Next Article in Journal
Synthesis of New Dehydrodieugenol Derivatives via Olefin Cross Metathesis and In Vitro Evaluation of Their Trypanocidal Activity
Next Article in Special Issue
Customized High-Value Agricultural Residue Conversion: Applications in Wastewater Treatment
Previous Article in Journal
Iron-Doped Nickel Hydroxide Nanosheets as Efficient Electrocatalysts in Electrochemical Water Splitting
Previous Article in Special Issue
Sulfadiazine Elimination from Wastewater Effluents under Ozone-Based Catalysis Processes
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Review

Progress in the Preparation of Metal Oxide Electrodes for the Electrochemical Treatment of Organic Wastewater: A Short Review

1
Department of Environmental Science and Engineering, Xi’an Jiaotong University, Xi’an 710049, China
2
State Key Laboratory of Eco-Hydraulics in Northwest Arid Region, Xi’an University of Technology, Xi’an 710048, China
3
Research Institute of Xi’an Jiaotong University, Hangzhou 311200, China
*
Author to whom correspondence should be addressed.
These authors contributed equally to this work and should be considered co-first authors.
Catalysts 2023, 13(7), 1096; https://doi.org/10.3390/catal13071096
Submission received: 19 June 2023 / Revised: 11 July 2023 / Accepted: 11 July 2023 / Published: 13 July 2023

Abstract

:
The direct discharge of untreated organic wastewater poses significant threats to the environment and to human health. To address these threats, electrocatalytic oxidation technology has emerged as a key solution for organic wastewater treatment. Building on research conducted over the past three years, this review highlights the considerable advantages of electrocatalytic oxidation technology in the context of organic wastewater treatment, with a particular emphasis on the application of metal oxide electrodes. The review also provides a summary of the primary methods used in the preparation of such electrodes. Subsequently, the applications of both single-metal-oxide electrodes and metal oxide composite electrodes in organic wastewater treatment are summarized. Finally, we discuss the future development of metal oxide electrodes.

Graphical Abstract

1. Introduction

Organic wastewater comprises wastewater containing a large number of organic substances [1,2,3,4,5,6], typically including chemical wastewater (containing pigments, dyes, and adhesives, etc.) [7,8,9,10,11,12,13], agricultural wastewater (containing pesticides, herbicides, and other agrochemicals) [14,15,16], domestic sewage (containing excrement, detergents, food residue, etc.) [17,18,19,20,21,22] and pharmaceutical wastewater (containing drugs, antibacterial agents, and hormones) [23,24,25]. The substances in these wastewaters generally possess significant toxicity and the potential for bioaccumulation, posing both direct and indirect threats to the ecological environment. The impact they have on ecosystems and human health is substantial. Therefore, the treatment of organic wastewater is of paramount importance.
Currently, the common treatment technologies for organic wastewater include physical treatment technology, chemical treatment technology, biological treatment technology, and advanced oxidation technology. Physical treatment technology [26,27,28] usually does not involve chemical reactions or biological processes. The common physical treatment methods can be divided into two categories: the first category mainly comprises precipitation, filtration, and flotation, which are typically used as pretreatment steps. The second category mainly comprises membrane separation and depth filters, which are commonly employed in the advanced treatment stage. These methods boast several advantages, such as rapid treatment speeds and minimal impact on the natural environmental microbial community. However, these physical treatment technologies also come with limitations; they offer limited treatment effects, present unstable treatment efficiency, and may potentially generate new solid waste as a byproduct. Chemical treatment technology [29,30] uses chemical reactions to convert organic matter in wastewater into manageable substances. Common chemical treatment methods include chemical precipitation and chemical flocculation. In the field of organic wastewater treatment, chemical treatment technology is usually used as an auxiliary method in combination with other treatment technologies to achieve better treatment effects. Notably, this technology has several strengths, such as rapid treatment speeds and a strong applicability in handling hard-to-degrade organic substances, especially those with high molecular weights. However, there are notable drawbacks to consider. Its operation entails the consumption of large amounts of chemical reagents, which may lead to secondary pollution issues. Biological treatment technology [31,32,33] employs microorganisms to decompose organic substances in wastewater into inorganic substances. Common biological treatment methods include the biofilm method, the activated sludge method, and aerobic and anaerobic treatments. These methods have several advantages, such as effective treatment results, low operating costs, and stable long-term operation. Additionally, the type and quantity of the microbial community can be regulated to optimize the treatment process. However, these techniques also present some challenges. They require a longer processing times compared to chemical and physical methods. They are also sensitive to fluctuations in temperature and pH, and to antibiotics and heavy metals, which can inhibit the activity of the microorganisms and thereby reduce the efficiency of the treatment process. Advanced oxidation technology [34,35] is a subset of the broader category of chemical treatment technologies, which decompose organic substances in wastewater through various chemical reactions. This technology can utilize ozone, hydrogen peroxide, and other oxidants to degrade organic substances in wastewater. It can also employ photocatalytic and electrocatalytic oxidation methods to degrade organic substances in wastewater into simple inorganic compounds. The aforementioned wastewater treatment technologies have their own characteristics, and advanced oxidation technology, represented by electrocatalytic oxidation, has been widely applied commercially in the field of organic wastewater treatment due to its operational simplicity. Compared to other advanced oxidation processes, electrocatalytic oxidation has certain advantages. It does not necessitate the addition of extra chemicals, unlike processes such as Fenton oxidation, and it has already found extensive real-world applications in wastewater treatment. Meanwhile, several other advanced oxidation technologies, exemplified by photocatalysis, are predominantly in the experimental stage, although there are instances of field applications.
In the study of electrocatalytic oxidation technology, the selection and optimization of electrode materials are key factors. At present, the electrode materials used in the related academic research and engineering practice mainly include carbon-based (such as graphite and boron-doped diamond) electrodes, precious metal (such as platinum-based alloys) electrodes, and metal oxide (such as lead oxide and ruthenium-iridium oxide) electrodes. The basic principle of the electrocatalytic oxidation treatment of organic wastewater is to accelerate the oxidation and decomposition of the organic matter in wastewater via an electrochemical reaction. Unlike the famous technique of Fenton oxidation [36,37] (which depends on the action of H2O2 and iron ions), electrocatalytic oxidation does not require the addition of other oxidants, but uses a current to generate redox reaction active free radicals on the electrode’s surface [38,39,40], thus oxidizing organic compounds in wastewater. This not only prevents the residual problem of leaving potentially toxic oxidants, which is caused by some advanced oxidation technologies [41], but also saves the cost of purchasing oxidants when used in practical settings. A schematic diagram of the technical principles of using electrocatalytic oxidation for organic wastewater treatment is shown in Figure 1. The oxidation of organic pollutants mainly occurs in two ways: direct and indirect electrocatalytic oxidation. In direct electrocatalytic oxidation, organic matter is directly oxidized on the anode surface under oxidation potentials. This process transforms the organic matter into carbon dioxide, water, and other harmless substances, as depicted in Equation (1). On the other hand, indirect electrocatalytic oxidation involves the reaction of organic matter with active species, such as oxygen free radicals, hydrogen free radicals, and hydroxyl free radicals. These active species are produced on the anode surface, leading to the generation of products similar to those produced by direct electrocatalytic oxidation.
Figure 1. Schematic diagram of the equipment and related technical principles of electrocatalytic oxidation for organic wastewater treatment.
Figure 1. Schematic diagram of the equipment and related technical principles of electrocatalytic oxidation for organic wastewater treatment.
Catalysts 13 01096 g001
R + MO X · OH CO 2 + H + + e + MO X
R: organic pollutants. MOx: active sites on the anode surface.
Due to the differences in the structure and physical and chemical properties of different active electrode materials [42,43,44], the efficacy of these materials in the electrocatalytic oxidation of wastewater varies. In the process of electrochemical treatment, the selection of the active electrode must usually account for the following points: the surface of the active electrode needs to have excellent catalytic performance [45,46,47,48], which means that the surface of the electrode should have a large enough specific surface area to form a large number of active sites and promote the redox reaction. The active electrode should also exhibit high conductivity and chemical stability [49,50,51] to ensure that it can withstand high-intensity currents while not being corroded by the chemicals in the wastewater. The cost and ease of use of active electrode materials must be reasonable [52,53]. For example, single-metal electrodes usually have the advantage of low costs, but their lower catalytic activity and narrower range of applications limit their use. In addition, it is necessary to consider the corrosion effect of different types of wastewater on the electrode [54]. For acidic or chlorine-containing wastewater, it may be more appropriate to choose active electrode materials with strong corrosion resistance.
From the above summary, it is clear that the judicious selection of active electrodes is of paramount importance for enhancing the efficiency and cost-effectiveness of electrocatalytic oxidation for wastewater treatment. Electrodes can be divided into categories based on the presence or absence of metal elements. Some carbon-based electrodes, such as graphite electrodes, lack metal elements and possess inherent conductivity and lower manufacturing costs. However, the electrocatalytic activity of these carbon-based electrodes is considerably lower than that of their metal counterparts, resulting in higher power consumption [55,56]. Furthermore, these electrodes exhibit low mechanical strength and are vulnerable to physical damage and chemical erosion, leading to unstable sewage treatment outcomes and the need for frequent replacement. Considering the limitations of current fabrication technologies, despite their excellent catalytic performance and lifespan, boron-doped diamond (BDD) electrodes still have the disadvantages of complex preparation processes and high costs [57,58,59]. These drawbacks add to the challenges and long-term operating costs of using carbon-based electrodes. Regarding electrodes containing metal elements, corrosion-resistant noble metal electrodes are not widely used in sewage treatment due to their high costs. Conversely, the use of many metal-based electrodes may result in issues such as electrode corrosion and metal ion contamination [60], particularly in organic wastewater with a complex composition. In light of these challenges of using metal and carbon-based electrodes, titanium emerges as an appealing compromise. Although titanium surfaces are prone to forming dense oxide films with poor conductivity when serving as an anode [49,61], the inherent advantages of titanium in terms of its mechanical strength, electrical conductivity, and reasonable costs outweigh these drawbacks. As a result, titanium is frequently utilized as a substrate for modified electrodes, including metal oxide electrodes, in various practical applications.
Compared with the above types of electrodes, metal oxide electrodes have higher catalytic activity and electrochemical stability [62,63,64], which can improve the reaction rate of the electrode. They not only have a longer service life, but can also be applied in a wide range of pH values. The advantages of metal oxide electrodes include the higher number of defect sites on their surfaces, which serve as catalytic centers for more effective reaction facilitation. These electrodes possess a relatively complex structure, often comprising various metal oxides, and they typically display highly dispersed nanocrystalline grains among other forms, thereby providing a large surface area and improving the number of active sites for catalytic reactions. Additionally, most metal oxides exhibit excellent electrical conductivity and chemical stability, particularly oxidation resistance. This enhances the efficiency of electron transport and broadens the application range of the electrodes. In summary, metal oxide electrodes have the potential to be widely applied in the electrocatalytic oxidation treatment of organic wastewater, which can produce an ideal treatment effect and high stability and applicability. The main characteristics of metal oxide electrodes are compared with those of several other types of electrodes in Figure 2.
There are numerous types of metal oxide electrodes, but they can mainly be categorized into the following two groups: single-metal-oxide electrodes [65,66,67] (represented by lead oxide electrode), and metal oxide composite electrodes [68,69,70] (various types, such as RuO2-IrO2 electrodes and SnO2-Sb2O5 electrodes). These electrodes have been widely used in the treatment of organic wastewater. This work summarizes the types and hazards of organic wastewater, highlights the significant advantages of using metal oxide electrodes in the electrocatalytic oxidation treatment of organic wastewater, and introduces the primary preparation methods for metal oxide electrodes, as well as the application of single-metal-oxide and metal oxide composite electrodes in organic wastewater treatment. The information presented in this paper will be useful to researchers and practitioners working in the field of wastewater treatment.

