Sustainable Bio-Based Plasticizers: Advances in Polyols and Natural Compound Derivatives from Sorbitol, Glycerol, Cardanol, and Limonene
Abstract
1. Introduction
2. Sorbitol and Polyol Esters
2.1. Raw Materials and Source
2.2. Chemical Structure and Key Features
2.3. Physicochemical and Mechanical Properties
2.4. Chemical Modification Strategies
2.5. Environmental and Toxicological Profile
2.6. Synthesis–Application Insight
3. Glycerol Derivatives
3.1. Raw Materials and Source
3.2. Chemical Structure and Key Features
3.3. Physicochemical and Mechanical Properties
3.4. Chemical Modification Strategies
3.5. Cost and Industrial Feasibility
3.6. Environmental and Toxicological Profile
4. Cardanol-Based Plasticizers
4.1. Raw Materials and Source
4.2. Chemical Structure and Key Features
4.3. Physicochemical and Mechanical Properties
4.4. Chemical Modification Strategies
4.5. Cost and Industrial Feasibility
4.6. Environmental and Toxicological Profile
5. Limonene-Based Plasticizers
5.1. Raw Materials and Source
5.2. Chemical Structure and Key Features
5.3. Physicochemical and Mechanical Properties
5.4. Chemical Modification Strategies (If Applicable)
- Polymerizing: Limonene polymerized for higher-molecular-weight derivatives with increased stability. Poly limonene oxide (PLO) was prepared by catalytic ring-opening polymerization [22].
- Covalently bonded: A second good substitute is molecular grafting. A limonene-derived polyhedral oligomeric silsesquioxane (POSS) modifier has been reported in which various limonene moieties were covalently bonded to a silicate cage through hydrosilylation [23].
- Esterification: Outside of changing limonene by means of itself, terpenoid esters of related nature like linalyl acetate and geranyl acetate have also been considered monomeric plasticizers. Migration behavior is the main drawback of low-molecular-weight plasticizers. To do this, the researchers used reactive extrusion with dicumyl peroxide, which stimulated peroxide-induced grafting from the terpene plasticizers to the PLA backbone. This chemical anchoring decreased leaching and maintained mechanical properties during aging [27].
- 4.
- Bio-additives: Limonene has also been utilized as one of the co-added compounds with other bio-additives for such multi-functional materials.
5.5. Environmental and Toxicological Profile
6. Techno-Economic Screening of Bio-Based Plasticizer Routes
6.1. Sorbitol Esters
6.2. Glycerol-Derived Systems
6.3. Cardanol/CNSL Derivatives
6.4. Limonene Derivatives
7. Challenges and Future Perspectives
7.1. Development of Polymeric Plasticizers from Renewable Resources
7.2. Exploration of Reactive Plasticizers with Covalent Bonding
7.3. Systematic Long-Term Aging and Durability Studies
7.4. Development of Standardized Testing Protocols and Regulatory Frameworks
8. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
| AcMAE | Acetylated Malate Ester |
| ASTM | American Society for Testing and Materials |
| CNSL | Cashew Nutshell Liquid |
| DEHP | Di(2-ethylhexyl) Phthalate |
| DINP | Diisononyl Phthalate |
| DOP | Dioctyl Phthalate |
| DOTP | Dioctyl Terephthalate |
| ECO-BDO | Butanediol-Modified Epoxidized Cardoon Oil |
| ECO-SORB | Sorbitol-Modified Epoxidized Cardoon Oil |
| EPA | Environmental Protection Agency |
| EU | European Union |
| FTIR | Fourier-Transform Infrared Spectroscopy |
| GC-MS | Gas Chromatography–Mass Spectrometry |
| GRAS | Generally Recognized as Safe |
| GT | Glycerol Trilevulinate |
| HNTs | Halloysite Nanotubes |
| HPLC | High-Performance Liquid Chromatography |
| ISO | International Organization for Standardization |
| LDPE | Low-Density Polyethylene |
| MSNs | Mesoporous Silica Nanoparticles |
| NMR | Nuclear Magnetic Resonance |
