Submitted:
10 June 2024
Posted:
11 June 2024
You are already at the latest version
Abstract
Keywords:
Introduction
1.1. Sources of Plastic in the Environment
Detection of MPs and NPs
Properties of MPs and NPs
- A wide size range, ranging from 1 μm to 1 mm (and up to 5 mm for larger MPs).
- Diverse polymer types with varying chemical compositions, including both conventional and biopolymers with different structures and densities.
- Various shapes such as spheres, irregular particles, fibers, films, and foams.
- Incorporation of different additives (antioxidants, light stabilizers, plasticizers, flame retardants, pigments, etc.), weathering byproducts, and adsorbed contaminants (persistent organic pollutants, antibiotics, heavy metals, etc.).
- Different aging states (primary and secondary MPs), biofouling, surface charge, and hydrophobicity [48].
Impact on the Environment and Human Healthy
The Techniques for Removing MPs and NPs from Water
5.1. Membrane Filtration
5.1.1. Ultrafiltration
5.1.2. Reverse Osmosis
5.2. Centrifugation
5.3. Flocculation
5.4. Photocatalytic Degradation
5.5. Bioreactors
5.6. Improved Adsorption
5.7. Utilizing Nanomaterials
MNPs (Properties, Synthesis Methods, Functionalization)
Published Scientific Articles on the Removal of MPs and NPs Using MNPs
Conclusions
Acknowledgments
Conflicts of Interest
References
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| PLACE | MPs TYPE | MPs SIZE | PROFUSION |
|---|---|---|---|
| Netherlands (tap and surface water) | PS, PE | 50, 100, 200, 500, 1000 nm (PS), 90-106 µm | 260 mg/L |
| Denmark (fish sample) | PS, PE | 100 nm (PS), 200-9900 nm (PE) |
1.3 mg/g fish |
| USA (seawater) | PP, PE, PS, PA | ≤ 5 mm | 0.025 g/mL |
| South Korea (seawater and beach) | expanded polystyrene (EPS) | ≤ 1 mm | 0–0.3 items/L (seawater), 631 items/L (beach) |
| China (surface sediment) | Rayon, PE, PP, PA, PET, PS, PMMA, PU | 34.97–4983.73 μm | 499.76 items/kg |
| Italy (shallow waters) | PE, PP, PS | ≤ 1 mm | 672-2175 items/kg |
| China (sediment) | High-density polyethylene (HDPE), PET, PE, PS | ≤ 5 mm | 5.1-87.1 items/g sediment |
| China (sewage) | PET, PS, PP | 681.46±528.73 μm | 0.59–12 items/L |
| China (freshwater bodies) | PES, rayon, PP, PA, nylon | 20 to 5000 μm | 0.9–2.4 items/L |
| Australia (shrimp) | PS, rayon | 0.190–4.214 mm | 0.40±0.27 items/L |
| China (fishes) | PE, PP, PES | 20–500 μm | 0.3–5.3 items per fish |
| Germany (bottled water) | PET, PP | 1–500 μm | 0–253 items/L |
| Mexico (milk) | PES, polysulfone (PSU) | ≤ 5 mm | 3–11 items/L |
| METHOD | THE SIZE OF REMOVED NP [nm] | REMOVAL EFFICIENCY [%] | LIMITS |
|---|---|---|---|
| Filtration | 217-333 | 32-92 | Not suitable for larger particles, as they may remain in the fraction. |
| Ultrafiltration | ≤ 150 | 74 | Particles can evade treatment; the process can be time-consuming. |
| Flocculation | 217 | 77 | More studies are needed to determine the optimal parameters. |
| Centrifugation | 206 | 98 | Time-consuming process. |
| Photocatalytic degradation | ≤ 100 | 17.1 | The phototransformation of NPs can vary and the photo-reactive activity in water can be high. |
| Membrane bioreactor filtration | ≥ 2 | 99 | Proper hydraulic retention time. |
| Sample types | MNPs | characterization | method | Particles size of MPs, NPs | Removal efficiency/ adsorption capacity | Main findings | Ref. |
|---|---|---|---|---|---|---|---|
| solutions of MP (PS) | Fe3O4 | XRD, FTIR, DLS, SEM, TEM | magnetic separation | 100, 500, 1000 nm | 83.1 % - 92.9 % in a 1 h period | Electrostatic attraction between electropositive Fe3O4 MNPs and electronegative MPs led to charge neutralization-induced aggregation and efficient removal MP performance. | [173] |
| solutions of MPs (PE, PP, PS, PET) in pure, artificial, and environmental water samples | magnetic nano-Fe3O4 | FTIR, SEM | surface absorption, magnetic separation | 200-900 μm | 62.83 % - 86.87 % in a max. 240 min | Physicochemical properties of MPs such as crystallinity, hydrophobicity, and density, as well as background solutions influence the removal efficiency. | [174] |
