1. Introduction
The processing of associated mineral resources and the nuclear fuel cycle inevitably generate large volumes of acidic wastewater enriched in uranium, thorium, and rare-earth elements such as europium (Eu3⁺)[1–4]. Although stable europium isotopes are non-radiotoxic, Eu3⁺ often coexists with radionuclides in hydrometallurgical effluents, introducing risks of environmental migration, nuclear safety issues, and long-term management challenges[5]. Furthermore, Eu3⁺ exhibits complex aqueous speciation and strong coordination ability with oxygen-donor ligands, which lead to its high solubility and hinder its selective separation from chemically similar species[6–7]. Therefore, the efficient removal and recovery of Eu3⁺ under highly acidic conditions remains a critical challenge for both environmental protection and resource recycling in radioactive mineral processing. Europium is a strategically important rare-earth element widely used in phosphors[8–12], nuclear detectors[13–14], and advanced energy materials[15–17]. However, its supply is limited due to the low abundance of Eu-bearing minerals and the complex processes required for separation from other lanthanides. Traditional extraction techniques, such as solvent extraction[18–19], ion exchange[20–21], and acid-based adsorption[22–24], have achieved moderate success but face significant limitations, including acid-induced damage to adsorbents, generation of secondary waste, poor selectivity in multi-ion systems, and limited regeneration capability. These challenges underscore the urgent need for environmentally benign, acid-tolerant, and recyclable materials capable of selectively capturing Eu3⁺ from complex metallurgical effluents.
Zero-valent iron (ZVI) has gained considerable attention in recent decades as a multifunctional material for the remediation of heavy metals, radionuclides, and organic pollutants, owing to its synergistic adsorption and reduction properties[25–27]. Its unique surface redox reactivity allows for the immobilization of metal ions through electron transfer[28–30] and coprecipitation[31]. However, in acidic environments typical of hydrometallurgical waste streams, pristine ZVI suffers from rapid proton-induced corrosion, excessive hydrogen evolution, and severe particle aggregation, which collectively deteriorates its reactivity and stability. To overcome these limitations, surface engineering strategies have been developed to enhance the acid resistance, reactivity, and functional selectivity of ZVI. Recent advances—including nonmetallic modification[32], chelating-agent stabilization[33], nanoscale structuring[34–35], and vacancy engineering[36–37]—have effectively improved electron transfer, suppressed corrosion, and expanded its applicability to complex aqueous systems. Nevertheless, achieving long-term stability and controlled reactivity in acidic and multicomponent environments remains a key challenge motivating further material innovations such as phosphate-functionalized ZVI. Among them, phosphorylation modification[38–43] offers a particularly promising route. Yet, despite its conceptual appeal, the adsorption behavior, mechanistic pathways, and thermodynamic characteristics of phosphorylation-modified ZVI for Eu3⁺ recovery remain insufficiently elucidated.
In this study, we report a zero-acid strategy for europium recovery using phosphorylation-engineered zero-valent iron (P-ZVIbm) as an adsorbent. The proposed system achieves simultaneous corrosion inhibition and selective Eu3⁺ capture under in an acidic environment, eliminating the need for acidification while maintaining high adsorption efficiency. Through comprehensive kinetic, isotherm, and thermodynamic analyses combined with spectroscopic characterization, we reveal a synergistic mechanism involving Eu3⁺ migration to negatively shifted Fe–O–P surfaces, inner-sphere complexation, and interfacial precipitation of Eu–phosphate species, supplemented by adsorption on secondary Fe oxyhydroxides formed during mild corrosion. This dual-function mechanism adsorption coupled with redox transformation enables robust performance and excellent reusability even under challenging chemical conditions, providing a sustainable and scalable strategy for europium recovery from radioactive mineral effluents and offering new insights into the design of acid-resistant functional materials for green metallurgical processes.
2. Materials and Methods
2.1 Materials
Iron powder (Fe, analytical grade, particle size < 50 µm), phosphoric acid (H3PO4, ≥ 85.0%), nitric acid (HNO3, 65.0–68.0%), and sodium hydroxide (NaOH, ≥ 96.0%) were purchased from Sinopharm Chemical Reagent Co., Ltd. Anhydrous ethanol was obtained from Macklin Biochemical Co., Ltd. Europium nitrate hexahydrate (Eu(NO3)3·6H2O, ≥ 99.9%) was supplied by Aladdin Reagent Co., Ltd. All solutions were prepared with deionized water.