2. Preparation of Metal Oxide Electrodes: Fundamentals, Challenges, and Progress

2.1. Fundamentals of Preparing Metal Oxide Electrode Materials

Based on the composition of the electrodes, metal oxide electrodes can be divided into two main types: pure metal oxide electrodes and surface-modified metal oxide electrodes. Pure metal oxide electrodes often possess high degrees of hardness and brittleness. However, surface-modified metal oxide electrodes can demonstrate varying properties, including differences in conductivity and the number of catalytic active sites, which are dependent on the specific metal oxide used and the applied modification technique. In certain applications, surface-modified metal oxide electrodes have attracted more attention due to the potentially superior characteristics they offer. These types of electrodes are also the main subject of the subsequent discussion. The preparation of metal oxide electrode materials typically involves the following elements. First, the selection of the preparation method, whereby the appropriate preparation method is selected based on the desired electrode morphology and application scenario. Second, the selection of raw materials: suitable metal ion sources and other additives (such as stabilizers, surfactants, etc.) are used. Third, the control of the reaction conditions, which involves regulating the characteristics of the prepared material through controlling the temperature, reaction time, and other parameters. Among these processes, the choice of preparation method has the greatest influence on the preparation of the metal oxide electrode, because it has a direct impact on the morphology, structure, and physical and chemical properties of the materials. The main methods for preparing metal oxide electrodes include: the thermal decomposition method [71,72,73]; the chemical vapor deposition (CVD) method [74,75,76]; the electrochemical deposition method [77,78]; the sol–gel method [79,80,81]; the hydrothermal method [82,83], and the physical vapor deposition method [84,85]. Figure 3 lists the basic processes and characteristics of these preparation methods. These include: (1) the thermal decomposition method. As shown in Figure 3a, when using this method, metal ions are dissolved in organic matter/other solutions, coated on the surface of a good conductor (substrate electrode), and decomposed by high temperatures to obtain metal oxide electrodes. The preparation method is simple and fast, but it also has some drawbacks, such as the need for high temperatures, high vacuum conditions, and organic residues. (2) The chemical deposition method. As shown in Figure 3b, the most typical method is chemical vapor deposition (CVD), where metal ions are reduced to metal atoms and deposited on the substrate electrode surface. These atoms are then oxidized to produce a metal oxide electrode. This preparation method can produce high-quality electrodes, has simple preparation conditions, and allows for good control. (3) The electrochemical deposition method. As shown in Figure 3c, the electrochemical deposition method electrolyzes metal ions in a solution, reduces them into metal atoms, and deposits them on the substrate electrode’s surface, finally obtaining a metal oxide electrode. This method has the advantages of simple preparation conditions, good control, and the ability to produce a uniform thin-film electrode. (4) The sol–gel method. As shown in Figure 3d, metal organic salt and a solvent are mixed to form a sol solution (with a catalyst added), and metal oxide materials are obtained through drying and calcination. This method can produce electrode materials with a large specific surface area, and the preparation process is relatively simple. However, some residual additives used in the process may affect the electrode’s performance. (5) The hydrothermal method. As shown in Figure 3e, by subjecting a mixture of the appropriate metal ion sources to high temperatures and pressures, a metal oxide electrode material is obtained after a period of time. The method makes it easy to control the shape and size of the product. However, this method has stringent requirements in terms of the equipment and operating conditions. (6) The physical vapor deposition (PVD) method. As shown in Figure 3f, utilizing physical vapor deposition technology, metals or metal oxides are evaporated and then deposited on the substrate electrode’s surface, forming a uniform oxide film. Metal oxide electrodes prepared using this physical deposition method exhibit high uniformity and controllable thickness. However, this method is associated with higher costs.

2.2. Challenges and Research Progress in the Preparation of Metal Oxide Electrodes

Despite its many advantages in practical applications, there are still some challenges in the preparation of metal oxide electrodes. One of the main issues is that some manufacturing processes, such as physical vapor deposition and chemical vapor deposition, require high standards for equipment and production environments, which may not be feasible for all research or industrial settings. Moreover, at the microscopic scale, effectively controlling the size, morphology, and distribution of metal oxide particles remains a persistent challenge, especially when scaling up to large-scale industrial electrodes. Although enhancing the specific surface area of the metal oxide layer benefits the progression of electrocatalytic oxidation reactions, it may also exacerbate the problems of layer shedding and corrosion in the oxide layer.
Electrochemical deposition is a relatively cost-effective method for electrode fabrication, which offers easy control over the reaction process. Guo and colleagues [86] managed to effectively control the surface morphology and structure of PbO2 electrodes by adjusting the power supply parameters, including the pulse frequency, duty ratio, average current density, and electrodeposition time. Using this approach, they successfully fabricated porous titanium-based PbO2 electrodes that possess a large number of active sites. By adjusting the elemental composition of the electrode surface, the grain size on the microscale and the actual electrochemical active area can be effectively controlled. Wang et al. [87] fabricated PbO2 electrodes doped with various rare earth elements using the electrochemical deposition method, which significantly improved the degradation effect of the metal oxide electrodes on p-nitrophenol; the pseudo-first-order kinetic constant increased from 0.19 to 0.41.
Titanium-based metal oxide electrode deposition technology currently faces challenges such as poor coating quality, a weak bonding ability between the coating and substrate, insufficient research on electrodeposition kinetics theory, and limited industrial applications. In response, Wu et al. [88] systematically studied iridium oxide electrodeposition preparation technology, covering the formulation of the deposition solution, substrate selection and treatment, the electrodeposition method, and the deposition time. They proposed several strategies for tackling the issue of coating quality, including optimizing the electrodeposition, combining multi-deposition processes, and co-deposition with metals such as tantalum and lanthanum. In related research, Zhou et al. [89] compared common preparation methods for lead dioxide and examined the electrochemical oxidation performance of lead dioxide in wastewater containing various contaminants. Their work provided a comprehensive reference for operating conditions and offered valuable insights for researchers in the field. Meanwhile, Guo et al. [49] addressed the key points and difficulties in the preparation of titanium sub-oxide electrodes. They suggested future research directions including process optimization, material modification, and application expansion.
Overall, studying the optimization methods and theory of metal oxide electrode preparation technology is of significant value for improving wastewater treatment efficiency and developing more advanced materials.

3. Single-Metal-Oxide Electrodes: Applications and Enhancements in Organic Wastewater Treatment

3.1. Application in Organic Wastewater Treatment

Metal oxide electrodes are crucial electrocatalytic materials that exhibit good chemical stability, electrochemical activity, and photocatalytic performance. Single-metal-oxide electrodes are those composed of a single type of metal oxide, such as lead oxide, copper oxide, and titanium sub-oxides. Each of these electrodes plays a different role in the treatment of organic wastewater. Table 1 presents several typical single-metal-oxide electrodes, along with their advantages and drawbacks. The lead oxide electrode, with its excellent performance, simple preparation process, and strong electrocatalytic oxidation abilities, is highly favored for organic wastewater treatment in the current industrial applications.

