Open Access Article
Saikat
Bolar
a,
Yoshikazu
Ito
b and
Takeshi
Fujita
*a
aSchool of Science and Engineering, Kochi University of Technology, 185 Miyanokuchi, Tosayamada, Kami City, Kochi 782-8502, Japan. E-mail: fujita.takeshi@kochi-tech.ac.jp
bInstitute of Applied Physics, Graduate School of Pure and Applied Sciences, University of Tsukuba, Tsukuba 305-8573, Japan
First published on 8th May 2024
The rapid advancement of electrochemical processes in industrial applications has increased the demand for high-performance electrode materials. High-entropy alloys (HEAs), a class of multicomponent alloys with unique properties, have emerged as potential electrode materials owing to their enhanced catalytic activity, superior stability, and tunable electronic structures. This review explores contemporary developments in HEA-based electrode materials for industrial applications and identifies their advantages and challenges as compared to conventional commercial electrode materials in industrial aspects. The importance of tuning the composition, crystal structure, different phase formations, thermodynamic and kinetic parameters, and surface morphology of HEAs and their derivatives to achieve the predicted electrochemical performance is emphasized in this review. Synthetic procedures for producing potential HEA electrode materials are outlined, and theoretical discussions provide a roadmap for recognizing the ideal electrode materials for specific electrochemical processes in an industrial setting. A comprehensive discussion and analysis of various electrochemical processes (HER, OER, ORR, CO2RR, MOR, AOR, and NRR) and electrochemical applications (batteries, supercapacitors, etc.) is included to appraise the potential ability of HEAs as an electrode material in the near future. Overall, the design and development of HEAs offer a promising pathway for advancing industrial electrode materials with improved performance, selectivity, and stability, potentially paving the way for the next generation of electrochemical technology.
The advancement of novel electrode materials for industrial applications is a dynamic field of research; consequently, scientists are continuously striving to create electrode materials with higher efficiency, selectivity, stability, and cost effectiveness to meet the demands of industrial processes.10 Electrochemical research is immensely significant for transforming electrochemical technology into practical applications and driving transformative advancements across various industries. Electrocatalysts and electrode materials serve as significant components of industrial applications, encompassing energy storage, energy conversion, chemical synthesis, sensors, corrosion protection, electroplating, water treatment and numerous other areas.10,11 The selection of electrode materials for a particular application is guided by a combination of factors, including the required conductivity, desired electrochemical properties, and economic considerations. Consequently, as the demand for electrochemical technology surges owing to the rapid industrialization of electrochemical processes, the demand for prospective electrode materials is also anticipated to rise (Fig. 1a).12–19 The selection of appropriate electrode materials is a crucial aspect of electrochemical processes, guided by the mechanistic pathways of electrochemical conversion and following the principles of modern electrocatalysis.14–18 Precious metals, especially Pt, Ru, Ir, and Au, are frequently employed in electrochemical processes because of their favorable electronic structure, abundance of active sites, high conductivity, selective catalytic activity, and exceptional durability under the respective electrochemical conditions.20 However, these properties may vary depending on the specific application within the respective electrochemical process. Despite their advantages, noble metals also exhibit certain limitations in both industrial and lab-scale applications.21–23 Their relative scarcity and expense hinder their widespread adoption in large-scale applications. Moreover, they may poison certain contaminants that appear during the electrochemical process. Researchers are actively exploring alternative catalyst materials and designing strategies to reduce the reliance on noble metals while maintaining or improving catalytic performance.22–24
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| Fig. 1 (a) Number of publications on high-entropy alloys (HEAs) according to the data collected from Scifinder Scholar, (b) mixing entropy of equimolar alloys as a function of the number of the components, reproduced with permission.27 Copyright 2021, Wiley-VCH. (c) Research articles on HEA (inset)-based electrocatalysts. Reproduced with permission.29 Copyright 2016, Elsevier Ltd. (d) HEA electrode materials for electrochemical application. | ||
Over the past few decades, researchers have endeavored to reduce the price-to-performance ratio of electrocatalysts to enhance their commercial viability and applicability in various industrial processes. This goal can be achieved through two primary approaches: (a) minimizing the utilization of noble metals in the catalyst formulation and (b) developing noble-metal-free electrocatalysts. Noble-metal electrocatalysts often exhibit operational instability under harsh working conditions, resulting in susceptibility to dissolution, agglomeration, and poisoning effects.10,16,20 To date, only a limited number of electrocatalysts have been proposed that meet the stringent requirements for industrial applications. Many traditional electrode materials struggle with stability and cost, demanding the exploration of alternatives. Alloy-based materials offer a promising solution, providing a cost-effective and often more stable alternative to expensive noble metal-based electrodes for various electrochemical processes like the OER, HER, and ORR. Recent research efforts have focused on exploring cost-effective alloy-based electrode materials to address the diverse design requirements of various electrochemical processes, considering the limited selection of available metals.24 Conventional alloys typically consist of one or two elements, and they often fail in obtaining the specific properties required for an effective electrocatalyst.25 With advancements in alloy preparation techniques, a variety of alloy materials have emerged, including low-, medium-, and high-entropy alloys (HEAs) (Fig. 1b).26–29 To date, thousands of research papers have been published annually highlighting the promising potential of HEAs in various fields, including electrochemical industrial applications (Fig. 1c).30–36
A HEA consists of at least five or more elements with equal or unequal proportions with atomic percentages in the range of 5–35% of each element (Fig. 1d).30–34 Owing to their atomic randomness and superior chemical and physical properties in comparison with those of conventional alloys, HEAs are more appealing for industrial applications. They exhibit several important properties such as the high-entropy effect (HEE), lattice distortion, slow diffusion, and the cocktail effect (CE), which provide considerable versatility and uniqueness compared to other developed materials (Fig. 2a and b).27,30,31 The selection of elements and their relative proportions in HEAs are crucial factors for determining their properties and performance. Owing to their wide range of possible compositions, HEAs can be tailored with specific properties, such as phase formation, stability, and processing conditions.19,22,26,33 HEAs offer several advantages compared to conventional alloys, including enhanced operational efficiency, productivity, and sustainability.31–37 The study of high-entropy alloys (HEAs) in materials science and engineering is exciting due to their unique characteristics and potential applications, driven by the fundamental principle of maximizing configurational entropy within the alloy system to yield desirable properties, including enhanced mechanical properties like strength, hardness, and wear resistance crucial for industrial electrode material design.33–36 The versatility of HEAs is one of the key advantages for multiple electrode designs. HEAs can be tailored to exhibit specific properties suitable for a wide range of applications by carefully selecting the constituent elements. This tunability allows for the development of HEAs with tailored electronic and structural features, enabling their application in various electrochemical processes through selective choice of periodic elements, structural features, and synthetic routes. Harnessing their unique properties, HEAs show promise for revolutionizing industrial processes by unlocking exceptional combinations of efficiency, selectivity, stability, and cost-effectiveness in electrochemical applications.
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| Fig. 2 (a) Structural and electronic modification to improve the catalytic performance of HEAs. Reproduced with permission.40 Copyright 2021, Wiley-VCH. (b) HEAs with core effects. Reproduced with permission.5 Copyright 2016, Elsevier Ltd. (c) Topographies of different alloys and their phase structure. | ||
This review delves into the terminology, governing parameters, properties, derivatives, synthesis procedures, structural behavior, and applications of HEA-based materials in diverse electrochemical processes. The discussion extends to theoretical considerations for designing electrode materials tailored to specific applications, providing a comprehensive overview of the potential applications, opportunities, and limitations of HEAs as promising industrial electrode materials.
It further elaborates on the current advancements and potential challenges associated with HEA-based electrode materials from an industrial perspective. The field of HEAs has witnessed continuous expansion, with researchers exploring novel alloy systems, developing advanced processing techniques, and investigating a broad spectrum of properties and applications. The evolving nature of HEAs demonstrates immense promise for further breakthroughs and discoveries in the years to come. The exploration of HEAs remains an active area of research, with scientists continuously pursuing the development of new alloy systems with enhanced properties.
| nmajor ≥ 5, 5 at% ≤ Ci ≤ 35 at%, and nminor ≥ 0 Cj ≤ 5, |
S = KB ln W | (1) |
| ΔSmix = ΔSconfmix + ΔSvibmix + ΔSmagmix + ΔSelecmix | (2) |
The mixing entropy is completely dependent on the configurational entropy. The configurational entropy of equimolar alloys increases with the increase in the number of elements in the HEA. In the context of the relationship between entropy and complexion, Boltzmann theory formulates the configurational entropy for liquid and solid solutions of equimolar alloys using the following equation:27,39
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| N | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| ΔSmix | 0 | 0.69R | 1.1R | 1.39R | 1.61R | 1.79R | 1.95R | 2.08R | 2.2R | 2.3R | 2.4R | 2.49R | 2.57R |
In particular, HEAs with a single phase can be distinguished as compositionally complex solid solutions (CCSSs), which are not fully covered by the aforementioned definition of a HEA. All HEAs are CCSSs, but not all CCSSs are HEAs, since HEAs are a special subset of CCSSs, with the main difference being the emphasis on having multiple main elements in approximately equal molar or higher concentrations. In contrast, complex concentrated alloys, multi-principal element alloys (MPEAs), compositionally complex alloys (CCAs), and multi-element alloys are all subsets of CCSSs and differ in elemental integrity, elemental homogeneity, phase structure, lattice structure, and solid solution behavior.40–44 The use of these terms in the context of electrocatalysts is often based on the assumption that the properties of both materials coexist. As a result, a HEA can be used as an established electrode material and its electrochemical performance can be considered for use as an industrial electrode material. The molar concentration (equimolar/quasi-equimolar) and phase structure (single or multi-phase) are two important parameters that determine the type of HEA, and based on these parameters, HEAs can be divided into first and second generation HEAs.27,29,39,44 Conversely, non-equimolar complex phase (matrix containing solid solution) alloys have attracted potential research attention due to their structural, compositional, and electronic diversity, which may affect their electrochemical performance compared to conventional alloys.
