specific activity ≥1000 U g⁻¹) was supplied by Novozymes (Bagsvaerd, Denmark) and prepared with 15 FPU g⁻¹ of lignocellulosic biomass for the production of hydrolysates rich in monomeric sugars. Glass microfibre filters (<1 µm pore size) were from Whatman, GE Healthcare Life Sciences (Boston, MA, USA). Folin & Ciocalteu's phenol reagents, anhydrous sodium carbonate and gallic acid were purchased from Sigma-Aldrich (France). 4032D PLA beads were obtained from NatureWorks PLA Ingeo (USA).

## Methods

**Biomass conditioning.** To ensure the homogeneity of the lignocellulosic substrates, native *Mxg* was milled with a planetary ball miller (Retsch PM400) for 90 s at a frequency of 25 s⁻¹ to achieve a size of less than 0.8 mm, and then freeze-dried. The samples were then stored in a desiccator until use.

**Chemical composition.** The chemical composition of the raw biomass (freeze-dried *Mxg*) was determined based on the NREL Laboratory Analytical Procedure.⁶⁶ All measurements

were made in triplicate and the data are reported in Table 1. The detailed experimental procedure is presented in the ESI.†

**CoffeeCat process.** Since MeTHF-3-one leads to a monophasic system when mixed with water, solvent elimination from generated fractions can be easily achieved by single water-washing. The physico-chemical properties of the solvents, the chosen amino acids (L-glutamic acid and L-aspartic acid) and of oxalic acid are presented in ESI, Tables S1 and S2.† These amino acids possess a density, and boiling and melting points compatible with implementation conditions and acidic properties ($pK_1 = 2.19$; $pK_2 = 4.25$ for L-glutamic acid, $pK_1 = 1.92$; $pK_2 = 3.87$ for L-aspartic acid) and comparable with the ones of oxalic acid ($pK_1 = 1.23$; $pK_2 = 4.30$) (see ESI, Table S2†). The two amino acids also have higher decomposition temperatures (185–280 °C) compared to oxalic acid (127–157 °C), which could help in preventing the thermal decomposition observed with oxalic acid in the Organocat process.⁷⁰ Finally, the GRAS amino acids used are both compatible with food applications.⁶¹ Based on preliminary experiments implemented in small volumes (12 mL), the conditions were fixed as follows: a MeTHF-3-one/water volume ratio of 3:1 was selected based on alkali lignin solubility in MeTHF-3-one/water mixtures, and the acid concentration and biomass loading were fixed at 0.1 M and 1% w/w, respectively (preliminary experiments are presented in ESI, Fig. S1 and S2†). Then, in a general procedure, freeze-dried *Mxg* (1% w/v) and 0.1 M acid (oxalic, aspartic or glutamic acid) were added to a 200 mL MeTHF-3-one/water mixture (volume ratio of 3:1) in a glass batch reactor equipped with a reflux condenser, then incubated under vigorous agitation in a thermostatically controlled oil bath (140 or 180 °C) for 6 h and finally cooled in an ice bath for 20 min. The pH of the suspension was controlled (2.98 ± 0.03 with oxalic acid, 5.03 ± 0.01 for aspartic acid and 5.15 ± 0.01 for glutamic acid). The liquid and solid phases were separated by vacuum filtration. The solid phase was washed with ultrapure (UP) water until a neutral pH was reached, and then freeze-dried and stored in a desiccator until further use (delignified biomass pulp namely DL-acid-temperature).

The solvent was then removed from the liquid fraction by evaporation under reduced pressure: 40 °C and 72 mbar to evaporate the water, and then the pressure was lowered to 20 mbar to evaporate the MeTHF-3-one. Structural integrity of the recovered MeTHF-3-one was verified by 1D NMR. The obtained residue was mixed with 50 mL of UP water and then centrifuged.