3.2. Optimization Strategy Based on Adding Intermediate Layers

Our previous research [86,101,102] confirmed that metal oxide electrodes, represented by lead oxide electrodes, possess strong cost-effectiveness advantages, and exhibit impressive performance in treating various types of organic wastewater. However, there are potential risks associated with the dissolution of toxic lead elements into the solution as lead ions, which potentially reduce the lifespan of the electrode and lead to secondary pollution.
The electrochemically active modified layer on the surface of a single-metal-oxide electrode is less stable and may release heavy metal ions into the water. Adding an intermediate layer between the surface-active layer and the substrate can effectively improve the electrode’s stability and can also potentially enhance the electrocatalytic performance. As shown in Figure 4a,b, Man et al. [92] first employed electrophoretic deposition to prepare a highly conductive MXene material as an intermediate layer for the fabrication of a novel PbO2 electrode. The electrochemical performance of the PbO2 electrode was significantly improved by the Ti3C2Tx interlayer. The charge-transfer resistance was reduced by nearly 90%, the internal active site increased by 5.21 times, and the ability to generate ·OH radicals increased by 4.07 times compared to the control anode. The new electrode could achieve the almost complete degradation of basic fuchsin within three hours. Similarly, Dai et al. [93] prepared a novel PbO2 electrode (GNP-PbO2) by adding graphene nanosheets (GNP) as an intermediate layer to the β-PbO2 active layer and used it to degrade the antibiotic enrofloxacin (ENO); Figure 4c shows the electrochemical treatment reactor. The GNP intermediate layer increased the oxygen evolution potential of the PbO2 electrode (2.05 V vs. SCE), which was conducive to inhibiting oxygen precipitation and promoting the production of ·OH, indicating that GNP-PbO2 is a promising material for the treatment of organic wastewater. The lifespan of such active electrodes is often limited, especially when dealing with wastewater with complex compositions (for example, some electroplating wastewater contains a lot of organic matter and heavy metal ions). As shown in Figure 4d, Rong et al. [103] prepared a bismuth-doped lead oxide (PbO2-Bi) electrode for the degradation of organic wastewater using the electrodeposition method; they demonstrated that the new structure of the electrode lasted 2.5 times longer than an ordinary PbO2 electrode.
The aforementioned studies demonstrated that the introduction of an intermediate layer between the electrode substrate and the active surface layer, or the doping of a single metal oxide, can markedly enhance the stability and longevity of the electrode, which is also always accompanied by an improvement in the catalytic oxidation performance of the electrode material. The above methods can improve the electrochemical performance of the electrode by increasing the number of internal active sites, improving its capacity to generate free radicals, and reducing its charge-transfer resistance.
However, when dealing with organic wastewater with a complex composition (especially electroplating wastewater, which contains a great deal of organic matter and heavy metal ions), involving factors such as chemical corrosion, electrochemical corrosion, and the destruction of the original crystal structure, the lifespan of single-metal-oxide electrodes tends to be limited, and the efficiency of the wastewater treatment can also be relatively low.

4. Metal Oxide Composite Electrodes: Relative Advantages and Progress in Electrochemical Wastewater Treatment

4.1. Relative Advantages

Although single-metal-oxide electrodes have certain advantages in terms of catalytic performance, compared with single-metal-oxide electrodes, metal oxide composite electrodes exhibit the following advantages in the electrochemical treatment of organic wastewater. First, they have better catalytic activity potential. Metal oxide composite electrodes are superimposed with different kinds or forms of metal oxides. This interaction can lead to the enhancement of catalytic activity, which significantly improves the efficiency of the wastewater treatment. They also exhibit better corrosion resistance; based on a specific composition of multiple metal oxides, the corrosion resistance of electrode materials can be improved by appropriate design choices, which allow them to function for longer in acid-based environments. Additionally, they have lower use costs; metal oxide composite electrodes exhibit higher catalytic activity and more lasting stability, which can reduce the frequency of electrode replacement and regeneration, thus reducing the use cost. Therefore, compared with single-metal-oxide electrodes, metal oxide composite electrodes have better catalytic activity, better corrosion resistance, a wide application range, and strong stability in the electrochemical treatment of organic wastewater with complex compositions. Like single-metal-oxide electrodes, metal oxide composites are often loaded on a substrate with excellent electrical conductivity and mechanical strength (such as a Ti electrode) rather than used alone; this not only makes the electrode more stable and reduces its likelihood of fracturing or succumbing to fatigue and other phenomena, but also effectively reduces the electrode production cost.
At present, the main metal oxide composite electrodes are as follows: the Ti/SnO2-Sb2O5 electrode, the Ti/RuO2-IrO2 electrode, the Ti/PbO2-SnO2 electrode, the Ti/IrO2-TiO2 electrode, the Ti/SnO2-TiO2 electrode, etc. Their advantages and drawbacks are shown in Table 2. It can be seen that, compared with single-metal-oxide electrodes (such as PbO2 electrodes), metal oxide composite electrodes generally have the following advantages: (1) high electrochemical activity. These electrodes possess exceptional reactivity on their surfaces, enabling them to catalyze reactions at low potentials. (2) High electrochemical stability: this kind of electrode material generally has good corrosion resistance, allowing for stable operation in a variety of corrosive media, including acidic and alkaline media, fluorine-containing compounds, and chlorides. (3) A long service life. Due to their ability to withstand higher current densities and their superior chemical stability, these types of electrodes can often be used for extended periods without requiring replacement.

4.2. Progress in the Design of Metal Oxide Composite Electrodes

The combination of various types of metal oxides can effectively improve the electrocatalytic activity of the electrode. As shown in Figure 5a, Sun et al. [112] prepared a CuO-SnO2-SbOx electrode with Ti as the base. The experimental results show that the prepared composite electrode exhibits high catalytic degradation activity and an oxygen evolution potential that is 0.4 V higher than that of the widely used Ti/SnO2-SbOx electrode. The complete mineralization of toxic p-nitrophenol can be achieved within four hours. Man et al. [113] used a hydrothermal method to add a three-dimensional Sb-doped SnO2 nanoflower intermediate layer onto a Ti substrate; the corresponding preparation process is shown in Figure 5b. The electrode, which has a three-dimensional structure, exhibits excellent electrical conductivity. Moreover, the preparation method employed in this study avoids environmental pollution and the short electrode lifespan associated with traditional thermal decomposition methods. This was demonstrated through an accelerated lifetime test. Compared with traditional PbO2 anodes, the novel electrode material has a tighter electrode surface with a high specific surface area, and it can effectively degrade three typical organic compounds: methylene blue (MB), norfloxacin (NOR), and p-dihydroxybenzene (p-DHB). In addition, the stability and safety of the anode are improved by this three-dimensional interlayer, and its life is extended by 2.70 times. This study provides a useful method for preparing PbO2 anodes with high catalytic activity and good stability for wastewater treatment. The number of active sites on the surface of the electrodes is crucial for the electrocatalytic oxidation efficiency, while methods to enhance the electrochemical activity of metal oxide electrodes are not limited to modifications of the electrodes themselves. Shao et al. [91] constructed a magnetic assembly electrode (MAE) system based on magnetic carbon nanotubes (CNTs) on the surface of metal oxide electrodes, as shown in Figure 5c. This method effectively increased the number of active sites and improved the efficiency of the organic wastewater treatment. Through systematic research, Shao et al. filled the gaps in the understanding of the mechanism of MAE. The use of MAE to increase the number of active sites on the electrode surface was also validated by Zhang [114] et al.
Metal oxide composite electrodes are composed of a variety of metal oxides. First, metal oxide composite electrodes have high catalytic activity because they have abundant electronic states and surface-active sites, which can adsorb and activate reactive substances to improve the reaction rate and efficiency. Additionally, the catalytic performance of the metal oxide composite electrode can be optimized and upgraded by adjusting its material structure and composition to meet the needs of different reactions. Moreover, the metal oxide composite electrode can be effectively compensated and stabilized by its compatibility with the substrate material, thus improving its reliability and lifespan in long-term operations. In summary, metal oxide composite electrodes are excellent materials with good catalytic activity, electrode stability, and corrosion resistance. They have a wide range of application prospects in the field of the electrocatalytic oxidation of organic wastewater.

5. Summary and Prospects

5.1. Summary

This paper systematically explored the detrimental impacts of organic wastewater and presented an overview of the main wastewater treatment technologies that are currently in use. Special emphasis was placed on the application of electrocatalytic oxidation technology in this domain, with a particular focus on the benefits associated with the use of metal oxide electrodes. The main methods for preparing metal oxide electrodes were explained in detail, including physical, chemical, and electrochemical approaches. Additionally, the primary classifications and characteristics of single-metal-oxide electrodes and metal oxide composite electrodes were introduced, along with the related research and their applications in the field of organic wastewater treatment. From a comprehensive review of the literature, it can be observed that the traditional preparation process for single-metal-oxide electrodes is relatively simple. However, it tends to be constrained by factors such as catalytic activity and the electrode’s lifespan. Current research on this type of electrode is primarily evolving towards the use of composite materials. The preparation process for metal oxide composite electrodes, while more complex compared to that for traditional single-metal-oxide electrodes, often results in higher catalytic activity and relatively low usage costs. Based on the descriptions provided in this paper, it can be concluded that metal oxide electrodes have broad application potential in the electrocatalytic oxidation treatment of organic wastewater. However, it is still necessary to further strengthen research in areas such as electrode manufacturing costs, catalytic degradation efficiency, and electrodes’ service life. It is essential to fit the appropriate electrode and degradation program to the actual situation, in order to effectively improve the treatment efficiency and quality of organic wastewater.