First-generation HEAs consist of at least five components with equal atomic ratios, and the phase structure is a single-phase solid solution. Second-generation HEAs consist of at least four main components with unequal atomic ratios and have a two- or multiphase structure.45,46 HEAs are a developing research area, and efforts are being focused on developing non-equimolar multiphase solid solution alloys from equimolar single-phase solid solution alloys in order to improve catalytic performance. Non-equimolar multiphase solid solution alloys are referred to as second generation HEAs and are being analyzed to design and develop more selective materials for electrochemical applications (Fig. 2c).45,46
Studies have identified that transition metals generally form single face-centered cubic (FCC) arrangements in a typical solid solution.40,43,46 The number of phases in a HEA is always less than the maximum equilibrium number based on the Gibbs phase rule, offering a new perspective on the strategies used for their synthesis. Yeh et al. determined that incorporating more elements generally increases the hardness of an alloy and investigated the corrosion inhibition behavior of HEAs, identifying that small passive metals and a lower mixing enthalpy contribute to corrosion resistance.23,27,31,39,43
The scientific understanding of HEAs has been broadly extended, employed, and accepted to various high-entropy materials (HEMs). In brief, HEA systems broadly encompass high-entropy solid solution alloys, high-entropy amorphous alloys, and narrowly defined HEA ceramics. High-entropy ceramics (HECs) are a specific class of ceramics that exhibit the principles of HEAs but in a ceramic context, where ceramics are solid solutions comprising five or more cation and anion sublattices with high configurational entropy.47,48 A variety of HEMs have been synthesized, including metal–organic frameworks (MOFs), carbonaceous materials, MXenes, oxides, chalcogenides, nitrides, phosphides, borides, and fluorides. However, high-entropy derivatives do not completely satisfy the parameters of a HEA system and should be defined as HEMs.49,50 The HEAs can be both amorphous and crystalline in nature, similar to conventional alloys. Therefore, the common crystal structures of HEAs and their derivatives can include FCC, body-centered cubic (BCC), hexagonal close-packed (HCP), and amorphous structures; therefore, the structural types are also varied by altering the synthesis process and, most notably, based on the periodic position of the elements (Fig. 3a).27,29,39,46,51 Recently, certain mixed-phase crystal structures have been reported with BCC and FCC lattices in the single phase.51,52 Elemental selection strategically influences the crystal structure, affecting multiple electrochemical processes diversely, with recent attention drawn to high-entropy alloy nanoparticles (HEA NPs) due to their superior activities and stability, offering opportunities for innovations in various aspects alongside HEAs and their derivatives, whereby HEA NPs with tunable electronic features, optimized morphology, surface-active sites, selective crystal structure, phase integrity, and comparable synthesis techniques significantly impact catalytic objectives.33
Depending on the periodic position of the elements, HEAs can be distinguished as noble-metal-based HEAs (NHEAs), non-noble-metal-based HEAs (NMHEAs), and refractory HEAs (RHEAs).39,47,49 In contrast, RHEAs are composed of refractory metals (Mo, Ti, V, Nb, Hf, Ta, W, and Cr) exhibiting significant application prospects owing to their superior mechanical properties and their potential in replacing Ni-based superalloys as the next generation of high-temperature electrode materials.53 Phase structure modification of HEAs has evolved as an effective approach to increase the strength of the RHEA systems.39,40,52,54 Eutectic HEAs (EHEAs) typically have FCC and BCC crystal lattice structures and exhibit two different properties, such as ductility and strength. Sumanta et al. reported an equiatomic CoCuFeNiTi EHEA with BCC and FCC structures, which exhibited optimum workability at high temperature and can be used in high temperature electrochemical applications such as high-temperature solid oxide electrolyzer cells (SOECs).55 However, no study reporting the application of EHEA- and high-entropy superalloy-based electrode materials in the electrochemical process has been published.
As configurational entropy increases in HEAs, Gibbs free energy decreases, enhancing system stability and promoting compatibility, favoring solid solution formation over intermetallic compounds, thereby improving thermodynamic stability.29,58–60 Moreover, the increase in configurational entropy significantly reduces the mixing kinetic energy barrier of constituent elements in HEAs, enabling adjustment and optimization of electronic and crystal structures for the development of HEA-based materials as potential electrocatalysts.61–63 For instance, random surface mixing in CoMoFeNiCu-HEA nanostructures, with uniform distribution of Co and Mo sites, facilitates the dehydrogenation of NH3 molecules and desorption of N2 from the HEA surface in catalytic decomposition reactions of NH3 (Fig. 4a).64
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| Fig. 4 (a) Schematic illustration of the rate-limiting factors in NH3 decomposition. Reproduced with permission.64 Copyright 2019, Springer Nature. (b) Schematic diagram of the variation of lattice potential energy and mean difference during the migration of a Ni atom in different matrices. Reproduced with permission.65 Copyright 2013, Elsevier Ltd. (c) Schematic exhibition of the advantages of Fe-enriched FeNi3 intermetallic nitrogen-doped carbon for bifunctional oxygen electrocatalysts. Reproduced with permission.69 Copyright 2021, Elsevier Ltd. | ||
The different elemental compositions redistribute the d-band structure of HEAs and modified density of states (DOS) altering the electronic structure and enhanced active surface sites, which was reflected in their alcohol oxidation efficiency.73,74 Moreover, chemical interaction and charge-transfer kinetics of HEA systems are governed by the developed CE, which can be described by using a potential energy diagram (Fig. 4b).65 Interestingly, a transition metal plays a vital role in creating synergistic interaction, thereby improving the electrochemical performance. Therefore, the CE in HEAs demonstrates significant impact on the electrochemical processes, particularly when incorporating selective transition metals with different d-orbital electronic configurations.71 However, physical consequences of this outcome remain unclear and require further experimental and theoretical investigation of the electronic and structural features to design a potential electrode material.
Thermodynamic features such as mixing enthalpy, configurational entropy, phase diagram representation, and solid solution stability are crucial parameters to characterize high-entropy alloys (HEAs), providing insights into their stability, phase formation, and properties, facilitating tailored designs for specific applications. Similarly, understanding the kinetic properties of HEAs, encompassing phase transformations, diffusion, and microstructural evolution, is essential for optimizing processing conditions, predicting material behavior, and designing HEAs with the desired microstructures and properties. These combined thermodynamic and kinetic effects serve as a foundation for utilizing HEAs as industrial electrode materials, although additional factors must also be considered in their design.
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| Fig. 5 (a–d) Effect of ΔHmix, ΔSmix, δ, and Δχ on phase stability in HEAs. The symbol ○ represents equiatomic amorphous phase forming alloys; ● represents non-equiatomic amorphous phase forming alloys; □ represents solid solution phases and △ represents intermetallic phases. Reproduced with permission78 Copyright 2011, Elsevier Ltd. | ||
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| Fig. 6 (a) Effect of valence electron concentration (VEC) on phase stability in HEAs. The symbol ○ represents equiatomic amorphous phase forming alloys; ● represents non-equiatomic amorphous phase forming alloys; □ represents solid solution phases and △ represents intermetallic phases. Reproduced with permission.78 Copyright 2011, Elsevier Ltd. (b) Relationship between parameters. Reproduced with permission.88 Copyright 2012, Elsevier Ltd. (c) Radius versus electronegativity mismatch for HEAs. Reproduced with permission.82 Copyright 2014, Elsevier Ltd. (d) Thermodynamic phase diagram of HEAs. Reproduced with permission.89 Copyright 2015, Elsevier Ltd. | ||
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This inequality condition includes a criterion for single-phase solid solution formation. Higher excess entropy and mixed enthalpy are observed in multicomponent systems containing amorphous phases, and their formation is almost favorable for obtaining the optimum enthalpy (Fig. 6d).77,89 This result suggests that a lower ratio of these two terms favors the formation of single phase solid solutions where entropy is dominant, and a higher ratio favors the formation of multiphase solid solutions and intermetallic compounds.76 Higher excess entropy and mixed enthalpy were observed in the multicomponent HEA systems containing amorphous phases, and their formation favors a combination of enthalpy and entropy.
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HEAs are grouped differently according to their corresponding Φ values. The different HEAs are separated by a critical value of Φc = 20. Clearly, HEAs exhibit a single-phase solid solution when Φ > Φc and a multiphase, even amorphous, structure when Φ < Φc (Fig. 7a).90 This behavior suggests that Φ is a promising descriptor for ranking HEAs based on their tendency to form single-phase solid solutions (Fig. 7b).90
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| Fig. 7 (a) Plot of Sc versus ϕ for a variety of HEAs with either single- or multiphase structures and (b) X-ray diffraction (XRD) pattern with the ϕ parameter. Reproduced with permission.90 Copyright 2015, Elsevier Ltd. (c) Plot of Λ (=ΔSmix/δ2) and ΔHmix (secondary y-axis) with the alloy number. Reproduced with permission.86 Copyright 2014, Elsevier Ltd. (d) Illustrated generalized thermodynamic phase diagram for equilibrium phases. Reproduced with permission.89 Copyright 2015, Elsevier Ltd. | ||
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The formation of the DSS for HEAs can be understood by considering the Λ parameter and comparing it with the other available parameters. Interestingly, the possibility of DSS is favored by an increased ΔSmix and decreased δ value; consequently, this geometric parameter is useful for identifying the condition of single- (Λ > 0.96), two- (0.24 < Λ < 0.96), and multiphase (Λ < 0.24) HEAs.77,90 A recent report suggested that the δ parameter can effectively predict the formation of different types of phases when compared to previously discussed parameters such as ΔHmix, VEC, Φ, δ, and Δχ parameters (Fig. 7c).86
(a) an atomic radius ratio of less than 15%;
(b) similar crystal structures of the constituent elements;
(c) comparable valency for complete dissolution;
(d) low electronegativity difference to avoid the formation of intermetallic compounds.
