Shuxian Weia,
Chuan Heb,
Lanyue Zhanga,
Canhua Li*ac,
Jiamao Li*d and
Gang DUa
aSchool of Metallurgical Engineering, Anhui University of Technology, Maanshan, Anhui 243002, China. E-mail: licanhua1979@163.com
bJiuquan Vocationl and Technical College, Jiuquan, GanSu 735000, China
cKey Laboratory of Metallurgical Emission Reduction & Resources Recycling (Ministry of Education), Anhui University of Technology, Maanshan, Anhui 243002, China
dSchool of Materials Science and Engineering, Anhui University of Technology, Maanshan, Anhui 243002, China. E-mail: lijiamao@ahut.edu.cn
First published on 20th August 2024
The pollutants such as heavy metals, organic matter, and nitrates in soil and water pose challenges to environmental remediation technology. Nano zero valent iron has shown enormous potential in the field of environmental remediation due to its excellent adsorption performance. By using carbon based materials, rock minerals, biomolecules, etc., as supporting materials for nZVI, and through structural and performance modifications, its performance has been successfully optimized, reducing defects such as aggregation and easy oxidation of the material. This article compares and summarizes the modification effects of different loadings on nZVI, and comprehensively reviews the latest progress, preparation methods, and application of nZVI particles in soil and water remediation. Specifically, this article explores in detail the impact and mechanism of nZVI particles in commonly used antibiotics contaminated environments. Firstly, the combination methods of different types of materials with zero valent iron, as well as the synthesis methods and application scenarios of nZVI, were integrated. Secondly, the interaction mechanism between pollutants and nZVI was introduced in detail, including adsorption, redox reactions, and co-precipitation. Subsequently, environmental factors that affect repair efficiency were emphasized, such as pH value, coexisting components, oxygen, contact time, and temperature. Finally, the challenges faced by the application of nZVI in actual polluted soil and water bodies, as well as the prospects for its long-term efficacy and safety evaluation, are proposed to promote further development in the future.
According to reports, the removal rate of antibiotics in sewage treatment plants ranges from 36% to 79% due to process limitations.9 Common treatment methods include traditional approaches like coagulation, filtration, or adsorption, as well as air flotation, membrane filtration, and biological methods. These techniques employ chemical and biological treatments to break down, convert, or precipitate pollutants through oxidation, reduction, neutralization, etc., thereby rendering harmful substances harmless or less harmful.10 However, these methods entail significant energy and equipment investments, leading to high costs and the risk of secondary pollution, thus increasing the environmental burden. Additionally, there are challenges related to low processing efficiency.
In recent years, nanoscale zero valent iron (nZVI) has been widely used for the removal of pollutants from water and soil due to its high specific surface area, excellent adsorption and reactivity.11 nZVI has Fe0 core and Fe oxide shell, where the core has reducing ability and the shell acts as a reaction site for chemical adsorption and electrostatic interactions. The mechanisms of reduction, absorption, precipitation, and mineralization have played a role in the removal of heavy metals from the aqueous phase using nZVI.12 However, due to the magnetism and high surface energy of the newly synthesized nZVI, it is prone to spontaneous agglomeration and oxidation under actual reaction conditions, leading to its rapid deactivation. The pollutant removal pathways determined by nZVI include adsorption, complexation, co precipitation, and surface mediated chemical reduction.13 However, the preparation of nZVI requires the use of strong reducing agents such as sodium borohydride/potassium, which increases the preparation cost, generates toxic gases, and poses a threat to the environment. Load based modification provides more active sites for nZVI by dispersing it onto a support carrier with a porous structure. This method can enhance the activity of nZVI, accelerate the reaction between pollutants and nZVI, and promote the degradation of pollutants. Common load materials include carbon based materials, clay minerals, polymer compounds, etc. In the treatment of polluted water, an increasing amount of theoretical and experimental evidence indicates that nZVI is an effective and widely applicable nano-material. The reaction mechanism of nZVI for the removal of heavy metals mainly includes adsorption, complexation, reduction, and co precipitation. This provides new solutions for dealing with other mixed system pollutants such as heavy metals, nitrates, organic matter, etc.
In summary, removing pollutants from wastewater has become an important issue that urgently needs to be addressed. However, the application of nZVI materials in the field of in situ remediation of environmental pollutants is currently limited. The defects of nZVI during use can be compensated for through load and other methods. Therefore, this article summarizes the materials loaded with nZVI, including carbon based materials, geological materials, and polymer compounds, whose mechanisms and application value in the remediation of antibiotic contaminated soil and water have not been systematically explored. The aim is to review the application, immobilization mechanism, and environmental impact of nZVI in the remediation of antibiotic contaminated soil and water. First, the synthesis methods of nZVI were summarized, and different types of loading materials and their combination with nZVI were introduced. Secondly, the environmental factors for the repair of commonly used antibiotics by nZVI were explored and the interaction mechanism between commonly used antibiotics and nZVI was summarized. In addition, this article summarizes the current situation of antibiotic pollution in water environment, soil, and sediment, aiming to draw attention to the issue of antibiotic pollution.