<table><caption>Table 1 Chemical composition of *Miscanthus x giganteus* raw biomass (freeze-dried *Mxg*) reported on a dry matter basis</caption><thead><tr><th></th><th></th><th>Experimental values<br>% w/w dry weight</th><th>Reported values for<br><i>Mxg</i> % w/w dry weight</th></tr></thead><tbody><tr><td>Water</td><td></td><td>2.8 ± 1.0</td><td>Not reported</td></tr><tr><td>Ash content</td><td></td><td>6.0 ± 0.1</td><td>3.1 ± 0.0 (ref. 67)</td></tr><tr><td>Ethanol extractives</td><td></td><td>4.4 ± 0.6</td><td>6.7 ± 0.2 (ref. 67)</td></tr><tr><td>Insoluble lignin (AIL)</td><td></td><td>24.3 ± 0.3</td><td>23.8 ± 2.7 (ref. 68), 24.1 (ref. 69)</td></tr><tr><td>Soluble lignin (ASL)</td><td></td><td>0.9 ± 0.1</td><td>0.9 ± 0.0 (ref. 67), 0.10 (ref. 69)</td></tr><tr><td>Total lignin</td><td></td><td>25.2 ± 0.2</td><td>24.2 (ref. 69)</td></tr><tr><td rowspan="2">Structural sugars</td><td>D-Glucose</td><td>36.7 ± 1.2</td><td>42.8 ± 0.2 (ref. 67)</td></tr><tr><td>D-Xylose</td><td>18.1 ± 0.4</td><td>22.3 ± 1.7 (ref. 26), 23.2 ± 0.1 (ref. 67)</td></tr></tbody></table>
This step was repeated at least 3 times until the water was colorless. Finally, the resulting solid was freeze-dried and stored in a desiccator until further use (enriched-lignin fraction namely L-acid-temperature). The enriched-lignin fraction yields (%) were calculated based on the weight of the latter fraction, using eqn (1).

Enriched-lignin fraction yield (%)

$$ = \frac{\text{lignin extracted in pretreatment solvent (g)}}{\text{initial lignin in raw } Mxg (\text{g})} \times 100 \quad (1) $$

**Analytical procedures.** Alkali lignin, raw Mxg and extracted lignin fractions were characterized by infrared spectrometry using a FTIR-8400S (Shimadzu, France) equipped with a universal ATR sampling accessory with a germanium crystal. The extracted lignins were also analysed by NMR after solubilization in dimethyl sulfoxide-D6 (10% w/v) using 1D and 2D NMR techniques. The experiments were performed on a spectrometer (Bruker Avance III 500 MHz spectrometer) equipped with a 5 mm probe operating at 125.7452 MHz (¹³C channel) and 500.0800 MHz (¹H channel) at 298 K. The ¹H, ¹³C and ¹H-¹³C HSQC were performed under standard conditions (using the pulse program hsqcetgspisp2.3). HSQC cross-signals were assigned based on the literature.⁷¹⁻⁷⁷ A semiquantitative analysis of the HSQC cross-signal intensities was performed.⁷⁴ SEC experiments were performed on the extracted lignins with a HPLC pump (LC10AD, Shimadzu) coupled to an autosampler (Autosampler VE 2001, Malvern Panalytical) and a multi-detectors system recording UV, light scattering (RALS and LALS) and refractive index signals (Viscotek TDA305, Malvern Panalytical). The calibration procedure and cross validation were performed with polystyrene standards (Viscotek PolyCal standards, Malvern Panalytical). Lignin samples were solubilized in THF at 25 g L⁻¹ and filtered through a 0.22 µm nylon-filter just before injection. The phenol content of the extracted lignin samples was determined based on Folin-Ciocalteu's method using gallic acid as the reference, as described in the literature.⁷⁸,⁷⁹ More details on the analytical procedures are provided in the ESI.†

**Lignin-based nanoparticle formation and characterization.** Lignin based nanoparticles were prepared by non-solvent addition, by adapting previously reported methods but replacing traditionally used ethylene glycol or acetone with the readily biodegradable GRAS solvent: MeTHF-3-one.⁸⁰,⁸¹ Briefly, 10 mg of extracted lignin (L-glu-140 or L-glu-180) was solubilized in 1 mL of the MeTHF-3-one/water mixture 9 : 1 (v/v) and stirred vigorously for 30 min at room temperature. After complete solubilization, the solution was poured into a volumetric flask and 99 mL of ultrapure water was gradually added to the lignin preparation, while stirring gently. The size, charge, and shape of the obtained nanoparticles were determined by dynamic light scattering (DLS), zeta potential analyses and scanning electron microscopy (SEM). The obtained particles were characterized for particle size and charge at 25 °C by dynamic light scattering (DLS) and zeta

potential analyses using a Zetasizer Pro (Malvern, UK). Measurements were performed in triplicate, in a disposable folded capillary cell. The results were analyzed using Malvern ZS Xplorer processing software. The nanoparticles were also observed with a high-resolution environmental scanning electron microscope (ESEM, FEI Quanta 200 FEG, OR, USA). A slight drop of each sample was placed on double-sided carbon tape adhered to aluminum SEM stubs. They were dried at room temperature for 72 h, and then the secondary electron images were acquired under high-vacuum mode with an Everhart-Thornley detector (ETD) at a pressure of 0.5 Torr using a pressure limiting aperture (PLA). Dry lignin samples were also observed using the same technique, but without 72 h of drying.