The formation of metal solid solutions is primarily governed by two crucial factors: radius mismatch and electronegativity alternation. These rules play a pivotal role in determining the characteristics of a HEA and its derivatives. However, when these factors alone are insufficient to explain HEA properties, other considerations come into play. These additional rules are consulted to fine-tune and optimize HEAs through adjustments in synthesis processes and precursor elements. The strategic design of HEAs for industrial electrode materials is paramount, necessitating meticulous experimental exploration and the judicious selection of elements. Hence, HEA design principles are centered on maximizing configurational entropy, introducing complex atomic arrangements, exploiting atomic size mismatch, and careful selection of the constituent elements to achieve the desired properties and ensure stability.
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| Fig. 8 (a) Synthesis procedure for the preparation of HE-MOF-RT under ambient conditions. Reproduced with permission.98 Copyright 2019, Royal Society of Chemistry. (b) Synthesis and structural characterization of high-entropy layered double hydroxides. Reproduced with permission.109 Copyright 2021, Elsevier Ltd. (c) Schematic illustration of the electrolytic synthesis of HEAs. Reproduced with permission.112 Copyright 2022, Elsevier Ltd. (d) Diagram of lattice distortions and formation enthalpy calculated using density functional theory (DFT) for five MAX phases with Ti, V, Zr, Nb, and Ta species. Reproduced with permission.116 Copyright 2021, Wiley-VCH. | ||
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| Fig. 9 (a) Schematic demonstration of the structure of high-entropy perovskite oxide nanoparticles with uniformly dispersed elements. (b) Configurational entropy of perovskites. Reproduced with permission.126 Copyright 2022, Wiley-VCH. (c) Unit crystal structure of anti-perovskite nitride. Reproduced with permission.144 Copyright 2023, Elsevier Ltd. (d) Synthesis of high-entropy perovskite fluorides. Reproduced with permission.145 Copyright 2020, American Chemical Society. | ||
m) (CrMnFeCoNi)9S8 (Fig. 10a).This high-entropy sulfide exhibited promising OER activity and stability owing to the high configurational entropy resulting from the presence of multiple components (Fig. 10b).147 A wurtzite-type HES (Zn0.25Co0.22Cu0.28In0.16Ga0.11S) was developed by McCormick et al. via a simultaneous multi-cation exchange synthetic route.150 HESs with their large number of randomly distributed elements, possess unique catalytic, electrochemical, and mechanical properties. The choice of the metal significantly influences the electrocatalytic performance since they serve as active centers in the electrochemical process. The OER performance of quaternary HESs was improved by the selective choice of Mn and Al metals, which can be attributed to the strong interaction among the multiple metals and sulfur that regulates the electronic structure of the overall HES.148 The phase structure of the HES can be optimized by using the metal-to-sulfur ratio, and a decrease in the metal-to-sulfur ratio increases the possibility of single-phase HES formation, as confirmed by the mechanochemical synthesis of (FeMnNiCoCr)S2, (FeMnNiCoCr)S2, (FeMnNiTiCr)S2, and (FeMnNiCoCu)S2. Interestingly, all these materials are used as active anode electrodes for Li-ion batteries (LIBs) by following intercalation and deintercalation mechanisms.149 Typically, most of the synthesized HESs can be potential candidates for OER electrodes because of the favorable formation prospect of (oxy)hydroxide intermediates.147–149,152
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| Fig. 10 (a) Schematic demonstrating the structure and activity of high-entropy metal sulfide ((CrMnFeCoNi)Sx) nanoparticles. (b) Calculated catalytic activity volcano plot. Reproduced with permission.147 Copyright 2021, Wiley-VCH. (c) DFT calculation in the edge mode; crystal structure of the monoclinic structure, (d) structural polymorphs of CoPS3 and CoVMnNiZnPS3 along the top views, and (e) hydrogen evolution reaction free-energy diagram of the corresponding edge sites. Reproduced with permission.155 Copyright 2022, American Chemical Society. (f) Elements in the synthesized high-entropy carbide (HEC) system. Reproduced with permission.166 Copyright 2013, American Chemical Society. | ||
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| Fig. 11 Identified crystal structures of (a) HEAs and (b) HECs used in energy-related fields. Reproduced with permission.177 Copyright 2021, Royal Society of Chemistry. (c) Crystal structures and their correlation with the enthalpy of mixing (ΔHmix) and atomic-size difference (δ) in various HEAs. Reproduced with permission.80 Copyright 2014, Spinger Nature. (d) VEC value with different phases of HEAs. Reproduced with permission.179 Copyright 2016, Elsevier Ltd. | ||
(a) FCC structure for VEC ≥ 8,
(b) BCC structure for VEC < 6.87, and
(c) mixed FCC + BCC structure for 6.87 ≤ VEC < 8.
The presence of Group 13 elements such as Al with larger atomic sizes than those of the principal elements generates less atomic packing and selective transformation of the FCC to the BCC structure. Above all, Al strongly reduces the local energy of the transition-metal atoms by p–d hybridization, which determines the overall structure of the HEA.184,185 Therefore, the addition of certain metals leads to a specific structure determined by the periodic placement of the metal, altering the original structure (BCC, FCC, and HCP).183,184 In HEAs such as AlxCrFeCoNi, the local energies suggest that Cr and Fe stabilize the BCC structure, whereas Co and Ni act as FCC stabilizers.
Interestingly, the structural features have no direct impact on the electrochemical performance of the HEAs as electrocatalysts or electrode materials. However, they exhibit an indirect influence on the strategic design of HEAs as they guide the selection of compatible metals from a structural perspective. Interestingly, BCC single-phase structures have attracted extensive attention in several fields, including hydrogen storage, owing to their unique structural characteristics because of their diverse composition, designable phase structure, and superior performance.186–188 The three primary crystal structures (BCC, FCC, and HCP) of HEAs can significantly impact their performance as electrode materials in electrochemical processes. BCC HEAs typically exhibit high strength and hardness but are also relatively brittle. They are more prone to forming passive films on their surfaces, enhancing their corrosion resistance. In addition, BCC HEAs are more susceptible to hydrogen embrittlement, compromising their toughness and ductility. FCC HEAs are generally more ductile and tough than BCC HEAs but less likely to form passive films.184,187,188 They are more resistant to hydrogen embrittlement and may exhibit favorable electrochemical performance in applications such as batteries, fuel cells, and electrochemical sensors. Consequently, FCC HEAs are preferred for energy storage applications owing to their high ductility and toughness. These are crucial parameters as batteries undergo significant volume changes during charging and discharging cycles. FCC HEAs have also demonstrated favorable Li-ion diffusion kinetics.175–179 HCP HEAs, which are less common than BCC and FCC HEAs, often exhibit properties that combine those of BCC and FCC HEAs. They can be strong and ductile while also resistant to hydrogen embrittlement (Table 2). However, HCP HEAs are susceptible to corrosion, which can be beneficial for electrochemical sensors. HCP HEAs are less likely to form passive films, a property that is advantageous when developing electrode materials for fuel cells. The good electrical conductivity and corrosion resistance properties of HCP- and FCC-based materials make them promising candidates for electrochemical sensors. Moreover, the large interstitial space in the BCC structure enhances ion diffusion performance, making it a potential electrode material for energy storage applications where charge is stored via ion diffusion.39,179
| Crystal structure | Strength | Toughness | Ductility | Ion diffusion | Corrosion resistance |
|---|---|---|---|---|---|
| FCC | Medium | High | High | Medium | Medium |
| BCC | High | Low | Low | High | High |
| HCP | Medium | Medium | Medium | Low | Low |
The presence of different crystal structures, such as FCC, BCC, and HCP, changes the electronic structure and creates distinct active sites, affecting the adsorption of reactant molecules and reaction kinetics. Therefore, while the electrochemical performance of a HEA is influenced by its crystal structure, the composition of the HEA, the specific environment, and the intended electrochemical application also play an important role in determining the behavior of each structure. Researchers often modify the composition and crystal structure of HEAs to take advantage of the unique properties of each crystal structure to optimize the electrochemical performance for a particular application. Certain crystals can provide exposed active sites of catalytically active metals or active crystal planes in certain electrochemical processes, and thus crystal structures can enhance the performance of HEA systems. For example, Cu atoms are stabilized by other metals in the FCC-facet crystalline structure of the AuAgPtPdCu HEA, which has been used as a potential electrode material for the CO2 reduction reaction (CO2RR).189 Another report suggested that a HEA with a Ni20Fe20Mo10Co35Cr15 FCC crystal structure has a greater number of coordination sites than that of the dual-phase structure (FCC+μ) and exhibited better HER catalytic performance in both acidic and alkaline media.190–193 Single-phase HEAs are more catalytically active than mixed or multiphase materials owing to their more exposed active sites. Therefore, the crystalline nature of HEAs has an influence on the electrochemical activity; consequently, strategic designing of HEAs is achievable by understanding their applicability and possibilities (Table 3).186–200 HECs can exhibit a variety of crystal structures, depending on the composition of the material and the processing conditions (Table 4).201–213 These varied crystal structures depend on metal ions and the counter anion 3d spatial arrangement of HECs (Fig. 11b).177 The crystal structure of HECs can significantly impact their electrochemical behavior and applications.