2.2 Synthesis of P-ZVIbm
Phosphorylated ball-milled zero-valent iron (P-ZVIbm) was prepared via a mechanochemical approach. Iron powder (3.0 g) and KH2PO4 (0.7309 g) were mixed and placed into an agate ball-milling jar together with a defined amount of agate balls. To avoid oxidation of Fe during milling, nitrogen gas was purged into the jar for 30.0 min prior to sealing. The mixture was then subjected to planetary ball milling at 300.0 rpm for 3.0 h. The resulting material was collected and stored in vacuum-sealed bags and denoted as P-ZVIbm. For comparison, ball-milled Fe powder without KH2PO4 was prepared under identical conditions and denoted as ZVIbm.
2.3 Characterization
The crystalline structure of the materials was analyzed using X-ray diffraction (XRD, Rigaku SmartLab SE, Cu-Kα radiation). Surface morphology was observed by scanning electron microscopy (SEM, TESCAN MIRA LMS) and transmission electron microscopy (TEM, JEOL JEM-F200). Surface functional groups were identified by Fourier transform infrared spectroscopy (FTIR, Thermo Nicolet iS5), while microstructural features and defects were investigated by Raman spectroscopy (Renishaw inVia). Elemental composition and chemical states were determined by X-ray photoelectron spectroscopy (XPS, LAUDA Scientific GmbH LSA-100X). P-ZVIbm was prepared using a ball mill (PML10, Netzsch Instruments). The magnetic properties of ZVIbm and P-ZVIbm were measured using a vibrating sample magnetometer (VSM, LakeShore 7404, USA). The surface charges of ZVIbm and P-ZVIbm were determined using a solid surface zeta potential analyzer (SurPASS 3, Anton Paar, Austria).
2.4 Batch Adsorption Experiments for Eu Removal
Eu(III) stock solution (1 g·L⁻1) was prepared as follows: 2.9353 g of Eu(NO3)3·6H2O was placed in a beaker, dissolved in 10.0 mL aqua regia under heating and stirring, and subsequently evaporated to dryness in a fume hood. After cooling the residue to room temperature, it was redissolved in 50.0 mL of deionized water and diluted to a final volume of 1.0 L in a volumetric flask. Batch adsorption experiments were conducted using the equilibrium method. Eu(III) solutions of desired concentrations were prepared by dilution of the stock solution and adjusted to target pH using 0.1 mol·L⁻¹ HNO3 or 0.1 mol·L⁻¹ NaHCO3. In a typical run, 5.0 mg of adsorbent was added to 25.0 mL of Eu(III) solution and shaken at 180.0 rpm at a constant temperature for a specified time. The residual Eu concentration was measured by inductively coupled plasma mass spectrometry (ICP-MS).
3. Results and Discussion
3.1 Structural and physicochemical properties of P-ZVIbm
The morphological and structural evolution of the zero-valent iron after ball-milling and phosphorylation modification (P-ZVIbm) was systematically characterized (Figs. 1A–D). As shown in the schematic illustration (Fig. 1A), the phosphorylated surface of P-ZVIbm provides abundant adsorption sites and facilitates Eu3⁺ immobilization through inner-sphere complexation and interface nucleation processes. SEM analysis (Fig. 1B) revealed that P-ZVIbm displayed rougher, flake-like structures with visible surface defects and micro-pores. These morphological changes indicate that phosphate incorporation during mechanical activation promotes surface reconstruction and fragmentation, thereby enlarging the specific surface area and exposing more reactive sites[44–45]. Energy-dispersive X-ray spectroscopy (EDS) further confirmed the presence of Fe (92.08%), O (5.57%), and P (2.35%) in P-ZVIbm, verifying the successful introduction of phosphate groups while maintaining Fe as the predominant component. X-ray diffraction (XRD) patterns (Fig. 1C) of P-ZVIbm exhibited characteristic reflections at 2θ = 44.5° and 65.0°, corresponding to the (110) and (200) planes of metallic Fe0 (PDF#65-4899). The absence of new crystalline peaks (2θ = 44.5°) in P-ZVIbm indicates that the Fe0 core structure was preserved after surface phosphorylation. However, the reduced intensity of Fe0 peaks suggests partial amorphization induced by high-energy milling and phosphate bonding. Fourier-transform infrared (FTIR) spectra (Fig. 1D) provide further evidence of chemical modification: absorption bands at 898.0 cm⁻1, 1090.0 cm⁻1, and 1280.0 cm⁻1 correspond to P–O, Fe–O–P, and P = O vibrations[45], respectively, confirming stable coordination between phosphate groups and iron atoms. The Fe–O–P linkage is expected to enhance the chemical durability of ZVI in acidic media by forming a protective passivation layer that limits proton attack[46].
