Swaroop
Chakraborty
*a,
Roland
Drexel
b,
Prathmesh
Bhadane
ac,
Nathan
Langford
a,
Pankti
Dhumal
a,
Florian
Meier
b and
Iseult
Lynch
a
aSchool of Geography, Earth & Environmental Sciences, University of Birmingham, Edgbaston, B15 2TT, UK. E-mail: s.chakraborty@bham.ac.uk
bPostnova Analytics GmbH, Landsberg am Lech, Germany
cIndian Institute of Technology, Gandhinagar, 382055, India
First published on 11th March 2025
Micro- and nanoscale plastics (MnPs), arising from the environmental degradation of plastic waste, pose significant environmental and health risks as carriers for potentially toxic element (PTE) metals. This study employs asymmetrical flow field-flow fractionation (AF4) coupled with multi-angle light scattering (MALS) and inductively coupled plasma mass spectrometry (ICP-MS) to provide a size-resolved assessment of chromium (Cr), arsenic (As), and selenium (Se) adsorption onto carboxylated polystyrene nanoparticles (COOH-PSNPs) of 100 nm, 500 nm, and 1000 nm. Cr exhibited the highest adsorption, with adsorption per particle surface area increasing from 9.45 × 10−15 μg nm−2 for 100 nm particles to 6.87 × 10−14 μg nm−2 for 1000 nm particles, driven by chemisorptive interactions with carboxyl groups. In contrast, As and Se exhibited slower adsorption rates and significantly weaker interactions, attributed to outer-sphere complexation and electrostatic repulsion. Smaller particles exhibited enhanced adsorption efficiency per unit mass due to their larger surface area-to-volume ratios and higher carboxyl group density (18.5 μEq g−1 for 100 nm compared to 7.9 μEq g−1 for 1000 nm particles). Se adsorption remained negligible across all sizes, near detection limits, highlighting its low affinity for carboxylated surfaces. Our study demonstrates the superior resolution of AF4-MALS-ICP-MS compared to that of bulk ICP-MS, which lacks the ability to discern particle-specific adsorption trends. Unlike bulk ICP-MS, which provides average adsorption values, AF4-MALS-ICP-MS reveals the size-dependent mechanisms influencing metal binding, offering critical insights into the role of MnPs as PTE vectors. The findings highlight the environmental implications of MnPs in facilitating PTE transport and highlights the need for size-specific mitigation strategies. This work sets a foundation for developing more precise risk assessment frameworks and advanced remediation approaches for MnP-contaminated environments.
In this context, the coupling of asymmetrical flow field-flow fractionation (AF4) with multi-angle light scattering (MALS) and inductively coupled plasma mass spectrometry (ICP-MS) represents a significant advancement in the study of MnPs and their interactions with PTEs.9–11 AF4, as an advanced separation technique, enables the fractionation of MnPs based on their hydrodynamic size without altering their native state, which is crucial for understanding how different sized particles behave in environmental systems.12 When combined with MALS, the technique provides precise real-time measurements of particle size and shape, while ICP-MS offers highly sensitive quantification of metal adsorption on MnPs, even at trace levels (<ng L−1). This hyphenated technique is particularly innovative because it overcomes the limitations of traditional bulk adsorption studies, which often fail to differentiate between various size fractions of MnPs or provide accurate quantification of adsorbed metals. The AF4-MALS-ICP-MS system allows simultaneous characterisation of particle size and metal content, providing a comprehensive understanding of how these factors influence PTE fouling on MnP surfaces.13 Asymmetric flow field-flow fractionation coupled with inductively coupled plasma mass spectrometry (AF4-ICP-MS) has been extensively applied to characterise the interactions of trace elements in natural and engineered colloidal systems. Previous studies have demonstrated its utility in examining the binding and transport of rare earth elements within iron–organic matter nanocolloids in an Alaskan river.14 Additionally, AF4-ICP-MS has been employed to study mercury complexation within the natural colloidal pool, providing insights into mercury mobility and transformation processes in polluted environments.15 The technique has also been used to quantify the adsorption of heavy metals such as copper and lead onto quantum dots, as well as uranium onto iron-oxide ferrihydrite.16 These studies highlight the versatility of AF4-ICP-MS in probing metal–colloid interactions and provide a framework for its application in emerging areas of research, such as the adsorption of trace elements onto nanoplastics. Such insights are critical for advancing our understanding of the environmental fate of MnPs in real environmental samples and their potential risks. Recent studies have highlighted the role of nano-colloids in controlling the adsorption and mobility of PTEs. Tadayon et al. (2024) investigated rare earth element (REE) interactions with synthetic mixed colloids using AF4-ICPMS, demonstrating that REE adsorption induces colloidal aggregation, significantly influencing environmental mobility.17 To strengthen our approach, Faucher et al. (2018) combined MALS and ICP-MS to characterise quantum dots in a natural matrix, showcasing how advanced fractionation techniques enhance the understanding of nanoparticle behavior in complex environmental media.18 Additionally, Worms et al. (2012) assessed the impact of nanoparticle interactions on metal bioavailability in microalgae, providing critical insights into how engineered nanomaterials modulate trace metal uptake and toxicity.19 These studies collectively validate our methodology and reinforce the environmental implications of our findings.