| OECD | Organisation for Economic Co-operation and Development |
| PBAT | Poly(butylene adipate-co-terephthalate) |
| PCL | Polycaprolactone |
| PHB | Polyhydroxybutyrate |
| PHBV | Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) |
| PLA | Poly(lactic acid) |
| PLO | Poly(limonene oxide) |
| POSS | Polyhedral Oligomeric Silsesquioxane |
| PU | Polyurethane |
| PVA | Poly(vinyl alcohol) |
| PVC | Poly(vinyl chloride) |
| REACH | Registration, Evaluation, Authorisation and Restriction of Chemicals |
| ROP | Ring-Opening Polymerization |
| SLNs | Solid Lipid Nanoparticles |
| NLCs | Nanostructured Lipid Carriers |
| TGA | Thermogravimetric Analysis |
| Tg | Glass Transition Temperature |
| Tm | Melting Temperature |
| ZnO | Zinc Oxide |
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| Sources | Extraction Method | Chemical Modification | Physicochemical Properties | Uses | Biocompatibility and Toxicity | Environmental Impact | Economic Considerations |
|---|---|---|---|---|---|---|---|
| Sorbitol (fruits/plants); glycerol (biodiesel by-product) | Commercially available; no extraction in study | None (used neat) | Improves flexibility and elongation by reducing H-bonding; glycerol increases permeability and flexibility | Plasticizers for starch-based biodegradable films | Safe; biodegradable; renewable | Eco-friendly; sustainable alternative to synthetic plasticizers | Low cost; abundant (notably glycerol) |
| Propylene glycol + fatty acids (bio-based) | Esterification of propylene glycol; epoxidation of unsaturated bonds | Polyol esters and epoxidized esters | Improved tensile strength and elongation; reduced swelling; enhanced barrier properties | Plasticizers for sodium alginate antimicrobial food packaging films | Bio-based; food-contact safe; antimicrobial when combined with extracts | Biodegradable; renewable | Cost-effective; scalable esterification |
| Isosorbide from glucose/sorbitol | Hydrogenation of glucose → sorbitol → isosorbide; esterification | Isosorbide esters | Thermally stable; biodegradable; hygroscopic | Plasticizers for starch polymers and PLA | Non-toxic; hygroscopicity is a limitation | Renewable; biodegradable | Biomass-based; processing complexity adds cost |
| Commercial sorbitol | Used as purchased | None (neat sorbitol) | Improves flexibility, elasticity, thickness, morphology of alginate–starch films | Plasticizer for alginate–starch films (packaging, pharma) | Safe; antioxidant activity observed | Eco-friendly; renewable | Low cost; industrially available |
| Sorbitol/isosorbide from glucose | Glucose hydrogenation; esterification with fatty acids | Fatty acid esters | Lower Tg; improved flexibility; reduced migration for high-MW esters | Plasticizers for PLA, PHB, PHBV, starch, cellulose | Non-toxic; phthalate alternative | Fully bio-based; biodegradable | Low cost from biomass; multi-step processing |
| Isosorbide from sorbitol | Catalytic dehydration; esterification | Isosorbide esters and oligoesters | Reduced Tg; improved ductility; low migration | Plasticizers for PLA and compostable blends | Non-toxic; food-contact suitable | Renewable; biodegradable | Scalable; catalyst-dependent cost |
| Commercial sorbitol | Used as purchased | None | Improves flexibility; lowers modulus; increases surface energy | Plasticizer for chitosan-based wound dressings | Non-toxic; promotes cell viability (HaCaT) | Biodegradable; medical-safe | Low cost; scalable |
| Commercial sorbitol | Used as purchased | None | Enhanced tensile strength, crystalline; reduced moisture uptake | Plasticizer for corn-starch bioplastic films | Safe; biocompatible | Renewable; biodegradable | Low cost; suitable for scale-up |