5.2. Prospects

5.2.1. Challenges and Potential Solutions in Using Electrocatalytic Oxidation Technology for Organic Wastewater Treatment

Compared with traditional wastewater treatment methods, electrocatalytic oxidation technology has advantages including high removal efficiency, short treatment times, simple operations, and no need for the addition of chemical agents, thus avoiding secondary pollution. Therefore, electrocatalytic oxidation technology has a wide range of potential applications in organic wastewater treatment. However, the electrocatalytic oxidation system centered around metal oxide electrodes still presents numerous challenges, primarily in the following areas. First, cost-effectiveness is still lacking; high power consumption in electrocatalytic oxidation treatment leads to elevated costs when treating organic wastewater using this method. Second, its catalytic capabilities are insufficient. The application scope of the catalytic oxidation method is limited; it can only treat organic wastewater of a certain concentration, making it challenging to handle large volumes of high-concentration wastewater. Third, the material stability needs improvement; the presence of excessive impurities in the wastewater can easily lead to electrode failure, necessitating the frequent cleaning and replacement of the electrodes. Fourth, safety issues; due to the inherent properties of the materials, traditional titanium-based metal oxide electrodes display a phenomenon of surface metal element dissolution during usage. This phenomenon persists throughout the electrode’s lifecycle, causing varying degrees of heavy metal secondary pollution risks. Intermediate products are compounds formed during the degradation process before complete mineralization (i.e., the conversion to CO2 and H2O) occurs. Depending on the nature of the pollutants being treated and the specific conditions of the electrochemical process, these intermediates can sometimes be more toxic or harmful than the original pollutants, which may pose safety concerns.
In view of the shortcomings of electrocatalytic oxidation technology in organic wastewater treatment, the following solutions may be adopted in the future. The development of new power generation technology is anticipated: electrocatalytic oxidation technology consumes a large amount of electric energy and has high costs, and it is possible to develop cheaper power generation technology in the future, which will directly reduce the use cost of electrocatalytic oxidation technology. Additionally, we should consider the integration of various wastewater treatment technologies; electrocatalytic oxidation technology can be combined with other wastewater treatment technologies, such as biodegradation, membrane separation, etc., to form a more efficient and comprehensive wastewater treatment program. Furthermore, the electrode materials and structure can be optimized. The electrodes used in the existing electrocatalytic oxidation technology are often prone to deactivation. In the future, new materials or structures may be used to manufacture electrodes to improve the stability and efficiency of the electrocatalytic oxidation reaction. In order to mitigate or prevent the formation of harmful intermediates in the electrochemical catalytic oxidation process of wastewater treatment, the following strategies can be adopted: the optimization of process conditions, the real-time monitoring of toxic substances, new post-treatment steps for toxic by-products, the development and use of more advanced electrode materials, etc.
Metal oxide electrodes have been widely used as active electrodes in the electrocatalytic oxidation treatment of organic wastewater due to their excellent properties. However, these materials also have some drawbacks, including high preparation costs; the cost of preparing metal oxide electrodes is high, resulting in a relatively high application cost. They are also susceptible to surface contamination: metal oxide electrodes often need to have full contact with sewage/organic molecules to exhibit their electrocatalytic oxidation capabilities, but the surfaces of these electrodes easily absorb pollutants, which may affect the electrocatalytic oxidation process and result in reduced efficiency for organic wastewater treatment. Moreover, the electrochemical active layer is prone to detachment and damage: external forces or chemical actions, among other factors, can cause the electrode’s surface to peel, become damaged, or fail. Such detachment or damage directly affects the performance and service life of the electrode.
To address the shortcomings of metal oxide electrodes, the following methods can be adopted: reducing the cost of electrodes by developing low-cost and easy-to-prepare metal oxide composite electrode materials to replace existing high-value metal oxides. Additionally, the cost of preparation can be reduced by improving the preparation technology and optimizing the production workflow. Electrode maintenance technology can also be optimized. Chemical or physical methods can be used to treat the electrode surface, such as surface oxidation treatment and high-temperature calcination, to reduce or eliminate surface contamination and improve electrochemical catalytic efficiency. Contaminants deposited on the electrode surface can also be removed by reversing the electrode (switching the polarity of the two electrodes). Additionally, electrode lifespans can be improved; the stability and durability of the electrode can be enhanced by improving the electrode structure and strengthening the bond between the electrochemically active layer and the electrode base (such as by introducing an intermediate layer). In conclusion, effectively overcoming the shortcomings of metal oxide electrodes and improving the performance and application value of electrocatalytic oxidation for organic wastewater treatment can be achieved by optimizing the material preparation processes, surface treatment methods, and electrode structure design.

5.2.2. The Possibility of Undertaking Electrocatalytic Oxidation Using Renewable Energy

Carbon peak and carbon neutrality are both important strategic goals in addressing global climate change. Electrocatalytic oxidation technology requires electrical energy to operate. If this electricity comes from coal-fired or other fossil-fuel-fired power plants, significant carbon emissions are generated in the process of treating the wastewater. However, if this electrical energy comes from renewable sources, such as solar or wind power, then electrocatalytic oxidation technology will have significantly lower carbon emissions during operation. Therefore, by changing the power source, electrocatalytic oxidation technology can have an impact on carbon peaking and carbon neutralization.
Electrocatalytic oxidation technology can effectively treat organic wastewater and convert organic matter into harmless substances such as water and carbon dioxide. Although the process produces carbon dioxide, electrocatalytic oxidation produces far less carbon dioxide than other treatment methods, such as incineration. In addition, if high-efficiency electrocatalytic oxidation technology is adopted, when the same amount of organic wastewater is treated, the amounts of electrical energy required and carbon dioxide generated will also be reduced, which is conducive to carbon peaking and carbon neutrality.

Author Contributions

Conceptualization, X.J. and X.W.; methodology, X.J. and X.W.; software, X.J.; validation, X.W. and H.X. formal analysis, X.L.; investigation, D.W.; resources, H.X. and W.Y. data curation, X.J. and X.W.; writing—original draft preparation, X.J. and X.W.; writing—review and editing, X.W. and H.X.; visualization, X.J. and X.W.; supervision, H.X. and W.Y.; project administration, H.X. and W.Y.; funding acquisition, H.X., X.L. and D.W. All authors have read and agreed to the published version of the manuscript.

Funding

This research is supported by the National Natural Science Foundation of China (52270078), Open Research Fund Program of State Key Laboratory of Eco-hydraulics in Northwest Arid Region, Xi’an University of Technology, (Grant No. 2021KFKT-7) and the Wel-fare Technology Research Plan of Zhejiang Province (LZY21E080003).