**Lignin incorporation into PLA.** Polylactic acid (PLA) beads were solubilized in MeTHF-3-one (100 g L⁻¹) under gentle stirring overnight at 40 °C. The enriched-lignin fraction was added to the solution (0.2 g lignin per g PLA)⁸²,⁸³ and gently stirred for 1 h until complete solubilization. The solution was either (i) dried at 50 °C for 1 h to obtain a film or (ii) dried in an oven at 105° overnight, and then ground in a mortar with a pestle to obtain a fine powder. The obtained samples were photographed and analysed by FTIR.

**Ionic liquid pretreatment of biomass.** The delignified fraction (DL-acid_tempature) generated by the CoffeeCat process was then subjected to ionic liquid pretreatment prior to enzymatic hydrolysis, as described by Auxenfans *et al.*⁸⁴ Briefly, 1 g of biomass was added to 50 mL of 1-ethyl-3-methylimidazolium acetate ([Emim][OAc], 2% w/v) and incubated in an oil bath at 110 °C with vigorous stirring for 40 min. After incubation, the sample was cooled and ultrapure water was added as an anti-solvent (2 : 1 v/v water/IL). The mixture was vigorously mixed for 30 min, and then centrifuged at 95 000 rpm for 20 min at 4 °C (Beckman coulter Allegra™ 64R Centrifuge, United States). The supernatant was removed, and the pellet was successively washed with ultrapure water (UP water) until the wash water conductivity was lower than 5 µS cm⁻¹ (conductivity of UP water). The pellet was then freeze-dried (LABCONCO freeze dryer FreeZone 2.5, USA), and the obtained fraction was stored in a desiccator until further use.

**Enzymatic hydrolysis.** The enzymatic hydrolysis (EH) procedure is adapted from a previous study.⁸⁵ For the hydrolysis reaction, 200 mg of the sample was added to 7.4 mL of citrate-phosphate buffer (50 mM, pH 5.5) and 2.6 mL of the Cellic CTec2 preparation (0.974 FPU mL⁻¹) with the aim to have an enzyme loading of 15 FPU g⁻¹ of dried biomass. The mixture was incubated in a Minitron incubation shaker (INFORS HT, United Kingdom) at 50 °C for 72 h. The reaction was stopped by incubating the mixture at 90 °C for 20 min. Then, the sample was diluted (50×) in ultrapure water and filtered (0.22 µm syringe PTFE filter) prior to sugar content quantification as described in the “Chemical composition” section. The hydrolysis reaction was repeated in duplicate.

The relative monomeric sugar yields were expressed in % according to eqn (2).

<figure><img src="image_7.png" /></figure>
<figure><img src="image_8.png" /></figure>

$$ \text{Monomeric sugar}^+ \text{ yield (\%)} = \frac{m_{\text{sugar}^+} \text{ (g) released after enzymatic hydrolysis} \times 100}{m_{\text{sugar}^+} \text{ (g) in the initial biomass (from acid hydrolysis)}}, \quad * \text{glucose or xylose} \quad (2) $$