| Sorbitol (glucose hydrogenation) | Catalytic hydrogenation (Raney Ni) | None (also intermediate for isosorbide) | Humectant; water-soluble; cooling effect; flexible plasticizer | Plasticizer for bioplastics; food and pharma uses | Non-toxic; laxative effect at high dose | Renewable; biodegradable | Low cost; million-ton industrial scale |
| Commercial sorbitol | Industrial glucose hydrogenation | None | Lowers Tg; increases ductility and flexibility; humectant effect | Plasticizer for PVA and biopolymer blends | Safe; food and medical compatible | Eco-friendly; renewable | Low cost; widely available |
| Sorbitol from biomass | Hydrogenation of glucose; esterification | Sorbitol esters | Improved flexibility; reduced Tg; enhanced elongation | Plasticizers for starch, PLA, PHB, cellulose | Non-toxic; food-contact safe | Biodegradable; renewable | Cost-effective; industrially scalable |
| Sorbitol + cardoon oil | Epoxidation of oil; acid-catalyzed ring opening with sorbitol | Sorbitol-modified epoxidized oil (ECO-SRB) | High OH number; Tg −16 °C; enhanced flexibility | Bio-plasticizer and biolubricant | Biodegradable; marine degradation confirmed | Renewable; circular economy | Cost-effective; added processing steps |
| Commercial sorbitol (with glycerol blend) | Used as purchased | None | Improved tensile strength, crystalline; reduced moisture uptake | Plasticizer for pullulan films and soft capsules | Safe; pharmaceutical grade | Biodegradable; renewable | Low cost; industrially viable |
| Sorbitol-based polyesters | Hydrogenation of glucose; melt polycondensation | Condensation with diacids/amino acids | High modulus; tunable degradation; biodegradable elastomers | Tissue engineering scaffolds; biomedical composites | Biocompatible; no toxicity reported | Renewable; biodegradable | Cost-effective feedstock synthesis-dependent cost |
| Sources | Extraction Method | Chemical Modification | Physicochemical Properties | Uses | Biocompatibility and Toxicity | Environmental Impact | Economic Considerations |
|---|---|---|---|---|---|---|---|
| By-product of biodiesel production (transesterification) | Chemical or enzymatic transesterification; purification by membrane separation or adsorption | Esterification to mono-, di-, and polyglycerol esters | Viscous, hygroscopic, water-soluble, high boiling point (~290 °C) | Food (humectant, emulsifier), cosmetics (moisturizer), pharmaceuticals (plasticizer, excipient) | GRAS; non-toxic; biocompatible | Biodegradable; eco-friendly | Low cost; abundant biodiesel by-product |
| Biodiesel production from vegetable oils | Glycerol separated during transesterification; melt blending with additives | Esterification and blending with citric acid, benzoic acid, and sunflower oil | Flexible; enhanced PVC compatibility; improved thermal stability; reduced crystallinity | PVC plasticizer; eco-friendly alternative to DOP | Non-toxic; safer than phthalates | Renewable; biodegradable; waste valorization | Low cost; high-value utilization of biodiesel waste |
| Renewable glycerol from biodiesel | Solvent-free esterification with succinic anhydride and alcohols | Glycerol–succinate derivatives with variable alkyl chains | Tg reduction in PLA (~44 °C); elongation up to 435%; thermal stability up to 293 °C; low migration | PLA plasticizer for food packaging | Non-toxic for C6 or shorter chains; moderate cytotoxicity for longer chains | Bio-based; biodegradable; low leaching | Renewable; scalable; potentially low cost |
| Biodiesel by-product from fats and oils | Direct recovery from transesterification process | Used directly or modified via esterification/blending | Trihydroxyl polyol; water-soluble; improves flexibility of biopolymers | Plasticizer for starch and cellulose-based biodegradable plastics | GRAS; non-toxic; biodegradable | Renewable; low environmental footprint | Low cost; industrial-scale availability |
