A Review on Ionic Liquids in the Design of Carbon-Based Materials for Environmental Contaminant Removal
Abstract
1. Introduction
2. Carbonization of Ionic Liquids
2.1. Influence of IL Type on the Structure and Porosity of Carbon Materials
2.2. Tailoring Surface Functional Groups During Carbonization
2.3. Benefits and Limitations of IL-Derived Carbons
2.4. Adsorption Applications of IL-Derived Carbons
3. Interactions of Ionic Liquids with Carbon Materials
3.1. Surface Modification Through IL Adsorption
3.2. Interactions Between ILs and Carbon Surfaces
3.3. Effects of IL Functionalization on Selectivity and Adsorption Capacity
4. Activation of Carbon Materials Using Ionic Liquids
4.1. IL-Assisted Activation Methods
4.2. Control of Pore Structure and Specific Surface Area
4.3. Comparison with Conventional Activation Techniques
4.4. Sustainability and Potential for Industrial Application
5. Examples of Adsorption Applications
6. Challenges and Future Perspectives
7. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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| Carbon Support | IL Type/Functionalization | Target Contaminant(s) | Adsorption Performance (If Reported) | Dominant Interactions/Advantages | Reference |
|---|---|---|---|---|---|
| MWCNT | Vinyl-pyridinium PIL grafting | Cr(VI) | Up to ~37% removal (12 h) | Electrostatic and π-interactions | [130] |
| Activated carbon | Confined amine-based ILs | CO2 | Improved uptake at elevated T | Chemical affinity + reduced pore blocking | [109] |
| GO laminate | Imidazolium IL (mimG-GO) | Anionic dyes (DR80, RB5, MO) | >99% for DR80, RB5, MO | Cation–π interactions improving membrane stability; controlled interlayer spacing, electrostatic and steric exclusion | [103] |
| Biochar (corn stover biochar, CSB) | Imidazolium IL grafted via trimethoxysilylpropyl linker | Cd2+ | qe ≈ 48.1 mg g−1 (vs. 44.0 mg g−1 for raw CSB) | Shifted adsorption sites, stronger H-bonding | [131] |
| Graphene | PIL grafting (poly(1-vinylimidazole) | MB | Up to 1910 mg g−1 | Strong π–π interactions, fast kinetics | [100] |
| GO | PIL covalent bonding (P[MATMA][BF4]) | CO2 | 21.54 cm3 g−1 at 0 °C and 900 mmHg (vs. 3.07 cm3 g−1 for GO) | Increased surface area, abundant BF4− sites enabling Lewis acid–base CO2 interactions, enhanced porosity, and affinity | [132] |
| GO | PIL microemulsion composite | MO | qmax up to 128 mg g−1 | Hydrogen bonding, hydrophobic PF6− interactions, improved GO dispersion, and increased adsorption sites | [133] |
| Activated carbon (from mixed recyclable waste) | Phosphonium IL | Hg(II) | qmax = 105 mg g−1 (vs. ~44 mg g−1 for unmodified AC at optimal pH) | Strong coordination/chelation via phosphorus sites in IL + enhanced surface functionality | [134] |
| Activated carbon | Hydrophobic IL grafting | PFAS | Up to ~2.26-times higher removal efficiency (six PFAS in DWTP influent) vs. pristine AC | Anion-exchange (IL sites) + hydrophobic interactions → selective PFAS uptake from real water | [106] |
| Activated carbon | Imidazolium IL impregnation ([C2MIM][NTf2], [C6MIM][NTf2]) | PFAS | 1.4–1.96× higher removal vs. pristine AC in real surface water, lower efficiency in DI water | Anion exchange + IL thin-film partitioning | [105] |
| CNT (MWCNT) | PIL grafting via mussel-inspired PDA + RAFT polymerization ([C16VIm][Br]) | CR | qmax = 254.6 mg g−1, qe ≈ 176 mg g−1 at 56 min; markedly higher vs. pristine CNT (100.9 mg g−1) | Electrostatic attraction + π–π stacking (imidazolium ring—CR aromatic system), enhanced dispersibility, dense IL-derived active sites | [135] |
| GO–cellulose composite (CGC) | IL processing in [Bmim]Cl | Ce(III) | qmax ≈ 109 mg g−1 | Ion-exchange mechanism (confirmed by XPS) | [136] |
| GO | Aliquat-336 impregnation (quaternary ammonium IL) | Cr(VI) | qmax = 285.71 mg g−1,, 99.8% removal in 45 min | Ion-pairing, pH-dependent selectivity | [97] |
| MWCNT | IL functionalization (tetra-n-heptylammonium bromide) | Cr(VI)/Cr(III) | qmax = 85.83 mg g−1, ~99.5% removal at 0.15–0.20 g dose, equilibrium in 40 min | Cation–π, anion–π, electrostatic | [95] |
| Reduced GO | IL modification | Cr(VI) | qmax ≈ 232.55 mg g−1 | Electrostatic and chemical interactions, enhanced adsorption over GO/rGO due to IL functionalization | [137] |
| GO sponge | Imidazolium IL | Cr(VI) | qmax = 208.3 mg g−1 at 23 °C, 99.3% removal of 10 ppm Cr(VI) | Electrostatic attraction + π-electron-assisted reduction of Cr(VI) → Cr(III), hierarchical porous sponge prevents GO restacking and increases accessibility of IL sites | [138] |