# Results and discussion

## Extraction performances

Extraction performances of the CoffeeCat process were evaluated highlighting lignin extraction yields and are presented in Table 2, along with photographs of the recovered samples. Extraction yields were similar for all acids at 140 °C (23.8 ± 2.1%, 26.5 ± 1.9%, and 26.8 ± 3.9 for oxalic, glutamic, and aspartic acid, respectively). Pretreatment at 180 °C did not increase extraction yields for aspartic acid (26.8 ± 3.9% at 140 °C vs. 24.2 ± 3.5% at 180 °C) and for oxalic acid (23.8 ± 2.1% at 140 °C vs. 30.7 ± 3.2% at 180 °C). However, the extraction yield was nearly twice that for glutamic acid (26.5 ± 1.9% for 140 °C against 43.3 ± 2.5% at 180 °C). These first results demonstrated the possibility of substituting oxalic acid with the two amino acids proposed as alternatives. Moreover, the use of glutamic acid could improve the extraction yields by increasing the temperature. Regarding the appearance of the samples, the modification of the acid led to significant differences in the color of the lignin samples, ranging from beige-orange for oxalic acid and aspartic acid to chocolate brown for glutamic acid. In addition, increasing the temperature led to the recovery of a brighter and darker lignin. This result was in agreement

with literature data, as several studies have already shown that the more severe the extraction conditions, the darker the lignins obtained.⁸⁶,⁸⁷ Based on these results, glutamic acid was selected for the implementation of the CoffeeCat process.

## Chemical compositions of isolated lignin fractions

The chemical composition of lignins obtained by the CoffeeCat process with glutamic acid depends on the process temperature. Their compositions are presented in Fig. 1. The enriched-lignin fractions are referred to as **L-glu-140** and **L-glu-180** for the lignins obtained at 140 °C and 180 °C, respectively. The isolated lignin fractions had very low residual sugar content (3.3 ± 1.4 and 1.4 ± 0.3 g glucose per 100 g dry matter for **L-glu-140** and **L-glu-180**, respectively, and 1.3 ± 0.6 and 0.5 ± 0.1 g xylose per 100 g dry matter for **L-glu-140** and **L-glu-180**, respectively). The ash content in lignins was lower than that in *Mxg* (Table 1) possibly indicating that silica and other inorganic materials do not solubilize during the pretreatment.⁸⁸ On the other hand, **L-glu-180** contained a very high proportion of acid insoluble lignin (AIL), e.g. 80 g per 100 g dry matter as well as 4 g per 100 g dry matter of acid soluble lignin (ASL). This corresponds to a total lignin content of 84% in the enriched-lignin fractions,

<table><caption>Table 2 Extraction yields and sample aspect after pretreatment (1% *Mxg* (w/v), amino acid or oxalic acid at a concentration of 0.1 M)</caption><thead><tr><th></th><th></th><th>Enriched-lignin fraction yields<sup>a</sup> (%)</th><th>Photographs of the extracted lignin fraction</th></tr></thead><tbody><tr><td rowspan="4">140 °C</td><td>Oxalic acid</td><td>23.8 ± 2.1</td><td></td></tr><tr><td>Glutamic acid</td><td>26.5 ± 1.9</td><td></td></tr><tr><td>Aspartic acid</td><td>26.8 ± 3.9</td><td></td></tr><tr><td>Oxalic acid</td><td>30.7 ± 3.2</td><td></td></tr><tr><td rowspan="2">180 °C</td><td>Glutamic acid</td><td>43.3 ± 2.5</td><td></td></tr><tr><td>Aspartic acid</td><td>24.2 ± 3.5</td><td></td></tr></tbody></table>

<footnote>a Enriched-lignin fraction yields (%) calculated using eqn (1).</footnote>
<figure><img src="image_9.png" /></figure>

<figure><img src="image_10.png" /><figcaption>Fig. 1 Chemical compositions of the enriched-lignin fractions obtained from the CoffeeCat process at 140 and 180 °C.</figcaption></figure>

which confirms that this process allows a lignin with a competitive purity in comparison with commercial lignins to be obtained. On the other hand, L-glu-140 contained 53 g per 100 g dry matter of AIL for 8 g per 100 g dry matter of ASL. Although the purity was lower (61%), it was interesting to note that a gentler fractioning allows the extraction of a higher amount of ASL.

A complementary analysis was performed to determine the total phenolic content of the two enriched-lignin fractions. Folin–Ciocalteu's method yielded, respectively, 14.0 ± 1.0 and 14.2 ± 0.1 mg GAE per g lignin for L-glu-140 and L-glu-180, similar to the 15.9 ± 0.2 mg of the commercially available alkali lignin.