| Biodiesel-derived glycerol from plant oils | By-product of biodiesel transesterification | Esterification to glycerol and succinate esters | Improves flexibility and thermal properties of PVC; reduces brittleness | Plasticizer for PVC films, medical devices, eco-packaging | Non-toxic; phthalate alternative | Biodegradable; low leachability | Abundant; industrially scalable |
| Commercial glycerol (renewable, biodiesel origin) | Commercially available; no extraction | None (used as pure glycerol) | Improves flexibility; increases moisture uptake; reduces density | Plasticizer for edible Persian gum films | Safe; edible; GRAS | Biodegradable; renewable | Low cost; readily available |
| Glycerol (biodiesel by-product) and adipic acid | Esterification synthesis | Hyperbranched glycerol–adipate polyesters | Flexible; biodegradable; compatible with compostable polymers | Plasticizer for PLA, PHB, PBAT green packaging | Non-toxic; food-contact suitable | Renewable; biodegradable; low toxicity | Cost-effective; scalable production |
| Glycerol (biodiesel) and levulinic acid (cellulose waste) | Solvent-free esterification under mild conditions | Glycerol trilevulinate (GT) | Reduces Tg and Tm; improves flexibility; low volatility and migration | Plasticizer for PVC, PLA, PHB, PHBV, PCL | Cytocompatible (IC50 ~4–6 mg/mL in fibroblasts) | Fully bio-based; biodegradable; waste valorization | Cost-effective; scalable |
| Biodiesel-derived glycerol | Esterification and alkyl functionalization | Glycerol esters with C3–C7 and branched alkyl chains | PVC Tg reduction (54–86 °C); high elongation; DOTP-like thermal stability | Flexible PVC plasticizers | Low cytotoxicity for short chains; mild toxicity for longer chains | Renewable; biodegradable | Low cost; scalable |
| Renewable malic acid | Esterification with alcohols followed by acetylation | Acetylated malate tri-esters (AcMAE-Cn) | High thermal stability (up to 336 °C); low migration; improved flexibility | Plasticizers for PVC and PLA packaging films | Bio-based; presumed safe (cytotoxicity not directly evaluated) | Renewable; biodegradable; low leaching | Scalable; potentially low cost |
| Ethylene glycol and natural fatty acids | Microwave-assisted esterification | Fatty acid esters of ethylene glycol | High flexibility; improved thermal stability; enhanced migration resistance | PVC plasticizers for biomedical and antimicrobial applications | Non-toxic; antimicrobial activity when combined with thiazoles | Biodegradable; safer than phthalates | Energy-efficient; cost-effective synthesis |
| Extraction Method | Chemical Modification | Physicochemical Properties | Uses | Biocompatibility and Toxicity | Environmental Impact | Economic Considerations |
|---|---|---|---|---|---|---|
| Cardanol synthesized by reaction with 3-chloro-2-hydroxypropanoic acid followed by cyclization with acetone/H2SO4 | Formation of cardanol-based dioxolanone for PLA copolymerization | Lowers PLA Tg; reduces crystallinity; increases amorphous phase and flexibility | PLA additive to improve flexibility and reduce brittleness | Bio-based; low toxicity expected; no direct biocompatibility assays reported | Renewable; biodegradable within PLA matrix | Cost-effective due to CNSL abundance |
| Flash column chromatography (MeCN/H2O/AcOH, 80:20:1) with solvent recovery (~82%) | Fractionation and optional epoxidation of triene moieties | Phenolic OH; unsaturated alkenyl chains; confirmed by NMR, GC-MS, HPLC, FTIR | Bio-plasticizers, coatings, polymers, adhesives, antibacterial and flame-retardant systems | No specific assays reported; expected lower toxicity than petrochemical analogues | Renewable; agro-waste valorization; solvent recovery improves sustainability | Cost-effective through CNSL utilization and solvent recycling |
| Steglich esterification with fatty acids followed by epoxidation (HCOOH/H2O2) | Esterification and epoxidation of phenolic and alkenyl groups | Lower Tg; enhanced flexibility; thermal and mechanical performance comparable to DINP-PVC | Primary PVC plasticizers (phthalate alternatives) | Low ecotoxicity; no endocrine disruption (YES/YAS); safer than DINP | Fully bio-based; biodegradable; eco-friendly | Cost-effective due to CNSL availability; industrially viable |
| Thermal decarboxylation of anacardic acid followed by chemical derivatization | Esterification, epoxidation, acetylation, etherification, glycidylation | Reduced Tg; improved thermal stability; higher elongation; phthalate-comparable mechanics | Plasticizers for PVC, PLA, cellulose acetate, and rubber | Several derivatives non-toxic and non-endocrine disrupting | Renewable; biodegradable; safer than petrochemical plasticizers | Economical due to CNSL; some routes use costly reagents |
| Vacuum-distilled cardanol; hydroxyethylation followed by methacrylation | Conversion to cardanol methacrylate monomer | Adjustable Tg (−35 to 10 °C); increased modulus; higher crosslink density | Bio-based latex coatings and films | No direct toxicity data; expected safer than petrochemical analogues | Renewable; reduced VOCs; high biorenewable carbon index | Cost-effective; suitable for coatings industry |
| Vacuum distillation followed by chemical functionalization | Esterification, sulfonation, quaternization; coupling with glycols, amines, sugars, epoxides | Amphiphilic behavior; reduced surface tension; biodegradable; antimicrobial activity | Surfactants, detergents, coatings, adhesives, bioplastics, plasticizers | Low toxicity; some derivatives antimicrobial with low cytotoxicity | Renewable; biodegradable; petrochemical replacement | Cost-effective; supports circular economy |
| Solvent extraction and vacuum distillation | Acetylation and epoxidation of cardanol | Lower Tg; enhanced flexibility; improved thermal and mechanical performance in PVC | PVC plasticizers; epoxy diluents; cellulose acetate additives | Bio-based; non-toxic; safer than phthalates | Renewable; biodegradable; agro-waste valorization | Cost-effective; some applications are higher than phthalates |
| Thermal decarboxylation and vacuum distillation; multi-step functionalization | Epoxidation, ring-opening, esterification, thiol–ene, Mannich reactions to polyols | High OH values (≤553 mg KOH/g); tunable flexibility; good thermal properties | Plasticizers for PU, polyesters, epoxies; coatings and adhesives | Low toxicity; biodegradable; some flame-retardant derivatives | Renewable; supports green chemistry | Economical feedstock: synthesis complexity may affect scale-up |
| Extraction with rosin acid derivative and esterification (oxalyl chloride/pyridine) | Cardanol–rosin ester plasticizer | Lower Tg; improved elongation; good miscibility with PVC | Phthalate-free PVC plasticizers | Non-toxic; no migration issues reported | Fully bio-based; biodegradable | Cost-effective from agro-waste; moderate synthesis cost |
| Friedel–Crafts alkylation (100 °C, p-TSA catalyst) | Polymerized cardanol (alkylated phenolic polymer) | Mw ≈ 4 × 104; Tg −20.7 °C; high elongation and rubber compatibility | Plasticizer/compatibilizer for rubber formulations | Bio-based; low toxicity expected; minimal migration | Renewable; solvent-free synthesis | Cost-effective; scalable rubber applications |
| Hot oil, solvent, or supercritical CO2 extraction; vacuum distillation | Esterification, epoxidation, phosphorylation, etherification | Lower Tg; enhanced thermal stability; high polymer compatibility | Plasticizers for PVC, NR, EPDM, EVA; surfactants and adhesives | Non-toxic; phthalate-free; no endocrine disruption | Renewable; biodegradable | Cost-effective; growing CNSL market |
| Pyrolysis or supercritical CO2 extraction; vacuum distillation | Esterification, epoxidation, Mannich, thiol–ene, polymerization | Thermally stable; hydrophobic; strong mechanical performance; low permeability | Plasticizers, coatings, adhesives, resins, rubbers, composites | Low toxicity expected; some flame-retardant derivatives | Renewable; fossil-free alternative | Cost-effective feedstock: purification may add cost |
| Sources | Extraction Method | Chemical Modification | Physicochemical Properties | Uses | Biocompatibility and Toxicity | Environmental Impact | Economic Considerations |
|---|---|---|---|---|---|---|---|
| Limonene (citrus fruits) | Infusion into cellulose fibers followed by hot pressing with PLA | None (physical encapsulation) | Lower Tg; improved flexibility and elongation; sustained antioxidant activity (>3 days) | Active food and cosmetic packaging; antibacterial applications | GRAS; non-toxic | Renewable; biodegradable; eco-friendly | Low cost from citrus waste; volatility requires encapsulation |
| Polyethylene glycol sorbitan esters (Tween® 20, 80) | Commercially obtained | None (used as plasticizers) | Reduced Tg (PLA 61 → ~29.5 °C); elongation up to 194%; higher impact resistance | PLA plasticizers for packaging and bioplastics | Non-toxic; widely used in food and pharma | Renewable; biodegradable; phthalate-free | Cost-effective; commercially available |
| d-Limonene (citrus peel oil) | Steam distillation, solvent, supercritical CO2, microwave hydrodistillation | None; nanoencapsulation (emulsions, SLNs, NLCs) | Volatile; low water solubility; bp 176 °C; oxidation-prone | Food packaging, cosmetics, pharma (antioxidant/antimicrobial) | GRAS; nanoform toxicity requires further study | Renewable; biodegradable; citrus waste valorization | Low raw material cost: encapsulation increases cost |
| Plant terpenes (essential oils) | Commercially sourced; blended into starch/CMC/CMS films | None | Lower Tg; higher flexibility; antimicrobial activity | Medical patches, wound dressings, antibacterial films | Low toxicity; dermatologically safe | Renewable; biodegradable | Cost-effective; volatility requires control |
| d-Limonene (citrus peel oil) | Steam distillation; solvent casting with chitosan | None | Higher flexibility; lower crystallinity; improved UV/WV barrier; reduced tensile strength at high loadings | Antimicrobial food packaging films | GRAS; non-toxic | Renewable; biodegradable | Low cost: stabilization needed |
| d-Limonene (citrus essential oils) | Electrospinning into PLA nanofibers | None (encapsulation) | Initial Tg reduction (~18 °C) with gradual increase due to evaporation | Antimicrobial wound dressings | GRAS; safe for medical use | Renewable; biodegradable | Low cost; volatility limits durability |
| d-Limonene (citrus essential oils) | Vacuum loading into mineral carriers; melt compounding with LDPE | Encapsulation in HNTs, MSNs, ZnONPs, molecular sieves | Lower tensile strength; higher flexibility; improved oxygen barrier | Antimicrobial food packaging films | GRAS; effective against E. coli | Renewable; sustainable additive | Low-cost feedstock: encapsulation adds complexity |