The importance of this work is highlighted by the fact that MnPs are now ubiquitous in global water systems, with significant implications for ecosystems and food safety. PTE contamination, exacerbated by the presence of MnPs, contributes to the long-term persistence of toxic substances in the environment.5,20,21 By employing AF4-MALS-ICP-MS, this study addresses key knowledge gaps in assessing and quantifying MnP interactions (particularly particles <1000 nm) with PTE co-pollutants, offering a novel and robust approach for studying the environmental behaviours of MnPs with PTE fouling. The outcomes of this research could have far-reaching implications, informing the development of mitigation strategies for plastic pollution and setting a new benchmark for environmental risk assessments of emerging contaminants.
ICP standards of chromium (Cr), arsenic (As), and selenium (Se) in 2% nitric acid were procured from PerkinElmer, USA, with the following oxidation states: Cr(III) (chromium(III) standard solution, present as Cr(H2O)63+), As(V) (arsenic(V) standard solution, present as H2AsO4−), Se(IV) (selenium(IV) standard solution, present as H2SeO3). These oxidation states were selected based on their environmental relevance and their influence on adsorption behaviour onto MnPs. The metal/metalloid solutions were prepared at a final concentration of 1 μg mL−1 (1 mg L−1) in 1 mM HEPES buffer (pH 7.4) with 1 mM EDTA—to investigate adsorption dynamics.
A 0.05% (from a 4 wt% stock) suspension of COOH-PSNPs was added to 50 mL of the metal ion solutions and incubated for seven days under gentle agitation, following established adsorption protocols. In addition to individual size fractions, a mixed sample was prepared by combining 100 nm, 500 nm, and 1000 nm COOH-PSNPs at 1.33 wt% and subsequently diluting it to a final working concentration of 0.05% for AF4-MALS-ICP-MS analysis. To verify accuracy, the AF4 recovery of both the nanoplastics and the metal ions was monitored by comparing the injected mass to that recovered in the collected fractions. Future work involving multiple concentrations would be required to fully determine the system's LOD and further validate the method's performance. The value of 1 μg mL−1 metal ion concentration was considered by taking into account high-exposure and contamination areas. A mixture of these PTEs (at a concentration of 1 μg mL−1) was prepared before adding the COOH-PSNPs to the solution. Also, individual PTE adsorption at a concentration of 1 μg mL−1 was also performed at a similar concentration of COOH-PSNPs. Cr concentrations can reach 10–50 μg L−1 in water, 100–500 mg kg−1 in soil, and 10–200 ng m−3 in air, often near tanneries or electroplating industries.22,23 Hotspots for As, like Bangladesh, show groundwater levels of 100–3000 μg L−1, soil up to 1000 mg kg−1, and air near smelters at 10–100 ng m−3.22–26 Se in irrigation basins (e.g., California) can exceed 500 μg L−1 in water, 100 mg kg−1 in soil, and 50–500 ng m−3 in air near coal plants.27,28 After incubation, samples were filtered using 0.02-micron syringe filters to remove the COOH-PSNPs, while the unbound metal ions passed through in solution. Metal concentrations in the filtrate were measured using inductively coupled plasma mass spectrometry (ICP-MS, Nexion 350, PerkinElmer, USA), operated in helium kinetic energy discrimination (KED) mode at 4 mL min−1 Helium purging was used to minimise polyatomic interferences during metal quantification (PerkinElmer, 2019). The adsorption efficiency, kinetics and selectivity were determined by comparing the initial and final concentrations of metals in the filtrate, with the amounts adsorbed onto the COOH-PSNPs calculated using the difference between the initial concentration of PTEs and the final concentration after adsorption. All experiments were performed in triplicate to ensure reproducibility and reliability. Blank controls without COOH-PSNPs were included to account for any non-specific adsorption of the metal ions onto the filtration system and glassware.
