Evaluating Green Solvents for Bio-Oil Extraction: Advancements, Challenges, and Future Perspectives
Abstract
:1. Introduction
2. Traditional Solvents vs. Green Solvents
2.1. Solvent Extraction with Traditional Organic Solvents
2.2. Environmental and Health Concerns Associated with Traditional Solvents
“VOC means any compound of carbon, excluding carbon monoxide, carbon dioxide, carbonic acid, metallic carbides or carbonates, and ammonium carbonate, which participates in atmospheric photochemical reactions, except those designated by EPA as having negligible photochemical reactivity”.
“VOCs, are organic chemical compounds whose composition makes it possible for them to evaporate under normal indoor atmospheric conditions of temperature and pressure”[56].
2.3. Introduction to Green Solvents and Their Advantages
3. Classification of Green Solvents
- Composition: Bio-based solvents are derived from renewable biomass sources, such as plants, algae, or microorganisms.
- Properties: Bio-based solvents are typically non-toxic and biodegradable, and have low VOC content. They offer favorable health and environmental profiles compared to petroleum-based solvents.
- Composition: Water is the primary component of water-based solvents, often supplemented with small amounts of other solvents or additives.
- Properties: Water-based solvents are non-toxic, non-flammable, and have low VOC emissions. They are readily available, inexpensive, and have high heat capacity.
- Composition: Supercritical fluids are typically gases or liquids that are above their critical temperature and pressure, resulting in a distinct supercritical state.
- Properties: Supercritical fluids are a hybrid between a gas and a liquid. Their solvating power is adjustable, they have low viscosity, and high diffusivity. The most popular choice for supercritical fluids is supercritical carbon dioxide (CO2).
- Composition: DES are liquid solvents composed of a eutectic mixture of two or more components, typically a hydrogen bond donor (HBD) and a hydrogen bond acceptor (HBA) [117]. These components can include both bio-based and non-bio-based compounds.
- Properties: They often have low toxicity, low volatility, and high thermal stability. DES can be tailored to possess specific characteristics, such as tunable polarity, viscosity, and solubility, by selecting different combinations of HBD and HBA components [118].
- Applications: DES find applications across various industries and processes. They have been used as green solvents in extraction processes for natural products, such as extraction of bioactive compounds from plant materials. DES have also shown promise in catalysis and electrochemistry, and as reaction media for organic synthesis. In addition, DES have been explored for their potential in industrial applications such as metal processing, biomass conversion, and separation processes [119].
3.1. Bio-Based Solvents
3.1.1. Ethyl Lactate
3.1.2. Limonene
3.1.3. 2-Methyltetrahydrofuran (2-MeTHF)
3.1.4. γ-Valerolactone (GVL)
3.1.5. Dimethyl Carbonate (DMC)
3.1.6. Ionic Liquids (ILs)
3.1.7. Terpenes
3.2. Water-Based Solvents
3.2.1. Water
3.2.2. Aqueous Solution of Acids
3.2.3. Aqueous Solutions of Bases
3.2.4. Aqueous Alcohol Solutions
3.2.5. Aqueous Organic Solvents
3.3. Supercritical Fluids
3.3.1. Supercritical Carbon Dioxide (scCO2)
3.3.2. Supercritical Water (scH2O)
3.3.3. Supercritical Ethanol (scEtOH)
3.3.4. Supercritical Propane (scC3H8)
3.3.5. Supercritical Nitrogen (scN2)
3.4. Deep Eutectic Solvents
3.4.1. Choline Chloride–Urea
3.4.2. Choline Chloride–Glycerol
3.4.3. Choline Chloride–Ethylene Glycol
3.5. Properties of Green Solvents
4. Performance Evaluation of Green Solvents
4.1. Solvent Power
4.1.1. Solubility Parameters
Interactions with Different Solute Classes
4.1.2. Bio-Oil Extraction Yields Using Green Solvents
4.1.3. Selectivity
4.2. Energy Requirements
4.2.1. Reduced Energy Consumption
4.2.2. Economics Feasibility and Scalability
5. Environmental Concerns: Challenges and Limitations
5.1. Safety, Health and Environmental Issues
Solvents | Safety Score | Health Score | Environmental Score | Ranking by Default | Ranking by Discussion | Overall Health and Environmental Concerns | |
---|---|---|---|---|---|---|---|