| Limonene (citrus peel oil) | Steam distillation followed by hydrosilylation | Hydrosilylation to silicone-modified limonene (SS-Limonene) | Lower Tg; improved rheology, adhesion, flexibility; higher thermal stability | PLA additives for 3D printing and injection molding | Low toxicity expected; long-term data limited | Renewable; waste-reducing | Cost-effective feedstock: reaction optimization needed |
| Linalool and geraniol (essential oils) | Commercial sourcing; melt compounding and reactive extrusion | Monomeric plasticizers; peroxide-assisted grafting | Elongation increase (~230–298%); Tg decrease (61.5 → 39.5 °C) | PLA packaging materials | Non-toxic; food-contact safe | Renewable; biodegradable | Cost-effective; REX adds complexity |
| d-Limonene (citrus peel oil) | Steam distillation; sol–gel ZnO synthesis with oleic acid modification | Oleic acid-modified ZnO; limonene blending | Lower Tg; higher crystallinity; antimicrobial activity | Antimicrobial food packaging and biomedical films | GRAS; ZnO provides sustained antibacterial action | Renewable; biodegradable | ZnO functionalization increases cost |
| d-Limonene (Calamansi waste) | Steam distillation; GC–MS/FTIR characterization | None | Volatile; antioxidant and antimicrobial activity | Plasticizer candidate; anticancer/pharma research | Cytotoxic to MCF-7 (IC50 7.98 μg/mL); lower toxicity to normal cells | Agro-waste valorization; biodegradable | Low cost; scalable |
| Limonene oxide (from d-limonene) | Steam distillation; catalytic ring-opening polymerization | ROP to poly limonene oxide (PLO) | PLA Tg decrease (~60 → 41 °C at 10 wt%); improved hydrophobicity | PLA plasticizer for packaging and agricultural films | Bio-based; non-toxic | Renewable; biodegradable | Cost-effective; catalyst optimization needed |
| Feedstock/Route | MSP (USD/kg) | CAPEX | OPEX | IRR (%) | Payback (y) | Key Cost Drivers |
|---|---|---|---|---|---|---|
| Sorbitol/polyol esters | 0.48–0.81 | NR | NR | 18.5–23.6 | NR | Sorbitol/glucose price; H2 uptake yield |
| Triacetin (glycerol) | ~2.2 | 18 M$ | NR | 16.8 | 4.6 | Glycerol feed cost; distillation energy (177 MJ/kg) |
| Glycerol carbonate | 0.628–0.689 | NR | NR | NR | NR | CO2 feed/purification; ionic-liquid catalysts |
| Cardanol/CNSL derivatives | NR | NR | NR | NR | NR | CNSL extraction yield; multi-step reaction costs |
| Limonene (extraction) | ~148 (oil) | NR | 148 (oil) | NR | NR | Extraction energy (supercritical CO2); peel availability |
| Limonene carbonate | NR | 161 $/tCO2 | 153 $/tCO2 | NR | NR | CO2 compression; IL catalyst cost |
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Share and Cite
Ghazzy, A.M.; Shraim, A.S.; Al-Sammarraie, T.R.; Al-Mohammadi, W.M.; Al-Hunaiti, A.H. Sustainable Bio-Based Plasticizers: Advances in Polyols and Natural Compound Derivatives from Sorbitol, Glycerol, Cardanol, and Limonene. Polymers 2026, 18, 985. https://doi.org/10.3390/polym18080985
Ghazzy AM, Shraim AS, Al-Sammarraie TR, Al-Mohammadi WM, Al-Hunaiti AH. Sustainable Bio-Based Plasticizers: Advances in Polyols and Natural Compound Derivatives from Sorbitol, Glycerol, Cardanol, and Limonene. Polymers. 2026; 18(8):985. https://doi.org/10.3390/polym18080985
Chicago/Turabian StyleGhazzy, Asma M., Ala’a S. Shraim, Tabarak R. Al-Sammarraie, Wurood M. Al-Mohammadi, and Afnan H. Al-Hunaiti. 2026. "Sustainable Bio-Based Plasticizers: Advances in Polyols and Natural Compound Derivatives from Sorbitol, Glycerol, Cardanol, and Limonene" Polymers 18, no. 8: 985. https://doi.org/10.3390/polym18080985
APA StyleGhazzy, A. M., Shraim, A. S., Al-Sammarraie, T. R., Al-Mohammadi, W. M., & Al-Hunaiti, A. H. (2026). Sustainable Bio-Based Plasticizers: Advances in Polyols and Natural Compound Derivatives from Sorbitol, Glycerol, Cardanol, and Limonene. Polymers, 18(8), 985. https://doi.org/10.3390/polym18080985