A carrier liquid consisting of 0.025% NovaChem (PN) was used throughout all fractionations. The AF4 fractionation method was operated at a constant detector flow rate of 0.5 mL min−1. The flow rates were stabilised for 2 min, and then the injection was carried out. After 5 min of focusing at an initial cross-flow rate of 1 mL min−1 and an injection flow rate of 0.2 mL min−1, a transition time of 0.5 min was used to change to elution mode. The initial cross-flow rate was maintained constant for 0.2 min, followed by a 40 min long power decay to a cross-flow rate of 0.05 mL min−1, which was maintained constant for 25 min. A rinse step of 12 min at 0.6 mL min−1 was applied to reduce potential carryover and memory effects. Fig. S1† illustrates the AF4 flow programming, outlining the three distinct phases of focusing, elution, and rinsing, which were applied consistently across all samples to achieve effective fractionation. Fig. S4† presents the reference fractograms obtained from AF4-MALS analysis of native COOH-PSNPs (100 nm, 500 nm, and 1000 nm), showing distinct elution profiles corresponding to each particle size based on the MALS 90° signal.
The MALS data analysis was carried out using the NovaAnalysis Software (PN, Version 2408). The software was also used to merge all detector traces including ICP-MS traces. MALS data were analysed using the sphere model and 19 active angles over an angular range of 12° to 156°. Signal processing and additional calculations were performed using Excel (Version 2410, Microsoft 365) and Origin 2019 (Version 9.6.0.172, Origin Lab Corporation). Particle number calculations from MALS scattering data were conducted based on the work of Kerker (1969).29 All quantitative results are normalised to 1 μL of suspension that was injected into the AF4-MALS-ICP-MS system. Incubated samples were tip-sonicated for 1 min in pulse mode to prevent thermal influence (5 mm tip, 0.5 s on, 0.5 s off, 40% amplitude, Hielscher Ultrasonics GmbH, Teltow, Germany). After diluting 100 μL of the stock solution of metal ion-incubated COOH-PSNPs in 2.9 mL of AF4 carrier liquid, the suspension was sonicated in an ultrasonication bath at 160 W (Sonorex Digital P10, Bandelin Electronics GmbH, Berlin, Germany) for 5 more minutes. Injection volumes of 50 μL to 100 μL were applied.
COOH-PSNP particles | TEM (nm) | DLS size (nm) | MALS size Rg (nm) | Zeta potential (mV) | Specific surface area (cm2 g−1) | Number of COOH group per particle | COOH titration (μEq g−1) |
---|---|---|---|---|---|---|---|
100 nm | 110 ± 10 | 130 ± 11 | 44.5 ± 2.29 | −55 ± 3 | 5.2 × 105 | 8.2 × 103 | 18.5 |
500 nm | 490 ± 18 | 550 ± 20 | 211.0 ± 3.74 | −70 ± 5 | 1.2 × 105 | 3.8 × 105 | 9.6 |
1000 nm | 1100 ± 44 | 1150 ± 17 | 429.0 ± 5 | −70 ± 3.5 | 5.2 × 104 | 3.5 × 106 | 7.9 |
The zeta potential data shown in Fig. 2(A) and (C) provide insights into the surface charge and colloidal stability of COOH-PSNPs. Fig. 2(C) shows the zeta potential values measured in deionised water and HEPES buffer for all particle sizes before and after metal adsorption. Pristine COOH-PSNPs exhibit highly negative zeta potentials (∼−70 mV) in both media, indicative of excellent colloidal stability due to electrostatic repulsion. This high negative charge is primarily attributed to the ionised carboxyl groups (–COOH) on the surface of the PSNPs, which deprotonate in aqueous environments, generating a strong negative surface charge.32 After metal adsorption, the zeta potential becomes less negative, especially in HEPES buffer. This shift indicates that the positively charged metal ions (Cr, As, and Se) are neutralising some of the negative charges on the PSNP surface, forming surface complexes. Such a reduction in zeta potential is typical of PTE binding, where the adsorption of cations neutralises the surface charges, potentially decreasing the colloidal stability of the particles.33Fig. 2(A) further corroborates this observation by showing the pH-dependent zeta potential of COOH-PSNPs, whereby the zeta potential becomes more negative with increasing pH, highlighting that the COOH-PSNPs are unstable under acidic to neutral conditions but exhibit higher stability in more alkaline environments.34 The hydrodynamic size measurements, shown in Fig. 2(B), indicate an increase in particle size post-metal adsorption, especially for the larger 500 nm and 1000 nm COOH-PSNPs. This increase in size is consistent with the formation of metal-ion complexes on the surface of the COOH-PSNPs, where the binding of metal ions such as Cr, As, and Se could lead to agglomeration or an increase in particle size due to the increased surface mass. The hydrodynamic size increased more in HEPES buffer than in deionised water, further supporting the enhanced metal complexation in buffer systems, which may stabilise the metal ions in solution and promote surface adsorption.