<figure><img src="image_11.png" /><figcaption>Fig. 2 SEM images of L-glu-140 (A), (C) and (E) and L-glu-180 (B), (D) and (F) with different magnifications.</figcaption></figure>

Structural characterization of isolated lignin fractions

The SEM micrographs of the enriched-lignin fractions after freeze-drying are presented in Fig. 2. L-glu-140 and L-glu-180 presented typical lignin surface morphologies corresponding to disordered micro-structures composed of various shapes. However, L-glu-140 appeared to have a structure composed of large irregular blocks, with a rather smooth surface (Fig. 2A and C), which resembles a typical lignin residue,⁸⁹⁻⁹¹ whereas L-glu-180 has a more brittle and compact structure (Fig. 2B), related to a “cleaner” lignin according to previous studies.⁸⁸

Fig. 3 shows the FTIR spectra of the enriched-lignin fractions in comparison to *Mxg*. Typical bands were observed between 1650 and 1730 cm⁻¹ (Fig. 3), corresponding to the stretching of conjugated and non-conjugated carbonyls, ketones or ester groups. Bands at 1600 and 1515 cm⁻¹ were assigned to the aromatic skeleton vibration, and bands at 1460, 1400 and 1370 cm⁻¹ corresponded respectively to CH deformations and aromatic ring vibrations, aromatic skeleton vibration and aliphatic C–H stretching in CH₃. The specific band at 1330 cm⁻¹

<figure><img src="image_12.png" /><figcaption>Fig. 3 FTIR spectra of raw *Mxg*, L-glu-140 and L-glu-180, in the range of 600 to 2000 cm⁻¹. The complete spectra (600 to 4000 cm⁻¹) are presented in ESI, Fig. S3.†</figcaption></figure>
<figure><img src="image_13.png" /></figure>

is related to the aromatic ring breathing of syringyl units, a specific band rarely observed in a lignin fraction contaminated by residual carbohydrates.⁸⁸ The band at 1265 cm⁻¹ is

related to aromatic ring breathing of guaiacyl units whereas the one at 1160 cm⁻¹ corresponds to C–H stretching in a guaiacyl unit. The signal at 1130 cm⁻¹ was assigned to aromatic in-plane

<figure><img src="image_14.png" /><figcaption>Fig. 4 Main identified lignin substructures and 2D HSQC NMR spectra of the side chain and aromatic region of (A) L-glu-140 and (B) L-glu-180.</figcaption></figure>
<figure><img src="image_15.png" /></figure>

bending in a syringyl unit, the signal at 1095 cm⁻¹ to C–O deformation in aliphatic ethers, the signal at 900 cm⁻¹ to aromatic CH out of plane deformation of a guaiacyl unit and the signal at 820 cm⁻¹ to aromatic CH out of plane deformation in a syringyl unit. The FTIR spectra revealed that the two isolated lignins had overall the same functional groups, and that the process temperature did not seem to significantly modify lignin structures.

To get more insight into the chemical structure of the enriched-lignin fractions, 2D ¹H–¹³C HSQC NMR analyses were performed (Fig. 4). The side chain (δC 50–90 ppm; δH 2.5–6.0 ppm) and aromatic lignin regions (δC 100–135 ppm; δH 5.0–8.5 ppm) of **L-glu-140** (Fig. 4A) and **L-glu-180** (Fig. 4B) were compared. The first observation is that the NMR 2D spectra confirmed the obtention of carbohydrate-depleted lignin fractions since there is no signal in the δC 70–80 ppm; δH 3–4 ppm region.⁹² Furthermore, the spectra of **L-glu-140** show the presence of β-aryl-ether (β-O-4) linkages that are not evidenced in **L-glu-180**.

The side chain and aromatic lignin regions of the 2D NMR spectra are of particular interest for the quantification of lignin linkages and monomer repartition as well as for the aromatic S/G/H ratio. The quantified relative amounts of the aromatic units and of the typical linkages in the lignins are listed in Table 3. Details for the calculation are provided in the ESI.† **L-glu-140** and **L-glu-180** had a S/G/H ratio consistent with reported values for raw *Mxg* (40/60/0).⁹³⁻⁹⁵ No significant differences were observed between **L-glu-140** and **L-glu-180** for the S/G/H ratio. Furthermore, the monomer repartition was not the same upon pretreatment temperature increase. Indeed, the lignin obtained at 180 °C contained less β-O-4 linkages than the one obtained at 140 °C (Table 3), and no β-5 and β-β linkages, as already reported in the literature, with a temperature increase.⁹⁶