Methods | Process | Advantages | Disadvantages | References |
---|---|---|---|---|
Liquid phase reduction method | Add highly reducing KBH4 or NaBH4 solution to Fe2+or Fe3+solution. After the reaction is complete, wash, separate, dry the solution, and reduce it to nZVI. Auxiliary methods: ultrasonic, microgravity, micro lotion, ball milling etc. | Easy to operate, mild conditions, and high product activity | Reducing agents are expensive and toxic; hydrogen and B(OH)3, a hazardous byproduct, are produced during the preparation process | 14 |
Electrodeposition method | Preparation of nano iron particles using external current electrolysis of ferrous or trivalent iron salt solutions | High purity, small particle size | The tendency for particle aggregation is relatively high | 15 |
Ball milling method | Under the action of rotating mechanical energy, zero valent iron powder is repeatedly compressed and broken by the grinding ball, continuously refining to the nanoscale, forming nZVI | Non toxic, high yield, low cost, and no excess by-products | The product has poor form and is prone to mixing impurities, resulting in high energy consumption | 16 |
Green synthesis method | Extracts are prepared by using solvents and specific plants or organic compounds as reducing agents, and mixed with Fe2+or Fe3+ solutions to reduce them to nZVI | Green and environmentally friendly, extracts can reduce clumping without the need for additional dispersants | Long process time and low yield | 4 |
Carbon thermal reduction method | Immerse the carbon source in an iron source solution and stir to disperse. After being filtered and dried, the iron source is thermally reduced by carbon in a high-temperature environment filled with protective gas. Auxiliary methods: aerosol, ultrasonic spray | Cheap raw materials | The production conditions are harsh, and producing hydrogen (flammable) and carbon monoxide (toxic) requires high energy and energy consumption | 17 |
Hydrogen thermal reduction method | Reduce iron oxide to nZVI using hydrogen gas at around 500 °C | Less by-products | Long production time, dangerous processes, and high energy consumption | 18 |
Evaporation–condensation method | The iron target is heated above the boiling point with a laser, and the iron atoms evaporate and condense rapidly in an inert gas atmosphere to form iron nanopowders. Auxiliary methods include laser ablation, electric arc and cathodic sput-tering | Low cost and environmentally friendly raw materials, good thermal conductivity of iron metal, high melting point, resulting in high purity, chemical activity, and surface cleanliness of iron nanoparticles, making it possible to prepare multi-component nanoparticles | Expensive equipment and high energy consumption | 19 |
This section will introduce different methods and their characteristics one by one. Cheng et al.22 prepared a series of sodium alginate/chitosan composite (SA/CTS) carbon aerogels with or without nano zero valent iron without supercritical process, and studied the relationship between the adsorption performance of carbon aerogels for Cr(VI). Including the relationship between pH value, adsorbent dosage and adsorption temperature. nZVI@CTS The composite material utilizes the excellent support structure of alginate, the high affinity between chitosan and Cr(VI), and the strong reducibility of nZVI, providing a relatively high specific surface area of 300 m2 g−1, excellent adsorption capacity of 204.35 mg g−1 at 318 K, and sufficient strength to maintain structural integrity for reuse. The preparation process is shown in Fig. 1a.
Fig. 1 Process flow of four different nZVI preparation methods (a–d).22–25 |
Wang et al.23 initially developed hydrophilic and functionalized polyacrylonitrile (PAN) membranes through a two-step process involving the addition of polyvinyl alcohol and the in situ polymerization of acrylic acid. Furthermore, they incorporated nZVI into the modified membranes.The prepared PAA/PANnZVI (PPN) composite material exhibits good reactivity towards metronidazole (MNZ), with a conversion rate and reaction rate 2.03 and 4.77 times higher than nZVI. Meanwhile, PPN composite materials maintain enhanced stability and recyclability during repeated cycles. The preparation process diagram is shown in Fig. 1b.
To obtain porous hydrochar loaded nZVI (nZVI@PHC) composite materials, Cao et al.24 mixed 60 mg of nZVI, 100 mg of PHC, and 100 mL of anaerobic water in a conical flask and oscillated them for 12 h in a water bath oscillator at 25 °C and 200 rpm. Finally, the composite material was obtained through magnetic separation, centrifuged three times with anaerobic ethanol and distilled water, and then dried in a freeze-drying machine to avoid oxidation. nZVI@PHC was obtained. The preparation process diagram is shown in Fig. 1c.
B. N. Akhgar et al.25 prepared nZVI from natural pyrite concentrate through mechanochemical reactions and subsequent separation steps. Nano zero valent iron (nZVI) was prepared by mechanochemical treatment of natural pyrite using metallic aluminum powder and a sonochemical leaching method. Fe–Al2S3 compound was prepared by co-grinding natural pyrite and alumina using a planetary mill. Next, the sonochemical leaching method was used to prepare nZVI by leaching with 1.5 mol L−1 NaOH solution at 80 °C for 45 min. The prepared nZVI had a size of less than 100 nm and a specific surface area of 116 m2 g−1. The preparation process diagram is shown in Fig. 1d.
In summary, physical, chemical, and biosynthetic methods all prove effective in synthesizing nZVI. While the physical synthesis method is straightforward and environmentally friendly, it is constrained by the need for specialized synthesis equipment and relatively stringent synthesis conditions. In contrast, chemical and biosynthetic methods are more convenient and flexible to operate, with controllable reaction conditions. The synthesized nZVI has a more uniform size, providing more choices for the synthesis of nZVI. Regardless of the method used to synthesize nZVI, its surface structure may be affected by agglomeration or passivation, and further modification is needed to maintain its chemical activity. After decades of development, the preparation and modification technology of nano zero valent iron has become increasingly mature. Nonetheless, challenges remain regarding its stability, reaction efficiency, and the safety of nanoparticles, which pose obstacles to its engineering applications.
Among them, bimetallic modification is the modification of the structure of nZVI. Bimetallic particles accelerate the corrosion of Fe0 by electrochemical effects in combination with metals with high redox potentials, such as Pd, Pt, Co, Ni, Ag, and Cu. The incorporation of metal particles proves advantageous in hastening iron corrosion, augmenting hydrogen production, and expediting electron transfer. Nonetheless, the high cost of raw materials for the preparation of bimetallic particles and the potential for secondary contamination have limited their widespread use.25–28 From an application perspective, developing low-cost metal particles and loading them onto the surface of nZVI to form bimetallic particles is one of the future research directions. Table 2 outlines the strengths and weaknesses of bimetallic-modified nZVI.