The number of carboxylic groups per particle (Table 1), specific surface area, and COOH titration for COOH-functionalised polystyrene nanoparticles (COOH-PSNPs) vary significantly across particle sizes. For 100 nm particles, the specific surface area is 5.2 × 105 cm2 g−1, with 8.2 × 103 COOH groups per particle and a COOH titration of 18.5 μEq g−1, while the zeta potential is −55 mV in deionised water, indicating decent electrostatic stability. In contrast, 500 nm particles have a reduced surface area of 1.2 × 105 cm2 g−1, 3.8 × 105 COOH groups per particle, and a lower COOH titration of 9.6 μEq g−1, with a more negative zeta potential of −70 mV, suggesting higher electrostatic repulsion. For the 1000 nm particles, the surface area decreases further to 5.2 × 104 cm2 g−1, but the number of COOH groups increases to 3.5 × 106 per particle, with the lowest COOH titration at 7.9 μEq g−1 and a zeta potential of −70 mV. The increasing zeta potential with size indicates stronger surface charge stabilisation despite the reduced specific surface area. These data were crucial in calculating the adsorption of Cr, As and Se on various sizes of COOH-PSNPs and their dependence on surface area and functional group density as determined using AF4-MALS-ICP-MS.
The FTIR spectra (Fig. 2D) of COOH-PSNPs before and after adsorption of Cr, As, and Se revealed critical insights into the interaction between these PTEs and the MnPs’ surface functional groups. The pristine MnPs (black spectrum) exhibited distinct peaks corresponding to the carboxyl groups (–COOH) and hydroxyl groups (–OH), particularly the CO stretching near ∼1700 cm−1 and O–H stretching between ∼3000–3500 cm−1.35 After metal adsorption (red spectrum), there was a significant reduction in transmission in these regions, indicating metal binding through surface complexation. This binding suggests that the metals form coordination complexes with the oxygen atoms of the carboxyl groups, a phenomenon widely reported in the literature for PTE adsorption onto oxygenated functional groups.36,37 Moreover, the appearance of new bands in the lower wavenumber region (∼500–800 cm−1) strongly indicated the formation of metal–oxygen bonds (Cr–O, As–O, Se–O), confirming direct metal–ligand interactions.38,39
Further analysis showed that post-adsorption, there were notable shifts in the C–O stretching region (∼1200–1300 cm−1), again supporting the formation of complexes between metal ions and the oxygen-containing groups on the MnPs. The decrease in intensity of the O–H and CO peaks reflects the involvement of hydroxyl and carboxyl groups in the binding process. These observations are consistent with the known mechanism of PTE adsorption, where Cr, As, and Se form coordination complexes with the carboxyl groups on MnPs, altering the surface chemistry.40 This strong interaction between metals and the surface of the COOH-PSNPs can lead to enhanced stability and persistence of these contaminants in the environment. Such behaviour is of significant concern in aquatic systems, where MnPs can act as vectors for the transport of toxic metals, potentially increasing their mobility and bioavailability, which poses long-term ecological risks.41,42
Pseudo-first-order kinetics | Pseudo-second-order kinetics | |||||
---|---|---|---|---|---|---|
q e (mg g−1) | K 1 (min−1) | R 2 | q e (mg g−1) | K 2 (g mg−1 min−1) | R 2 | |
q e is the adsorption capacity at equilibrium, k1 (min−1) and k2 (g mmol−1 min−1) represent the parameters for kinetic rate constants for the pseudo-first-order and pseudo-second-order models, respectively, and R2 is the correlation coefficient. | ||||||
Mixed elements with 100, 500, and 1000 nm | ||||||
Cr | 0.82 | 8.2272 × 10−4 | 0.85 | 5.76 | 0.0094 | 0.99 |
As | 0.45 | 3.53673 × 10−5 | 0.10 | 0.99 | 0.0069 | 0.93 |
Se | 0.20 | 1.09592 × 10−4 | 0.05 | 1.24 | 0.0118 | 0.98 |
Mixed elements with 100 nm | ||||||