Data Availability Statement

This work is a review article, it does not include any direct data obtained from laboratory experiments conducted by the authors.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. He, C.; Zhong, H.; Zhang, Y.; Li, Y.; Chung, K.H.; Fang, L.; Zhang, W.; Wu, B.; Xu, C.; Shi, Q. Organic matter in delayed coking wastewater: Molecular composition and its effect on emulsification. Fuel 2020, 279, 118432. [Google Scholar] [CrossRef]
  2. Fukami, K.; Oogi, T.; Motomura, K.; Morita, T.; Sakamoto, M.; Hata, T. Effective Purification of Eutrophic Wastewater from the Beverage Industry by Microbubbles. Water 2021, 13, 3661. [Google Scholar] [CrossRef]
  3. Ishak, S.A.; Murshed, M.F.; Md Akil, H.; Ismail, N.; Md Rasib, S.Z.; Al-Gheethi, A.A.S. The Application of Modified Natural Polymers in Toxicant Dye Compounds Wastewater: A Review. Water 2020, 12, 2032. [Google Scholar] [CrossRef]
  4. Umair Hassan, M.; Aamer, M.; Umer Chattha, M.; Tang, H.; Khan, I.; Seleiman, M.F.; Rasheed, A.; Nawaz, M.; Rehman, A.; Talha Aslam, M.; et al. Sugarcane Distillery Spent Wash (DSW) as a Bio-Nutrient Supplement: A Win-Win Option for Sustainable Crop Production. Agronomy 2021, 11, 183. [Google Scholar] [CrossRef]
  5. Hua, T.; Wang, H.; Li, F. Degradation of TBBP-A wastewater by the process of electro-activated sodium persulfate. Environ. Pollut. Control 2020, 42, 539–542. [Google Scholar]
  6. Wang, B.; Xiong, M.; Wang, P.; Shi, B. Chemical characterization in hydraulic fracturing flowback and produced water (HF-FPW) of shale gas in Sichuan of China. Environ. Sci. Pollut. Res. 2020, 27, 26532–26542. [Google Scholar] [CrossRef]
  7. Pasmionka, I.B.; Gospodarek, J. Assessment of the Impact of Selected Industrial Wastewater on the Nitrification Process in Short-Term Tests. Int. J. Environ. Res. Public Health 2022, 19, 3014. [Google Scholar] [CrossRef]
  8. Park, J.W.; Kim, S.Y.; Noh, J.H.; Bae, Y.H.; Lee, J.W.; Maeng, S.K. A shift from chemical oxygen demand to total organic carbon for stringent industrial wastewater regulations: Utilization of organic matter characteristics. J. Environ. Manag. 2022, 305, 114412. [Google Scholar] [CrossRef]
  9. Meng, S.; Wen, S.; Han, G.; Wang, X.; Feng, Q. Wastewater Treatment in Mineral Processing of Non-Ferrous Metal Resources: A Review. Water 2022, 14, 726. [Google Scholar] [CrossRef]
  10. Anisuzzaman, S.M.; Joseph, C.G.; Pang, C.K.; Affandi, N.A.; Maruja, S.N.; Vijayan, V. Current Trends in the Utilization of Photolysis and Photocatalysis Treatment Processes for the Remediation of Dye Wastewater: A Short Review. ChemEngineering 2022, 6, 58. [Google Scholar] [CrossRef]
  11. Zeng, W.; Wang, H.; Yan, M.; Jiang, N.; Liu, Y.; Li, Y.; Huang, M. Resources Recycle of Printing and Dyeing Wastewater: UF/FO Hybrid System Optimization and TPA Recovery. ACS EST Water 2022. [Google Scholar] [CrossRef]
  12. Zhang, S.; Ren, H.; Fu, K.; Cheng, W.; Wu, D.; Luo, C.; Jiang, S.; Li, J.; Zhang, M. Preparation of Mn/Mg/Ce Ternary Ozone Catalyst and Its Mechanism for the Degradation of Printing and Dyeing Wastewater. Front. Energy Res. 2022, 9, 815633. [Google Scholar] [CrossRef]
  13. Zhou, J.; Geng, C.; Zhao, A. Pilot-scale experimental study on advanced treatment of printing and dyeing wastewater by catalytic ozonation. Water & Wastewater Engineering 2022, 48, 75–80. [Google Scholar]
  14. Masoner, J.R.; Kolpin, D.W.; Cozzarelli, I.M.; Bradley, P.M.; Arnall, B.B.; Forshay, K.J.; Gray, J.L.; Groves, J.F.; Hladik, M.L.; Hubbard, L.E.; et al. Contaminant Exposure and Transport from Three Potential Reuse Waters within a Single Watershed. Environ. Sci. Technol. 2023, 57, 1353–1365. [Google Scholar] [CrossRef]
  15. Abou-tammame, D.; Zouhri, A.; Boutarfa, A.; Fathi, J.; Aboutayeb, R. The Effect of Purified Wastewater on the Physicochemical Properties of Agricultural Soils in Chaouia in Morocco. J. Ecol. Eng. 2022, 23, 34–42. [Google Scholar] [CrossRef]
  16. Akinnawo, S.O.; Ayadi, P.O.; Oluwalope, M.T. Chemical coagulation and biological techniques for wastewater treatment. Ovidius Univ. Ann. Chem. 2023, 34, 14–21. [Google Scholar] [CrossRef]
  17. Lan, J.; Liu, L.; Wang, X.; Wu, X.; Wang, Z. DOM tracking and prediction of rural domestic sewage with UV-vis and EEM in the Yangtze River Delta, China. Environ. Sci. Pollut. Res. 2022, 29, 74579–74590. [Google Scholar] [CrossRef]
  18. Zhang, X.; Kim, D.; Karanfil, T. Effect of activated sludge treatment on the formation of N-nitrosamines under different chloramination conditions. J. Environ. Sci. 2022, 117, 242–252. [Google Scholar] [CrossRef]
  19. Chen, Q.; Wu, W.; Guo, Y.; Li, J.; Wei, F. Environmental impact, treatment technology and monitoring system of ship domestic sewage: A review. Sci. Total Environ. 2022, 811, 151410. [Google Scholar] [CrossRef]
  20. Sui, Y.; Al-Huqail, A.A.; Suhatril, M.; Abed, A.M.; Zhao, Y.; Assilzadeh, H.; Khadimallah, M.A.; Ali, H.E. Hydrogen energy of mining waste waters: Extraction and analysis of solving issues. Fuel 2023, 331, 125685. [Google Scholar] [CrossRef]
  21. Grgas, D.; Stefanac, T.; Baresic, M.; Toromanovic, M.; Ibrahimpasic, J.; Pavicic, T.V.; Habuda-Stanic, M.; Herceg, Z.; Dragicevic, T.L. Co-composting of Sewage Sludge, Green Waste, and Food Waste. J. Sustain. Dev. Energy 2023, 11, 1100415. [Google Scholar] [CrossRef]
  22. Ng, M.; Dalhatou, S.; Wilson, J.; Kamdem, B.P.; Temitope, M.B.; Paumo, H.K.; Djelal, H.; Assadi, A.A.; Phuong, N.-T.; Kane, A. Characterization of Slaughterhouse Wastewater and Development of Treatment Techniques: A Review. Processes 2022, 10, 1300. [Google Scholar] [CrossRef]
  23. Balu, S.; Chuaicham, C.; Balakumar, V.; Rajendran, S.; Sasaki, K.; Sekar, K.; Maruthapillai, A. Recent development on core-shell photo(electro)catalysts for elimination of organic compounds from pharmaceutical wastewater. Chemosphere 2022, 298, 134311. [Google Scholar] [CrossRef]
  24. Quang, H.H.P.; Nguyen, T.P.; Nguyen, D.D.D.; Bao, L.T.N.; Nguyen, D.C.; Nguyen, V.-H. Advanced electro-Fenton degradation of a mixture of pharmaceutical and steel industrial wastewater by pallet-activated-carbon using three-dimensional electrode reactor. Chemosphere 2022, 297, 134074. [Google Scholar] [CrossRef]
  25. Liu, J.; Wang, J.; Chen, C.; Chen, Y.; Zheng, X. Preparing coal slurry from organic wastewater to achieve resource utilization: Slurrying performance and dispersant suitability. Fuel 2023, 339, 126970. [Google Scholar] [CrossRef]
  26. Abdollahi, N.; Moussavi, G.; Giannakis, S. A review of heavy metals’ removal from aqueous matrices by Metal-Organic Frameworks (MOFs): State-of-the art and recent advances. J. Environ. Chem. Eng. 2022, 10, 107394. [Google Scholar] [CrossRef]
  27. Naghdi, S.; Shahrestani, M.M.; Zendehbad, M.; Djahaniani, H.; Kazemian, H.; Eder, D. Recent advances in application of metal-organic frameworks (MOFs) as adsorbent and catalyst in removal of persistent organic pollutants (POPs). J. Hazard. Mater. 2023, 442, 130127. [Google Scholar] [CrossRef]
  28. Lin, S.H.; Kiang, C.D. Combined physical, chemical and biological treatments of wastewater containing organics from a semiconductor plant. J. Hazard. Mater. 2003, 97, 159–171. [Google Scholar] [CrossRef]
  29. Türk, O.K.; Zoungrana, A.; Çakmakci, M. Chemical precipitation and membrane distillation process for the treatment of acidic anodic oxidation wastewaters. J. Environ. Chem. Eng. 2022, 10, 108036. [Google Scholar] [CrossRef]
  30. Li, M.; Liu, L.; Sun, Z.; Hu, B.; Li, X.; Lan, M.; Guo, H.; Li, B. Mainstream wastewater treatment by polyaluminium ferric chloride (PAFC) flocculation and nitritation-denitritation membrane aerated biofilm reactor (MABR). J. Water Process. Eng. 2023, 52, 103563. [Google Scholar] [CrossRef]
  31. Wang, S.; Hu, C.; Cheng, F.; Lu, X. Performance of a combined low-consumption biotreatment system with cost-effective ecological treatment technology for rural domestic sewage treatment. J. Water Process. Eng. 2023, 51, 103380. [Google Scholar] [CrossRef]
  32. Wang, T.; Wang, W.; Hu, H.; Khu, S.-T. Novel Quantitative Evaluation of Biotreatment Suitability of Wastewater. Water 2022, 14, 1038. [Google Scholar] [CrossRef]
  33. Jiang, P.; Zhou, T.; Bai, J.; Zhang, Y.; Li, J.; Zhou, C.; Zhou, B. Nitrogen-containing wastewater fuel cells for total nitrogen removal and energy recovery based on Cl•/ClO• oxidation of ammonia nitrogen. Water Res. 2023, 235, 119914. [Google Scholar] [CrossRef]
  34. Manna, M.; Sen, S. Advanced oxidation process: A sustainable technology for treating refractory organic compounds present in industrial wastewater. Environ. Sci. Pollut. Res. 2013, 30, 25477–25505. [Google Scholar] [CrossRef]