Modification methods | Advantages | Disadvantages | References |
---|---|---|---|
Biochar bimetallic particles | Good dispersibility, high activity, and good stability | High preparation cost | 23 |
Fe–Ag bimetallic nanoparticles | High efficiency, good performance | Expensive raw materials | 29 |
Fe–Pd bimetallic nanoparticles | Acting as a reducing agent, efficient | Secondary pollution | 30 |
Fe–Ni bimetallic nanoparticles | Fast, complete response | Requires other techniques | 31 |
Fe Cu bimetallic nanoparticles | High activity, fast hydrogen production | Excessive inhibition | 32 |
Xie et al.33 uniformly loaded nZVI onto the surface and inner walls of nano-activated alumina (γ-Al2O3) using a liquid-phase reduction method, preparing magnetic nano zero-valent iron/activated alumina composite material (nZVI/γ-Al2O3). The material was characterized, and the adsorption isotherms and kinetics of five typical heavy metal ions Zn2+, Cu2+, Cd2+, Cr3+, and Mn2+ on nZVI/γ-Al2O3 were simulated. Additionally, the competitive adsorption and synergistic adsorption behavior in a multi-heavy metal ion system were investigated. The results indicated that magnetic nano zero-valent iron loaded on nano activated alumina not only overcame the agglomeration of nZVI particles caused by volume and surface interface effects but also kept nZVI in a stable high surface energy state. The modification of nZVI with bimetallic particles accelerated the corrosion process of iron, increased hydrogen production, and facilitated electron transfer. However, bimetallic particles were prone to secondary pollution and required modification using other expensive technologies, necessitating further research on them. At present, researchers are committed to exploring cleaner and more economical methods for modifying bimetallic particles.
The research suggests that incorporating magnetic nZVI onto nano-activated alumina effectively mitigated the agglomeration of nZVI particles due to volume and surface interface effects, while preserving nZVI in a stable high surface energy state.9–15,20,21 However, the use of bimetallic particles posed risks of secondary pollution and necessitated modification through other costly technologies. Thus, further investigation is warranted in this field.33
Materials | Structural form | Factors affecting removal | Disadvantages | Advantages | Ref. |
---|---|---|---|---|---|
Activated carbon (AC) | Highly porous with a wide range of pore size distribution from micro to macro pores. Particle size and shape can be adjusted according to application needs, such as powder, granule, column etc. | Pore structure development, large specific surface area, nZVI loaded on the pores of AC, functional groups such as –OH and –COOH on the surface are favorable for the binding of nZVI | The production cost is high, the adsorption capacity is limited, the selectivity is poor, and the regeneration process is complex | Low production cost and abundant precursor resources | 14 |
Biochar (BC) | Porous structure, particle size can range from a few millimeters to tens of micrometers, with irregular morphology | Functional groups on the surface of biochar (e.g. hydroxyl, carboxyl, etc.) can form chemical bonds with pollutants | Low selectivity, uneven pore size distribution, difficult regeneration, unstable adsorption performance | High porosity, rich in oxygen-containing functional groups, simple production process, waste as raw material | 15 |
Graphene nanotubes (GNs) | Hollow, long tubular structures with diameters in the nanometer range | nZVI can be loaded on the outside of carbon nanotubes or within the pores and cracks of a reticulated structure | Difficulty in dispersion, toxicity, and processing and handling | Easy to identify adsorption sites and mechanisms, with a very high specific surface area | 16 |
Canotubes (CNT) | Two-dimensional planar structure with single or few layers, thickness of only one or a few carbon atoms, honeycomb hexagonal lattice structure | Graphene nanosheets with folded edges can support nZVI nanoparticles | High production costs, complex processing, unstable properties, and potential environmental and health risks | Large specific surface area, multiple active centers and functional groups, porous structure | 4 |
At present, the use of nano zero valent iron and carbon based nanocomposites for environmental remediation of water, soil, and other environments has become one of the hot topics of widespread concern for scholars around the world.29–32,34,35 Carbon based materials as carriers of nZVI can not only increase its specific surface area, reduce its aggregation, but also accelerate electron transfer efficiency. In addition, composite materials based on carbon based materials are difficult to completely separate from environmental media, increasing the risk of secondary pollution. The focus of future research lies in developing methodologies for the recovery and reuse of contaminants from environmental media.
Chen et al.36 employed agricultural waste straw biochar as a carrier for synthesizing zero-valent iron nanoparticles on straw biochar via the co-precipitation method. The removal of p-nitrophenol (PNP) was achieved through the activation of sodium persulfate (PS), and they investigated various factors influencing the degradation of PNP. The results indicated that at pH = 7, BC@nZVI exhibited the best activation effect when the dosage was 2 g L−1 and the PS concentration was 1 mM. During this condition, the removal of 40 mg L−1 PNP reached 91.7% within 10 min. By enhancing the dispersibility of nano zero-valent iron (nZVI), reducing its aggregation, and mitigating passivation, the activation performance of PS has been significantly improved. This provides a promising method for treating challenging pollutants such as PNP. BC@nZVI exhibits high stability, allowing for up to threefold repetition of catalytic experiments, thereby expanding the material's applicability and ensuring its reusability in water treatment applications.37
Mortazavia et al.38 developed a two-step synthesis method to immobilize nanoscale zero-valent iron (nZVI) particles onto activated carbon (AC/nZVI), enabling simultaneous adsorption and reduction of hexavalent chromium (Cr(VI)) from aqueous solutions. The two-step synthesis procedure was employed to fix nZVI particles onto activated carbon (AC/nZVI), exhibiting 33 times higher adsorption capacity and greater affinity towards Cr(VI) compared to AC alone. Meanwhile, Liu et al.39 utilized Fe2O3 and activated carbon (AC) as raw materials, subjected them to planetary ball milling followed by gas-phase reduction at 850 °C under a hydrogen atmosphere to prepare AC/nZVI composite materials. Experimental results demonstrated that the ball milling and gas-phase reduction method could partially achieve nanoscale Fe0 and load it onto AC, successfully synthesizing the nZVI-AC material. Zhang et al.40 synthesized efficient oxidative desulfurization (ODS) catalysts by encapsulating nZVI in self catalytic carbon nanotubes (CNTs). The nZVI@CNT catalyst demonstrates excellent catalytic performance and enhanced stability, with its initial performance remaining at 80% even after 6 cycles. This highlights effective optimization and regulation between carbon nanotubes and iron particles. It was verified that the unique coating structure and porous configuration contributed to enhancing desulfurization efficiency. The research results can provide reference for the effective synthesis strategies of nZVI high-efficiency oxidation desulfurization catalysts in practical industrial applications.