Cr | 0.01 | 4.0133 × 10−4 | 0.13 | 0.62 | 0.22 | 0.99 |
As | 0.10 | 6.18926 × 10−4 | 0.55 | 0.32 | 0.037 | 0.98 |
Se | 0.06 | 6.74654 × 10−4 | 0.72 | 0.23 | −0.19 | 0.99 |
Mixed elements with 500 nm | ||||||
Cr | 0.02 | 4.69531 × 10−4 | 0.46 | 0.62 | 0.15 | 1 |
As | 0.15 | 5.72366 × 10−4 | 0.49 | 0.25 | 0.08 | 0.99 |
Se | 0.15 | 4.84598 × 10−4 | 0.67 | 0.19 | 0.16 | 0.98 |
Mixed elements with 1000 nm | ||||||
Cr | 0.03 | 5.94644 × 10−4 | 0.62 | 0.62 | 0.14 | 1 |
As | 0.17 | 5.21051 × 10−4 | 0.64 | 0.28 | 0.01 | 0.99 |
Se | 0.17 | 6.11379 × 10−4 | 0.79 | 0.22 | 0.012 | 0.99 |
Fig. 3 (panels A–D) shows the time-dependent adsorption of Cr, As, and Se onto COOH-PSNPs, revealing that Cr adsorption rapidly reached equilibrium within the first hour across all particle sizes, with nearly 1.0 μg L−1 adsorbed from the solution. This rapid uptake for Cr suggests a high affinity between Cr ions and the carboxyl groups (–COOH) on the PSNP surface, indicative of chemisorption via inner-sphere complexation. This behaviour aligns with studies on metal binding to carboxyl-functionalised MnPs, where Cr ions exhibit strong adsorption due to covalent bonding potential with oxygen atoms on the COOH-PSNP surface.43,44 As and Se exhibited slower adsorption rates and reached equilibrium at lower adsorption capacities, approximately 0.4 μg L−1 and 0.2 μg L−1, respectively. The lower adsorption for As and Se suggests weaker interactions, likely due to outer-sphere complexation or physisorption mechanisms. This slower equilibrium is consistent with the literature indicating that As and Se ions, particularly in their higher oxidation states, form weaker bonds with carboxylated surfaces and may experience electrostatic repulsion due to similar surface charges.45–48
To further elucidate the adsorption mechanism, kinetic data were fitted to both PFO (Fig. S4†) and PSO models49 (Fig. 4), with parameters for both models shown in Table 2. The pseudo-PSO kinetic model was applied using adsorption data obtained from triplicate experiments (n = 3) as presented in Fig. 3. Standard deviations were considered in the adsorption studies, with Cr adsorption showing minimal variation, indicating high reproducibility. While error bars are not explicitly shown in Fig. 4 due to the nature of the kinetic fitting, the consistency of adsorption trends supports the reliability of the model. Across all particle sizes and metals, the PSO model (calculated using eqn (S6)†) exhibited a superior fit (R2 > 0.99), suggesting that chemisorption, which involves the sharing or exchange of electrons between metal ions and COOH-PSNP functional groups, predominantly controls the adsorption process. In contrast, the PFO model (calculated using eqn (S5)†), often associated with physisorption, showed lower R2 values, indicating that physical adsorption is minimal for metal ion binding on COOH-PSNPs. The high qe value of 5.769 mg g−1 for mixed-size COOH-PSNPs and 0.6289 mg g−1 for 100 nm COOH-PSNPs highlights the strong affinity between Cr ions and carboxyl groups. The PSO rate constant (K2) for Cr adsorption (e.g., K2 = 0.00949 g mg−1 min−1 for mixed sizes) further supports the rapid chemisorption mechanism, as Cr ions quickly form stable, inner-sphere complexes with surface –COOH groups. This is corroborated by the FTIR results (Fig. 2D) showing shifts in the CO stretching (∼1700 cm−1) after Cr adsorption, which indicates coordination bonding between Cr and carboxyl groups. For As and Se, the PSO model also fits with lower qe and K2 values, indicating weaker interactions. As shows a qe of 0.993 mg g−1 and K2 of 0.00697 g mg−1 min−1, while Se has a qe of 1.244 mg g−1 and K2 of 0.01187 g mg−1 min−1. The slower adsorption rates for As and Se suggest the occurrence of outer-sphere interactions and possibly some physisorption, resulting in less stable and more reversible binding.