  35. Gao, Y.; Gao, W.; Zhu, H.; Chen, H.; Yan, S.; Zhao, M.; Sun, H.; Zhang, J.; Zhang, S. A Review on N-Doped Biochar for Oxidative Degradation of Organic Contaminants in Wastewater by Persulfate Activation. Int. J. Environ. Res. Public Health 2022, 19, 14805. [Google Scholar] [CrossRef]
  36. Guo, C.; Zhang, J.; Yu, P.; Wu, Y. Study on degradation effect of pretreatment to cephalosporin pharmaceutical wastewater and removal of organic matter. Ind. Water Treat. 2022, 42, 89–95. [Google Scholar]
  37. Lin, R.; Li, Y.; Yong, T.; Cao, W.; Wu, J.; Shen, Y. Synergistic effects of oxidation, coagulation and adsorption in the integrated fenton-based process for wastewater treatment: A review. J. Environ. Manag. 2022, 306, 114460. [Google Scholar] [CrossRef]
  38. Dong, H.; Su, H.; Chen, Z.; Yu, H.; Yu, H. Fabrication of Electrochemically Reduced Graphene Oxide Modified Gas Diffusion Electrode for In-situ Electrochemical Advanced Oxidation Process under Mild Conditions. Electrochim. Acta 2016, 222, 1501–1509. [Google Scholar] [CrossRef]
  39. Zhou, S.; Zhu, J.; Wang, Z.; Yang, Z.; Yang, W.; Yin, Z. Defective MOFs-based electrocatalytic self-cleaning membrane for wastewater reclamation: Enhanced antibiotics removal, membrane fouling control and mechanisms. Water Res. 2022, 220, 118635. [Google Scholar] [CrossRef]
  40. Cardozo, J.C.; da Silva, D.R.; Martínez-Huitle, C.A.; Quiroz, M.A.; Vieira dos Santos, E. The versatile behavior of diamond electrodes—Electrochemical examination of the anti-psychotic drug olanzapine (OL) oxidation as a model organic aqueous solution. Electrochim. Acta 2022, 411, 140063. [Google Scholar] [CrossRef]
  41. Ahmed, M.M.; Chiron, S. Solar photo-Fenton like using persulphate for carbamazepine removal from domestic wastewater. Water Res. 2014, 48, 229–236. [Google Scholar] [CrossRef]
  42. Zhu, J.; Cao, G.; Zhou, Y.; Li, Y.; Zheng, J.; Zhang, D. Influence of the Synthesis Route on the Properties of Hybrid NiO-MnCo2O4-Ni6MnO8 Anode Materials and their Electrochemical Performances. ChemSusChem 2020, 13, 1890–1899. [Google Scholar] [CrossRef]
  43. Qiao, S.; Huang, N.; Zhang, Y.; Zhang, J.; Gao, Z.; Zhou, S. One-step synthesis of nanoblocks@nanoballs NiMnO3/Ni6MnO8 nanocomposites as electrode material for supercapacitors. Int. J. Hydrogen Energy 2019, 44, 18351–18359. [Google Scholar] [CrossRef]
  44. Bernaecker, C.I.; Rauscher, T.; Buettner, T.; Kieback, B.; Roentzsch, L. Powder Metallurgy Route to Produce Raney-Nickel Electrodes for Alkaline Water Electrolysis. J. Electrochem. Soc. 2019, 166, F357–F363. [Google Scholar] [CrossRef]
  45. Duran, S.; Elmaalouf, M.; Odziomek, M.; Piquemal, J.-Y.; Faustini, M.; Giraud, M.; Peron, J.; Tard, C. Electrochemical Active Surface Area Determination of Iridium-Based Mixed Oxides by Mercury Underpotential Deposition. ChemElectroChem 2021, 8, 3519–3524. [Google Scholar] [CrossRef]
  46. Zhou, C.; Zhang, F.; Wu, H. Boosting pH-Universal Hydrogen Evolution of FeP/CC by Anchoring Trace Platinum. Crystals 2022, 12, 37. [Google Scholar] [CrossRef]
  47. Huang, H.; Shen, B.; Yan, M.; He, H.; Yang, L.; Jiang, Q.; Ying, G. Coupled spinel manganese-cobalt oxide and MXene electrocatalysts towards efficient hydrogen evolution reaction. Fuel 2022, 328, 125234. [Google Scholar] [CrossRef]
  48. Wen, Y.; Xu, S.; Wang, P.; Shao, X.; Sun, X.; Hu, J.; Shi, X.-R. Bimetallic FeCo phosphide nanoparticles anchored on N-doped carbon foam for wide pH hydrogen evolution reaction. J. Alloys Compd. 2023, 931, 167570. [Google Scholar] [CrossRef]
  49. Guo, S.; Xu, Z.; Hu, W.; Yang, D.; Wang, X.; Xu, H.; Xu, X.; Long, Z.; Yan, W. Progress in Preparation and Application of Titanium Sub-Oxides Electrode in Electrocatalytic Degradation for Wastewater Treatment. Catalysts 2022, 12, 618. [Google Scholar] [CrossRef]
  50. Chen, J.; Zhang, B.; Wang, B.; Zhang, W.; Wang, J.; Cui, C.; Wang, S. Heterogeneous electro-Fenton using three-dimension Fe-Co-Bi/kaolin particle electrodes for degradation of quinoline in wastewater. Environ. Sci. Pollut. Res. 2013, 30, 1399–1412. [Google Scholar] [CrossRef]
  51. Yang, Z.; Liu, Y.; Yang, H.; Hu, C.; Li, H.; Jing, H. Preparation of titanium suboxide electrode and its application in wastewater treatment. Ind. Water Treat. 2022, 42, 56–64. [Google Scholar]
  52. Chi, C.; Zhou, X.; Wang, Y.; Zhang, H.; Meng, G.; Hu, Y.; Bai, Z. Preparation of needle coke composite cathode and its treatment of RhB wastewater. J. Electroanal. Chem. 2022, 920, 116612. [Google Scholar] [CrossRef]
  53. Krishna, B.R.; Bhuvaneshwari, S.; Majeed, F.; Aravind, S.P. Development and applicability of Aluminium-Copper alloy electrodes for dairy wastewater treatment. J. Water Process. Eng. 2022, 48, 102915. [Google Scholar] [CrossRef]
  54. Zhang, W.; Zhang, M.; Yao, J.; Long, J. Industrial indigo dyeing wastewater purification: Effective COD removal with peroxi-AC electrocoagulation system. Arab. J. Chem. 2023, 16, 104607. [Google Scholar] [CrossRef]
  55. Siburian, R.; Hutagalung, F.; Silitonga, O.; Paiman, S.; Simatupang, L.; Simanjuntak, C.; Aritonang, S.P.; Alias, Y.; Jing, L.; Goei, R.; et al. The New Materials for Battery Electrode Prototypes. Materials 2023, 16, 555. [Google Scholar] [CrossRef]
  56. Ferreira de Oliveira, A.E.; Pereira, A.C.; Ferreira, L.F. Fully handwritten electrodes on paper substrate using rollerball pen with silver nanoparticle ink, marker pen with carbon nanotube ink and graphite pencil. Anal. Methods 2022, 14, 1880–1888. [Google Scholar] [CrossRef]
  57. Bansal, R.; Verduzco, R.; Wong, M.S.; Westerhoff, P.; Garcia-Segura, S. Development of nano boron-doped diamond electrodes for environmental applications. J. Electroanal. Chem. 2022, 907, 116028. [Google Scholar] [CrossRef]
  58. De Luna, Y.; Bensalah, N. Review on the electrochemical oxidation of endocrine-disrupting chemicals using BDD anodes. Curr. Opin. Electrochem. 2022, 32, 100900. [Google Scholar] [CrossRef]
  59. Zhang, T.; Xue, Z.; Xie, Y.; Huang, G.D.; Peng, G.P. Fabrication of a boron-doped nanocrystalline diamond grown on an WC-Co electrode for degradation of phenol. RSC Adv. 2022, 12, 26580–26587. [Google Scholar] [CrossRef]
  60. Nagels, M.; Verhoeven, B.; Larché, N.; Dewil, R.; Rossi, B. Corrosion behaviour of lean duplex stainless steel in advanced oxidation process (AOP) based wastewater treatment plants. Eng. Fail. Anal. 2022, 136, 106170. [Google Scholar] [CrossRef]
  61. Okur, M.C.; Akyol, A.; Nayir, T.Y.; Kara, S.; Ozturk, D.; Civas, A. Performance of Ti/RuO2-IrO2 electrodes and comparison with BDD electrodes in the treatment of textile wastewater by electro-oxidation process. Chem. Eng. Res. Des. 2022, 183, 398–410. [Google Scholar] [CrossRef]
  62. Kuhl, M.; Henning, A.; Haller, L.; Wagner, L.I.; Jiang, C.-M.; Streibel, V.; Sharp, I.D.; Eichhorn, J. Designing Multifunctional Cobalt Oxide Layers for Efficient and Stable Electrochemical Oxygen Evolution. Adv. Mater. Interfaces 2022, 9, 2200582. [Google Scholar] [CrossRef]
  63. Khan, S.; Shah, S.S.; Ahmad, A.; Yurtcan, A.B.; Katubi, K.M.; Janjua, N.K. gamma-Alumina Supported Copper Oxide Nanostructures Promoted with Ruthenium Oxide (RuO2-CuO/Al2O3) and Palladium Oxide (PdO-CuO/Al2O3): Efficient Electrodes for Heterogeneous Catalysis of Ammonia Electrooxidation. J. Electrochem. Soc. 2022, 169, 076512. [Google Scholar] [CrossRef]
  64. Ibupoto, Z.H.; Tahira, A.; Shah, A.A.; Aftab, U.; Solangi, M.Y.; Leghari, J.A.; Samoon, A.H.; Bhatti, A.L.; Bhatti, M.A.; Mazzaro, R.; et al. NiCo2O4 nanostructures loaded onto pencil graphite rod: An advanced composite material for oxygen evolution reaction. Int. J. Hydrogen Energy 2022, 47, 6650–6665. [Google Scholar] [CrossRef]
  65. Zou, C.; Ma, C.; Chen, F.; Shao, X.; Cao, L.; Yang, J. Crystal facet controlled stable PbO2 electrode for efficient degradation of tetracycline. J. Electroanal. Chem. 2022, 914, 116330. [Google Scholar] [CrossRef]
  66. Yan, Y.; Ma, X.; Xia, Y.; Feng, H.; Liu, S.; He, C.; Ding, Y. Mechanism of highly efficient electrochemical degradation of antibiotic sulfadiazine using a layer-by-layer GNPs/PbO2 electrode. Environ. Res. 2023, 217, 114778. [Google Scholar] [CrossRef]
  67. Chen, S.; Chen, J.; Xi, G.; Zhang, X.; He, Z. Sonoelectrochemical oxidation of aged landfill leachate with high-efficiency Ti/PANI/PDMS-Ce-PbO2 anode. J. Environ. Chem. Eng. 2022, 10, 107499. [Google Scholar] [CrossRef]
  68. Wen, Z.; Ren, S.; Zhang, Y.; Li, J.; Zhang, Z.; Wang, A. Performance of anode materials in electro-Fenton oxidation of cefoperazone in chloride medium: New insight into simultaneous mineralization and toxic byproducts formation. J. Clean. Prod. 2022, 377, 120793. [Google Scholar] [CrossRef]