Water- and Bio-Based solvents | Water | 1 | 1 | 1 | Recommended | Recommended | Water and bio-based green extraction solvents offer reduced toxicity and environmental impact. Concerns include water pollution, human health effects (inhalation and skin contact), ecological impacts on aquatic ecosystems, and sustainability of sourcing and production. Proper waste management, safety measures, and research are essential for safe and responsible use. |
Ethanol | 4 | 3 | 3 | Problematic | Recommended | ||
EA | 5 | 3 | 3 | Recommended | Recommended | ||
Diethyl ether | 10 | 3 | 7 | Hazardous | Highly Hazardous | ||
MTBE | 8 | 3 | 5 | Hazardous | Hazardous | ||
MeTHF | 6 | 5 | 3 | Problematic | Problematic | ||
DME | 7 | 10 | 3 | Hazardous | Hazardous | ||
Cyclohexane | 6 | 3 | 7 | Problematic | Problematic | ||
Benzene | 6 | 10 | 3 | Hazardous | Highly Hazardous | ||
Carbon disulfide | 9 | 7 | 7 | Hazardous | Highly Hazardous | ||
Glycerol | 1 | 1 | 7 | Problematic | Problematic | ||
GVL | 1 | 5 | 7 | Problematic | Problematic | ||
CPME | 7 | 2 | 5 | Problematic | Problematic | ||
D-limonene | 4 | 2 | 7 | Problematic | Problematic | ||
p-cymene | 4 | 5 | 5 | Problematic | Problematic | ||
DMC | 4 | 1 | 3 | Recommended | Recommended | ||
Ethyl lactate | 3 | 4 | 5 | Problematic | Problematic | Deep Eutectic Solvents (DES) extraction solvents present low toxicity and biodegradability. | |
DES Solvents | ChCl (HBA) | - | - | - | Not a hazardous substance [235] | ||
Gly (HBD1) | - | - | - | ||||
ChCl/Gly | - | - | - | All DESs were toxic [236] |
5.2. Other Challenges and Limitations
- Sourcing and availability of biomass feedstock;
- Cost fluctuations and economic feasibility;
- Variability in solvent properties due to biomass composition;
- Limited compatibility with certain solute classes.
- Limited solubility for hydrophobic compounds;
- Potential formation of emulsions in biphasic systems;
- Difficulty in extracting polar compounds;
- Challenges in separating solvent from water after extraction.
- High energy requirements for maintaining supercritical conditions;
- Limited solubility for certain compounds;
- High capital costs associated with supercritical fluid extraction equipment;
- Challenges in recovering and recycling supercritical fluids.
- Limited understanding of long-term environmental impacts;
- Challenges in optimizing DES properties for specific applications;
- Potential for high viscosity and reduced mass transfer rates;
- Limited availability of DES with desired properties.
5.2.1. Bio-Based Solvents Challenges
5.2.2. Water-Based Solvents Challenges
5.2.3. Supercritical Fluid Challenges
5.2.4. DES Challenges
6. Future Research and Outlook
6.1. Bio-Based Solvents
6.2. Water-Based Solvents
6.3. Supercritical Fluids
- Exploration of alternative sources for supercritical fluids with high availability and sustainability.
- Development of innovative methods for extracting and producing supercritical fluids from renewable resources.
- Optimization of supercritical fluid extraction processes to enhance efficiency and reduce energy consumption.
- Development of cost-effective methods for supercritical fluid generation and recovery.
- Modification of supercritical fluid properties through the addition of modifiers or co-solvents to improve selectivity and extraction efficiency.
- Investigation of new solvents or solvent blends with tailored properties for specific extraction applications.
- Evaluation of the environmental impact and carbon footprint of supercritical fluid extraction processes.
- Implementation of sustainable practices in supercritical fluid production, such as using renewable energy sources and reducing waste generation.
- Investigation of scale-up strategies for supercritical fluid extraction processes to facilitate commercial production.
- Application of supercritical fluid extraction in various industries, such as pharmaceuticals, food processing, and natural product extraction.
- Integration of supercritical fluid extraction with other green technologies to enhance overall process efficiency and sustainability.
- Development of innovative extraction techniques and equipment to improve the performance and versatility of supercritical fluid extraction.
6.4. DES Solvents
- Exploration of novel DES compositions to expand the range of solvents available for different extraction applications.
- Investigation of the influence of DES composition and structure on extraction efficiency, selectivity, and solute compatibility.