The selective adsorption of Cr over As and Se is highlighted by the distribution coefficients (Kd) (calculated using eqn (S1), (S2) and (S3)†) and separation factors (S.F.; calculated using eqn (S4)†).50 The high Kd values for Cr, especially for 100 nm COOH-PSNPs (779896.21 mL g−1), relative to As (4556.69 mL g−1) and Se (2679.63 mL g−1), reflect Cr's preferential binding to COOH-PSNPs. The calculated separation factors (e.g., S.F. (Cr/As) = 171.15 and S.F. (Cr/Se) = 291.04 for 100 nm PSNPs) indicate that COOH-PSNPs are significantly more selective for Cr ions than for either As or Se, consistent with other studies where Cr demonstrates stronger chemisorptive interactions with carboxylated surfaces.51
The adsorption capacity of COOH-PSNPs for Cr, As, and Se decreases with increasing particle size. Smaller particles (100 nm) consistently exhibit higher adsorption capacities, likely due to their larger surface area-to-volume ratios, which provide more accessible active sites for binding. For instance, the adsorption capacity at equilibrium, qe, of Cr on 100 nm PSNPs is higher than that on 1000 nm PSNPs, suggesting that smaller MnPs enhance adsorption efficiency through increased surface availability, whereas the larger particles (1000 nm) show higher adsorption per COOH group due to the presence of higher number of COOH group on their surface. Interestingly, the effect of particle size is more pronounced for Cr than for As, due to Cr's stronger chemisorptive interactions, whereby additional surface area and more COOH groups lead to more covalent bonding sites for Cr ions. For As and Se, which primarily interact via weaker forces, the increase in surface area with smaller particles does not substantially impact adsorption capacity.
The FTIR spectra (Fig. 2, panel D) revealed significant changes in the CO stretching region (∼1700 cm−1) after Cr adsorption, supporting the formation of inner-sphere complexes between Cr ions and carboxyl groups on COOH-PSNPs. In contrast, As and Se binding induced smaller shifts, indicating weaker binding likely due to physisorption or outer-sphere complexation. This selective interaction with Cr corroborates the PSO kinetic model, confirming that Cr binds through chemisorption, while As and Se primarily interact through physical or weaker chemical forces. The FTIR findings support existing literature where Cr is shown to form stronger covalent bonds with oxygen-containing groups,52,53 and from its binding stability on carboxylated MnPs. This mechanism is further validated by the high qe and Kd values for Cr (Table 2), demonstrating the practical potential of COOH-PSNPs for selective Cr removal from environmental media.
The quantitative analysis of PTE adsorption (Table 3) on COOH-PSNPs using AF4-MALS-ICP-MS revealed significant differences based on particle size (100 nm, 500 nm, and 1000 nm) and the type of PTEs. Cr exhibited the highest adsorption across all metrics, while As demonstrated considerably lower adsorption, and Se adsorption was negligible. For Cr, the adsorption per total particle surface area increased with particle size, ranging from 9.45 × 10−15 μg nm−2 for 100 nm particles to 2.98 × 10−14 μg nm−2 for 500 nm and 6.87 × 10−14 μg nm−2 for 1000 nm particles. Similarly, per particle, Cr adsorption increased significantly with particle size, from 7.05 × 10−12 μg nm−2 for 100 nm to 5.35 × 10−10 μg nm−2 for 500 nm and 5.26 × 10−9 μg nm−2 for 1000 nm particles. When normalised to the number of COOH groups, the trend indicated that Cr adsorption was highest for 1000 nm particles (1.503 × 10−15 μg per COOH group), followed by 500 nm particles (1.407 × 10−15 μg per COOH group) and 100 nm particles (8.597 × 10−16 μg per COOH group). These results suggest that the lower density of COOH groups on larger particles reduces steric hindrance, enabling stronger interactions and greater metal ion adsorption efficiency. However, when normalised to particle mass, Cr adsorption decreased with increasing particle size, from 0.763 mg g−1 for 100 nm particles to 0.404 mg g−1 for 500 nm and 0.201 mg g−1 for 1000 nm particles. This indicates that smaller particles have a higher adsorption efficiency per unit mass due to their larger surface area-to-volume ratio.