Chemical reduction technology utilizing nano zero-valent iron (nZVI) stands out as a highly effective approach for on-site remediation of contaminated water. Nevertheless, overcoming the associated surface passivation during the reaction process proved challenging, leading to a loss of reducing reactivity. Li et al.34 studied a novel system based on nZVI/graphene nanosheets (nZVI/GNS) for the effective removal of Cr(VI) from water. The experiment fixed nZVI on graphene to improve the stability of nZVI, while graphene coupling promoted electron transfer in nZVI and delayed the passivation of nZVI surface, thereby enhancing the performance of nZVI in removing Cr(VI). The two-dimensional structure of graphene may provide skeleton support for nZVI, thereby solving the bottleneck of aggregation and passivation. Mon et al.41 established the synthesis of nZVI/graphene from azalea leaves and FeCl3. During this process, it was confirmed that magnetic Fe3O4/amorphous carbon undergoes a phase transition to nZVI/graphene composite materials through a carbon thermal reduction process. The nZVI particles are sandwiched between graphene sheets with a diameter of approximately 16–40 nm, and the two-dimensional structure of graphene may provide skeletal support for nZVI, thereby solving the bottleneck of aggregation and passivation. Graphene provides good conductivity, skeleton support, and long-term electron release characteristics, which can accelerate the reduction of Cr(VI) to Cr(III) and exhibit fast and high Cr(VI) removal ability from aquifers.
Sahu et al.46 successfully synthesized red mud-supported nZVI (RM-nZVI) composite materials using the sodium borohydride reduction method, where red mud served as a stable support medium for the development of red mud-modified nZVI. In the presence of red mud, sodium borohydride (NaBH4) was used to reduce iron and synthesize RM-nZVI. The morphological characteristics of RM-nZVI have been confirmed, indicating that it is in a diffusion state with small aggregation. The use of red mud as a carrier material enhanced the reactivity of RM-nZVI and reduced the aggregation of nZVI. Extensive characterization of RM-nZVI has confirmed that the removal of Hg2+ initially occurs through rapid physical adsorption, followed by the reduction of Hg2+ to Hg0. Adsorption mainly occurs on the surface of RM-nZVI, followed by reduction to Fe0. Red mud, as a supporting agent, has the advantages of strong adsorption capacity, low cost, renewability, and easy treatment in wastewater treatment. It can effectively adsorb organic matter and heavy metal ions, purify water quality, reduce treatment costs, and comply with sustainable development principles.
Zhao et al.51 enhanced the denitrification effect of vertical flow constructed wetlands (VFCWs) using montmorillonite loaded nanoscale zero valent iron immobilized sodium alginate (SA/Mt nZVI). This study showed that SA/Mt nZVI, as a cost-effective material, is feasible and feasible for purifying VFCWs wastewater. The maximum NO3−–N removal efficiency reached 75.81 ± 1.6%. In addition, after adding SA/Mt nZVI, the biodiversity and richness of CW-nZVI are higher. The micro beads of SA/Mt nZVI improved water quality, reduced the burden of separation, and reduced the potential risk of nanomaterials to VFCW.
Ma et al.52 rapidly synthesized nZVI composite materials (PDA/ATP-nZVI) loaded with polydopamine (PDA) modified attapulgite (ATP) under acidic conditions. PDA/ATP-nZVI composite materials exhibit excellent Cr(VI) removal efficiency even in the presence of interfering ions under acidic conditions. The effect of low concentration coexisting ions on the removal of Cr(VI) can be ignored, while high concentration interfering ions can promote the removal of Cr(VI). The experiments showed that Fe2+ plays a key role in the reduction of Cr(VI) by PDA/ATP-nZVI. PDA enhances the elimination of Cr(VI) by supplying electrons to Cr(VI) and accelerating the conversion of Fe3+ to Fe2+. Fan et al.53 prepared nZVI by liquid-phase chemical reduction method and loaded it on expanded perlite to prepare nFe@EP materials used to remove phosphates from water bodies. Examined the initial pH, temperature, and nFe@EP The influence of added mass concentration and initial phosphate mass concentration. The results indicate that, nFe@EP good adsorption of phosphate in water, with a removal rate of 95.7% and an adsorption capacity of 31.9 mg g−1. Fig. 3 shows the scanning electron microscope images of nZVI loaded on different minerals, demonstrating the morphology of the different minerals. The loaded nZVI particles are mostly aggregated, and the nanoparticles have a large specific surface and porosity. Mineral-supported nZVI enhances its stability, dispersibility, and adsorption capacity, thereby improving efficiency and safety in environmental remediation and pollution control. Additionally, it adapts to various environmental conditions, offering a promising solution for environmental management.54
Jin et al.55 prepared nZVI by hydrothermal method and mixed it with polyvinyl alcohol (PVA) in solution to prepare a polyvinyl alcohol/nano-sized zero valent iron composite film with better structure and oxygen resistance. The results showed that with the increase of nZVI content, the glass transition temperature of the composite film gradually increased, the tensile strength and elongation after fracture first increased and then decreased, the oxygen permeability coefficient first decreased and then increased, and the thermal stability decreased.
Cheng et al.56 designed a series of sodium alginate/chitosan composite (SA/CTS) carbon aerogels and elucidated that the mechanism of adsorption of Cr(VI) mainly includes electrostatic interactions, hydrogen bonding attraction and redox reactions. Therefore, CTS and nZVI@CTS have a promising application in water and wastewater containing Cr(VI).