- Development of environmentally friendly and sustainable methods for synthesizing DES.
- Assessment of the environmental impact and biodegradability of DES to ensure their safe and sustainable use.
- Optimization of DES extraction processes through the study of extraction parameters, such as temperature, pressure, and solvent-to-feed ratio.
- Development of innovative extraction techniques and equipment to improve the efficiency and scalability of DES-based extraction processes.
- Development of efficient and cost-effective methods for the recovery and recycling of DES to minimize waste generation.
- Exploration of techniques for regenerating and reusing DES to enhance the economic feasibility and sustainability of the extraction process.
- Investigation of the solute–solvent interactions in DES-based extraction processes to enhance selectivity and improve the extraction of target compounds.
- Understanding the influence of DES composition on solute compatibility and the extraction of different classes of compounds.
- Evaluation of the scalability of DES-based extraction processes for industrial applications.
- Demonstration of the feasibility and economic viability of DES extraction on a larger scale in various industries, such as pharmaceuticals, biotechnology, and natural product extraction.
7. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Bio-Oil | Temperature (°C) | Extraction Solvents | Extraction Yield (wt.%) | Ref. | |
---|---|---|---|---|---|
Feedstocks | Production Process | ||||
Biomass | Thermal Liquefaction | 25–70 | Alcohols (i.e., methanol) | 24–65 | [32] |
Alkanes (i.e., n-hexane) | |||||
Acetic acids | |||||
Furfural | |||||
Diethyl ether | |||||
Toluene | |||||
Ethylbenzene | |||||
Water | |||||
Water/methanol mixture | |||||
Microalgae | Hydrothermal Liquefaction (HTL) | 250–310 | Dichloromethane (DCM) | 23 | [33] |
Sewage sludge (SS) | HTL | 350 | DCM | 9.34 | [34] |
SS | Catalytic-HTL (catalyst and ethanol as solvent) | 350 | DCM | 61.51 | |
Rubberwood sawdust | Liquefaction in subcritical water | 280–320 | Acetone | 30.41 | [35] |
Ethanol | 23.45 | ||||
DCM | 28.14 | ||||
Ethyl acetate (EA) | 27.66 | ||||
Rubberwood sawdust | Liquefaction in subcritical ethanol | 280–320 | Acetone | 30.29 | |
Ethanol | 25.15 | ||||
DCM | 29.76 | ||||
EA | 31.69 | ||||
Pine wood | Catalytic-Pyrolysis | 500 with heating rate (100/min) | DCM | 61.1–72 | [36] |
Pine wood | Non-catalytic Pyrolysis | 500 with heating rate (100/min) | DCM | 71.6 | |
Pine sawdust | Fast Pyrolysis | 500 | Acetone | ~36 * | [37] |
Pine sawdust | Catalytic-Pyrolysis | 550 | Acetone | 53.4 | |
Delonix regia (Lignocellulosic biomass) | Catalytic-Pyrolysis | 600 | DCM | 26.48 | [38] |
Delonix regia | Non-catalytic Pyrolysis | 600 | DCM | 27.18 | |
Olive mill waste water sludge | Fast Pyrolysis | 500 | DCM | 60 | [39] |
Spent coffee grounds traditional | Pyrolysis | 700 | DCM | 12.64 | [40] |
Spent coffee grounds decaffeinated | Pyrolysis | 700 | DCM | 9.90 | |
Jatropha Curcas seed cake | Slow Pyrolysis | 550 with heating rate (5/min) | EA | 3.79 | [31] |
DCM | 3.63 | ||||
Carbon tetrachloride | 1.02 | ||||
Diethyl ether | 2.50 | ||||
Benzene | 2.02 | ||||
hexane | 2.34 | ||||
Rice straw | Pyrolysis | 500 | DCM | 41–47 | [41,42] |
Yarrowia lipolytica (oleaginous yeast) | SE + | Room Temperature (RT) | Methanol/Hexane | 10–28 | [43] |