PTE adsorption (μg per total particle surface area) | |||||
---|---|---|---|---|---|
Cr (μg)per nm2 (PS) | As (μg) nm−2 (PS) | ||||
COOH-PS100 | COOH-PS500 | COOH-PS1000 | COOH-PS100 | COOH-PS500 | COOH-PS1000 |
9.45 × 10−15 | 2.98 × 10−14 | 6.87 × 10−14 | 7.22 × 10−16 | 2.54 × 10−15 | 7.10 × 10−15 |
PTE adsorption (μg per particle) | |||||
---|---|---|---|---|---|
Cr (μg) per particle | As (μg) per particle | ||||
COOH-PS100 | COOH-PS500 | COOH-PS1000 | COOH-PS100 | COOH-PS500 | COOH-PS1000 |
7.05 × 10−12 | 5.35 × 10−10 | 5.26 × 10−09 | 5.39 × 10−13 | 4.56 × 10−11 | 5.44 × 10−10 |
PTE adsorption (mg g−1) of particles | |||||
---|---|---|---|---|---|
Cr (mg) per g of particle | As (mg) per g of particle | ||||
COOH-PS100 | COOH-PS500 | COOH-PS1000 | COOH-PS100 | COOH-PS500 | COOH-PS1000 |
0.76 | 0.40 | 0.20 | 0.05 | 0.03 | 0.02 |
PTE adsorption (μg per COOH group) | |||||
---|---|---|---|---|---|
Cr (μg) per COOH group | As (μg) per COOH group | ||||
COOH-PS100 | COOH-PS500 | COOH-PS1000 | COOH-PS100 | COOH-PS500 | COOH-PS1000 |
8.597 × 10−16 | 1.407 × 10−15 | 1.503 × 10−15 | 0.657 × 10−16 | 1.207 × 10−16 | 1.554 × 10−16 |
In contrast, As adsorption was markedly lower. Per total particle surface area, adsorption increased with particle size, from 7.22 × 10−16 μg nm−2 for 100 nm particles to 2.54 × 10−15 μg nm−2 for 500 nm and 7.10 × 10−15 μg nm−2 for 1000 nm particles. Per particle, As adsorption ranged from 5.39 × 10−13 μg per particle for 100 nm particles to 4.56 × 10−11 μg per particle for 500 nm and 5.44 × 10−10 μg per particle for 1000 nm particles. When normalised to COOH groups, As adsorption was significantly lower than Cr, with values of 6.57 × 10−17 μg per COOH group for 100 nm particles, 1.207 × 10−16 μg per COOH group for 500 nm, and 1.554 × 10−17 μg per COOH group for 1000 nm. Normalisation by particle mass also reflected this trend, with As adsorption decreasing from 0.0583 mg g−1 for 100 nm particles to 0.0344 mg g−1 for 500 nm and 0.0208 mg g−1 for 1000 nm. These results suggest that weaker binding mechanisms, such as physisorption or outer-sphere complexation, dominate As adsorption on COOH-PSNPs. Se adsorption was negligible across all particle sizes, with values close to the detection limit of 0.18 ppb, indicating an inherently low affinity for the carboxylated surfaces of COOH-PSNPs under the experimental conditions.
The adsorption behaviour of PTEs on COOH-PSNPs is strongly influenced by particle size, surface chemistry, and the type of metal ion. Cr demonstrated high adsorption efficiency, driven by its strong chemical affinity for COOH groups, with larger particles offering enhanced adsorption due to reduced steric hindrance. As, on the other hand, exhibited weaker adsorption, likely due to its reliance on less stable physisorption mechanisms. Se's negligible adsorption highlights the importance of electrostatic compatibility and chemical affinity in determining adsorption efficiency. These findings highlight the role of surface functional group and particle size of MnPs in modulating the adsorption of specific PTEs. For Cr ions, larger particles are advantageous for bulk adsorption, while smaller particles may be more efficient for applications requiring high adsorption per unit mass.
The adsorption behaviour of Cr and As aligned closely with their intrinsic chemical affinities for the carboxyl groups on the COOH-PSNP surface. Cr consistently exhibited stronger chemisorptive interactions, reflected in its higher adsorption per particle and per unit surface area, while As showed weaker bonding, likely due to differences in binding mechanisms. The negligible adsorption of Se further emphasises the selectivity of COOH-PSNPs for Cr and, to a lesser extent, As. Overall, AF4-MALS-ICP-MS provided a comprehensive assessment of COOH-PSNP size-dependent adsorption behaviour. The AF4-MALS-ICP-MS fractograms (Fig. 5 and 6) and quantitative data (Table 3) collectively highlight the robustness of the methodology in elucidating the adsorption dynamics of PTEs onto MnPs. The fractograms in Fig. 6 were obtained under the same experimental conditions as those in Fig. 5, ensuring a consistent comparison of Cr, As, and Se adsorption across different particle sizes. These findings also highlight the environmental implications of Cr and As fouling on COOH-PSNPs and their potential role as vectors for PTE transport in aquatic ecosystems.