| GO | Dicationic IL | Cr(VI) | qmax = 263.8–281.5 mg g−1 (298–308 K), experimental qe ≈ 260.9 mg g−1 at pH 3 | Electrostatic attraction between anionic Cr(VI) species and protonated imidazolium N+, combined with partial reduction of Cr(VI) → Cr(III) | [139] |
| GO | Amine-functionalized IL grafting | Phthalates (PAEs) | Adsorption capacities ranged ~266–484 µg g−1 (for different PAEs | π–π interactions, hydrophobic interactions with IL alkyl chains, enhanced GO interlayer spacing and increased surface area → improved uptake of hydrophobic phthalates | [91] |
| GO | Imidazolium IL grafting | DR80 | qmax = 500 mg g−1, equilibrium in ~10 min, 99.2% removal retained after 4 cycles | Strong electrostatic, H-bonding, and π–π interactions, IL prevents GO restacking, ultrafast adsorption rate (588 mg g−1 min−1) | [82] |
| GO | IL 1-hexyl 3-decahexyl imidazolium | Pharmaceuticals (sulfamethoxazole SMZ, carbamazepine CBZ, ketoprofen KET) | Higher adsorption than pristine GO (q ≈ 27.25 mg g−1 for SMZ on GO–IL vs. lower on GO) | Hydrogen bonding + van der Waals + electrostatic/π–π (IL–drug interactions) + improved dispersion of GO in water | [83] |
| GQDs | IL-capped | Cr(VI) | qmax = 934.6 mg g−1 (pH 7) | Electrostatic attraction between protonated IL groups and anionic Cr(VI) species + surface complexation/ion-exchange, IL capping prevents GQD aggregation and increases accessible active sites | [140] |
| MoS2-RGO | Imidazolium IL coating | MB | qmax = 143.9 mg g−1, high removal; reusable ~78% after 5 cycles | Electrostatic attraction + π–π interactions, IL improves dispersion, magnetic separation | [141] |
| GO | PIL functionalization | CR | qmax = 191.9 mg g−1, near-saturation within 5 min | Electrostatic attraction between cationic PIL and anionic CR, π–π stacking; H-bonding; enhanced uptake vs. pristine GO | [142] |
| Spherical activated carbon (SAC) | Polymerized IL (poly(1-vinyl-3-butylimidazolium hexafluorophosphate) | Ibuprofen | ≈2-fold higher adsorption capacity vs. pristine SAC | Improved hydrophobic and electrostatic interactions from the PIL layer | [143] |
| MWCNT | IL-based polyether (poly(1-glycidyl-3-methylimidazolium chloride), PGMIC) | Anionic azo dyes (Orange II, Sunset Yellow FCF, Amaranth) | qmax = 67.57 mg g−1 (Orange II), 85.47 mg g−1 (Sunset Yellow), 47.39 mg g−1 (Amaranth) at 25 °C, rapid adsorption | Electrostatic attraction + charge neutralization, IL polymer improves CNT dispersion | [144] |
| GO–SiO2 composite | IL-assisted synthesis | Pb(II), As(III) | qmax = 527 mg g−1 for Pb(II), qmax = 30 mg g−1 for As(III), >99% removal within 60 min, stable over 4 cycles | Synergistic porosity + IL-assisted dispersion of GO, electrostatic attraction, ligand exchange, surface complexation | [108] |
| Nanoporous carbon | Task-specific ionic liquid precursors (EBI-T, EBI-B, BBI-T, HBI-T, NBI-T, XBI-T) | CO2 | CO2 uptake = 2.01–3.59 mmol g−1 at 0 °C, 1.23–2.49 mmol g−1 at 25 °C, surface area 588–1277 m2 g−1 (depending on IL precursor) | High N-doping from IL precursors enhances CO2 affinity, IL structure determines microporosity/mesoporosity and adsorption strength, TSILs act as both carbon and heteroatom source | [145] |
| GO-magnetic composite (MGO) | Bifunctional ionic liquid + chitosan grafting (IL/Chit@MGO) | Tetracycline | High loading capacity for aptamer (5.80 × 10−7 mol g−1), rapid binding (20 min) | Electrostatic attraction (positive IL/Chit@MGO—negative aptamer), π–π stacking, H-bonding, IL provides selective interaction sites, magnetic separation | [146] |
| GO (electrochemically N/B/F-codoped RGO) | Imidazolium IL precursor ([EMIM][BF4] | Tetracycline | 93% removal (5 mg L−1) in 60 min, TOC removal 40% | Nonradical AOP pathways; high electron-transfer efficiency | [147] |
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Terzić, T.; Mitrović, T.; Perović, M.; Lazarević-Pašti, T. A Review on Ionic Liquids in the Design of Carbon-Based Materials for Environmental Contaminant Removal. Processes 2026, 14, 352. https://doi.org/10.3390/pr14020352
Terzić T, Mitrović T, Perović M, Lazarević-Pašti T. A Review on Ionic Liquids in the Design of Carbon-Based Materials for Environmental Contaminant Removal. Processes. 2026; 14(2):352. https://doi.org/10.3390/pr14020352
Chicago/Turabian StyleTerzić, Tamara, Tatjana Mitrović, Marija Perović, and Tamara Lazarević-Pašti. 2026. "A Review on Ionic Liquids in the Design of Carbon-Based Materials for Environmental Contaminant Removal" Processes 14, no. 2: 352. https://doi.org/10.3390/pr14020352
APA StyleTerzić, T., Mitrović, T., Perović, M., & Lazarević-Pašti, T. (2026). A Review on Ionic Liquids in the Design of Carbon-Based Materials for Environmental Contaminant Removal. Processes, 14(2), 352. https://doi.org/10.3390/pr14020352