Sweet melon seeds | SE + | RT | n-Hexane | 0.5–1 | [44] |
Citrus seeds (mandarin) | SE (Soxhlet) + | 60 | n-Hexane | 27.61 | [45] |
Citrus seeds (bitter orange) | SE (Soxhlet) + | 60 | n-Hexane | 36.42 | |
Wastewater scum of dairy industry | SE | 25–50 | Hexane | 48–54 | [46] |
Wet SS | SE | RT | Hexane | 38–41 | [14] |
Dewatered SS | SE | RT | Hexane | 30 | [47] |
Dried SS | SE (Soxhlet) + | n-Hexane | 0.94–1.75 | [48] | |
Lyophilized algae | SE (Soxhlet) + | n-Hexane | 13.41 | [49] | |
Chukrasia tabularis L. (C. tabularis) seed | SE (Soxhlet) + | n-Hexane | 27.9 | [50] | |
Petroleum ether | 27.7 | ||||
Chloroform | 24 | ||||
Acetone | 15 | ||||
Chukrasia tabularis L. (C. tabularis) seed | AUH = + SE (Soxhlet) + | n-Hexane | 32 | ||
Petroleum ether | 30 | ||||
Chloroform | 26 | ||||
Acetone | 15.2 | ||||
Seeds of Jatropha curcas | SE+ | 25–80 | n-Hexane | 41–46 | [51] |
Petroleum ether | 39–44 | ||||
Ethanol | 37–41 | ||||
Karanja Seed | SE (Soxhlet) + | 50 | n-Hexane | 22–34 | [52] |
Algae | 40–50 |
Solvents | Classification | Boiling Range (°C) | Environmental and Human Health Hazards | Ref. | |
---|---|---|---|---|---|
Environmental Concerns | Human Health Concerns | ||||
Methanol | VVOCs | <0 to 50–100 °C | Water Pollution: Methanol contaminates water, harms aquatic ecosystems. Groundwater Contamination: Leaked methanol endangers groundwater quality. Atmospheric Pollution: Methanol worsens smog and formaldehyde formation. | Toxicity: Highly toxic if ingested or absorbed. Inhalation: Respiratory irritation and CNS depression. Fire Hazard: Flammable and explosive. Handle with care. | [55,56,59,60,61,62,63,64] |
DCM | Improper disposal contaminates water, threatens aquatic life. DCM contributes to ozone depletion, damaging the ozone layer. DCM pollutes air, contributes to ozone and smog formation. | DCM is a potential human carcinogen, linked to liver and lung cancer. Inhalation causes dizziness, headaches, confusion, and potential neurological damage. Metabolized in the liver, DCM can cause liver toxicity and affect kidney function. | [65,66,67,68] | ||
Ethanol | VOC emissions contribute to ozone and smog formation. Energy-intensive production and crop cultivation impact land and water, and cause deforestation. Improper handling contaminates water and soil, harming ecosystems. | Flammability and Fire Hazard: Highly flammable, requires proper storage and fire safety. Inhalation Risks: Respiratory irritation, CNS depression, potential organ damage. Impaired Judgement and Addiction: Excessive use leads to intoxication, impaired coordination, addiction. | [69,70,71,72] | ||
Chloroform | Persistence and Bioaccumulation: Chloroform harms ecosystems and aquatic life by persisting and bioaccumulating. Water Contamination: Improper disposal pollutes water, threatens drinking water supplies. Ozone Depletion: Chloroform contributes to upper atmosphere ozone depletion. | Carcinogenic Potential: Probable human carcinogen linked to liver, kidney, and bladder cancers. Central Nervous System Effects: Inhalation causes dizziness, confusion, potential unconsciousness. Liver and Kidney Damage: Chronic exposure leads to toxicity in liver and kidneys. | [73,74,75,76] | ||