The integration of AF4-MALS and ICP-MS highlights their distinct yet complementary strengths in analysing the interactions of MnPs with metal(loid) ions. AF4-MALS-ICP-MS offers detailed insights into particle size-dependent adsorption trends and surface interactions, while ICP-MS alone quantifies the bulk metal(loid) concentrations in the solution. The analysis revealed contrasting observations. AF4-MALS-ICP-MS showed a clear decreasing trend in adsorption capacity with increasing particle size of COOH-PSNPs for all metal ions. Specifically, adsorption capacity reduced from 0.763 mg g−1 for 100 nm COOH-PSNPs to 0.201 mg g−1 for 1000 nm COOH-PSNPs (Table 3). However, ICP-MS measurements showed no significant variation in adsorption capacity with particle size, as demonstrated by the nearly constant Cr adsorption of approximately 0.62 mg g−1 across all sizes (Table 2). This discrepancy suggests that while ICP-MS provides a reliable bulk measurement, it may lack the resolution needed to capture the surface-level and particle-specific variations that AF4-MALS-ICP-MS can identify. Therefore, the integration of these methods underscores the complexity of adsorption processes, highlighting the influence of both particle size and analytical technique on the observed adsorption behaviour. These findings emphasise the importance of employing advanced, complementary techniques to achieve a more nuanced understanding of MnP behaviour in environmental systems. Such insights are critical for developing targeted strategies to mitigate MnP-associated pollution, particularly by addressing size-dependent interactions and their implications for pollutant transport and removal efficiency.
In particular, the lower size detection limit in AF4-MALS-ICP-MS is determined primarily by the ultrafiltration membrane cut-off and the MALS detector threshold—factors that are largely independent of particle type—whereas the minimum detectable size in spICP-MS depends strongly on material-specific ionisation efficiencies. While spICP-MS can achieve very low detection limits for materials such as gold and silver (due to their favourable ionisation characteristics), the detection thresholds for oxidic nanomaterials—including TiO2 and SiO2—are notably higher. This material dependence has been demonstrated in the literature.54 We acknowledge that faster dwell times and improving instrumentation continue to push the detection limits of spICP-MS lower; nevertheless, these advancements remain more material-dependent than the fundamental limitations imposed by AF4-MALS. Consequently, AF4-MALS-ICP-MS provides a robust and composition-independent platform for comprehensive characterisation of MnPs and their interactions with PTEs, without compromising particle integrity.
The results reveal that Cr exhibits the highest adsorption to COOH-PSNPs among the tested metals, driven by strong chemisorptive interactions with carboxyl groups, while As and Se exhibit weaker adsorption mechanisms. Importantly, the adsorption trends were largely independent of particle size in mixed COOH-PSNP-sized systems, suggesting that intrinsic chemical affinity plays a dominant role. These insights have far-reaching implications for assessing the environmental behaviour of MnPs, particularly their role as vectors for PTEs in aquatic ecosystems.
By providing detailed and accurate quantification of PTE adsorption across size fractions, AF4-MALS-ICP-MS establishes itself as a critical method for environmental risk assessment. In contrast to spICP-MS, which is a very sensitive and fast screening technique, AF4-MALS-ICP-MS has a lower size detection limit for various MnPs and is able to efficiently characterise particle size in the presence of interfering matrices (e.g., metal ions) as well as in complex media. Future studies can leverage this technique to investigate the interaction of MnPs with other environmental pollutants in complex media and particle systems and to inform the development of mitigation strategies for plastic pollution. The relevance of this work extends beyond academic research, impacting policies aimed at reducing the risks associated with MnP contamination. By bridging the gap between fundamental science and environmental monitoring, this study paves the way for advanced monitoring and regulatory frameworks to address emerging contaminants in global water systems. The AF4-MALS-ICP-MS technique is a stepping stone towards setting a new benchmark for analysing complex pollutant interactions, offering a robust approach for safeguarding ecosystems and public health.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d5nr00353a |
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