  69. Wang, G.; Fu, R.; Li, X.; Jia, Z.; Qu, J. Study on the anode stability of polyaniline with its pyrolysis products as electroactive components and the experimental study of cobalt electrowinning in chloride system. Energy Rep. 2022, 8, 754–768. [Google Scholar] [CrossRef]
  70. Eguiluz, K.I.B.; Hernandez-Sanchez, N.K.; Doria, A.R.; Santos, G.O.S.; Salazar-Banda, G.R.; de Leon, C.P. Template-made tailored mesoporous Ti/SnO2-Sb2O5-IrO2 anodes with enhanced activity towards dye removal. J. Electroanal. Chem. 2022, 910, 116153. [Google Scholar] [CrossRef]
  71. Yudha, C.S.; Rahmawati, M.; Apriliyani, E.; Nisa, S.S.; Jumari, A. Synthesis of Nickel Cobalt Manganese Ternary Transition Metal Oxide from Mixed Hydroxide Precipitate as a Precursor to NCM811. Defect Diffus. Forum 2022, 417, 131–139. [Google Scholar] [CrossRef]
  72. Huang, Z.; Mai Thanh, N.; Sim, W.J.; Takahashi, M.; Kheawhom, S.; Yonezawa, T. CoxNi1-xO-NiCo2O4/rGO synergistic bifunctional electrocatalysts for high-rate rechargeable zinc-air batteries. Sustain. Energy Fuels 2022, 6, 3931–3943. [Google Scholar] [CrossRef]
  73. Fan, Z.; Yu, H.; Jiang, G.; Yao, D.; Sun, S.; Chi, J.; Qin, B.; Shao, Z. Low precious metal loading porous transport layer coating and anode catalyst layer for proton exchange membrane water electrolysis. Int. J. Hydrogen Energy 2022, 47, 18963–18971. [Google Scholar] [CrossRef]
  74. Nguyen, T.K.; Yu, S.H.; Yan, J.; Chua, D.H.C. SnO2-anchored carbon fibers chemical vapor deposition (CVD) synthesis: Effects of growth parameters on morphologies and electrochemical behaviors. J. Mater. Sci. 2020, 55, 15588–15601. [Google Scholar] [CrossRef]
  75. Mathur, S.; Erdem, A.; Cavelius, C.; Barth, S.; Altmayer, J. Amplified electrochemical DNA-sensing of nanostructured metal oxide films deposited on disposable graphite electrodes functionalized by chemical vapor deposition. Sens. Actuator B-Chem. 2009, 136, 432–437. [Google Scholar] [CrossRef]
  76. Li, X.; Wang, Z.; Qiu, Y.; Pan, Q.; Hu, P. 3D graphene/ZnO nanorods composite networks as supercapacitor electrodes. J. Alloys Compd. 2015, 620, 31–37. [Google Scholar] [CrossRef]
  77. Wang, Z.; Tan, Z.; Yuan, S.; Li, H.; Zhang, Y.; Dong, Y. Direct current electrochemical method for removal and recovery of heavy metals from water using straw biochar electrode. J. Clean. Prod. 2022, 339, 130746. [Google Scholar] [CrossRef]
  78. Pozio, A.; Bozza, F.; Lisi, N.; Chierchia, R.; Migliorini, F.; Donde, R.; De Iuliis, S. Cobalt Oxide Synthesis via Flame Spray Pyrolysis as Anode Electrocatalyst for Alkaline Membrane Water Electrolyzer. Materials 2022, 15, 4626. [Google Scholar] [CrossRef]
  79. Le Luu, T.; Ngan, P.T.K. Fabrication of high performance Ti/SnO2-Nb2O5 electrodes for electrochemical textile wastewater treatment. Sci. Total Environ. 2023, 860, 160366. [Google Scholar] [CrossRef]
  80. Peroni, M.B.; Navas, M.B.; Ocsachoque, M.A.; Lick, I.D.; Casella, M.L.; Jaworski, M.A. Elimination of NO3 from water using Pd and PdCu catalysis supported on ZrO2-CeO2 materials: Effect of the support preparation. Mater. Chem. Phys. 2023, 296, 127186. [Google Scholar] [CrossRef]
  81. Zhang, Y.W.; Li, Y.T.; Yao, Z.H.; Wang, J.; Zhong, Q. Iron-nickel aerogels anchored on GO nanosheets as efficient oxygen evolution reaction catalysts under industrial conditions. Int. J. Hydrogen Energ. 2022, 47, 6996–7004. [Google Scholar] [CrossRef]
  82. Deng, S.; Dai, Y.; Situ, Y.; Liu, D.; Huang, H. Preparation of nanosheet-based spherical Ti/SnO2-Sb electrode by in-situ hydrothermal method and its performance in the degradation of methylene blue. Electrochim. Acta 2021, 398, 139335. [Google Scholar] [CrossRef]
  83. Shivakumar, M.; Manjunatha, S.; Nithyayini, K.N.; Dharmaprakash, M.S.; Nagashree, K.L. Electrocatalytic detection of nitrite at NiCo2O4 nanotapes synthesized via microwave-hydrothermal method. J. Electroanal. Chem. 2021, 882, 115016. [Google Scholar] [CrossRef]
  84. Kalinic, B.; Girardi, L.; Ragonese, P.; Faramawy, A.; Mattei, G.; Frasconi, M.; Baretta, R.; Bogialli, S.; Roverso, M.; Rizzi, G.A.; et al. Diffusion-driven formation of Co3O4 nanopetals layers for photoelectrochemical degradation of organophosphate pesticides. Appl. Surf. Sci. 2022, 596, 153552. [Google Scholar] [CrossRef]
  85. Xiao, Z.H.; Wang, J.; Liu, C.H.; Wang, B.W.; Zhang, Q.; Xu, Z.L.; Sarwar, M.T.; Tang, A.D.; Yang, H.M. In-situ surface structural reconstruction of NiMoO4 for efficient overall water splitting. Appl. Surf. Sci. 2022, 602, 154314. [Google Scholar] [CrossRef]
  86. Guo, H.; Xu, Z.; Qiao, D.; Dan, W.; Xu, H.; Yan, W.; Jin, X. Fabrication and characterization of porous titanium-based PbO2 electrode through the pulse electrodeposition method: Deposition condition optimization by orthogonal experiment. Chemosphere 2020, 261, 128157. [Google Scholar] [CrossRef]
  87. Wang, K.; Xing, X.; Liu, W.; Jiang, Y.; Li, H.; Lu, Y.; Chen, H.; Ren, H. Fabrication of a novel PbO2 electrode with rare earth elements doping for p-nitrophenol degradation. J. Environ. Chem. Eng. 2023, 11, 109513. [Google Scholar] [CrossRef]
  88. Wu, D.; Wu, X. Research Progress in Electrodeposition Technology of Titanium-Based Iridium Oxide Electrode. J. Electrochem. 2021, 27, 35–44. [Google Scholar] [CrossRef]
  89. Zhou, Q.; Zhou, X.; Zheng, R.; Liu, Z.; Wang, J. Application of lead oxide electrodes in wastewater treatment: A review. Sci. Total Environ. 2022, 806, 150088. [Google Scholar] [CrossRef]
  90. Zhang, Z.; Yi, G.; Li, P.; Wang, X.; Wang, X.; Zhang, C.; Zhang, Y. Recent progress in engineering approach towards the design of PbO2-based electrodes for the anodic oxidation of organic pollutants. J. Water Process Eng. 2021, 42, 102173. [Google Scholar] [CrossRef]
  91. Shao, D.; Li, W.; Wang, Z.; Yang, C.; Xu, H.; Yan, W.; Yang, L.; Wang, G.; Yang, J.; Feng, L.; et al. Variable activity and selectivity for electrochemical oxidation wastewater treatment using a magnetically assembled electrode based on Ti/PbO2 and carbon nanotubes. Sep. Purif. Technol. 2022, 301, 122008. [Google Scholar] [CrossRef]
  92. Man, S.; Luo, D.; Sun, Q.; Yang, H.; Bao, H.; Xu, K.; Zeng, X.; He, M.; Yin, Z.; Wang, L.; et al. When MXene (Ti3C2Tx) meet Ti/PbO2: An improved electrocatalytic activity and stability. J. Hazard. Mater. 2022, 430, 128440. [Google Scholar] [CrossRef]
  93. Dai, J.; Feng, H.; Shi, K.; Ma, X.; Yan, Y.; Ye, L.; Xia, Y. Electrochemical degradation of antibiotic enoxacin using a novel PbO2 electrode with a graphene nanoplatelets inter-layer: Characteristics, efficiency and mechanism. Chemosphere 2022, 307, 135833. [Google Scholar] [CrossRef]
  94. You, S.J.; Liu, B.; Gao, Y.F.; Wang, Y.; Tang, C.Y.Y.; Huang, Y.B.; Ren, N.Q. Monolithic Porous Magneli-phase Ti4O7 for Electro-oxidation Treatment of Industrial Wastewater. Electrochim. Acta 2016, 214, 326–335. [Google Scholar] [CrossRef]
  95. Pei, S.; Zhu, L.; Zhang, Z.; Teng, J.; Liu, X.; You, S. Electrochemical properties of titanium sub-oxide membrane electrode and application for electro-oxidation treatment of dyeing wastewater. Acta Sci. Circumst. 2020, 40, 3658–3665. [Google Scholar]
  96. Huang, P.; Lei, J.; Sun, Z.; Hu, X. Fabrication of MOF-derivated CuOx-C electrode for electrochemical degradation of ceftazidime from aqueous solution. Chemosphere 2021, 268, 129157. [Google Scholar] [CrossRef]
  97. Safarvand, D.; Naser, I.; Samipourgiri, M.; Arjmand, M. Efficient Photoelectrocatalytic Degradation of BTEX Using TiO2/CuO/Cu2O Nanorod-Array Film as the Photoanode and MWCNT/GO/Graphite Felt as the Photocathode. Electrocatalysis 2020, 11, 188–202. [Google Scholar] [CrossRef]
  98. Lei, J.; Zhang, Y.; He, P. An alpha-Fe2O3/Circulating Fluidized Bed Fly Ash Based Geopolymer Composite Anode for Electrocatalytic Degradation of Indigo Carmine Dye Wastewater. J. Renew. Mater. 2021, 9, 2277–2289. [Google Scholar] [CrossRef]
  99. Hou, Y.; Sun, X.; Dang, Y.; Yu, S.; Chen, S.; Tang, J.; Zhang, L.; Zhou, Y. Electrochemical Acceleration of Redox Reaction Cycles on the Surface of Fe2O3-MnO2 Cathode to Activate the Peroxymonosulfate for the Efficient Removal of Levofloxacin. J. Electrochem. Soc. 2022, 169, 023505. [Google Scholar] [CrossRef]
  100. Cao, X.; Jiang, D.; Huang, M.; Pan, J.; Lin, J.; Chan, W. Iron oxide nanoparticles wrapped in graphene aerogel composite: Fabrication and application in electro-fenton at a Wide pH. Colloids Surf. A Physicochem. Eng. Asp. 2020, 587, 124269. [Google Scholar] [CrossRef]
  101. Guo, H.; Xu, Z.; Wang, D.; Chen, S.; Qiao, D.; Wan, D.; Xu, H.; Yan, W.; Jin, X. Evaluation of diclofenac degradation effect in “active” and “non-active” anodes: A new consideration about mineralization inclination. Chemosphere 2022, 286, 131580. [Google Scholar] [CrossRef]