| microPS particles from the water | magnetic iron oxide (Fe3O4) nanoparticles | TEM, FTIR | adsorption process, desorption process | 0.08, 0.43, 0.7 and 1 μm | 42.0 % - 93.7 % depending on the concentration, total surface area and number of PS particles | Hydrophobic interactions are the main interactions involved in the aggregation of Fe3O4 with PS particles. The Fe3O4particles could be recovered from the Fe3O4-PS complexes by desorption process. | [4] |
| Salt and freshwater samples | iron oxide nanoparticles with several polydimethylsiloxane hydrophobic coatings | SEM, TEM, SQUID, DLS, XRD, zeta potential | absorption process | 2-5 mm; 100-1000 nm | 90.0 % - 100 % | They removed 100 % of particles in a range of sizes, from 2-5 mm, and nearly 80 % of NP particles with a size range from 100 nm to 1000 nm using a sample 2-inch permanent NdFeB magnet. | [3] |
| solution of PS, PMMA, ME | modified superparamagnetic γ-Fe2O3, 9.6 nm | ATR-FTIR, TGA, DLS; SEM, | magnetic removal | 100 nm – 100 μm | polymer types of 2.5 – 5 μm for the maximum removal yield in terms of removed MPs and NPs mass (up to 5.38 g/g SPION); MPs and NPs of 100 nm – 1 μm in terms of highest numbers (up to 10 trillion MP and NP fragments per gram SPIONs) | If the size of the MPs is further increased, number as well as mass related efficiency is reduced as the specific surface area decreases rapidly. | [175] |
| nonmarine waters in a recyclable and scalable way | SMR consists of an ion-exchange resin microsphere functionalized by superparamagnetic Fe3O4 nanoparticles | SEM, EDX, magnetic measurements, DLS, a confocal microscope | dynamic adsorption process; magnetic removal | 0.2 – 40 μm | > 90 % over 100 treatment cycles | As a result of the long-range electrophoretic attraction established by recyclable ion-exchange resin, the magnetorobot shows sustainable removal efficiency of > 90 % over 100 treatment cycles, with verified broad applicability to varying plastic compositions, sizes, and shapes as well as nonmarine water samples. | [176] |
| solutions of MPs (PS, PE) | Magnetic Janus microparticles (MJMs) synthesized via a modified Pickering emulsion method with aminated Fe3O4@SiO2 as the raw material | FTIR, TGA, SEM, contact angle analysis | adsorption process | 10 μm | 92.08 % for PS and 60.67 % for PE in just 20 min | Kinetic and thermodynamic studies confirmed the remarkable rate and capacity of the MJMs (0.759 min-1 and 2.72 mg/mg for PS, 0.539 min-1 and 2.42 mg/mg for PE), underlining their potential as a promising method for the rapid removal of MPs from water. | [177] |
| MPs in five liquid food systems | Fe3O4@Cn (n= 12, 14, 16, 18), modified by different saturated fatty acids (C12, C14, C16, C18) | TEM, AFM, FTIR, XRD, XPS, VSM, BET, TGA, contact angle measurements | nitrogen adsorption measurements | 100 nm | Fe3O4@C12 exhibited 92.89 % adsorption efficiency | A practical and simple method for the adsorption and removal of MPs from various liquid samples, where Fe3O4@C12 showed the desired adsorption efficiency. | [178] |
| PE MPs in water | Fe3O4; PEG/Fe3O4; PEI/Fe3O4; CA/Fe3O4 | FTIR, BET, zeta potential analysis, XRD, | magnetism adsorption | 13-149 μm | 2202.55 mg/g | The PEG/Fe3O4 exhibited a high magnetic capture efficiency of PE MPs in water. | [179] |
| PS MPs | magnetic activated biochar-zeolite composite (MACZ) coated with PEG and PEI (PMACZ) | SEM, EDX, BET, XRD, TGA, VSM | adsorption | 2 and 15 μm | 736 mg/g and 769 mg/g for PMACZ on 2 μm and 15 μm MP | After 4 cycles, the efficiency of the adsorbent decreased by 2.3 % and 2 % for PMACZ and MACZ, respectively, demonstrating the efficiency and high cycling capacity of these adsorbents. | [180] |