n-Hexane | VOCs | 50–100 to 240–260 | Air Pollution: Volatile emissions contribute to ozone and smog formation in VOC-rich areas. Soil and Water Contamination: Improper disposal harms soil, water, and aquatic life. Hazardous Waste Generation: Hexane use creates hazardous waste, needs proper disposal to prevent pollution. | Inhalation Hazards: Headaches, dizziness, respiratory irritation. Prolonged exposure leads to neuropathy. Flammability: Highly flammable, fire and explosion hazards. Follow proper handling. Occupational Health Risks: Prolonged exposure causes neurological disorders. Implement safety measures. | [55,77,78,79,80] |
Ethyl ether | VOC Emissions: Contributes to ground-level ozone and smog formation, degrading air quality. Flammability: Highly flammable, forms explosive mixtures. Improper handling poses fire and explosion risks. | Inhalation Hazards: Respiratory irritation, dizziness, CNS depression. Narcotic Effects: Drowsiness, loss of consciousness. Environmental Persistence: Short lifespan, but improper disposal causes contamination. | [81,82,83,84] | ||
Acetone | VOC Emissions: Degrades air quality, contributes to ozone and smog formation. Water Contamination: Improper disposal harms aquatic ecosystems. Effects on Ozone Layer: Negligible ozone depletion potential, not regulated. | Inhalation Hazards: Respiratory irritation, coughing, CNS depression with excessive exposure. Skin and Eye Irritation: Contact causes dryness, redness, eye irritation. Use protective measures. Flammability: Highly flammable, low flash point. Follow proper storage, fire safety. | [85,86,87,88,89] | ||
Benzene | Air Pollution: VOC contributes to ozone and smog formation. Water and Soil Contamination: Improper disposal pollutes water and soil, risks ecosystems. Toxic Effects on Plants and Animals: Impairs growth, reduces crop yields, harms aquatic organisms. | Carcinogenicity: Human carcinogen linked to blood-related cancers. Blood Disorders: Affects cell production, causes anemia, impaired immune function. Neurological and Developmental Effects: Headaches, cognitive impairment, potential developmental abnormalities. | [90,91,92,93,94,95] | ||
Furfural | Air Pollution: Contributes to ozone, smog, degrading air quality. Water Contamination: Improper disposal harms water, risks aquatic organisms. Soil and Ecosystem Impacts: Potential effects on soil, microbial activity. Further study needed. | Irritation and Sensitization: Causes skin, eye, respiratory irritation; risk for individuals with respiratory conditions. Occupational Hazards: Workers at risk; implement safety measures. Carcinogenic Potential: Further research needed on genotoxic and carcinogenic effects. | [96,97,98,99] | ||
Acetic acid | Water Contamination: Improper disposal contaminates water, harms aquatic organisms. Acidification: Disrupts ecosystems, impacts aquatic life. Hazardous Waste Generation: Proper disposal prevents environmental pollution. | Inhalation Hazards: Irritates respiratory system, worsens pre-existing conditions. Skin and Eye Irritation: Causes burns, eye damage on contact. Corrosive Properties: Damages tissues with prolonged contact. | [100,101,102] | ||
Petroleum ether | Air Pollution: VOC emissions contribute to ozone, smog formation. Water and Soil Contamination: Improper handling contaminates, harms ecosystems. Persistence: Petroleum ether can persist, contaminate soil, water. | Flammability and Explosion Hazard: Highly flammable, forms explosive mixtures. Inhalation Hazards: Respiratory irritation, CNS effects with prolonged exposure. Skin and Eye Irritation: Causes dryness, redness, temporary vision disturbances. | [103,104,105] |