3.2. Adsorption Performance of Eu3+ Removal
The adsorption performance of Eu3⁺ on ZVIbm and P-ZVIbm was systematically evaluated under varying conditions, including pH, solid-to-liquid ratio, contact time, concentration, and temperature (Fig. 2A). The speciation of Eu varies significantly with pH (Fig. 2B). At low pH (< 4), Eu3+ predominantly exists, whereas with increasing pH, hydrolyzed species such as Eu(OH)2⁺ progressively form in solution[47]. Figure 2C presents the magnetization curves of ZVIbm and P-ZVIbm. The Ms of ZVIbm reaches 225.15 emu·g⁻1, while that of P-ZVIbm decreases to 73.82 emu·g⁻1 due to phosphate surface modification. Nevertheless, both materials retain sufficient magnetic responsiveness, allowing efficient separation and recovery from Eu(III)-containing radioactive wastewater under an external magnetic field. To evaluate the electron transfer rate and corrosion resistance of the materials, Tafel tests were conducted using a three-electrode electrochemical system. As shown in Fig. 2D, the corrosion potentials of ZVIbm and P-ZVIbm are − 0.386 V and − 0.315 V, respectively. The positive shift in corrosion potential indicates that phosphate modification slightly reduces the electron transfer rate but significantly enhances the corrosion resistance of P-ZVIbm. Considering that Eu exists predominantly as cations in aqueous solution, the surface charge of the adsorbent is expected to strongly influence the removal process. Therefore, the zeta potentials of the samples were measured over a pH range of 3–8, as shown in Fig. 2E. As the pH increased, the zeta potential of ZVIbm decreased from + 28.34 mV to − 3.83 mV, while that of P-ZVIbm exhibited a more pronounced shift from − 2.65 mV to − 50.03 mV. This pronounced negative shift for P-ZVIbm is attributed to the introduction of PO43⁻ groups on the surface, which increases overall surface electronegativity[48–49]. The influence of the S/L ratio is presented in Fig. 2F. Increasing the S/L ratio from 0.1 to 0.6 g·L⁻1 enhanced the overall removal efficiency; however, the adsorption capacity per unit mass peaked at S/L = 0.2 g·L⁻1. The subsequent decrease in capacity at higher loadings is attributed to excessive unused sites and a diminished concentration gradient driving force. As shown in Fig. 2G, both adsorbents exhibited pronounced pH-dependent adsorption behavior within the acidic range (pH 2–6). The removal efficiency increased steadily with pH, reaching a maximum at pH = 3, where adsorption capacities were 7.92 mg·g⁻1 for ZVIbm and 121.76 mg·g⁻1 for P-ZVIbm. The low uptake under strong acidity was mainly due to proton competition and partial Fe0 dissolution, while the enhanced performance at higher pH reflected the deprotonation of surface hydroxyls and the increasing contribution of negatively charged Fe–O–P sites[50], which facilitated Eu3⁺ electrostatic attraction and inner-sphere complexation. These observations confirm that phosphate functionalization significantly improves acid tolerance and enhances active-site accessibility. As the initial Eu3⁺ concentration increased (Fig. 2H), the adsorption capacity rose sharply at low-to-moderate concentrations and then gradually reached saturation, yielding maximum capacities of 48.33 mg·g⁻1 for ZVIbm and 152.49 mg·g⁻1 for P-ZVIbm. Kinetic experiments (Fig. 2I) revealed rapid Eu3⁺ uptake during the initial stage, followed by equilibrium at 43.23 mg·g⁻1 for ZVIbm and 150.17 mg·g⁻1 for P-ZVIbm. Temperature-dependent adsorption results (Fig. 2J) demonstrated a clear enhancement in Eu3⁺ uptake with rising temperature, reflecting the endothermic nature of the process. The equilibrium capacity of P-ZVIbm increased from 118.64 mg·g⁻1 at 293 K to 155.21 mg·g⁻1 at 313.0 K, whereas that of ZVIbm increased modestly from 34.11 to 47.65 mg·g⁻1 over the same range.
3.3. Adsorption Mechanism Elucidation for Eu3+ Removal
Post-adsorption analyses were conducted to elucidate the structural and chemical evolution of ZVIbm and P-ZVIbm after Eu3⁺ capture (Fig. 3A–H). SEM-EDS characterization revealed distinct morphological changes in ZVIbm and P-ZVIbm after Eu adsorption, showing surface alteration and discontinuous deposits. Elemental mapping indicated homogeneous distributions of Eu, Fe, O, and P on the ZVIbm surface, whereas Eu on P-ZVIbm appeared sparsely and locally concentrated. EDS quantification further showed that the Eu content on P-ZVIbm (17.92 wt%) was nearly three times that of ZVIbm, confirming the enhanced Eu affinity induced by phosphate functionalization. XRD results (Fig. 3C) provided structural evidence for distinct immobilization mechanisms. Both materials retained the characteristic Fe⁰ reflections at 2θ = 44.5° and 65.0°, but their intensities weakened after adsorption, indicating partial oxidation of the metallic core. For P-ZVIbm, new diffraction peaks at 2θ = 25.8°, 28.2°, and 31.3° corresponded to crystalline Eu3PO7 phases (PDF#49-1024), confirming that phosphate groups on the surface acted not only as adsorption sites but also as active participants in interfacial precipitation with Eu3⁺. XPS spectra (Figs. 3D–G) further clarified the chemical states of key elements. The Eu 3d spectrum of P-ZVIbm exhibited two well-defined peaks at 1134.5 eV and 1164.2 eV, characteristic of Eu3⁺. The P 2p signal decreased in intensity and shifted from 133.4 eV to 134.1 eV after adsorption, indicating coordination between phosphate oxygens and Eu3⁺ through Fe–O–P–Eu linkages. Concurrently, Fe 2p spectra showed the disappearance of metallic Fe0 (706.9 eV) and the emergence of Fe2⁺/Fe3⁺ peaks at 710.8 eV and 724.6 eV, evidencing oxidation of Fe0 into Fe2O3, Fe3O4, and Fe(OH)3. The O 1s spectra displayed increased contributions from hydroxyl (Fe–OH) and phosphate (P–O–Fe, P–O–Eu) bonds, confirming the coexistence of redox transformation and chemical complexation during adsorption. Compared with ZVIbm, P-ZVIbm underwent more extensive surface oxidation and formed abundant reactive interfaces enriched with phosphate and iron oxyhydroxides, offering diverse coordination environments for Eu3⁺[44].
3.4. DFT Elucidation of the Interfacial Adsorption Mechanism
Density functional theory (DFT) calculations were employed to gain atomic-level insight into the adsorption mechanism of Eu3⁺ on phosphate-modified Fe–O surfaces (Fig. 4A–F). The optimized configurations reveal that Eu3⁺ strongly coordinates with surface oxygen atoms from phosphate and Fe–O–P groups, forming inner-sphere complexes with Eu–O bond lengths of approximately 2.1–2.3 Å and O–Eu–O angles between 77.929–79.545°. The corresponding adsorption energies progressively increase from − 8.015 eV for simple bidentate coordination to − 14.709 eV for multidentate bridging complexes, indicating that phosphate functionalization creates high-affinity sites capable of capturing Eu3⁺ through strong chemisorption. The enhanced stability of these configurations suggests that phosphate groups not only serve as anchoring ligands but also promote interfacial nucleation of Eu–phosphate species. Charge density difference analysis (Fig. 4E) displays pronounced electron accumulation around oxygen and depletion around europium, confirming substantial electron transfer from Eu³⁺ to the phosphate–oxygen framework and the mixed ionic–covalent nature of Eu–O bonding. This charge redistribution stabilizes Eu at the Fe–O–P interface and facilitates partial oxidation of surface Fe atoms. The projected density of states (Fig. 4F) further supports this conclusion, showing hybridization between Eu 4f/5d and O 2p orbitals near the Fermi level, accompanied by a narrowed band gap and shifted Fe 3d states. Together, these results establish that Eu3⁺ adsorption on P-ZVIbm is dominated by inner-sphere complexation and chemisorptive interaction, wherein phosphate groups create electron-rich, multidentate coordination environments[51] that strongly bind Eu³⁺ and drive the formation of stable Eu–phosphate precipitates. This DFT-supported mechanism coherently explains the experimentally observed high adsorption energy, temperature-enhanced uptake, and structural evolution of the adsorbent, confirming that phosphorylation transforms the Fe0 surface into a robust, electronically active interface for selective Eu3⁺ immobilization and recovery.
3.5. Application of ZVIbm and P-ZVIbm in real mine wastewater treatment
To evaluate the practical applicability of the developed adsorbents, both ZVIbm and P-ZVIbm were tested for Eu3⁺ removal from actual mine wastewater containing multiple coexisting metal ions (Table 1 and Fig. 5A–D). The wastewater exhibited a complex matrix with high concentrations of competing cations such as Ce (1832.03 mg·L⁻1), Gd (634.69 mg·L⁻1), La (541.37 mg·L⁻1), Sm (361.79 mg·L⁻1), and other trace elements including Si, Ba, Ni, and Zn. These multicomponent conditions pose a significant challenge for selective adsorption of Eu3⁺, especially under slightly acidic conditions typical of mine drainage systems. As shown in Fig. 5A, both materials displayed effective Eu3⁺ uptake with increasing contact time, but the removal efficiency of P-ZVIbm was substantially higher across all conditions. At equilibrium, P-ZVIbm achieved a Eu3⁺ removal efficiency of 92.4%, compared with only 48.7% for ZVIbm, confirming that phosphate functionalization significantly enhances adsorption performance in complex aqueous systems. The improvement is attributed to the strong inner-sphere complexation of Eu3⁺ with surface phosphate ligands and the formation of Eu–phosphate precipitates[52–53], which are less susceptible to ionic competition. The selectivity of P-ZVIbm toward Eu3⁺ among the coexisting metal ions is presented in Fig. 5B. While both adsorbents showed some affinity for light rare-earth elements such as La3⁺, Ce3⁺, and Gd3⁺, the Eu3⁺ adsorption capacity of P-ZVIbm was nearly fourfold higher than that of ZVIbm, with minimal interference from high concentrations of neighboring REEs. This selectivity arises from the specific coordination geometry and bond energy matching between Eu3⁺ and Fe–O–P sites, as confirmed by DFT and XPS results. Furthermore, the negligible adsorption of common transition metals (Ni2⁺, Zn2⁺, Co2⁺) suggests that P-ZVIbm possesses both chemical selectivity and environmental compatibility for rare-earth recovery from metallurgical effluents. The kinetics of Eu3⁺ removal in real wastewater (Fig. 5C) followed a rapid initial uptake phase, reaching equilibrium within 30.0 mins for P-ZVIbm, compared to nearly 120.0 minutes for ZVIbm. The faster equilibrium rate reflects improved surface accessibility and higher electrostatic attraction due to the negatively charged phosphate groups. In the presence of multiple ions, P-ZVIbm maintained an adsorption capacity of 132.5 mg·g⁻1, representing 86.0% of its performance in simulated single-ion systems, whereas ZVIbm retained only 57.0%. This demonstrates the structural stability and anti-interference ability of the phosphorylated surface in realistic environments. The recyclability of P-ZVIbm was further verified by five consecutive adsorption–desorption cycles using H3PO4 regeneration (Fig. 5D). The Eu3⁺ removal efficiency remained above 85.0% after five cycles, with only minor declines due to partial surface passivation and loss of active sites. In contrast, ZVIbm exhibited a pronounced capacity drop to below 50% after the third cycle, resulting from severe corrosion and aggregation under acidic regeneration conditions. The retained magnetic response of P-ZVIbm enabled facile separation from treated water by an external magnetic field, further supporting its suitability for practical wastewater applications. In summary, the results demonstrate that phosphorylation effectively transforms conventional ZVI into a highly stable, selective, and recyclable adsorbent capable of capturing and recovering Eu3⁺ from complex mine effluents. The enhanced affinity toward Eu3⁺, high tolerance to competing ions, and strong regeneration capacity confirm that P-ZVIbm bridges the gap between laboratory-scale synthesis and field-scale application. This work provides a feasible pathway for resource recovery from rare-earth-associated radioactive wastewater, aligning with the principles of green metallurgy and sustainable waste valorization.
Table 1
Chemical composition of the real wastewater sample
Element | Cx (mg/L) |
|---|
Si | 325.927 |
As | 1.530 |
Au | 5.541 |
B | 7.700 |
Ba | 42.162 |
Be | 10.303 |
Bi | 2.817 |
Cd | 0.090 |
Ce | 1832.032 |
Co | 1.317 |
Ga | 8.218 |
Gd | 634.693 |
Ge | 0.970 |
La | 541.373 |
Ni | 11.633 |
Sm | 361.793 |
Zn | 8.525 |
4. Conduction
In summary, phosphorylation-modified zero-valent iron (P-ZVIbm) exhibits markedly enhanced physicochemical properties, including reduced particle size, enlarged surface area, more negative surface potential, and superior resistance to corrosion, all of which synergistically improve its Eu³⁺ removal efficiency in acidic media. Under optimized conditions, P-ZVIbm achieves a maximum adsorption capacity of 152.49 mg·g⁻1. Mechanistically, Eu3⁺ migrates toward the negatively shifted interface, undergoes inner-sphere complexation with Fe–O–P groups, and nucleates as Eu3PO7 precipitates. This multi-pathway process not only overcomes the intrinsic instability of ZVI in acidic environments but also establishes a material and mechanistic framework for efficient rare-earth separation in radioactive wastewater treatment.