Molecular weights of both **L-glu-140** and **L-glu-180** samples were determined using size exclusion chromatography (SEC). For each one, a single peak was detected on each detector at the same elution volume. *M*<sub>w</sub> determination by light scattering gave *M*<sub>w</sub> values of ~20 045 Da and ~33 179 Da for **L-glu-140** and **L-glu-180**, respectively. These values ranged in the same order of magnitude, as illustrated by near elution volumes of 12.306 mL and 12.224 mL for **L-glu-140** and **L-glu-180**, respectively (see ESI, Fig. S4†). Interestingly, the enriched-lignin fractions presented higher molecular weight than commercial alkali lignins, which have a *M*<sub>w</sub> of ~10 000 Da,⁹⁷ or organosolv lignins with *M*<sub>w</sub> between 1000 and 12 000 Da,⁵⁸,⁹⁷⁻⁹⁹ but ranged in the *M*<sub>w</sub> of “native-like-lignin” from *Mxg*, which has been reported to be ~30 000 Da.¹⁰⁰ However, comparisons with literature data may be questionable as the analytical conditions and solubility of lignins may be highly variable. The *M*<sub>w</sub>*M*<sub>n</sub> values were 1.148

<table><caption>**Table 3** S/G/H units and monomer repartition in lignins for 100 units</caption><thead><tr><th></th><th>S/G/H (%)</th><th>β-5/β-β/β-O-4<br>(interunit linkages/100 aromatic units)</th></tr></thead><tbody><tr><td><strong>L-glu-140</strong></td><td>33/67/0</td><td>3/2/28</td></tr><tr><td><strong>L-glu-180</strong></td><td>42/57/0</td><td>0/0/9</td></tr></tbody></table>

and 1.427 for **L-glu-140** and **L-glu-180**, respectively, suggesting a low polydispersity for these fractions. The slight difference observed between the *M*<sub>w</sub> of **L-glu-140** and **L-glu-180** could agree with bond cleavages such as the β-O-4 linkages (Fig. 1 and Table 3), providing reactive intermediates susceptible to repolymerization with lignin. Indeed, this is phenomenon more particularly pronounced at high temperatures of extraction.¹⁰¹

Fraction valorization

After demonstrating the proof of concept of the CoffeeCat process, several pathways of valorization of the generated fractions were explored: (i) the enzymatic production of fermentable sugars from delignified biomass pulp; (ii) the conception of lignin-based nanoparticles and (iii) the feasibility of making polylactic acid (PLA) lignin-based composites.

The enzymatic production of platform monomeric sugars was first studied. For the bioconversion of the polysaccharide fraction, one promising sustainable route is enzymatic hydrolysis.¹⁰² However, enzymatic hydrolysis of delignified biomass pulp, (**DL-glu-140** and **DL-glu-180**) led to low yields of glucose and xylose, as was the case for raw *Mxg* (less than 6% xylose yield and less than 10% glucose yield, according to eqn (2)) (Fig. 5). These results suggest that the CoffeeCat process did not affect the enzymatic digestibility of the polysaccharides. They also support the current idea in the literature that enzymatic digestibility is not solely related to the lignin content, but also to the disruption of the hydrogen bond network and to some extent to the cellulose crystallinity⁴² or to the presence of impurities and potential inhibitors. To this end, ionic liquids can be used¹⁰³⁻¹⁰⁵ to overcome the persistent recalcitrance of the biomass.²⁵⁻²⁸ It was thus chosen to perform enzymatic hydrolysis after an additional mild pretreatment, the classically used 1-ethyl-3-methylimidazolium acetate ([Emim][OAc])-based pretreatment.²⁵,²⁶,³⁰,⁶⁸,⁸⁴,⁸⁵,¹⁰⁶ Glucose and xylose yields after enzymatic hydrolysis of both raw *Mxg* or delignified biomass pulp before and after [Emim][OAc]-pretreatment are presented in Fig. 5.

<figure><img src="image_16.png" /><figcaption>**Fig. 5** Glucose and xylose yields after enzymatic hydrolysis (EH) of raw *Mxg*, **DL-glu-140** and **DL-glu-180** with or without previous [Emim][OAc] pretreatment (PT [Emim][OAc]), in g of hydrolysed sugar per 100 g of biomass.</figcaption></figure>
<figure><img src="image_17.png" /></figure>

As expected, [Emim][OAc]-pretreatment increased enzymatic digestibility of *Mxg*. However, an interesting result was that hydrolysis yields were significantly improved for **DL-glu-140** and **DL-glu-180** obtained by the CoffeeCat process. Here, a synergistic effect induced by the two subsequent pretreatments was observed, leading to hydrolysis yields higher than 80% for xylose and higher than 99% for glucose for **DL-glu-140** obtained by the CoffeeCat process. This result is very promising as it supports the current trend to use combined pretreatments for biomass full valorization.¹⁰⁷ Moreover, the FTIR spectra of the residual solid fraction evidenced the isolation of a residual left enzymatic hydrolysis lignin (see ESI, Fig. S5†). Indeed, the FTIR spectrum revealed well-resolved characteristic bands of the lignin polymer according to the FTIR spectrum of alkali lignin.

For the enriched-lignin fractions (**L-glu-140** and **L-glu-180**) the conception of lignin-based nanoparticles (LNPs) was first proposed as a way of valorization. Indeed, a major limitation for lignin industrial processes is its insolubility in water. However, recent studies have demonstrated the possibility of preparing aqueous LNPs,¹⁰⁸⁻¹¹¹ that could be used for drug and gene delivery due to their biocompatibility, or for other applications such as as antibacterial and antioxidant agents, UV absorbents or hybrid nanocomposites.¹¹⁰,¹¹² The synthesis of LNPs has been performed *via* a combination of chemical and physical methods, such as polymerization, ultrasonication, interfacial crosslinking, freeze-drying, homogenization or alkaline precipitation.¹¹² However, many of these processes involve the use of hazardous solvents or energy-consuming techniques. The scientific community agrees on the need to create eco-friendly methods for LNP formation.¹¹⁰,¹¹² One perspective currently proposed in the literature is the simple use of antisolvent precipitation, but life cycle assessment calculations have demonstrated that the thermal energy needed for the recovery of the solvents used (ethanol, acetone or THF, mainly) was a hot spot.¹¹³⁻¹¹⁵ Here, we proposed to use the antisolvent precipitation method, with a mixture of water/MeTHF-3-one. Thus, **L-glu-140** and **L-glu-180** were dissolved in MeTHF-3-one/water 9:1, and then diluted 100 times to reach a final concentration of 0.1 g L⁻¹. Particle size distribution, charge and shape were determined using DLS, zeta-potential analysis and SEM. The formed nanoparticles illustrated a regular spherical shape as indicated by scanning electron microscopy (SEM) images in Fig. 6. The sizes of the LNPs observed by SEM appeared to be consistent with the size distribution obtained by DLS (Table 4). The LNPs synthesized from **L-glu-140** were slightly smaller (272 ± 9 nm) than those obtained from **L-glu-180** (472 ± 6 nm) but also less polydisperse (PdI < 0.2). This result is in accordance with literature data, confirming that more severe extraction conditions produce larger LNPs than milder conditions.¹⁰⁰ The diameter of the particles is a key parameter to evaluate their properties and potential applications.¹¹⁶ Therefore, it is valuable to have the possibility to tailor the LNP size by controlling the temperature of the CoffeeCat process.

Zeta potential values were also measured (Table 4). The smaller particles made from **L-glu-140** had a higher negative charge (−29.2 ± 0.8 mV) than the bigger particles made from **L-glu-180** (−20.8 ± 0.4 mV), as reported in the literature for

<figure><img src="image_18.png" /><figcaption>Fig. 6 SEM images of the particles synthesized from (A) and (B) L-glu-140 and (C) and (D) L-glu-180 at a concentration of 0.1 g L⁻¹.</figcaption></figure>

<table><caption>Table 4 Z-Average (d nm), PdI and zeta potential (mV) of LNPs prepared from L-glu-140 and L-glu-180 at a concentration of 0.1 g L⁻¹</caption><thead><tr><th></th><th>Z-Average (d nm)</th><th>PdI</th><th>Zeta potential (mV)</th></tr></thead><tbody><tr><td>L-glu-140</td><td>272 ± 9</td><td>0.16 ± 0.03</td><td>-29.2 ± 0.8</td></tr><tr><td>L-glu-180</td><td>472 ± 6</td><td>0.36 ± 0.05</td><td>-20.8 ± 0.4</td></tr></tbody></table>

LNPs.¹⁰⁰ The observed negative charge is typical of LNPs, and ensures the stability of LNPs over time.¹¹⁷ Preliminary experiments have shown that these particles can be stable up to 30 days (data not shown). These results suggested the possibility to produce lignin nanoparticles with tailorable sizes, depending on the CoffeeCat process temperature, which can be produced in a fully food grade mixture (MeTHF-3-one/water) if this label is required.

Another way of valorisation for lignin-enriched fractions could be their incorporation into PLA to design PLA-lignin composites. Indeed, PLA is one of the main commercially available bio-based and biodegradable polyesters used for a wide range of industrial applications, such as 3D printing applications.⁸²,⁸³,¹¹⁸ However, PLA suffers from drawbacks such as intrinsic brittleness.⁸³,¹¹⁹⁻¹²¹ Several studies have proposed to improve its physical properties to extend its applications, especially in the field of food packaging. One strategy is to incorporate lignin to design composite polymers with improved physical and mechanical properties.⁸²,¹¹⁸,¹¹⁹,¹²² However, due to the poor miscibility of commercially available lignin in a polymer matrix, the mixing of lignin with PLA often requires manual mixing and extrusion, melting, and solubilization in toxic solvents such as chloroform, or lignin chemical
<figure><img src="image_19.png" /></figure>

modification.⁸³,¹¹⁹,¹²²,¹²³ Here we proposed for the first time to solubilise PLA in MeTHF-3-one, in which **L-glu-140**, the less coloured lignin-enriched fraction, is also soluble. Fig. 7A shows the complete miscibility of **L-glu-140** in the PLA-MeTHF-3-one mixture. The obtained solution was treated by two different ways as described in the experimental section. Fig. 7B depicts the powder obtained after drying the solution overnight at 105 °C and grinding. The FTIR spectra of PLA, **L-glu-140** and **PLA-L-glu-140** powder are presented in Fig. 7D. The FTIR spectrum of PLA showed typical absorption bands at 1750 cm⁻¹, 1180 cm⁻¹ and 1080 cm⁻¹ which respectively correspond to the C=O stretching of the carbonyl group, C=O stretching of esters and carbonyl C=O stretching.⁸²,⁸³ The characteristic peaks of **L-glu-140** were already assigned (Fig. 3). In the **PLA-L-glu-140** powder spectrum, small peaks between 1510 and 1530 cm⁻¹ were

observed, which were attributed to the C=C groups of lignin aromatic rings.⁸³,¹²⁴ Furthermore, Fig. 7C shows the film obtained after drying the solution at 50 °C for 1 h. The obtained film seemed homogeneous and flexible. This suggested the feasibility of easy incorporation of lignin into PLA in MeTHF-3-one without requiring lignin modification.

## Conclusions

At this academic stage, the process still needs to be improved in order to be economically viable. One of the major disadvantages is certainly the use of water needed for the washing steps, although this is not exclusive to this process and commonly shared with some others such as organosolv, ionic liquid or deep eutectic pretreatments of LCB, which is additional to the cost of the solvent and the recycling of the fluids. However, the proposed strategy allowed a lignin fraction rich in β-O-4 linkages to be obtained when performed at mild temperature (140 °C) which is recovered by solvent evaporation, similar to other organosolv processes.⁷⁴,⁹⁸,⁹⁹ This easy recovery method is clearly an advantage over the use of non-volatile ionic liquid for LCB pretreatment. Moreover, the use of a food grade solvent, already described as readily biodegradable,⁵⁹ may reassure end-users and enlarge the panel of applications (e.g. cosmetics) even if traces of solvent remain after the washing step. Another point that can be highlighted and can be an advantage for subsequent transformation or direct use, is that the lignin obtained is in a powder state and not a liquor as in other processes such as IL or OrganoCat pretreatments.⁴³,⁴⁴ For example, the obtained lignin was incorporated without further modification into PLA. Finally, the lignin fraction is nearly carbohydrate-free and the validity of the process was suggested by the mass balance closure related to the three main polymers of *Miscanthus* (see ESI, Fig. S7†).

## Conflicts of interest

The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be considered a potential conflict of interest.

## Acknowledgements

The authors would like to thank Dr Dominique Cailleu for helping in the NMR experimentation implementation and Dr Arash Jamali for SEM observations.

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