Solvents | Molar Mass (g.mol−1) | Solubility in Water | Boiling Point (°C) | Melting Point (°C) | Density (g/mL) | Vapor Pressure | Viscosity | Appearance | Ref. |
---|---|---|---|---|---|---|---|---|---|
Water | 18 | 100 | 0 | 1.000 at 3.98 °C | 23.8 mmHg at 25 °C | 0.8949 mPa·s at 25 °C | colorless | [165,166] | |
Ethanol | 46.07 | 106 mg/mL at 25 °C | 78.24 | −114.4 | 0.7893 at 20 °C | 10 kPa at 29.2 °C | 1.074 mPa·s at 25 °C | colorless | [167,168] |
EA | 88.1 | 8.3 g/100 mL at 20 °C | 77.1 | −83.6 | 0.9006 at 20 °C 0.8945 at 25 °C | 73.0 Torr at 20 °C | 0.45 cP at 20 °C | colorless | [169,170] |
Diethyl ether | 74.12 | 6.05 g/100 mL at 25 °C | 34.55 | −116.3 | 0.7133 at 20 °C 0.7076 at 25 °C | 442 Torr at 20 °C | 0.24 cP at 20 °C | colorless | [171,172] |
MTBE ** | 88.2 | 4.2 g/100 mL at 20 °C | 55 | −109 | 0.74 at 25 °C | 27 kPa at 20 °C | 0.36 cP at 25 °C | colorless | [173] |
MeTHF * | 86.13 | 15 g/100 mL at 25 °C | 80.2 | −136 | 0.854 at 25 °C | 3.6 kPa at 20 °C 34.5 kPa at 50 °C | 4 mPa·s at 25 °C | colorless | [174,175] |
DME ++ | 46.07 | 71 g/L at 20 °C | −24 | −141 | 0.735 (liquid, at −25 °C) | 592.8 kPa at 25 °C | colorless gas | [176,177] | |
Cyclohexane | 84.161 | immiscible | 80.7 | 6.47 | 0.7739, liquid at 25 °C | 78 mmHg at 20 °C | 1.02 cP at 17 °C | colorless | [178,179] |
Benzene | 78.114 | immiscible | 80.5 | 5.5 | 0.8765 at 20 °C | 12.7 kPa at 25 °C | 0.6076 cP at 25 °C | colorless | [180] |
Carbon disulfide | 76.13 | slightly soluble | 46.5 | −111.5 | 1.266 at 25 °C | 48.1 kPa at 25 °C | 0.363 cP at 20 °C | colorless | [181] |
Glycerol | 92.094 | miscible | 290 | 17.9 | 1.26 at 25 °C | 0.40 Pa at 50 °C | 1.412 Pa·s at 20 °C | colorless | [182,183] |
GVL | 100.116 | 100 mg/mL | 205 | −31 | 1.0546 at 20 °C | 3.5 kPa at 80 °C | colorless | [184,185] | |
CPME + | 1.1 g/100 g at 23 °C | 106 | −140 | 0.86 at 25 °C | 59.9 hPa at 25 °C | 0.57 cP at 20 °C | colorless | [186,187] | |
D-limonene | 136.238 | insoluble | 176 | −74.35 | 0.844 at 25 °C | 190 Pa at 20 °C | 0.8462 mPa·s at 25 °C | colorless | [188,189] |
p-cymene | 134.222 | insoluble | 177 | −68 | 0.86 at 25 °C | 1.5 mmHg at 20 °C | 0.81–7.1 mm2/s | colorless | [190] |
DMC | 90.078 | 13.9 g/100 mL at 25 °C | 90 | 2–4 | 1.069 at 25 °C | 18 mmHg at 21.1 °C | 0.625 cP at 20 °C | colorless | [191] |
Ethyl lactate | 118.131 | miscible | 154.2 | −25 | 1.0328 at 20 °C | 1.16 mmHg at 25 °C | 0.0261 cP at 20 °C | colorless | [192] |
Feedstocks | Process | Extraction | Green Solvents | Extraction Yield (wt.%) | Conventional Solvents | Extraction Yield (wt.%) | Ref. |
---|---|---|---|---|---|---|---|
Rapeseed oil | SE | Fatty acids | MeTHF | 45.96 | n-Hexane | 46.34 | [197] |
Oleaginous Yeast Biomass | SE | Lipids | MeTHF | 14.56 | n-Hexane | 14.04 | [198] |
CPME | 15.33 | ||||||
IPA - | 15.48 | ||||||
ethanol | 15.02 | ||||||
ethyl acetate | 14.05 | ||||||
ethyl lactate | 15.23 | ||||||
DMC | 14.94 | ||||||
p-cymene | 15.57 | ||||||
d-Limonene | 13.67 | ||||||
α-pinene | 13.97 | ||||||
Rice bran | SE | Oil | d-limonene | 15.8 | n-Hexane | 18.9 | [199] |
Fennel seed | SE | Oil | MeTHF | ~20 | n-Hexane | ~15.3 | [200] |
Anise seed | SE | Oil | MeTHF | ~23 | n-Hexane | ~15.1 | |
Carum carvi seeds | SE | Oil | MeTHF | ~16 | n-Hexane | ~12 | [201] |