| PE, PET, PA | magnetic carbon nanotubes (M-CNTs) | UV-Vis, VSM, XRD, SEM, FTIR, XPS, zeta potential, TGA | magnetic force | 48 μm | 100 % | The mechanism analyses clearly suggested that the adsorption of M-CNTs by PE was caused by the strong hydrophobicity of MPs, the adsorption of M-CNTs by PET was caused by hydrophobic interaction and π-π electron conjugation, and π-π electron interaction, complexation, electrostatic interaction, and hydrogen bonding interaction on the PA surface all contributed to the adsorption of M-CNTs. | [181] |
| PS NPs in water | CuNi carbon material (CuNi@C) | SEM, FTIR, XPS, XRD, BET | adsorption process | 100 nm | 99.18 % | After 4 times cycles, CuNi@C can still remove ~ 75 % of total PS NPs from water. | [123] |
| PE, PP and PS in aquatic environments | Ag nanoparticles | UV-Vis, DLS, TEM, XRD, SEM, EDX | adsorption process | 0.2-0.25 mm | 94.52 % | Results revealed that Ag nanoparticles could be captured on the surface of PS MPs but coexisted with PE and PP MPs in water solutions. | [182] |
| PE in wastewater | magnetic magnesium hydroxide coagulant (MMHC) through the combination of Mg(OH)2 and Fe3O4 | SEM, FTIR, XRD, zeta potential | adsorption process | ≤ 270 μm | 73.4 % - 92.6 % | Among the three kinds of MMHCs, the removal is the highest when the ratio of Mg2+ to OH- reaches 1:1, due to the dense bubble-like structure on its surface. | [183] |
| PS MPs in water | CuFe2O4 | XRD, VSM, BET, FTIR, SEM, EDX, XPS, | remove MPs with different photoaging degrees | 0.96 – 1.59 μm | 98.02 % | Hydrogen bonding played a key role in the removal of pristine PS MPs and the destruction of C=O by Fe-OOH also played an important role in the removal of aged PS MPs. | [184] |
| PS NPs in aqueous solutions | fly ash modified with Fe ions | UV-Vis, FTIR, SEM-EDX, XRD, XPS, VSM | adsorption process | 94.1 % | The adsorption-desorption experiments show that the fly ash modified with Fe ions adsorbents have excellent reusability for PS NPs; they can be used 4 times. | [185] | |
| PS MPs | a zeolitic imidazolate framework (ZIF-8) magnetic porous nanocomposite modulated with n-butylamine (nano-Fe@ZIF-8) | SEM, XRD, FESEM, BET, nitrogen adsorption-desorption measurements | magnetic removal | 1.1 μm | ≥ 98 % | The results illustrate the synthesis of a simple, environmentally friendly and high performing material for the fast removal of both soluble organic pollutants and microparticulated organic pollutants. | [186] |
| metal-doped PS NPs in ultrapure water, synthetic freshwater, synthetic freshwater with a model natural organic matter isolate and synthetic marine water | hydrophobically functionalized magnetic nanoparticles | EDX, DLS, SEM, XRD, | magnetic separation flow cell | 229 nm | 56.1 – 84.9 % | MNPs in combination with a flow-through system is a promising technique to extract NPs aqueous suspensions with various compositions. | [187] |
| PS NP/MPs in drinking water | magnetic bismuth ferrite (BiFeO) microparticles | XRD, zeta potential measurements, | 70-11000 nm | ≈ 95.5 % in 90 minutes | The results demonstrated that using photocatalysis + physical-adsorption is a feasible strategy to quickly remove MPs contaminants from the water. | [188] | |
| Polyethylene (PE) and PET MPs from model aqueous suspensions | Composite magnetic Fe-C-NH2 MNPs | DLS, SEM, optical microscopy, XRD, UV-Vis | Magnetic sedimentation | 5-30 μm | > 99 % | PE and PET MPs can be effectively separated from water by adding Fe-C-NH2 MNPs and performing subsequent sedimentation in a gradient magnetic field. | [189] |
| Amino – modified PS in aqueous suspension | Magnetic algae robots (algae cells with Fe3O4 bound on its surface) | SEM, EDX, XRD, zeta potential, magnetic measurements, fluorescence intensity measurements. | Removal under rotating magnetic field | 50 nm and 1.5 μm | 70 – 92 % | Magnetic field driven algae-mased microrobots can be used for effective capture and removal of micro/nanoplastics from the aquatic environment. | [190] |
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