The intensification of industrial processes and human activities has caused heavy metal pollution in water, which has attracted global attention. We need to find an environmentally friendly and effective remedy. Zhao et al.57 prepared sodium alginate nZVI biochar composite material (CANRC) using calcium alginate encapsulation and liquid-phase reduction method. This composite material was used for the first time to remove Pb2+, Zn2+, and Cd2+ from water. CANRC is a heavy metal adsorbent with good regeneration performance, providing an effective method for removing heavy metals from wastewater. Gao et al.58 studied the effects of carboxymethyl cellulose sodium (CMC) as a stabilizer on the physicochemical properties, reactivity, and reusability of S-nZVI for the degradation of nitrobenzene (NB). Characterization shows that CMC improves the degree of vulcanization, significantly inhibits surface oxidation of S-nZVI, enhances hydrophobicity, and reduces electron transfer resistance. Meanwhile, CMC-S-nZVI exhibits superior reusability in NB degradation compared to S-nZVI.59 Table 4 summarizes the properties, structures, advantages, and disadvantages of common geological and biomacromolecule materials and loaded nanomaterials.
Materials | Structural form | Factors affecting removal | Disadvantages | Advantages | Ref. |
---|---|---|---|---|---|
Red mud (RM) | The particle size affects its surface activity and reaction efficiency | Porous structure and high specific surface area, functional groups on the surface react with pollutants to improve adsorption efficiency | Poor selective adsorption performance, difficult to regenerate after use, may cause pollution, and needs to be treated before using | Low cost, easy to obtain, capable of achieving various functions such as photocatalysis and antibacterial | 46 |
Zeolite | Regular shape and porous structure | Zeolite loaded nanoparticles can remove ionic pollutants from water through ion exchange reaction | Poor selective adsorption makes it difficult to regenerate after use, which may lead to secondary pollution | It has a high specific surface area, is easy to obtain, and has good ion exchange capacity | 47 |
Bentonite | Similar to red mud | High specific surface area and good pore structure, capable of removing ionic contaminants from solution by ion exchange | Poor selective adsorption performance makes it difficult to regenerate after use, resulting in secondary pollution | A mineral with high specific surface area, good pore structure, excellent ion exchange capacity, and low cost and easy availability | 50 |
Chitosan (CS) | Tens of microns to hundreds of microns, can be made into films or fibers | Amino and hydroxyl groups can adsorb pollutants through van der Waals forces and hydrogen bonds | Poor solubility in neutral or alkaline environments, and difficult to regenerate | Excellent biodegradability, good environmental protection, high adsorption capacity | 56 |
Calcium alginate (CA) | When gel is formed, its thickness can vary from several microns to several millimeters | The gel with loaded nanoparticles is formed, and its surface and pores can absorb pollutants | Not very stable in acidic environments, and the regeneration process after use is complex | Able to form stable gels with good biocompatibility and biodegradability. Relatively cheap and easy to obtain | 57 |
Polyvinyl alcohol (PVA) | Between tens and hundreds of micrometers | The loaded nanoparticles may react with contaminants to form colloidal precipitates that are removed from solution | Inherent low mechanical strength, poor solvent resistance in water | Good solubility in water for ease of preparation and application. Highly adjustable and biocompatible | 55 |
Carboxymethyl cellulose sodium (CMC) | Tens of micrometers to hundreds of micrometers, forming a viscous solution or gel in water | Carboxymethyl groups can react chemically with loaded nanoparticles or contaminants | Poor stability: stable at extreme pH values | Good solubility in water, easy preparation, good adsorption capacity, and strong adjustability | 58 |
Huang et al.61 used nZVI particles to quickly remove Cr6+from the solution. In the experiment, different nZVI particles of electric spray (E-nZVI) and non electric spray (NE-nZVI) were used to treat Cr6+solution with a concentration level of 100 mg mL−1. When the nZVI concentration reaches 0.93 mg mL−1, the removal rate approaches 100%. Based on the XPS results, no Cr6+was detected on the particle surface, and it can be concluded that the removal of Cr6+ is mainly achieved through precipitation and reduction.62 Pullin et al.49 discussed the application and mechanism of zero valent iron nanoparticles (nZVI) in the removal of Zn2+. This indicates that nZVI has a significant effect on the removal of Zn2+. Among them, pH and dissolved oxygen (DO) are important factors for the removal of Zn2+ by nZVI. DO improves the removal efficiency of Zn2+, and under oxygen-containing conditions, it can exhibit outstanding adsorption affinity. The FeOOH shell layer can improve the adsorption efficiency of nZVI. The removal efficiency of Zn2+ increases with the increase of pH. The acidic conditions reduce the removal efficiency of Zn2+ by nZVI, as the presence of H+ in the solution inhibits the formation of iron hydroxide (oxygen). In contrast, due to the multifunctional properties of nZVI and its inherent pH stability, which has a good tolerance to influent fluctuations, it is easy for nZVI to obtain stable and lower levels of Zn2+. In the case of nZVI, aqueous corrosion continuously releases Fe2+and OH−, and the reaction mechanism is shown in formula (1).
Fe0 + 2H2O → Fe2+ + 2OH− + H2 | (1) |
The adsorption effect of nZVI on Zn2+: the surface of nZVI is composed of a layer of FeOOH, which has a prominent affinity for metal cations.49,50 The gradual corrosion of Fe0 by water leads to the formation of iron oxide in the form of discrete particles or deposits on the surface of nZVI, resulting in a significant increase in surface area.63
Liu et al.56 found through research that compared with other types of adsorbents, nZVI has higher adsorption capacity and is the most effective adsorbent for removing cadmium from aqueous solutions. The author points out that the extremely small particle size, large surface area, and high-density reaction and adsorption sites make nZVI a potential candidate for environmental applications, especially for Cd2+ removal. Compared with the newly produced biochar nZVI composite adsorbent, nZVI formed on biochar through adsorption and complexation processes.55–58,64,65
In summary, increasing the dosage of nZVI is beneficial for improving the removal efficiency of heavy metal ions in the removal process. Due to the competition between H+ and Pb2+for surface active sites, weak acidic conditions are more conducive to the removal of most heavy metal ions. The mechanism of using nZVI to remove heavy metal ions is mainly due to the combined effects of adsorption, reduction, and complexation adsorption, which precipitate iron minerals and form co precipitation. In summary, the characteristics of extremely small particle size, large surface area, and high-density reaction and adsorption sites enable nZVI to have better adsorption capacity. The mechanism of nZVI removal of heavy metals is shown in Fig. 4.
Fig. 4 Reaction mechanism diagram of nzVI removal of heavy metals.66 |
Fig. 5 Source and fate of antibiotics in the environment.60,67–74 |
In order to reduce the harm of tetracycline, it is necessary to use and manage tetracycline antibiotics reasonably, including controlling the rationality of agricultural use, strengthening environmental monitoring and governance, promoting rational use of drugs, and preventing the development of drug resistance. Wang et al.73 successfully prepared a modified membrane supported iron composite material PDA/PAN/BC-Fe0 (PPBN) by functionalizing hydrophilic porous polyacrylonitrile (PAN) membranes with sisal fiber biochar (SF-BC) and polydopamine (PDA) as carriers. Studied the effects of different reaction conditions and interference factors on the degradation performance of TC. In addition, the cycling and stability of PPBN were also evaluated. Effectively inhibiting the aggregation and release of nZVI particles, enhancing the reactivity and stability of PPBN.
The results show that the removal rate of TC by PPBN can reach 90.16% within 120 min, which is 36.16% higher than that of nZVI. After 6 regeneration cycles, the removal rate of TC by PPBN only decreased by 10.22%. Three degradation pathways for removing TC were proposed. The removal mechanism includes the synergistic effect of physical adsorption, chemical oxidation, and reduction, and the redox reaction induced by hydroxyl radicals (˙OH) and superoxide radicals (˙O2−) plays a key role. The research results provide a simple, efficient, and stable material for the treatment of antibiotic wastewater. Experiments have shown that the removal efficiency of TC is better under low pollutant concentration, high temperature, and neutral conditions.
Chen et al.74 designed a combined system of polyvinylpyrrolidone (PVP) and nanoscale zero valent iron (nZVI) and copper (Cu) bimetallic particles (PVP nZVI/Cu) for the reduction of ciprofloxacin (CIP) under weak magnetic field (WMF) conditions. Further characterization of the surface morphology and physicochemical properties of the new catalytic material. In addition, the catalytic reactivity of PVP nZVI/Cu was measured in the presence or absence of WMF. The experimental results show that the introduction of WMF enhances the catalytic performance of the PVP nZVI/Cu system, with a maximum CIP removal rate of 95.6% (120 min). The study provides new insights into the removal of CIP by NZVI, and has prospects for its practical application.
The natural passivation phenomenon generated by the formation of surface oxide layers in nZVI is a bottleneck in exploring the complete potential of this material. B. Nandana et al.75 solved by in situ synthesis of nZVI/Cu bimetallic heterostructures. The passivation bypass of nZVI is achieved by synthesizing nZVI copper bimetallic nanoparticles (nZVI/Cu). Research has shown that nZVI/Cu has higher performance than bare nZVI. When using nZVI and nZVI/Cu as catalysts, the degradation efficiency of nZVI/Cu for TC and CIP was 99.99% and 98.59%, respectively, with rate constants of 0.0631 min−1 and 0.032 min−1. In addition, the removal rates of TET and CIP in the antibiotic mixture by nZVI/Cu were 99.34% and 99.9%, respectively. By utilizing the inherent magnetism of nZVI/Cu samples, catalysts can be easily recovered.
Yang et al.76 prepared a series of biochar supported nano zero valent iron catalysts (nZVI-BC) by co pyrolysis of soybean straw and Fe2O3 at different pyrolysis temperatures. It can effectively degrade tetracycline in water and reduce the total organic carbon content. In the future, it has potential application prospects. On the basis of preparing nZVI-BC, it should be possible to design and introduce more active functional groups and active sites to further improve the catalytic performance of the catalyst. However, in real water environments, the system is relatively complex and has limitations due to other pollutants such as heavy metals, pesticides, dyes, etc. Therefore, in future research, the problem of simultaneous removal and interaction of various pollutants should be addressed. Contribute to the development of advanced oxidation technology catalysts.
Nguyen et al.77 synthesized bimetallic palladium zero valent iron (Pd/nZVI/rGO) composite materials loaded with reduced graphene oxide using a one-step liquid-phase reduction method. Analysis shows that the presence of rGO flakes prevents the aggregation of Pd/nZVI nanoparticles and delays the transformation of iron corrosion products from magnetite/hematite to scale bluestone, resulting in more uniform dispersion of these nanoparticles. In addition, loading Pd/nZVI nanoparticles can effectively avoid the stacking of rGO sheets. The synthesized Pd/nZVI/rGO composite material is used to remove the antibiotic oxytetracycline (OTC) from aqueous solution. Research has found that introducing the optimal amount of rGO into Pd/nZVI nanoparticles significantly enhances the removal of OTC. The removal of OTC is the result of a combination of adsorption process, Fenton like reaction, and reduction reaction. The Pd/nZVI/rGO composite material exhibits better reusability than the original nZVI particles. A pathway for OTC degradation on Pd/nZVI/rGO nanocomposites was also proposed.
Li et al.79 prepared sulfurized nZVI (S-nZVI) using ball milling, vacuum chemical vapor deposition (CVD), and liquid-phase reduction techniques. Experiments have shown that the removal of 2,4,6-trichlorophenol (TCP) by nZVI and S-nZVI is based on surface adsorption and subsequent direct reduction of Fe0, in situ oxidation of ROS, and polymerization on the surface of these materials. During the reaction process, the corrosion products of these materials are transformed into crystalline Fe3O4 and α/β- FeOOH enhances the stability of nZVI and S-nZVI materials, facilitating electron transfer from Fe0 to TCP, as well as TCP's strong affinity for Fe or FeSx phases. All of these contribute to the high removal and mineralization performance of nZVI and sulfurized nZVI towards TCP in continuous cycling experiments. Zheng et al.89 prepared porous CaCO3 using microbial induced calcium carbonate precipitation (MICP) technology, which was then used as a carrier material for CaCO3@nZVI Composite materials. CaCO3@nZVI The main products of TCE degradation in composite materials are acetylene, ethylene, and ethane, and the synergistic effect of adsorption degradation is the main mechanism for removing TCE.
Jing et al.80 successfully synthesized nano zero valent iron reduced graphene oxide (NZVI rGO) in their research and applied it to the removal of 2,4-DCP. The characterization results indicate that nZVI particles were successfully loaded onto rGO nanosheets, improving the dispersion of the particles. The removal experiment showed that compared with bare nano zero valent iron, the presence of rGO significantly improved the removal efficiency of 2,4-DCP. The removal mechanism of 2,4-DCP during simultaneous removal is adsorption, which provides theoretical support for the treatment of combined pollution of chlorinated organic compounds and heavy metals.
Zarime et al.81 studied the removal of methylene blue (MB) using nano zero valent iron (Gr-nZVI) loaded on residual granite soil to investigate its potential use as an efficient adsorbent. According to adsorption analysis, compared with Gr-nZVI and nZVI, Gr exhibits higher MB removal adsorption capacity. Overall, it provides experimental support for the selection of nZVI carrier materials, which helps to promote the development and progress of green restoration materials.
However, using nZVI for organic pollutant remediation still faces some challenges. The application of nZVI-based materials for the removal of organic pollutants is still limited by the high cost of raw materials and the complexity of the synthesis method, which makes it difficult to develop industrialized practical applications in large quantities. Therefore, reducing the cost of synthesis and exploring new methods of preparation that increase the activity of nZVI, produce large scale outputs, and are adapted to real-world production are essential for realizing the widespread application of nZVI and its basic materials.82
Pei et al.84 successfully prepared nZVI/LDH nanocomposites by loading nano zero valent iron (nZVI) onto the surface of layered double hydroxides (LDH) using a liquid-phase reduction method. To adsorb coupled reduction of nitrate (NO3−–N), nZVI/LDH composite materials were prepared. The results showed that the removal rates of NO3−–N and total nitrogen by nZVI/LDH composite material within 180 min were 88.64% and 77.63%, respectively. The selectivity for N2 was 55.21%, and the selectivity for ammonia nitrogen was only 1.86%. The mechanism of NO3−–N synergistic adsorption reduction degradation, including rapid adsorption of initial NO3−–N, was proposed by measuring the content of NO3−–N, nitrite NO3−–N, and NH4+–N in the aqueous and adsorbed phases during the reaction process. LDH, as a loading material for nZVI, significantly reduces the agglomeration of nZVI and provides more Fe0 active sites. This is mainly due to the synergistic effect of nZVI and LDH in nZVI/LDH composite materials. Therefore, nZVI/LDH composite materials can be applied as an efficient and stable material in real water. Zhou et al.85 studied and prepared a novel composite filler consisting of tea polyphenols, nZVI, and modified polyethylene carrier (TP nZVI/PE). The removal rate of nitrate by TP-nZVI/PE composite microorganisms is 79.88 ± 0.17%, which is three times that of TP-NZVI/PE. The oxidized nZVI is converted into Fe2+/Fe3+, which is easy to adsorb nitrate and then co precipitate, which is conducive to further removal of nitrate.
The rapid, environmentally friendly preparation and efficient application of nZVI exhibit excellent performance in the reduction and removal of nitrate. The above study not only enriches the application of nZVI and biological denitrification treatment technology. The possible mechanisms in nitrate removal are shown in Fig. 6.
Fig. 6 Possible mechanism of nitrate removal by nano zero valent iron.83–85 |
pH value is a key factor in the nZVI reaction process. Chen et al.74 designed a composite material consisting of polyethylene pyrrolidone (PVP) and nanoscale zero valent iron (nZVI) and copper (Cu) bimetallic particles (PVP nZVI/Cu). In the presence or absence of an external weak magnetic field (WMF), the pH (2–10) increased from 2 to 6 with the initial pH, and the removal rate of CIP increased from 48.8% to 85.7%. However, as the initial pH further increased to 10, the removal efficiency significantly decreased to 19.7%. The mechanism proposed for the decrease in catalytic ability at pH < 6.0 is the extremely rapid corrosion of PVP-nZVI/Cu at low pH, resulting in H2 (eqn (2)) covering the surface of the composite material, which will limit the interaction between CIP and PVP-NZVI/Cu. In addition, the partial dissolution of PVP-nZVI/Cu at pH 2.0 also weakened the adsorption of CIP on PVP-nZVI/Cu particles, leading to a decrease in CIP removal efficiency. However, as the pH value continues to increase, the passivation layer formed by the precipitation of iron hydroxide on the surface of PVP-NZVI/Cu in high pH solutions hinders the corrosion of iron (eqn (3)). As the initial solution pH increases, the CIP removal rate gradually decreases. Acidic and neutral conditions are more conducive to the removal of CIP than alkaline conditions. This is because the Fe2+ formed by the corrosion of nZVI under acidic conditions can activate PS. As the pH decreases, the concentration of Fe2+ in the solution increases, and the removal rate of CIP also increases.
(2) |
(3) |
As the initial solution pH rises, the removal rate of CIP gradually diminishes. Acidic and neutral conditions prove more favorable for CIP removal compared to alkaline environments. This phenomenon arises from the activation of PS by Fe2+ generated through nZVI corrosion under acidic conditions. With decreasing pH, the concentration of Fe2+ in the solution rises, correspondingly enhancing the removal efficiency of CIP.
