Abstract
The use of nanoscale zero-valent iron (nZVI) to remove heavy metal ions like Ni2+ from groundwater has been extensively studied; however, the compositional transformation of the Ni2+ and Fe0 during the removal is not clearly comprehensible. This study provides an insight into the componential, structural, and morphological transformations of Ni2+ and Fe0 at a solid–liquid interface using various characterization devices. The underlying mechanism of transformation was investigated along with the toxicity/impact of the transformed products on the groundwater ecosystem. The results indicated that Fe0 is transformed into lath-like lepidocrocite (γ-FeOOH), twin-crystal goethite (α-FeOOH), and spherical magnetite (Fe3O4), while Ni2+ is converted into Fe0.7Ni0.3 alloy and Fe–Ni composite (trevorite – NiFe2O4) with a fold-fan morphology. The Fe0 transformation mechanism includes the redox of Fe0 with Ni2+, H2O, and dissolved oxygen, the combination of Fe2+ and OH– produced by Fe0 corrosion to amorphous ferrihydrite, and the further mineralogical transformation to Fe oxides with the aid of Fe2+ adsorbed on ferrihydrite. The conversion of Ni2+ is accomplished by reduction by Fe0 and surface coordination with Fe oxides. Compared with Ni2+ and Fe0, the toxicity and bioavailability of the transformed products are significantly reduced, hence conducive to the application of zero-valent iron technology in groundwater remediation.
HIGHLIGHTS
The experiments were carried out for the mechanism of Fe0 and Ni2+ transformation by nZVI.
Heavy metals in wastewater have a direct effect on the transformation rate of Fe0 to Fe2+.
Fe0 and Ni2+ transformed into lath-like lepidocrocite, twin-crystal goethite, spherical magnetite, Fe0.7Ni0.3 alloy, and NiFe2O4 after reaction.
The environmental toxicity of the transformed products was significantly lower than nZVI and Ni2+.
INTRODUCTION
Nickel ion (Ni2+) is among the most prevalent heavy metal ions that are of concern to human and environmental health (Sprynskyy et al. 2006; Luo et al. 2015; Sachan & Lal 2017; Ahmad et al. 2019). The presence of Ni2+ in the environment through natural and anthropogenic processes makes water and soil unsafe for human consumption and crop cultivation, respectively (Torres-Caban et al. 2019; Hashem et al. 2020). Considering the potential damaging effects of Ni2+, it is important to ensure that the concentration of Ni2+ in environmental media meets the corresponding quality standards.
The removal of Ni2+ from the aquatic system such as groundwater has been achieved through the employment of various techniques such as adsorption (Tsai et al. 2015; Matern et al. 2018; Ong et al. 2018), membrane separation (Volchek et al. 1993; Tanhaei et al. 2014), ion exchange (Moghbeli et al. 2017), bioremediation (Francy et al. 2020; Singh & Mishra 2020), and nanotechnology (Matlochova et al. 2013; Rathor et al. 2017). Among these techniques, nanotechnology which involves the use of nanoscale zero-valent iron (nZVI) has proven effective in reducing Ni2+ (Matlochova et al. 2013; Ulucan-Altuntas et al. 2018; Gil-Díaz et al. 2020).
Extensive efforts have been made to elucidate the performance, influence factors, and mechanism of Ni2+ removal by nZVI. Furthermore, review articles such as Vardhan et al. (2019), Aziz et al. (2023) and Bilal et al. (2021) focused on the removal of toxic metals from aquatic systems by traditional methods, while suggesting methods of improving low cost adsorbents to ensure efficient removal of heavy metals. It is worth noting that there are few reports on the transformations of Fe0 in the aqueous system as compared to the traditional methods of removing toxic substances from water. For instance, Roh et al. (Filip et al. 2019; Gil-Díaz et al. 2020) investigated the conversion of Fe0 filing/foam in reactive iron barrier under varying conditions (alkalinity, pH) and types of contaminants (TCE, U-235, Tc) in the field and laboratory. Amorphous iron (hydr)oxides, intermediate products (green rusts), and hydrated forms of ferric oxides such as goethite (α–FeOOH), ichlorina (β–FeOOH), and lepidocrocite (γ–FeOOH) were identified as the main corrosion products of Fe0. The composition of the products varied with contaminant identities, iron types, and environmental media. Anang et al. (2021) examined the compositional evolution of nZVI in the ichlorination of 2,4-dichlorophenol by attapulgite-supported Fe/Ni nanoparticles. It was found that ferrihydrite was first formed, which later resulted in the formation of lepidocrocite, goethite, and magnetite. Sohn et al. (Su et al. 2014) employed nZVI to reduce nitrate in the solution that was deoxygenated by a N2 stream for 2 h before adding nZVI, and the results showed that Fe0 was transformed to crystalline magnetite. In addition, ageing of nZVI in static water under oxic and anoxic conditions has been reported (Liu et al. 2015, 2017). The main corrosion product of nZVI at oxic conditions for 72 h is γ–FeOOH, whereas a mixture of FeO, α–FeOOH and β–FeOOH is formed in anoxic water.
Even though the above studies have examined the transformation of Fe0 in static water or in the removal of chlorinated organics, radioactive elements and nutrient contaminants, no investigation has focused on the chemical transformation of Fe0 nanoparticles and Ni2+ during the removal. In particular, the changes in the composition and form of Ni2+ after removal, as well as the potential ecological effects of nZVI and Ni2+ transformation products on the environment have not been reported. This leaves a gap in the literature that needs to be filled. An evaluation on the componential, structural, and morphological transformations of Ni2+ and Fe0 at solid–liquid interface is critical in understanding their fate in the environment and the associated risks, and predicting the application potential of Fe0 nanomaterials in groundwater remediation.
In this study, various methods and devices characterizing material composition, morphology and structure, including scanning electron microscopy (SEM), transmission electron microscopy (TEM), specific surface area analyzer, X-ray diffraction (XRD), and X-ray photoelectron spectroscopy (XPS), are used to identify the transformation products of Ni2+ and Fe0 in nZVI during the removal of Ni2+ by nZVI and elucidate their physicochemical properties. The schematic description of the transformation process is presented. In addition, the implications of transformation of Ni2+ and Fe0 to groundwater remediation are discussed.
EXPERIMENT
Chemicals and materials
The chemicals which included iron(II) sulfate heptahydrate (FeSO4•7H2O), sodium borohydride (NaBH4), and nickel sulfate (NiSO4•6H2O) were purchased from Tianli Chemical Reagent Company in Tianjin, China. All the chemicals were of analytical grade. Deionized water was used to prepare the chemical solutions.
Preparation of nZVI
The liquid phase reduction method was used to prepare the nZVI (Mukherjee et al. 2015; Hu & Li 2018). 50 mL of H2SO4 (0.01 mol/L) was added to 13.9 g of the FeSO4•7H2O before the synthesis. 40 mL of the resulting mixture was then pipetted into a three-necked round bottom flask and stirred mechanically for 5 min (200 rpm). 3.026 g of NaBH4 was mixed with 40 mL of de-ionized water and stirred before adding dropwise to the FeSO4•7H2O solution in the flask. The mixture was mechanically stirred under N2 atmosphere. The resulting mixture was allowed to sit and stir mechanically for 15 min after all the NaBH4 solution was used up. The as-prepared nZVI was vacuum-filtered and washed with deionized water. The material was then dried under vacuum at −30 °C for 14 h in a freeze dryer.
Batch experiments
The nZVI was used to remove Ni2+ in the solution in order to investigate the transformation of the Ni2+ and Fe0 after removal. At the initial stages, 0.1 g of the prepared nZVI was added to 200 mL of NiSO4 solution (concentration = 5 mmol/L; initial pH = 4.0 ± 0.1). Two millilitres (2 mL) of the mixture was sampled at pre-determined time intervals (5, 10, 20, 30, 45, 60, 90, and 120 min) and filtered through a 0.45-μm nitrocellulose membrane. The filtrate of the sampled mixture at pre-determined time intervals was measured to determine the removal efficiency by the nZVI. The batch experiments were performed in duplicate in order to ensure precision. The residue of the nZVI after reaction with Ni2+ was freeze dried at −30 °C for 14 h, before used in characterizing the morphological and structural transformations of the Ni2+ and Fe0 (Anang et al. 2021).
Analytical methods
The concentration of Fe2+ in the solution with different reaction time was measured by spectrophotometry using phenanthroline as the chromogenic agent. The concentration of total iron was determined by an atomic absorption spectrometer. The difference between total iron concentration and Fe2+ concentration is the concentration of Fe3+.
The concentration of dissolved oxygen (DO) was analyzed by a JPSJ-606L dissolved oxygen meter (Shanghai Yidian Scientific Instruments Co. Ltd, China).
Material characterizations
The morphological characteristics of Ni2+ and Fe0 in nZVI before and after reaction (120 min) were analyzed using SEM (Nova 400 Nano, FEI, USA) and TEM (Tecnai G2 F30, S-Twin, FEI, USA). The crystalline structure of the pristine and reacted nZVI was characterized using an X-ray diffractometer (XRD) (D/MAX-2500, Rigaku Co, Japan) operated at 45 kV and 250 mA with Cu Kα. The material surface composition of pristine and reacted nZVI was analyzed with the aid of X-ray Photoelectron Spectrometer (XPS) (Escalab 250Xi, Thermo Fisher Scientific, USA) with a monochromatic Al Kα X-ray source. The binding energies of the samples were calibrated using the C1s peak at 284.8 eV. The specific surface area and pore parameters of nZVI before and after removal of Ni2+ were determined by a specific surface area analyzer (Micromeritics ASAP 2020, USA).
RESULTS AND DISCUSSION
Removal of Ni2+ by nZVI
Compositional transformation of Ni2+ and Fe0 in nZVI
XRD analyses
SEM analyses
TEM analyses
XPS analyses
Mechanism on transformation of Ni2+ and Fe0 in nZVI
Implications of the transformation of Ni2+ and Fe0 to groundwater remediation by nZVI
Researchers perceived that most of the toxicity of nZVI in cells and complete organisms comes from the production of reactive oxygen species (ROS), including free radicals such as hydroxyl radicals, superoxide anions, and non-radical hydrogen peroxide (Liu et al. 2013; Wu et al. 2014). ROS is produced in Fenton and Haber–Weiss reaction with Fe0 as the main initiator (Wang et al. 2012; Wu et al. 2014). However, Fe0 in nZVI undergoes a series of reactions with Ni2+, H2O, and DO during the removal of Ni2+ by nZVI, transforming into lepidocrocite, goethite, and magnetite with the depletion of Fe0. The reactivity of these iron oxides is relatively weak, and it is difficult to react and produce ROS. As a result, the impact on groundwater ecosystems will be significantly reduced. In addition, many researchers reported that iron oxides provide high affinity for heavy metal ions and organic pollutants, which exert certain positive effects on aquatic ecological environment. Kooner (1993) revealed that at neutral pH, although 50% of zinc was still available for transport, almost 100% of lead and copper got adsorbed onto the surface of goethite. Scott et al. (Fendorf et al. 1997) investigated chromate and arsenate retention mechanisms on goethite and it was found that three different surface complexes exist on goethite for both oxyanions. Zhang et al. (Zhang & Huang 2007) examined the adsorption of seven fluoroquinolone (FQ) antibacterial agents with goethite and the results showed that 50–76% of the added FQs were strongly adsorbed by goethite under experimental conditions. Sheydaei et al. (Sheydaei & Khataee 2015) indicated that γ-FeOOH can be effectively used as catalyst in successive ultrasonic/γ-FeOOH /H2O2 processes for decolorization of a textile wastewater containing Reactive Orange 29. Lin et al. (2012) reported the oxidative transformation of bisphenol A (BPA) by laboratory and synthetic commercial goethite, both of which are considered to be effective in inducing BPA conversion.
In addition, the magnetic attraction between nanoscale iron oxide is significantly lower than that of nZVI, resulting in weakened aggregation. Therefore, the specific surface area of iron oxides will be obviously increased compared to nZVI, which is favorable for iron oxides to remove/degrade contaminants through adsorption/catalysis. Table 1 shows the BET specific surface area and pore parameters for pristine nZVI and reacted nZVI. It can be seen that the BET specific surface area (46.67 m2·g−1) and pore volume (0.2283 cm3·g−1) of the iron oxides (reacted nZVI) are 5.3 times and 6.4 times of that of pristine nZVI (8.76 m2·g−1 and 0.0358 cm3·g−1), respectively.
Materials . | SBET (m2·g−1) . | Smicro (m2·g−1) . | Sext (m2·g−1) . | Vtotal (cm3·g−1) . | Vmicro (cm3·g−1) . | Vmeso (cm3·g−1) . | Pore size (nm) . |
---|---|---|---|---|---|---|---|
Pristine nZVI | 8.76 | 1.53 | 7.22 | 0.0358 | 0.0008 | 0.0361 | 16.59 |
Reacted nZVI | 46.67 | 8.57 | 38.10 | 0.2283 | 0.0044 | 0.2294 | 18.21 |
Materials . | SBET (m2·g−1) . | Smicro (m2·g−1) . | Sext (m2·g−1) . | Vtotal (cm3·g−1) . | Vmicro (cm3·g−1) . | Vmeso (cm3·g−1) . | Pore size (nm) . |
---|---|---|---|---|---|---|---|
Pristine nZVI | 8.76 | 1.53 | 7.22 | 0.0358 | 0.0008 | 0.0361 | 16.59 |
Reacted nZVI | 46.67 | 8.57 | 38.10 | 0.2283 | 0.0044 | 0.2294 | 18.21 |
The transformation of Ni2+ will also have an impact on its fate and bioavailability in groundwater ecosystem, as the toxicity of heavy metals to fish and other aquatic organisms depends primarily on free (hydrated) metal ions (Stumm 1992). Fe0.7Ni0.3 alloy and trevorite, which are transformed during the removal of Ni2+ by nZVI, will exist in a colloidal or suspended state, and most of them will be quickly transferred onto the suspended solids or the sediments at the bottom of the groundwater, thus the impact on aquatic organisms is negligible.
From the above, in the process of using nZVI to remediate groundwater contaminated by Ni2+, not only Ni2+ can be removed, but also the toxicity and bioavailability of Fe oxides and Fe–Ni composites formed by transformation are significantly reduced compared with Ni2+ and Fe0. Other heavy metal ions and organic contaminants in groundwater can also be adsorbed/catalyzed by iron oxides. The findings suggest that nZVI is a promising environmentally friendly technology in groundwater remediation.
CONCLUSION
A clear insight into the compositional transformation of Ni2+ and Fe0 during Ni2+ removal by nZVI was established in this study. XRD patterns indicated that the reaction of Fe0 with Ni2+ resulted in the transformation of the Fe0 into lepidocrocite (γ-FeOOH), goethite (α-FeOOH), and magnetite (Fe3O4). The Ni2+ became converted into trevorite (NiFe2O4) and Ni0 which existed in the form of Fe0.7Ni0.3 alloy. The results were confirmed by the d-spacing values obtained from HR-TEM images and the elemental composition obtained from TEM-mapping. In addition, SEM and TEM images showed that the morphologies of lepidocrocite, goethite, magnetite, and trevorite were lath-like, twin-rod, spherical, and folding fan, respectively. The mechanism of Ni2+ transformation includes reduction to Ni0 due to the reducibility of the Fe0, and the surface coordination of Ni2+ with Fe oxides to form Fe–Ni composite. The conversion of Fe0 undergoes a series of reactions, mainly composed of the redox of Fe0 with Ni2+, H2O, and DO, the combination of Fe2+ and OH− produced by Fe0 corrosion to amorphous ferrihydrite, and the further mineralogical transformation to Fe oxides with the aid of Fe2+ adsorbed on ferrihydrite. Compared with Fe0, the toxicity of Fe oxides to aquatic organisms decreased, the specific surface area increased, and the affinity for heavy metal ions and organic pollutants was higher. In addition, most of the Fe0.7Ni0.3 alloy and trevorite, which exist in the suspended or colloidal state, will be transferred to the suspended solids or the sediments at the bottom of groundwater. The findings indicate that the use of nZVI technology to remediate Ni2+-contaminated groundwater is environmentally friendly.
ACKNOWLEDGEMENTS
The authors would like to thank the Analytical and Testing Center, Wuhan University of Science and Technology for helpful contributions in the execution of this study.
FUNDING
The authors would like to express their gratitude to the Key Project of Natural Science Foundation of China (Grant No. 41230638), for the financial support. The support from the Open Fund of Hubei Key Laboratory for Efficient Utilization and Agglomeration of Metallurgic Mineral Resources from Wuhan University of Science and Technology (2017zy008) is duly acknowledged.
AUTHORS’ CONTRIBUTIONS
E.A. made substantial contribution to conception of the study, performed data analysis, investigation, synthesized material, curated data, and wrote the first draft. H.L. made substantial contribution to conception of the study, supervised the experiments, reviewed, and edited the manuscript. X.F. performed software edits, reviewed and edited the manuscript, and provided technical and material support.
DATA AVAILABILITY STATEMENT
All relevant data are included in the paper or its Supplementary Information.
CONFLICT OF INTEREST
The authors declare there is no conflict.