Microalgae (C. vulgaris) | SE | Oil | d-limonene | 1.29 | n-Hexane | 0.88 | [202] |
α-pinene | 0.91 | ||||||
ρ-cymene | 1.52 | ||||||
Microalgae (Chlorella vulgaris) | SE | Oil | Ethyl acetate | 11.7 | n-Hexane | 7 | [203] |
Ethyl lactate | 20.8 | ||||||
CPME+ | 9.4 | ||||||
MeTHF | 14.8 | ||||||
Microalgae (Nannochloropsis sp.) | Ethyl acetate | 13.6 | n-Hexane | 9.8 | |||
Ethyl lactate | 31.1 | ||||||
CPME | 11.4 | ||||||
MeTHF | 19.1 | ||||||
Spent coffee ground | SE | DME Bio-crude | Liquified DME | 16.8 | [204] | ||
Tea leaf waste | 16.2 | ||||||
Orange peel | 6.2 | ||||||
Gramineous weed | 5.8 | ||||||
Spent coffee ground | SE | DME Bio-crude | Liquified DME | 16.8 | n-Hexane | 17.2 | [205] |
Tea leaf waste | 16.2 | 1.9 | |||||
Orange peel | 6.2 | 0.9 | |||||
Wet microalgae (Chlorella pyrenoidosa) | SE | Lipids | MeTHF | 69.8 | [206] | ||
CPME | 68.0 | ||||||
Dried rapeseed (Brassica napus) | SE | FFA | MeTHF | 99.2 | [197] | ||
Sterols | 91.9 | ||||||
Almond (dry) | SE | Lipids | D-limonene | 95.7 | [207] | ||
Corn (dry) | 95.3 | ||||||
Olive (dry) | 93.2 | ||||||
Dried palm seeds (Phoenix dactylifera L.) | SE | Lipids | MeTHF | 82.5 | [208] | ||
Brassica napus straw | SE | HTL Bio-crude | Ethyl acetate + Ethanol | 22.11 | [209] | ||
Duckweed Lemna minor (L. minor) | SE | HTL Bio-crude | Ethyl acetate | 20 | DCM | 24 | [210] |
Carbon disulfide | 17 | n-Hexane | 3 | ||||
Cyclohexane | 9 | Petroleum ether | 4 | ||||
Benzene | 18 | ||||||
IPA | 26 | ||||||
Diethyl ether | 17 | ||||||
Dichloroethane | 19 | ||||||
Microalgae (Nannochloropsis sp.) | SE | HTL Bio-crude | MTBE | 29–37 | DCM | 26–35 | [211] |
Ethyl acetate | 19–45 | n-Hexane | 13–28 | ||||
Acetone | 29–32 | ||||||
Chloroform | 32–40 | ||||||
Fennel seed | SFE -- | Oil | Sc-CO2 | ~15 | n-Hexane | ~15.3 | [200] |
Anise seed | SFE | Oil | SC-CO2 | ~17 | n-Hexane | ~15.1 | |
Carum carvi seeds | SFE | Oil | SC-CO2 | ~12 | n-Hexane | ~12 | [201] |
Algae (Nannochloropsis salina sp.) | SFE | Oil | SC-CO2 | 31.37 | [212] | ||
Grape Seed | SFE | Phenolic Compounds | SC-CO2 | 12.32 | [213] | ||
Cotton Seed | SFE | Oil | SC-H2O | 21.7–56 | [214] | ||
Jojoba Seed | SFE | Oil | SC-H2O | 94 | [215] | ||
Citrus hystrix DC. leaves | SFE | Oil | SC-H2O | 2.14 | [216] | ||
De-oiled Jatropha curcas cake | SE | HTL Bio-crude | ChCl–KOH DES (1:4) ~ | 43.53 | [217] | ||
ChCl–p-TsOH DES (1:4) ~ | 38.31 | ||||||
ChCl–Gly (1:3) ~ | 26.63 | ||||||
ChCl–FeCl3 (1:3) ~ | 30.80 |
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Usman, M.; Cheng, S.; Boonyubol, S.; Cross, J.S. Evaluating Green Solvents for Bio-Oil Extraction: Advancements, Challenges, and Future Perspectives. Energies 2023, 16, 5852. https://doi.org/10.3390/en16155852
Usman M, Cheng S, Boonyubol S, Cross JS. Evaluating Green Solvents for Bio-Oil Extraction: Advancements, Challenges, and Future Perspectives. Energies. 2023; 16(15):5852. https://doi.org/10.3390/en16155852
Chicago/Turabian StyleUsman, Muhammad, Shuo Cheng, Sasipa Boonyubol, and Jeffrey S. Cross. 2023. "Evaluating Green Solvents for Bio-Oil Extraction: Advancements, Challenges, and Future Perspectives" Energies 16, no. 15: 5852. https://doi.org/10.3390/en16155852
APA StyleUsman, M., Cheng, S., Boonyubol, S., & Cross, J. S. (2023). Evaluating Green Solvents for Bio-Oil Extraction: Advancements, Challenges, and Future Perspectives. Energies, 16(15), 5852. https://doi.org/10.3390/en16155852