Chen et al.74 investigated the relationship between the removal efficiency of CIP by PVP nZVI/Cu particles and reaction temperature (288.15–308.15 K). It can be seen that the removal efficiency increases with the increase of temperature. Under weak magnetic field conditions, the removal rate of CIP increased from 86.2% to 98.4%. Higher temperatures may increase the migration rate of CIP from solution to nano-particles. In addition, higher temperatures can also accelerate the corrosion of PVP-NZVI/Cu.
Wang et al.87 prepared a new aluminum hydroxide gel coated with nanometer zero valent iron (AHG@nZVI), studied AHG@nZVI Studied the presence of NaCl in aqueous solutions of different concentrations. As the salt concentration increased from 0.1 mol L−1 to 0.5 mol L−1, the TC removal capacity (mg g−1) increased by 12.8% and 18%, respectively. The removal effect of NaCl on TC is significant. However, high ion concentration (1 mol L−1 NaCl) often reduces the removal ability of TC. At low chloride ion concentrations (0.1–0.5 mol L−1 NaCl), the coating on the surface of nZVI inhibits the formation of chloride complexes with iron oxide, thereby playing a positive role in the removal of TC. In contrast, at 1 mol L−1 NaCl, the concentration of competitive anions reached the competitive saturation point, leading to AHG@NZVI The adsorption capacity decreases.85 Research has found that cations K+, Ca2+, and Mg2+ all have inhibitory effects on the removal of TC,73 with the inhibition intensity in the order of Ca2+ > Mg2+ > K+. The reason may be that Ca2+and Mg2+ in aqueous solutions are more likely to hydrolyze to form precipitates in the form of hydroxides than Na+ and K+, leading to masking of reaction sites. When the concentration of Ca2+and Mg2+ increases to 10 mM, the inhibitory effect becomes more pronounced and the removal rate decreases significantly, which may be attributed to the easy reaction of Ca2+ and Mg2+ with iron hydroxide (oxygen). The removal effect of anions on TC varies, with SO42− having a weaker inhibitory effect and HCO3− having a more pronounced inhibitory effect. This may be because bicarbonate can act as a scavenger and inhibitor of hydroxyl radicals,88 producing OH− and inhibiting the production of ˙OH in the reaction system, thereby reducing reactivity.89
Fig. 7 Possible mechanism diagram of nZVI removal of tetracycline.92 |
Fig. 8 Schematic diagram of the possible reaction mechanism of nZVI for removing pollutants in redox reactions.94 |
According to the experiment 97,98 in the particle electrode loaded with nZVI mainly removes CIP from the system through adsorption, reduction, and ˙OH oxidation in a three-dimensional electrode reactor. Due to the attack of ˙OH, the C–F bond in CIP breaks, and the F on quinolones is replaced by ˙OH through a defluorination process to generate new compounds. The CC next to the carboxyl group on quinolones is destroyed due to hydroxylation, achieving the goal of degradation. Product analysis shows that the cleavage of ammonia, carbonyl, hydroxyl, and dimethylamino groups is the main pathway for TC conversion. Chemical reactions are induced by electron or atomic hydrogen (H*) species by oxidizing nZVI with H2O/H*.
Wang et al.99 found that Fenton oxidation (Fenton oxidation refers to the addition of hydrogen peroxide and iron ions), usually Fe2+, to the treated water to produce hydroxyl radicals (˙OH), which have strong oxidizing properties when oxidizing organic pollutants. Fenton oxidation can efficiently degrade organic compounds in organic wastewater and is one of the effective water treatment methods. The contribution of three reaction mechanisms, namely specific coordination and material adsorption, to the removal of OTC from materials. Fenton oxidation is the main mechanism for OTC removal. For the removal of OTC by specific coordination, it may be that after the addition of water absorbing gel coated nano zero valent iron (PPAA-nZVI), a certain amount of Fe3+ is dissolved in the material, and specific coordination occurs with OTC; Subsequently, the nZVI inside the material is oxidized, producing ˙OH, at which point Fenton oxidation begins to dominate; As the reaction time increases, the oxidation of Fenton begins to weaken, and at the same time, there is more Fe3+in the solution, enhancing the specific coordination effect.
Fe0 + O2 + 2H+ → 2[H] → Fe2+ + H2O | (4) |
Fe2+ + H2O2 → Fe3+ + OH− + ˙OH | (5) |
Due to flocculation, a certain amount of TC can be adsorbed. Wang et al.99 used PPAA-nZVI to remove OTC from water. The experimental analysis showed that there are three ways to remove OTC: firstly, the ˙OH generated by the Fenton system oxidizes and degrades OTC; the second is that Fe3+ in the solution chelates with OTC, resulting in specific coordination; The third is the adsorption of OTC by the surface active sites of the material. Sun et al.100 prepared a sulfurized nano zero valent iron loaded on blast furnace slag using liquid-phase reduction method (S-nZVI@BFS) Materials were used to remove oxytetracycline (OTC) from wastewater. The degradation mechanism shifts from Fendon oxidation and complexation precipitation to electrostatic adsorption.101 Discovered under acidic conditions S-nZVI@BFS The dissolved iron ions can undergo complexation precipitation reaction with oxytetracycline, generating insoluble products in water.
(1) Further research is needed to explore the effectiveness and mechanisms of joint pollutant remediation, as well as simultaneous and selective remediation of target pollutants. Currently, nZVI primarily focuses on single pollutant systems in antibiotic contamination remediation, with insufficient understanding of composite heavy metal or nitrate organic compound pollution systems.
(2) Clean preparation methods and novel modification techniques for nZVI are currently hot topics in experimental research. Improving its physical and chemical properties can address the issue of performance degradation due to spontaneous aggregation.
(3) Green preparation methods involving biological and microbial extraction of reducing agents will reduce residual toxicity after removing heavy metals from water, thereby minimizing secondary pollution. However, addressing the high cost associated with new preparation and modification methods remains a significant challenge for industrial applications, although it would facilitate broader adoption.
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