  102. Jiani, L.; Zhicheng, X.; Hao, X.; Dan, Q.; Zhengwei, L.; Wei, Y.; Yu, W. Pulsed electrochemical oxidation of acid Red G and crystal violet by PbO2 anode. J. Environ. Chem. Eng. 2020, 8, 103773. [Google Scholar] [CrossRef]
  103. Rong, H.; Zhang, C.; Sun, Y.; Wu, L.; Lian, B.; Wang, Y.; Chen, Y.; Tu, Y.; Waite, T.D. Electrochemical degradation of Ni-EDTA complexes in electroless plating wastewater using PbO2-Bi electrodes. Chem. Eng. J. 2022, 431, 133230. [Google Scholar] [CrossRef]
  104. Kim, T.; Kim, G.-P.; Lee, D.; Kim, Y.; Shim, S.E.; Baeck, S.-H. Electrochemical Oxidation of Organic Matter in the Presence of Chloride Over Ti/SnO2-Sb2O5 Prepared via Sol-Gel Methods. J. Nanosci. Nanotechnol. 2016, 16, 10892–10897. [Google Scholar] [CrossRef]
  105. Chen, X.M.; Gao, F.R.; Chen, G.H. Comparison of Ti/BDD and Ti/SnO2-Sb2O5 electrodes for pollutant oxidation. J. Appl. Electrochem. 2005, 35, 185–191. [Google Scholar] [CrossRef]
  106. Adams, B.; Tian, M.; Chen, A. Design and electrochemical study of SnO2-based mixed oxide electrodes. Electrochim. Acta 2009, 54, 1491–1498. [Google Scholar] [CrossRef]
  107. Ganzoury, M.A.; Ghasemian, S.; Zhang, N.; Yagar, M.; De Lannoy, C.-F. Mixed metal oxide anodes used for the electrochemical degradation of a real mixed industrial wastewater. Chemosphere 2022, 286, 131600. [Google Scholar] [CrossRef]
  108. Wei, L.; Mao, X.; Lin, A.; Gan, F. PbO2-SnO2 composite anode with interconnected structure for the electrochemical incineration of phenol. Russ. J. Electrochem. 2011, 47, 1394–1398. [Google Scholar] [CrossRef]
  109. Hu, Z.; Cai, J.; Song, G.; Tian, Y.; Zhou, M. Anodic oxidation of organic pollutants: Anode fabrication, process hybrid and environmental applications. Curr. Opin. Electrochem. 2021, 26, 100659. [Google Scholar] [CrossRef]
  110. Duan, X.; Sui, X.; Wang, W.; Bai, W.; Chang, L. Fabrication of PbO2/SnO2 composite anode for electrochemical degradation of 3-chlorophenol in aqueous solution. Appl. Surf. Sci. 2019, 494, 211–222. [Google Scholar] [CrossRef]
  111. Memar, M.; Rezvani, A.R.; Saheli, S. Synthesis, characterization, and application of CuO nanoparticle 2D doped with Zn2+ against photodegradation of organic dyes (MB & MO) under sunlight. J. Mater. Sci. Mater. Electron. 2021, 32, 2127–2145. [Google Scholar] [CrossRef]
  112. Sun, G.; Wang, C.; Gu, W.; Song, Q. A facile electroless preparation of Cu, Sn and Sb oxides coated Ti electrode for electrocatalytic degradation of organic pollutants. Sci. Total Environ. 2021, 772, 144908. [Google Scholar] [CrossRef]
  113. Man, S.; Ge, X.; Xu, K.; Yang, H.; Bao, H.; Sun, Q.; He, M.; Xie, Y.; Li, A.; Mo, Z.; et al. Fabrication of a Ti/PbO2 electrode with Sb doped SnO2 nanoflowers as the middle layer for the degradation of methylene blue, norfloxacin and p-dihydroxybenzene. Sep. Purif. Technol. 2022, 280, 119816. [Google Scholar] [CrossRef]
  114. Zhang, F.X.; Shao, D.; Yang, C.A.; Xu, H.; Yang, J.; Feng, L.; Wang, S.Z.; Li, Y.; Jia, X.H.; Song, H.J. New Magnetically Assembled Electrode Consisting of Magnetic Activated Carbon Particles and Ti/Sb-SnO2 for a More Flexible and Cost-Effective Electrochemical Oxidation Wastewater Treatment. Catalysts 2023, 13, 7. [Google Scholar] [CrossRef]
Figure 2. Comparison of the main characteristics of various electrodes that are suitable for organic wastewater treatment.
Figure 2. Comparison of the main characteristics of various electrodes that are suitable for organic wastewater treatment.
Catalysts 13 01096 g002
Figure 3. Main metal oxide electrode preparation methods. Thermal decomposition method (a); chemical deposition method (b); electrochemical deposition method (c); sol–gel method (d); hydrothermal method (e); physical vapor deposition method (f).
Figure 3. Main metal oxide electrode preparation methods. Thermal decomposition method (a); chemical deposition method (b); electrochemical deposition method (c); sol–gel method (d); hydrothermal method (e); physical vapor deposition method (f).
Catalysts 13 01096 g003
Figure 4. The preparation procedure of few-layered Ti3C2Tx (a) and a novel PbO2 electrode with a MXene material as the intermediate layer (b) [92]. The electrochemical treatment reactor for a GNP-PbO2 electrode (c) [93]. The fabrication procedure for the PbO2-Bi electrode (d) [103].
Figure 4. The preparation procedure of few-layered Ti3C2Tx (a) and a novel PbO2 electrode with a MXene material as the intermediate layer (b) [92]. The electrochemical treatment reactor for a GNP-PbO2 electrode (c) [93]. The fabrication procedure for the PbO2-Bi electrode (d) [103].
Catalysts 13 01096 g004
Figure 5. The preparation procedure for Ti/CuO-SnO2–SbOX electrodes (a) [112]. The preparation procedure for the Ti/Sb-SnO2 NFs/PbO2 electrode (b) [113]. A schematic diagram of the MAE system (c) [91].
Figure 5. The preparation procedure for Ti/CuO-SnO2–SbOX electrodes (a) [112]. The preparation procedure for the Ti/Sb-SnO2 NFs/PbO2 electrode (b) [113]. A schematic diagram of the MAE system (c) [91].
Catalysts 13 01096 g005
Table 1. Typical metal oxide electrodes and their main advantages and drawbacks.
Table 1. Typical metal oxide electrodes and their main advantages and drawbacks.
Electrode TypesMain AdvantagesMain DrawbacksRefs.
Lead oxide electrodes (PbO2 electrode, etc.) Lead oxide electrodes have good electrical conductivity, corrosion resistance, and catalytic activity, and their preparation cost is relatively low.Lead oxide electrodes have the potential to gradually release lead ions into the water, which can lead to heavy metal contamination.[90,91,92,93]
Titanium sub-oxide electrodes (Ti4O7 and Ti5O9 electrodes, etc.)They have good electrocatalytic activity and stability, and their potential toxicity is very low.The manufacturing cost of the electrode is relatively high, and it is easily deactivated by some external pollutants in practical applications.[49,94,95]
Electrodes based on copper oxidesCopper oxides demonstrate remarkable catalytic activity, providing an effective solution to the degradation of some resistant organic substances, particularly antibiotics.Compared with lead oxide electrodes, their preparation costs are relatively high and the preparation technology is complex.[96,97]
Electrodes based on iron oxidesIron oxides can enhance the electrode’s capacity to degrade organic wastewater. Furthermore, they can elevate the electrode’s oxygen evolution potential and reduce the electrode’s inherent resistance in certain application environments.Iron oxides are susceptible to corrosion in highly acidic environments.[98,99,100]
Table 2. Typical metal oxide composite electrodes and their advantages and drawbacks.
Table 2. Typical metal oxide composite electrodes and their advantages and drawbacks.
Electrode TypesMain AdvantagesMain DrawbacksRefs.
Ti/SnO2-Sb2O5 electrodeHigh catalytic activity, excellent corrosion resistance, and stable electrochemical performance.High price and brittleness.[104,105,106]
Ti/RuO2-IrO2
electrode
High catalytic activity, excellent corrosion resistance, stable electrochemical performance, and can withstand high current densities.High preparation costs, and the treatment effect of some organic wastewater types is not good. [107]
PbO2-SnO2
electrode
High catalytic activity, good corrosion resistance, and a long service life.High preparation costs, and the treatment effect of some organic wastewater types is not good. [108,109,110]
ZnO/CuO
electrode
High catalytic activity, good chemical stability, and low manufacturing costs.The requirements in terms of water quality are relatively high (e.g., ion content, pH value).[111]
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Jing, X.; Wang, X.; Li, X.; Wang, D.; Xu, H.; Yan, W. Progress in the Preparation of Metal Oxide Electrodes for the Electrochemical Treatment of Organic Wastewater: A Short Review. Catalysts 2023, 13, 1096. https://doi.org/10.3390/catal13071096

AMA Style

Jing X, Wang X, Li X, Wang D, Xu H, Yan W. Progress in the Preparation of Metal Oxide Electrodes for the Electrochemical Treatment of Organic Wastewater: A Short Review. Catalysts. 2023; 13(7):1096. https://doi.org/10.3390/catal13071096

Chicago/Turabian Style

Jing, Xiaosheng, Xinyu Wang, Xiaoliang Li, Dongqi Wang, Hao Xu, and Wei Yan. 2023. "Progress in the Preparation of Metal Oxide Electrodes for the Electrochemical Treatment of Organic Wastewater: A Short Review" Catalysts 13, no. 7: 1096. https://doi.org/10.3390/catal13071096

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop