Deep Eutectic Solvents as a Potential Alternative Extraction Technique for the Isolation of Phenolic Compounds from Economically Important European Tree Species
Abstract
1. Introduction
2. Selected Trees in the Forests of the European Union
2.1. Pedunculate and Sessile Oaks (Quercus robur/petraea)
2.2. European Beech (Fagus sylvatica)
| Tree Species | Phenolic Acids | Flavonoids * | Stilbenes * | Tannins |
|---|---|---|---|---|
| Hardwood Bark | ||||
| Beech | ellagic acid gallic acid vanillic acid | catechin and quercetin | - | roburin |
| Oak | ellagic acid gallic acid vanillic acid coumaric acid and syringic acid | catechin, epicatechin, taxifolin and quercetin | - | - |
| Hornbeam | chlorogenic acid and ellagic acid | myricetin, luteolin, quercetin and apigenin | - | - |
| Softwood bark | ||||
| Pine | - | kaempferol, quercetin and taxifolin | pinosylvin | - |
| Spruce | - | quercetin and myricetin | resveratrol piceid piceatannol | - |
| Fir | gallic acid vanillic acid coumaric acid and ferulic acid | catechin, taxifolin, epicatechin and quercetin | - | - |
2.3. Hornbeam (Carpinus betulus)
2.4. Scots Pine (Pinus sylvestris)
2.5. Norway Spruce (Picea abies)
2.6. Silver Fir (Abies Alba)
3. Extraction Techniques for Isolation of Phenolic Compounds
3.1. Conventional Extraction Techniques
3.2. Nonconventional Extraction Techniques
3.3. Deep Eutectic Solvents as Bark Extraction Agents
3.3.1. The Position of DES Extraction Among Current Extraction Methodologies
3.3.2. The Concept of DESs and Their Classification
| HBD with Various Functional Groups | |||||
|---|---|---|---|---|---|
| Carboxylic Acid-Based DESs | |||||
| Monocarboxylic acids | |||||
| Formic acid | Acetic acid | Butyric acid | Lactic acid | Glycolic acid | Propionic acid Levulinic acid |
| Di/Tricarboxylic acids | |||||
| Oxalic acid | Malonic acid | Succinic acid | Malic acid | Citric acid | Maleic acid Glutaric acid |
| Amine/amide-based DESs | |||||
| urea, formamide, acetamide, ethanolamine, diethanolamine, imidazole, methyl diethanolamine | |||||
| Polyalcohol/saccharide-based DESs | |||||
| glycerol ethylene glycol propylene glycol 1,4-butanediol glucose fructose xylitol sucrose | |||||
| DESs based on phenolic compounds (derived from lignin) | |||||
| resorcinol catechol vanillin p-hydroxybenzaldehyde p-hydroxybenzyl alcohol p-hydroxybenzoic acid p-coumaric acid gallic acid salicylic acid | |||||
| HBAs with various functional groups | |||||
| choline chloride betaine guanidine hydrochloride proline choline dihydrogen citrate | |||||
| ethyl ammonium chloride acetylcholine chloride choline dihydrogen phosphate benzyl triethyl ammonium chloride benzyl trimethyl ammonium chloride | |||||
| Catalysts/co-solvents | |||||
| Inorganic and organic acids | |||||
| sulfuric acid phosphotungstic acid phosphomolybdic acid silicotungstic acid p-toluenesulfonic acid | |||||
| Metal salts or hydrates | |||||
| AlCl3 × 6H2O FeCl3 × 6H2O CrCl3 × 6H2O FeCl2 × 4H2O ZnCl2 CuCl2 | |||||
| Non-polar solvents n-butanol | |||||
| Others water and alkaline hydrogen peroxide | |||||
- Ionic liquids composed of acids and bases;
- Neutral NADESs prepared solely from carbohydrates or from carbohydrates combined with other polyalcohols;
- Neutral NADESs with bases, formed from carbohydrates or polyalcohols and organic bases;
- Neutral NADESs with acids, prepared from carbohydrates or polyalcohols and organic acids;
3.3.3. Methods of DES Preparation
3.3.4. Physical–Chemical Properties of DESs
3.3.5. Techno-Economic Aspects and Engineering Challenges of Industrializing DES Extraction
4. Isolation of Phenolic Compounds from Forest Biomass Using DESs/NADESs
5. Use of Phenolic Compounds from Bark Extracts
5.1. Polymer Industry
5.2. Agricultural and Food Industry
5.3. Pharmaceutical and Cosmetic Industries
5.4. Protection of Cultural Heritage Objects
6. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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| Chemical Composition of Wood and Bark (wt%) | Coniferous Trees | Deciduous Trees | ||
|---|---|---|---|---|
| Wood | Bark | Wood | Bark | |
| Lignin | 25–30 | 40–55 | 18–25 | 40–50 |
| α-Cellulose | 45–58 | Not detected | 42–48 | Not detected |
| Polysaccharides | 66–72 | 30–48 | 74–80 | 32–45 |
| Hemicelluloses | 13–18 | Not detected | 18–27 | Not detected |
| Extractive compounds | 2–9 | 2–25 | 2–5 | 5–10 |
| Ash | 0.2–0.6 | 1–2.5 | 0.2–0.6 | 1.5–11 |
| Extraction Category | Method | Main Advantages | Main Disadvantages |
|---|---|---|---|
| Traditional methods | Maceration | Simple protocol and low operation costs. No sophisticated equipment required. Suitable for thermolabile compounds (at room temperature). | Extremely long extraction times (hours to days). Low extraction yields. High consumption of hazardous organic solvents. |
| Soxhlet extraction | High extraction efficiency due to continuous recycling of fresh solvent. No filtration required after extraction. | High risk of thermal degradation of sensitive phenolics. High energy consumption (continuous heating). Large volumes of toxic organic solvents needed. | |
| Non-traditional methods | Ultrasound-assisted extraction (UAE) | Short extraction time. Enhanced mass transfer via acoustic cavitation. Reduced solvent consumption. | Difficult to scale up to industrial levels. Potential degradation of compounds due to localized high temperatures/pressures. |
| Microwave-assisted extraction (MAE) | Very rapid heating and short extraction times. High extraction yields. Reduced environmental impact compared to Soxhlet. | High equipment costs. Restricted to polar or moderately polar solvents. Risk of thermal degradation for highly volatile/sensitive compounds. | |
| DES-based extraction | DES extraction (often combined with UAE/MAE) | Highly tunable selectivity (‘designer solvents’). Negligible vapor pressure and high thermal stability. Biodegradable, nontoxic, and nonflammable (for most biomass-derived DESs). High extraction capacity for both hydrophilic and hydrophobic phenolic compounds. | High viscosity limits mass transfer (requires dilution with water or heating). Difficult and energy-intensive recovery of both target compounds and the solvent. Lack of comprehensive Life Cycle Assessment (LCA) data. |
| Methods of Recovery | Mechanism/Principle | Main Technical Difficulties and Challenges |
|---|---|---|
| Antisolvent precipitation | Water is added to disrupt the DES hydrogen bonding network, decreasing the solubility of target phenolics and forcing them to precipitate. | High energy consumption required to evaporate water during subsequent DES recycling. Restricted mainly to hydrophobic or poorly water-soluble phenolic compounds. |
| Macroporous resin adsorption | Phenolics are selectively adsorbed onto solid polymeric resins (e.g., XAD series), while the DES passes through. Phenolics are then recovered using a volatile eluent (ethanol). | High viscosity of the DES impairs mass transfer and flow rate, leading to column clogging. Requires initial dilution, leading to partial DES dissociation. Gradual loss of resin adsorption capacity over repeated cycles. |
| Membrane filtration (ultrafiltration or nanofiltration) | Pressure-driven separation occurs, where target molecules and DES components are separated based on molecular weight cut-off (MWCO) and size exclusion | Severe membrane fouling due to the complex nature of bark extracts. High operating pressures required to process highly viscous DES fluids. Limited chemical compatibility of some commercial membranes with aggressive DES components (e.g., organic acids). |
| Supercritical CO2 (scCO2) extraction | Supercritical CO2 is used as a green solvent to selectively back-extract phenolic compounds directly from the DES phase. | High investment costs for high-pressure industrial equipment. Low solubility of highly polar, multi-hydroxyl phenolic compounds in pure scCO2 (requires co-solvents). |
| DES Composition | Molar Ratio and Water Content | Target Phenolic Compounds | Source Material (Literature) | Prospective European Tree Species | Extraction Conditions and Yield | Ref. |
|---|---|---|---|---|---|---|
| PART A: Prospective applications based on food industry by-products (proof of concept models) | ||||||
| Choline chloride + Lactic acid | 1:2 20 wt% | Quercetin glycosides | Walnut tree leaves (Juglans regia L.) | Beech Oak Hornbeam Pine | * HAE (50 °C, SESR of 0.15 g/5 mL, 600 rpm for 60 min) 5.7–9.9 mg/g | [119] |
| Choline chloride + Lactic acid | 1:2 20 wt% | Chlorogenic acid | Mulberry leaves (Morus alba L.) | Hornbeam | * MAE (60 °C, power 600 W, SESR of 0.05g/mL for 20 min) 4.507 mg/g | [120] |
| Choline chloride + Glycerol | 1:3 10 wt% | Total polyphenols and flavonoids | Lemon peels (Citrus limon) | Beech Oak Hornbeam, Pine Spruce Fir | * UAE (80 °C, sonification power 140 W, frequency 37 kHz for 90 min, SESR of 100 mL/g 53.76 mg GAE/g, 19.42 mg RE/g | [121] |
| Choline chloride + Lactic acid | 1:2 - | Apigenin | Virgin olive oil (Olea europaea) | Hornbeam | * SLE (40 °C, with agitation for 1 h, being vortexed for 1 min every 15 min, SESR of 1 g/g 0.120 mg/kg | [122] |
| PART B: Validated applications on bark matrices (directly related to this review) | ||||||
| Levulinic acid + Formic acid | 28:12 (v/v) 60 (v/v) | Polyphenols | Bark (Pinus Pinaster) | All investigated species | USE (20 kHz, 130 W) 1.5 g of biomass/10 mL solvents, 30 °C, 40 min) 315.50 mg GAE/g | [123] |
| Choline chloride + Glycolic acid | 1:2 10 wt% | Total phenolic compounds | White birch bark (Betula papyrifera) | All investigated species | UAE (56 °C, 16 min, 423 W, 1:51.49 g/mL 29.17 mg/g | [124] |
| L-proline + Sorbitol | 1:2 10 wt% | Flavonoids | Bark (Cercis chinensis) | All investigated species | UAE (42 °C, 40 min and 8 wt% of water) 87.6 mg/g | [125] |
| Levulinic acid + Formic acid | 70:30 (v/v) | Polyphenols | Maritime pine (Pinus pinaster Aiton) | All investigated species | UAE (30 °C, 40 min, with ultrasound amplitude of 80% at 37 kHz) ~60 mg/g | [115] |
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Štosel, M.; Ház, A.; Nadányi, R.; Jančíková, V. Deep Eutectic Solvents as a Potential Alternative Extraction Technique for the Isolation of Phenolic Compounds from Economically Important European Tree Species. Processes 2026, 14, 1877. https://doi.org/10.3390/pr14121877
Štosel M, Ház A, Nadányi R, Jančíková V. Deep Eutectic Solvents as a Potential Alternative Extraction Technique for the Isolation of Phenolic Compounds from Economically Important European Tree Species. Processes. 2026; 14(12):1877. https://doi.org/10.3390/pr14121877
Chicago/Turabian StyleŠtosel, Martin, Aleš Ház, Richard Nadányi, and Veronika Jančíková. 2026. "Deep Eutectic Solvents as a Potential Alternative Extraction Technique for the Isolation of Phenolic Compounds from Economically Important European Tree Species" Processes 14, no. 12: 1877. https://doi.org/10.3390/pr14121877
APA StyleŠtosel, M., Ház, A., Nadányi, R., & Jančíková, V. (2026). Deep Eutectic Solvents as a Potential Alternative Extraction Technique for the Isolation of Phenolic Compounds from Economically Important European Tree Species. Processes, 14(12), 1877. https://doi.org/10.3390/pr14121877