| HEA | Phase | Synthesis method | Electrochemical process | Reference |
|---|---|---|---|---|
| PtFeCoNiCuAg | FCC | Sputter | MOR | 186 |
| IrOsReRhRu | HCP | Pyrolysis | MOR | 187 |
| AlCoCrFeNi | FCC + HCP | Dealloying | Corrosion resistance | 188 |
| AuAgPtPdCu | FCC | Mechanical milling | CO2RR | 189 |
| NiFeMoCoCr | FCC/FCC+μ | Arc melting | HER | 190 |
| FeCoPtPdIr | FCC | Moving bed pyrolysis | HER | 191 |
| IrPdPtRhRu | FCC | Polyol method | HER | 192 |
| MnFeCoNiCu | FCC | Solvothermal pyrolysis | OER | 103 |
| AlNiCoFeX (X = Mo, Nb, Cr) | FCC | Top-down synthesis | OER | 194 |
| CoFeLaNiPt | Amorphous | Electrosynthesis | WS | 195 |
| PtAuPdRhRu | FCC | Wet chemistry | WS | 196 |
| AlNiCoIrMo | FCC | Dealloying | WS | 197 |
| AlCuNiPtMn | FCC | Dealloying | ORR | 198 |
| PtPdFeCoNi | FCC | Carbothermal shock | ORR | 199 |
| Hollow RuIrFeCoNi | FCC | Droplet-to particle | Li–O2 battery cathode electrode | 200 |
| HECs | Structure | Crystallography | Reference |
|---|---|---|---|
| High-entropy oxide (HEO) | Rock salt | Cubic (Fm m) |
201 |
| Fluorite | A2B2O7 cubic (Fm m) |
202 | |
| Perovskite | ABO3 orthorhombic (Pbnm) | 203 | |
| Perovskite | ABO3 cubic (Pm3m) | 204 | |
| Perovskite | ABO3 hexagonal (P63/mmc) | 205 | |
| Spinel | AB2O4 cubic (Fd m) |
132 and 206 | |
| Pyrochlore | A2B2O7 cubic (Fd m) |
207 | |
| High-entropy nitrides (HENs) | NaCl-type | Cubic (Fd m) |
208 |
| High-entropy carbides (HECbs) | Rock-salt (NaCl-type) | Cubic (Fd m) |
209 |
| High-entropy borides (HEBs) | AlB2 | Hexagonal (P6/mmm) | 169 |
| High-entropy silicides (HESis) | CrSi2 prototype | Hexagonal (P6222) | 211 |
| High-entropy fluorides (HEFs) | Perovskite | ABF3 cubic (Pm3m) | 145 and 212 |
| High-entropy phosphates (HEPO4) | Monazite-type | Monoclinic (P21/n) | 213 |
The properties of HECs, such as surface area, electronic structure, and reactivity, greatly affect their electrocatalytic performance.194–197 Furthermore, HECs with narrow band gaps tend to have higher electrocatalytic activity than those with wide band gaps. This is attributed to the easier electron transfer from HECs to reactants, which promotes electrochemical reactions. Furthermore, the reactivity of HECs plays an important role in their electrocatalytic performance (Table 5). It is important to note that factors such as composition, particle size, and microstructure also influence the electrocatalytic activity of HECs.197–200 Although research on HEC electrocatalysts is still in its early stages, current findings show great promise. HECs have a wide variety of potential applications, including energy production, fuel cells, and water electrolysis.
| Crystal structure | Electronic structure | Surface area | Reactivity | Electrocatalytic performance |
|---|---|---|---|---|
| Rock-salt | Narrow | High | High | High |
| Perovskite | Wide | Low | Medium | Medium |
| Fluorite | Wide | High | Low | Low |
| Spinel | Medium | Medium | Medium | Medium |
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| Fig. 12 (a) Free energy diagram. Reproduced with permission.219 Copyright 2021, Wiley-VCH. (b) OH* adsorption energies. Reproduced with permission.220 Copyright 2019, Elsevier Ltd. (c) Contour plot for adsorption energy. Reproduced with permission.226 Copyright 2022, American Chemical Society. (d) Schematic illustration of the combinatorial and high-throughput synthesis of HEAs and (e) compositional designs and their corresponding oxygen reduction reaction (ORR) performances presented in a neural network diagram. Reproduced with permission.199 Copyright 2020, PNAS. | ||
In contrast, MD simulations are better suited for studying materials with multiple elements because they can handle larger systems with shorter computation times. However, a major limitation of MD simulations is that they disregard interatomic potentials, making it challenging to elucidate the complex chemistry of multicomponent ceramics. These methods have inherent limitations, which become even more complex when considering HEAs and their electrochemical performance. Challenges include high operational costs, inadequate experimental conditions, and hypothetical structures that lack thermodynamic stability. In recent years, the combination of big data and artificial intelligence (AI) has advanced owing to the progress of material genomics projects and rapid development of AI technologies.214–216 ML is a crucial subfield of AI that utilizes various algorithms to build models, uncover potential relationships from historical data, and design new HEA-based materials for specific applications, such as electrocatalysts.223 The ML approach involves rapid screening of a vast number of target property combinations required for catalytic applications. This can be accomplished through high-throughput (HT) experiments that combine computational and experimental methodologies.
The use of combinatorial synthesis is anticipated to expedite the discovery of new catalysts, enabling screening of a vast array of compositions in samples with tailored compositional gradients for HEAs, which are subsequently screened by machine learning to fabricate HEA-based electrodes. The optimization of existing catalysts and discovery of new catalysts are facilitated by valuable insights gained from the synthesis of new catalysts and theoretical calculations related to HEA-based electrocatalysts. An effective descriptor can expedite the development of ML models and elucidate the fundamental physical principles underlying the catalytic process. The ML approach can be employed to design HEA-based electrode materials for a wide range of industrial applications, including batteries, fuel cells, and sensors. This can contribute to the accelerated development of new and improved electrode materials with tailored properties.
A ML approach to develop HEA-based industrial electrode materials can be divided into the following steps: (a) data collection and preparation, (b) feature engineering, (c) model selection and training, and (d) model validation and deployment.215 ML is a powerful tool for accelerating catalyst discovery as it can be used to construct highly accurate models, predict the catalytic performance of uncharacterized catalysts, and elucidate structure–property–performance relationships, particularly for HEA catalysts with vast compositional spaces. The key to successful ML models lies in the utilization of suitable general descriptors that can accurately and comprehensively represent the structural information of the catalysts. An effective descriptor can expedite the development of ML models and uncover the fundamental physical nature of the catalytic process. HT techniques are essential for scientists to efficiently generate large databases and subsequently extract valuable information.
For HEAs with vast compositional spaces, HT techniques can be effectively employed to discover and develop HEAs. HT techniques can achieve more automated, parallel, and efficient HEA research.224 Singh et al. employed ML and DFT to predict the adsorption free energy of key reaction intermediates on HEAs, thereby quantitatively unifying the ligand (element identity) and coordination (surface structures) effects for HEA catalysts. A neural network (NN) model was utilized to evaluate the OH* adsorption energy over the IrPdPtRhRu HEA catalyst.225 These results suggest that electrochemical ability and structure–activity relationships of HEAs can be evaluated using ML via NN models. With the understanding of catalytically active sites, stability and activity are two crucial parameters for HEA-based electrocatalysts. ML tools have successfully identified the most promising composition with the highest catalytic stability and activity among Cu, Co, Ni, Zn, and Sn-based HEA alloys. The designed electrode materials have exhibited promising activity, selectivity, and stability toward CO2 hydrogenation to methanol. The DFT-calculated adsorption energies of the Cu (111) surface displayed good agreement with the ML-based results. Using screening criteria and considering the pure Cu (111) surface as a reference catalyst, contour plots were used to identify 35 active and selective catalysts for methanol formation, among which 34 were HEA catalysts and one was a medium-entropy alloy (Fig. 12c).226 Pedersen et al. proposed a method for discovering selective and active catalysts for the reduction of CO2 and CO on HEAs.227 The CO and H adsorption energies of all sites on the Cu (111) surfaces of disordered CoCuGaNiZn and AgAuCuPdPt HEAs were predicted by combining DFT with Gaussian process regression. This enabled the optimization of the HEA composition, increasing the likelihood that weak hydrogen-adsorbing sites can suppress the formation of molecular hydrogen.
The combination of a ML approach and experimental testing of PtFeCu NPs for the ORR was demonstrated by Chun et al.228 In the optimization of the PtFeCu alloy ratio, low PtFe and high Cu amounts exhibited the best catalytic performance among the ternary samples. Thus, ab initio computations with an ML approach can provide a solution for the design of nanocatalysts, thereby bridging the gap between the experiment and simulation. A HT combinatorial synthesis method yielded polymetallic HEAs with tailor-made surface chemistry that demonstrated significant potential for catalytic applications such as PtPdFeCoNi and PtPdRhNi HEAs as HER electrode materials (Fig. 12d and e).119,199,228
Recently, HT characterization datasets were used as an input for the refinement of the model. The refined model could correctly predict activity maxima of the Ag–Ir–Pd–Pt–Ru model system.229 The method has exhibited unprecedented power for the identification of optimal complex solid solution materials for electrocatalytic reactions. To identify complex solid solution compositions with high electrocatalytic ORR activity, they combined simulation, ML, data-driven combinatorial synthesis, and HT characterization. Banko et al. applied a combinatorial strategy to acquire large experimental data sets of 5D compositional spaces and the RuRhPdIrPt HEA system.230 Both advanced simulations (ML) and extensive experimental data analysis are used to estimate the electrocatalytic OER activity and solid solution stability trends in the 5D compositional space of the HEA system (Fig. 13a).230 Therefore, HT and ML models are two complementary approaches for designing the most promising HEA system for electrochemical studies. Before designing an industrial electrode material, it is essential to utilize theoretical and computational tools. These tools not only minimize time and chemical wastage but also aid in selecting the optimal route and composition for achieving the highest catalytic efficiency in HEA alloy-based electrode design.218
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| Fig. 13 Activity map and high-throughput screening. Reproduced with permission.230 Copyright 2022, Wiley-VCH. | ||
Table 6 shows the effect of specific periodic elements on the microstructure and properties.
| Element | Physical property | Chemical property | Other |
|---|---|---|---|
| Fe | — | Change in magnetism | No effect on the solid solution phase or microstructure |
| Al | Increases porosity | — | Favors the FCC or BCC phase structure |
| Ti | Increases hardness and strength | Increases lattice distortion | Favors the BBC lattice structure |
| Zr | Reduces strength and plasticity | — | Intermetallic compound |
| V | Increases hardness and strength | Reduces oxidation resistance | Favors nanoparticle formation |
| Au | — | — | Cr, Mo, Fe, Ni, and Cu |
| Cu | — | — | Favors FCC solid solution |
| Ni | — | Paramagnetism | Favors FCC solid solution |
| Co | Improves wear resistance | Ferromagnetism | Favors FCC solid solution |
| Cr | Reduces strength and hardness | Favors BBC solid solution | |
| Mo | Increases strength, hardness, and plasticity | Greater lattice distortion | Favors BBC solid solution |
| Mn | — | — | Reduces oxidation possibility |
The utilization of HEAs is increasing with the strategic modification of the structure, electronic environment, and compositional integrity. Several designing strategies have been proposed to achieve potential activity, and they can be successfully exploited in industrial processes. The well-explored techniques are presented subsequently.
The tri-functional electrocatalytic performance of convex-cube-shaped Pt34Fe5Ni20Cu31Mo9Ru nanocrystals is attributed to the formation of specific surface facets, strain, and coordination environments over the surface atoms of HEA catalysts.232 Usually, high-index facets are more active and exhibit higher catalytic activity than low-index facets owing to the cleavage and formation of chemical bonds. Along with morphology, particle size of the HEA has played an important role in adsorption and desorption processes at the electrode–electrolyte interface. Homogenous distribution and tuned particle size of the HEA can improve the electrode performance by improving the catalytic selectivity by altering the reactant or intermediate adsorption configuration. The orbital hybridization and overall charge transfer between metals and reactants exhibit a pronounced effect on the electronic structure of HEA NPs, which enhanced the electrocatalytic performance of PtRuNiCoFeMo HEA nanowires, resulting in high mass and specific activities for alkaline hydrogen oxidation reaction (HOR).233 Huang et al. synthesized defect-rich HEA nanowires that can achieve the electron transfer effect within the lattice structure.233 A 14-element nanoporous HEA (comprising Al, Ag, Au, Co, Cu, Fe, Ir, Mo, Ni, Pd, Pt, Rh, Ru, and Ti) was synthesized using the dealloying method, which was used as it can accommodate a far greater number of elements, resulting in a stable electrode material for water electrolysis.234 Transmission electron microscopy (TEM) analysis of the alloys showed a hierarchical, nanoporous, and nanocrystalline FCC structure with uniformly distributed elements; besides, Al leaching increased the number of accessible active sites on the surface structure (Fig. 14a).234 Recently, Guo et al. proposed a new technique to improve faradaic efficiency by forming ultrathin noble-metal-based PtPdIrRuAg HEA sub-nanometer ribbons via galvanic exchange reactions between different metal precursors and Ag nanowire templates (Fig. 14b).235 The 2D structure of the PtPdIrRuAg HEA provides large specific surface area, abundant active sites, and high density of unsaturated atoms, making it a potential candidate for the ORR.
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| Fig. 14 (a) Transmission electron microscopy (TEM) image of a HEA, Reproduced with permission.234 Copyright 2021, Royal Chemical Society. (b) High-angle annular dark-field scanning TEM (STEM) image and energy-dispersive X-ray spectroscopy (EDS) element mapping images of one segment of an HEA. Reproduced with permission.235 Copyright 2022, American Chemical Society. (c) Screening to design HEAs using frequency. Reproduced with permission.236 Copyright 2017, Elsevier Ltd. (d) Crystalline arrangements and consequences. Reproduced with permission.241 Copyright 2019, Elsevier Ltd. (e and f) Comparison of surface valence band photoemission spectra of HEAs. Reproduced with permission.244 Copyright 2021, Springer Nature. | ||
Miracle et al. summarized the frequency of use of each element in an HEA and confirmed that transition metals are the most frequently used and provide superior electrocatalytic performance (Fig. 14c).236 In particular, energy conversion processes require bifunctional catalysts and a HEA is undoubtedly a good choice. The systematic removal of each element from a Cr–Mn–Fe–Co–Ni quinary alloy system was shown to result in a significant lowering of ORR activity, thus indicating the importance of the synergistic combination of all five elements; this occurred probably because of the formation of a single solid solution phase with altered properties, which aids in overcoming the limitations that occur when using only single elements. The formation of single-solution and homogeneous distributions promotes the development of more active sites over the surface of HEAs, concurrently enhancing their catalytic activity. However, careful selection and compositional optimization are necessary to improve single-element lamination by increasing the number of active sites. The variation of Mn content in the Cr–Mn–Fe–Co–N alloy was experimentally confirmed to lead to superior intrinsic catalytic activity for the ORR.237 These findings underscore the significance of synergistic interactions among the five or more components in the HEA system and the resulting alterations in their electronic properties, overcoming the limitations of individual components.
Thus, multicomponent design strategies offer boundless possibilities for developing advanced catalysts. The synergistic interaction within the HEA system can be enhanced by augmenting the elemental diversity through compositional adjustments in the designed HEA system. An improved AOR performance was observed in senary RuRhPdOsIrPt alloy NPs when compared to ternary PdPtRh, quaternary IrPdPtRh, and quinary IrPdPtRhRu systems, suggesting that catalytic activity increases gradually with the number of components, thereby highlighting the importance of synergistically incorporating multiple metal elements.238 The catalytic performance can be varied by selecting appropriate design methodologies and optimizing the number of elements of the HEA system. Fujita et al. observed that HER and OER performances varied with the optimized compositional, structural, and electronic characteristics. Specifically, their findings suggest that a 12-element HEA is more superior to 14-element HEA systems in terms of the HER rather than OER processes, which contradicts the other findings related to the significant improvement of HEA systems with the increase in the number of elements.234 In an optimized Co0.25Mo0.45Fe0.1Ni0.1Cu0.1 HEA nanostructure, the systematic regulation of the Co/Mo ratio could modulate the chemical and physical properties of the HEA, resulting in an improved catalytic performance for the NH3 decomposition process.64 A rational configuration of the HEA electrocatalyst can adjust the adsorption energy of intermediate species to enhance the reaction rate.239 Low-electronegativity Mn and high-electronegativity Cu were combined with base metals (Fe, Co, and Ni) to form FeCoNiCuMn HEA NPs, which resulted in strong local electron interactions owing to the difference in electronegativity values. The theoretical interpretation is that the inactive Cu moves to the electron-rich active sites, resulting in lower adsorption energies of reactants, intermediates, and products, which increase the HER and OER activities of the HEA.240 Therefore, by combining experimental and theoretical understanding with specific compositional outputs, optimized, active, stable, and efficient HEAs can be obtained.
HEAs typically exhibit numerous surface defects, owing to the complexity of their structures as they are composed of five or more elements in equal or nearly equal concentrations. This high elemental diversity can lead to a variety of structural imperfections, such as vacancies, dislocations, and grain boundaries (Fig. 14d).241 Surface defects can be used to improve the catalytic activity of HEAs for the HER. For instance, Kruzic et al. developed a new high-entropy metallic glass via dealloying to create a nanoporous structure,242 as a result of the large specific surface area with defects. The theoretical studies confirm that surface defects play a key role in improving catalytic activity and act as nucleation sites for the formation of hydrogen bubbles, which is a crucial step and helps in reducing the energy barrier for the HER. Surface defect modification in HEAs is still at an early stage, but it has the potential to pave the way for the development of novel and enhanced HER catalysts based on HEAs. HEAs are susceptible to forming defects, including vacancies, dislocations, and stacking faults, which can enhance electrocatalytic activity by creating more exposed sites. With a deeper understanding of defect engineering, more efficient HEAs can be developed, showcasing enhanced properties and innovative functionalities.
The occurrence of strain in HEAs has significant effects on their electrocatalytic performance. First, strain can alter the electronic structure of HEAs, making them more active for specific electrocatalytic reactions. For instance, strain can increase the DOS near the Fermi level, enhancing the activity of HEAs in reactions involving electron transfer. Second, strain can improve the stability of HEAs, making them more durable in electrocatalytic applications in harsh electrochemical processes in industry. The improved stability originates from the strain-induced alteration of atomic arrangements and the stabilization of active sites on the surface and subsurface. Third, strain can increase the number of active sites on the surface of HEAs, further improving their electrocatalytic performance. However, strain can induce the formation of dislocations and other defects on the HEA surface, which can serve as additional active sites for electrocatalytic reactions. The d-band center is significant for HEA electrocatalysis as it determines the strength of the interaction between the multimetallic catalyst surface and the reactant molecules. A stronger interaction between the HEA-based electrode surface and electrolyte leads to a lower energy barrier for the charge-transfer process, resulting in improved electrode activity. Thus, strain engineering is a promising strategy for improving the electrocatalytic performance of HEAs. By carefully controlling the strain in HEAs, new and improved electrocatalysts can be developed for a variety of applications. The work of Rossmeisl et al. provides a new understanding of how lattice distortion affects the adsorption energies of OH* and O* on IrPdPtRhRu and AgAuCuPdPt HEAs and is important for understanding the effects of distortion and its consequences.243
Lattice distortion effectively alleviates the impact of local strain on adsorption energies due to the relaxed atomic environment surrounding the bonded atoms. This suggests that the effect of local strain on HEA activities is minimal, and the broadening of the adsorption energy distribution primarily occurs because neighboring atoms disturb the electronic environment of the binding sites. This finding holds significant implications for the design of HEAs for catalytic applications. TEM and scanning TEM (STEM) analyses implied that strain-induced PtFeCoNiCu HEAs obtained via heat treatment at 700 °C (HEA-700) exhibited 0.94% more compressive strain than the HEA obtained at 400 °C (HEA-400).244 The enhanced methanol oxidation reaction (MOR) activity can be attributed to the shorter Pt–Pt bond distances resulting from the compressive strain of HEA-700. Furthermore, a comparison of the d-band centers of the HEAs in the surface valence band emission spectra demonstrated that the development of compressive strain lowered the d-band center, leading to improved catalytic performance at higher temperatures (Fig. 14e).244
Strain in HEAs can also affect surface morphology, forming strain-induced defects such as dislocations, vacancies, and grain boundaries. These defects may act as active sites for catalytic reactions, providing new reaction pathways or altering the adsorption behavior of reactants. In addition, strain-induced defects can also alter mass transport properties and charge-transfer kinetics, affecting the overall electrocatalytic activity as defects provide a heterogeneous surface for catalysis. For example, Huang et al. fabricated single-phase FCC MnFeCoNiCu HEA NPs of less than 5 nm.233 These NPs exhibited a highly deformed lattice, resulting in various defects (e.g., twins, dislocations, and stacking faults) and act as active sites for the ORR.245 Strain engineering is a promising strategy for improving the electrocatalytic performance of HEAs. Although there are still some gaps in our understanding of the optimal methods for introducing and controlling strain in high-entropy alloys (HEAs), this approach has great potential for advancing the development of novel and improved HEA electrocatalysts.
An upward shift of the d-band center leads to stronger interactions within metals, while a downward shift represents the opposite. Additionally, the electronic structure of HEAs is influenced by the so-called ligand effect where the interactions between the d-bands of the constituent metals can alter the d-band centers of the active components.246–248 This modulation affects the binding energies of the key intermediates, ultimately improving the activity and selectivity.71,247–249 For instance, the projected DOS (PDOS) of nanoporous AlNiCoIrMo HEAs reveals a shift in the d-band center of Ir following alloy formation, leading to stronger Ir–O covalent bonds which further contribute to the enhanced OER activity. By strategically designing and optimizing the composition of HEA components, the adsorption energy of the d-band center can be continuously tuned, enabling the modulation of key intermediates and ultimately achieving optimal catalytic performance (Fig. 15a).197
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| Fig. 15 (a) Projected partial density of states of HEA d-states. Reproduced with permission.197 Copyright 2019, Wiley VHC. (b) Raman spectra. (c) Schematic of the band structure. Reproduced with permission.254 Copyright 2017, Royal Chemical Society. | ||
The shift in the d-band center is a consequence of strain formation and simultaneously affects the charge-transfer ability and bandgap alteration within the compositionally complex HEAs.250–253 A lowering of the bandgap was observed by Sarkar et al. during the synthesis of fluorite-type rare-earth HEO. The presence of Pr with oxidation states other than 4+ results in the formation of oxygen vacancies in multicomponent equiatomic rare-earth oxides, which was confirmed by Raman spectroscopy and a reduction in bandgap due to electronic state involvement (Fig. 15b and c).254 The charge redistribution on the surface of HEAs is an inimitable and important property that can be used to enhance their catalytic activity.255 The alteration in local charge density generates active sites for the adsorption and activation of reactant molecules.256–259 Moreover, it influences the d-band centers of the alloy, thereby modifying the adsorption modes of reactants and further impacting catalytic activity and selectivity. HEAs, with their diverse compositional metals, possess the potential to exhibit pronounced surface charge redistribution, inducing an alternating pattern of electron accumulation and depletion across the entire HEA surface.254–259 This implies that the charge density of each surface metallic atom differs from that of its neighboring atoms in HEAs, creating a greater number of active centers for chemical transformations.260 Hence, careful selection of components with differing work functions for HEA synthesis allows for control over the surface charge density of HEAs. This contributes to the adsorption and activation of reactants, further enhancing the catalytic performance of HEA-based catalysts for industrial applications.
| Synthesis | Equipment | Condition | Synthesis time | Size | Element distribution | Product percentage |
|---|---|---|---|---|---|---|
| Mechanical alloying | Planetary ball mill | RT, air | >1 day | Micrometer range | Poor | ≥10 g |
| Spark discharge | Spark discharge | High voltage | Fraction of a second | Nano- to micrometer | Good | Above 80 |
| UAWC | Ultrasonicator | Below 100 °C | Nanometer | Good | Above 70 | |
| Dealloying | Smelting furnace/Spinning machine | ≤500–700 °C and 1 atm, both inert and air atmospheres | ≥2 h and ≤5 h | Pore size within 10 nm | Good | ≥10 g |
| One-pot synthesis | Hydrothermal reactor and furnace | High temperature, inert or air atmosphere | Few minutes to a day depending on the process | Variable | Good | ≥10 g |
| Calcination-assisted method | Furnace | High temperature, above 500 °C | Few hours | Porous structure | Good | 50–90 |
| Electrodeposition method | Electrochemical set up | Room temperature, air | Few minutes to several hours (≤24 h) | Nanometre range | Good | ≤10 mg |
| Sputtering deposition and electrospinning method | UHV deposition system | RT/Ultrahigh vacuum | >25 h | ≤1–10 nm | Good | <200 mg |
| Carbothermal shock method | Current pulse device | 1 atm and > 1000 K and an inert atmosphere | Millisecond | Nanometre range | Good | <200 mg |
| Fast moving bed pyrolysis | Tube furnace | ≤1000 K and an inert atmosphere | Few seconds | 5–50 nm | Good | ∼100 mg |
| Laser scanning ablation technology | Pulsed laser | RT, air | Millisecond | Good | ||
| Microwave heating | Microwave reactor | ≤2000 K | Few seconds | ≤20 nm | Good | ≤10 mg |
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| Fig. 16 (a) Synthesis procedure of HEAs by cryomilling. Reproduced with permission.266 Copyright 2021, American Chemical Society. (b) Ultrasonic-assisted wet chemistry method for HEA design. Reproduced with permission.268 Copyright 2019, Wiley VCH. (c) Dealloying method for HEA design. Reproduced with permission.234 Copyright 2021, Royal Chemical Society. (d) One-pot synthesis procedure and STEM-EDS of the HEA system. Reproduced with permission.275 Copyright 2019, Wiley VCH. | ||
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| Fig. 17 (a) Contour maps of the composition of different elements deposited at various Ton and Toff values. Reproduced with permission.281 Copyright 2023, Elsevier Ltd. (b) Electrochemical approach to synthesize HEAs. Reproduced with permission.287 Copyright 2023, The Royal Society of Chemistry. (c and d) Carbothermal shock synthesis of HEA nanoparticles. Reproduced with permission.288 Copyright 2018, AAAS. | ||
Electrospinning is an advanced, inexpensive, and extended technique of sputtering deposition and can be used to produce nanofibers from a variety of materials, including polymers, metals, and ceramics. To synthesize HEAs using electrospinning, a metal precursor solution is typically used that contains all the desired alloying elements in the anticipated proportions. The precursor solution is then electrospun to produce HEA nanofibers. However, note that the electrospinning process is sensitive to multiple factors, such as the type of solvent, precursor solution concentration, and applied voltage. Consequently, producing HEA nanofibers with a consistent composition and microstructure is difficult. By combining the electrospinning technique and graphitization process, Hao et al. synthesized FeCoNiMnRu HEA NPs with potential water electrolysis efficiency due to the modified electronic structure.285 The difference in electronegativity values between the mixed elements in the HEA induces significant charge redistribution, creating highly active Co and Ru sites with optimized energy barriers for simultaneous stabilization of OH* and H* intermediates, thereby significantly improving water dissociation efficiency under alkaline conditions.285 A similar approach was involved in the synthesis of FeCoNiMoRu HEA NPs supported on carbon nanofibers (CNFs). The in situ electrochemical Raman results demonstrated that the Fe, Co, Ni, and Ru metal sites are involved in synergistically catalyzing urea electro-oxidation.286 Dual-phase B-doped FeCoNiCuPd HEA (DP-B-HEA) NPs with superior NRR ability were in situ grown on electrospun CNFs via the thermodynamically driven solid-phase diffusion approach by combining the electrospinning technology with the high-temperature carbonization approach (Fig. 17b).287In situ characterization confirmed that CNFs were used as hosts to control the phase stability of DP-B-HEA NPs via the unique dual phase and electronic structure modification of B atoms. Electrospinning, a versatile technique for fabricating nanomaterials with tunable morphologies and properties, exhibits significant potential for the largescale production of HEAs. While HEA production by electrospinning is still in its early stages of development, it offers several advantages compared to conventional synthesis methods.
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| Fig. 18 (a) Schematic diagram of the fast-moving bed pyrolysis experimental setup for synthesis of HEA nanoparticles and compression using fixed bed pyrolysis. Reproduced with permission.191 Copyright 2020, Spinger Nature. (b) Synthesis of HEA nanoparticles using the laser scanning ablation method. Reproduced with permission.291 Copyright 2023, Cell Press. (c) Schematic illustration of the formation of HEA nanoparticles on reduced graphene oxide via microwave heating. Reproduced with permission.293 Copyright 2021, American Chemical Society. | ||
Inductively coupled plasma mass spectrometry (ICP-MS), inductively coupled plasma absorption emission spectrometry (ICP-AES), and inductively coupled plasma optical emission spectrometry (ICP-OES) techniques provide information on the elemental composition of HEA-based electrode materials.234,256 Energy-dispersive X-ray analyses provide information on the homogenous distribution of the HEA. Electron microscopy techniques such as scanning electron microscopy, TEM, and high-angle annular dark-field STEM (HAADF-STEM) are commonly used to reveal the surface morphology, particle size, distribution, and exposed surface area of HEA materials.234,239 Atomic-scale HAADF-STEM and corresponding fast Fourier transform analysis can also help in identifying lattice planes and further refine the crystal structure of HEAs. X-ray photoelectron spectroscopy is another tool that can be used to estimate the chemical composition of HEAs.40,239 Brunauer–Emmett–Teller and Barrett–Joyner–Halenda methods were used to determine the specific surface area, pore volume, and pore size distribution of porous HEAs. XRD analysis determines the phase composition of HEAs from the peak position and intensity. Currently, the HEAs used as catalysts are primarily single-phase HEAs, while only a few two-phase HEAs have been proposed. XRD patterns of single-phase HEAs usually show only a series of diffraction patterns, such as FCC, BCC, and HCP, whereas HEAs with two or more phases show additional diffraction peaks in the XRD patterns.39,257 The oxidation state and local coordination environment of HEA-based electrode materials exhibit a significant influence on their catalytic activity. In particular, oxidation of surface elements and oxide film formation on the HEA surface have been reported to enhance catalytic activity and stability. The chemical state of HEAs can be further confirmed via X-ray absorption spectroscopy, X-ray absorption near edge structure (XANES), and extended X-ray absorption fine structure (EXAFS). In general, the XANES distribution indicates if the constituent elements of the HEA are in the metallic state and have chemical bonding properties. In the case of multi-element HEAs, more types of M–M bonding can be inferred, and the local coordination environment of HEAs is more complex than that of binary alloys. Several methods have been used to characterize HEAs, and the results obtained must be analyzed comprehensively to determine the HEA properties. Characterization methods are essential for ensuring the quality and suitability of HEAs for industrial applications. These methods provide important insights into the structure, properties, and performance of HEAs and enable researchers and engineers to tailor these materials to specific applications.
| Electrode | Synthesis | Electrolyte | Performance η @ 10 mA cm−2, b = Tafel slope | Key points | Reference |
|---|---|---|---|---|---|
| FeCoNiCuMnN/CC-400 | Hydrothermal | Alkaline | η = 184 mV, b = 113 mV dec−1 | Superior corrosion and oxidation resistance | 143 |
| Co0.6(VMnNiZn)0.4PS3 | Solid-state reaction | 1 M KOH | η = 65.9 mV, b = 65.5 mV dec−1 | Exposed S and Mn edge sites and basal P sites | 155 |
| Ni20Fe20Mo10Co35Cr15 | Arc-melting | 0.5 M H2SO4 | η = 107 mV, b = 41 mV dec−1; η = 172 mV, b = 66 mV dec−1 | TM active sites provide corrosion resistance | 190 |
| IrPdPtRhRu NPs | Polyol process | 0.5 M H2SO4 | η = 33 mV, η = 22 mV | HEA NPs contain different atomic arrangements with unique local density of states | 192 |
| AlNiCoIrMo | Dealloying | 0.5 M H2SO4 | η = 18.5 mV, b = 33 mV dec−1 | Synergistic effect | 197 |
| Al87Ag1Au1Co1Cu1Fe1Ir1Mo1Ni1Pd1Pt1Rh1Ru1Ti1 | Dealloying | 0.5 M H2SO4 | η = 32 mV, b = 30.1 mV dec−1 | Synergistic effect and nanoporous structure | 234 |
| Nanoporous Ni14Co14Fe14Mo6Mn52 | One-step dealloying | Alkaline | η = 150 mV @ 1000 mA cm−2 | Synergetic effect of optimized hydrogen adsorption in the segregation area | 271 |
| Mn70Ni7.5Cu7.5Co4.2V4.2Fe2Mo2Pd0.5Pt0.5Au0.5Ru0.5Ir0.5 | One-step dealloying | Alkaline | η = 21 mV, b = 21.5 mV dec−1 | Nano-porous, distribution elements, and strong interaction of mixed-metal elements | 272 |
| NiCoFePtRh NPs | Co-reduction method | 0.5 M H2SO4 | η = 27 mV, b = 30.1 mV dec−1 | Active sites, tunable electronic structures, and synergistic effect improve performance | 278 |
| FeCoNiMnRu/CNFs | Electrospinning | 1.0 M KOH | η = 71 mV @ 100 mA cm−2, b = 67.4 mV dec−1 | Co site facilitates H2O dissociation and Ru sites accelerate combination of H* to H2 | 285 |
| PtIrCuNiCr HEA NPs | Laser scanning ablation | 1 M KOH | η = 200 mV @ 100 mA cm−2 | Strain enhances electrode activity | 291 |
| Pt18Ni26Fe15Co14Cu27/C | One-pot oil-phase synthesis | 1 M KOH | η = 11 mV, b = 30 mV dec−1 | Multiple active sites are effective for intermediate adsorption | 295 |
| PdMoGaInNi | Wet chemical method | 0.5 M H2SO4 | η = 13 mV, b = 108.9 mV dec−1 | Pd–Mo–Ga promising HER catalyst | 298 |
| FeCoNiCuIr | Hydrothermal | 0.1 M HClO4 | η = 71 mV, b = 41.7 mV dec−1 | Incorporation of TM modifies the electronic structure | 299 |
| PdPtRhIrCu | Hydrothermal | 1 M KOH | η = 15 mV, b = 37 mV dec−1 | Coupling and bonding interactions facilitate electron transfer | 300 |
| NiFeCoCuTi | Arc melting | 1 M KOH | η = 209 mV @ 2 A cm−2, b = 43 mV dec−1 | Ni skeleton enhances electron/mass transfer | 301 |
| WMoVNbCeB | Thermal reduction method | 1 M KOH | η = 117 mV @ 50 mA cm−2, b = 111 mV dec−1 | Combination of electron orbit of the outer layer of the element promotes the HER | 303 |
| ZnNiCoIrMn | Sol–gel method | 0.1 M HlO4 | η = 50 mV, b = 30.6 mV dec−1 | Mn incorporation tailors electrode performance | 309 |
The electroactive sites in a self-supported hierarchical nanoporous high-entropy NiFeCoCuTi alloy facilitate electron transfer and mass transportation processes during an alkaline HER process. The multicomponent NiFeCoCuTi alloy serves as a multisite electroactive center that accelerates water dissociation and mediates the combination of H* into H2.301 The enhanced HER activity of PtCoMoPdRh/PtNiMoPdRh HEA nanoflowers is attributed to the multiple active sites in HEAs and the strain effect induced by a unique structure that reduces the water dissociation energy barriers (Fig. 19a).302 The water dissociation activation energy of Pt16 in the Pt35Co5Mo10Pd25Rh25 (111) plane decreases from 0.57 to 0.16 eV as compared to that in the pure Pt (111) plane, indicating a chemical environment that alters the electronic structure and accelerates the Volmer step. The Pt (111) plane is considered to be the main active site for H adsorption, whereas Rh, Mo, Pd, and Co regulate the electronic and chemical environments, which benefits the HER process. Recently, Dong et al. developed three different rare-earth transition-metal HEB structures (WMoVNbCeB (HEB-Ce), WMoVNbSmB, and WMoVNbLaB) and determined that the temperature is a function of the d-band structure, thereby achieving a better catalytic performance at a higher synthesis temperature.303 In HEB-Ce, the d-band center of V, Nb, and Ce moved deep down the conduction band and deviated from the Fermi level, which strengthened the antibonding impact and promoted H2O decomposition. The choice of metal and HBE for the developed electrode materials can judiciously replace commercially used HER electrode materials in PEMWE, AEM, AEMWE, and SOWE systems. In general, HEAs are more efficient and stable than HEC electrodes as HER electrodes, possibly due to the potential mechanistic pathway of the HER process. Therefore, HER-active transition and noble metals can be used to design pristine HEAs for cathode materials for water electrolyzers. Moreover, the choice of electrode also varies depending on the design of the electrolyzer, which should be considered before designing the electrode.
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| Fig. 19 (a) H adsorption over the Pt (111) plane. Reproduced with permission.302 Copyright 2023, Elsevier Ltd. (b) Structural evolution of HEA nanoparticles in terms of the oxygen evolution reaction. Reproduced with permission.304 Copyright 2023, American Chemical Society. (c–e) Electrochemical X-ray photoelectron spectroscopy (XPS) data in the survey mode for HEAs. Reproduced with permission.306 Copyright 2023, Wiley VCH. | ||
OER electrocatalysts play a crucial role in efficient water electrolyzers. Effective OER electrode materials require multifunctional active sites that interact with intermediates such as HO* and HOO* to facilitate the four-electron-transfer water oxidation reaction.112,144,193,206 HEAs exhibit significantly modified local coordination environments and electronic structures owing to the synergistic effects of compositionally complex multimetallic moieties, making them promising OER candidates. Noble metals such as Ir and Ru and their oxides, as well as transition-metal-based metal oxides/hydroxides, demonstrate remarkable OER activity.206,212 Designing active electrode materials for the OER involves incorporating active materials that can effectively regulate the electronic environment of HEA-based materials to achieve enhanced electrochemical performance (Table 9). The structural reconstruction and evolution of active intermediates in IrFeCoNiCu HEA NPs on a carbon-paper substrate led to better OER performance when compared to that of the mono-metallic Ir counterpart owing to the presence of the synergistic effect and modified d-band structure. After electrochemical activation, delamination of the encapsulated carbon layers and the dissolution of the constituent 3d metal atoms (Fe, Co, Ni, and Cu) from the surface of the NP occurred, leaving an Ir-rich shell layer, while the core maintained the homogeneous single-phase HEA structure (Fig. 19b).304 This exposed Ir-rich surface provides a high number of OER active sites and concurrently improves the electrode performance in the water oxidation reaction.
| Electrode | Synthesis | Electrolyte | Performance η @ 10 mA cm−2, b = Tafel slope | Key points | Reference |
|---|---|---|---|---|---|
| FeCoNiCuCrNps | Mechanical ball milling | 1 M NaOH | η = 330 mV, b = 80 mV dec−1 | OER activity optimized by tuning compositions | 63 |
| CoFeNiCrV-LH | Electrochemical method | 1 M KOH | η = 232 mV, b = 38.6 mV dec−1 | Defect-rich, low-crystalline active sites originating from entropy-driven lattice distortions and oxygen vacancies | 112 |
| La(CrMnFeCo2Ni)O3 | Mechanochemical method | 1 M KOH | η = 325 mV, b = 51.2 mV dec−1 | Unique structure forms defects and tunes the structure | 121 |
| (Co, Cu, Fe, Mn, Ni)3O4/MWCNT | Solvothermal synthesis | 1 M KOH | η = 350 mV, b = 59.5 mV dec−1 | — | 132 |
| Cu0.5Fe0.5NNi2Co0.5Fe0.5 | Chemical solution deposition (CSD) | 1 M KOH | η = 370, b = 55 mV dec−1 | Anti-perovskite metal nitrides exclusively for the OER | 144 |
| K0.8Na0.2(MgMnFeCoNi)F3 | Hydrothermal method | Alkaline | η = 314, b = 55 mV dec−1 | High-entropy perovskite fluorides effective for the OER | 145 |
| (CoFeNiMnCu)S2 NPs | Solvothermal method | 1 M KOH | η = 284 mV, b = 57 mV dec−1 | Pyrite structure contains exposed active sites | 152 |
| MnFeCoNiCu HEAN MOFs | Solvothermal method | 1 M KOH | η = 263 mV, b = 43 mV dec−1 | Single-phase FCC HEA nanoparticles with a size of sub 5 nm | 103 |
| AlNiCoIrMo | Dealloying | 0.5 M H2SO4 | η = 233 mV, b = 55.2 mV dec−1 | Mo enhances OER performance | 197 |
| CoCuFeMoOOH | Solvothermal method and electrochemical reconstruction | 1 M KOH | η = 119 mV, b = 48.8 mV dec−1 | Co-based (oxy)hydroxide HEA with M−O covalency enhances the OER | 219 |
| Al89Ag1Au1Co1Cu1Fe1Ir1Ni1Pd1Pt1Rh1Ru1 | Dealloying | 0.5 M H2SO4 | η = 258 mV, b = 84.2 mV dec−1 | Synergistic effect and nanoporous structure | 234 |
| Nanoporous Ni14Co14Fe14Mo6Mn52 | One-step dealloying | 1 M KOH | η = 350 mV, b = 43 mV dec−1 | Porous structure increases electrochemically active area and exposes electrochemically active sites | 271 |
| Mn70Ni7.5Cu7.5Co4.2V4.2Fe2Mo2Pd0.5Pt0.5Au0.5Ru0.5Ir0.5 | One-step dealloying | Alkaline | η = 205 mV, b = 74.2 mV dec−1 | Nanoporous structure, distribution of elements, and strong interaction of mixed-metal elements | 272 |
| LiMoFeCoNi HEH | Coprecipitation method | 1 M KOH | η = 187 mV, b = 82 mV dec−1 | Lattice distortions in HEHs lead to superior performance to that in LEHs | 276 |
| FeCoNiMnRu/CNFs | Electrospinning | 1.0 M KOH | η = 241 mV | Multiple metals serving as active centers | 285 |
| PtIrCuNiCr HEA NPs | Laser scanning ablation | 1 M KOH | η = 176 mV | Strain enhances electrode activity | 291 |
| CoNiFeMnCr | — | 0.5 M H2SO4 | η = 528 mV, b = 150 mV dec−1 | Self-selection and reconstruction improve activity and stability | 306 |
| Ni/CoNiFeMoCr | Polymer/metal precursor spray synthesis | 1 M KOH | η = 350 mV @ 50 mA cm−2 | Multiple active sites | 307 |
| NiMnFeCrCu | Mechanical milling | 1 M KOH | η = 310 mV, b = 83 mV dec−1 | Contains FCC phases and a BCC phase | 308 |
| ZnNiCoIrMn | Sol–gel method | 0.1 M HlO4 | η = 237 mV, b = 46 mV dec−1 | Mn incorporation tailors electrode performance | 309 |
Ru-based ultrasmall FeCoNiIrRu HEA NPs on electrospun CNFs were synthesized, and experimental analyses demonstrated that metal combinations and crystallization temperatures could tune the OER activity. An in situ characterization approach showed that phase transition in the HEA enhances OER efficiency, and thereby achieving a certain specific phase can reduce the required potential for the OER. Theoretical calculations demonstrated that electron density transport occurs from a transition-metal-based low-electronegative element (Fe, Co, and Ni) to a high-electronegative noble metal (Ir and Ru) on FeCoNiIrRu HEA NPs, which promotes the OOH* to O2 transformation.305 The combination of passivation elements and catalytically active elements has played a significant role in designing corrosion resistance and catalytically active electrode materials. Considering this, Ito et. al. systematically designed a nine-element HEA by combining the corrosion-resistant Ti, Zr, Nb, and Mo elements with catalytically active Cr, Co, Ni, Mn, and Fe, which exhibited optimal corrosion resistance and catalytic abilities in terms of the OER.306 The self-selection and self-construction processes control the OER catalytic activity and stability of the HEA system (Fig. 19c–e). The corrosion-resistant multi-element alloys with high catalytic activity are crucial for replacing noble-metal catalysts not only in proton exchange membrane-type water electrolyzers but also in other types of electrolyzers, electrolytic systems, and battery systems. A straight forward and scalable polymer/metal precursor spraying synthesis technique was developed to produce different multi-metal catalyst powders for the OER. Operando Raman spectroscopy results indicated that the formation of multiple M−O active sites on CoNiFeMoCr improved the OER performance.307
In this regard, HEAs containing refractory elements can be an alternative choice for use under harsh electrolyte conditions in water electrolyzers. Specifically, they can be utilized in SOWE systems that operate at high operating temperatures. An improved electrocatalytic property could be attributed to the formation of electrochemically active orthorhombic species with active sites on the NiMnFeCrCu HEA.308 Schuhmann et al. investigated the optimized overall water splitting performance of the CoNiFeMoCr/Nif HEA as an anode and cathode electrode in a three-electrode configuration flow-through cell. They determined that catalyst loading influenced the electrode performance. The designed HEA electrode materials were successfully applied as cathode and anode materials in a membrane electrode assembly comprising 1 M KOH, demonstrating their potential for industrial use.307 In general, HECs are more effective for the oxygen evolution reaction (OER) compared to HEAs due to the possibility of easy formation of the pre-catalyst from the HEC during the OER. Moreover, the choice of metals and anions, and the morphology of the electrode material have a pronounced effect on the electrode performance in the respective electrolyzers.
A proton exchange membrane electrolysis is considered as the most advanced water electrolyzer for hydrogen economy. In this regard, Song et al. synthesized Ir-based electrocatalysts using a ZnNiCoIrX HEA platform containing two elements (X: Fe and Mn) that implied emerging faradaic efficiency.309 Interestingly, the incorporation of Mn in a HEA adjusts the electronic structure of the Ir sites, moving the d-band center away from the Fermi level and weakening the adsorption energy. Compositional engineering adjusts the electronic structure of the active Ir sites, thereby altering the aggregation and adsorption energies and inhibiting elemental dissolution. Choi et al. developed a photothermal method that satisfies the atmospheric pressure, large-area, remote-process, and material selection requirements. They designed and tested polymeric HEA NPs (PtIrFeNiCoCe) with high activity and stability in water splitting over 5000 cycles. This approach is efficient in mass and time productivity and compatible with the atmosphere, achieving the homogeneous synthesis of multi-metal catalysts. These advantages suggest the industrial applicability of HEA-based electrode materials for water electrolysis in different electrolyzer systems (Table 10).310 Moreover, before designing the cathode and anode electrodes, the operating conditions, electrolytic medium, mechanism, and setup should be considered.
| Electrode | Synthesis | Electrolyte | Performance @ 10 mA cm−2 | Key points | Reference |
|---|---|---|---|---|---|
| (CoCrFeMnNi)P | Calcination | 1 M KOH | 1.78 V @ 100 mA cm−2 | Synergistic effect improves electrode activity | 153 |
| Al89Ag1Au1Co1Cu1Fe1Ir1Ni1Pd1Pt1Rh‖Al87Ag1Au1Co1Cu1Fe1Ir1Mo1Ni1Pd1Pt1Rh1Ru1Ti1 | Dealloying | 0.5 M H2SO4 | 1.53 V | Synergistic effect | 234 |
| AlNiCoIrMo | Dealloying | 0.5 M H2SO4 | 1.4 V | — | 197 |
| Nanoporous Ni14Co14Fe14Mo6Mn52 | One-step dealloying | 1 M KOH | 1.48 V | Porous structure increases electrochemically active area and exposes electrochemically active sites | 271 |
| PtIrCuNiCr HEA NPs | Laser scanning ablation | 1 M KOH | 1.42 V | Strain enhances electrode activity | 291 |
The Sabatier principle is a useful guideline for designing ORR catalysts with optimal intermediate adsorption (Table 11). Along with the OER performance, the CrMnFeCoNi HEA demonstrated promising ORR activity with a half-cell potential of 0.78 V and an onset potential of 0.88 V, which are comparable to those of a commercial Pt/C catalyst (Fig. 20a).311 The potential gap (Egap) between the OER overpotential and ORR half-cell potential of CrMnFeCoNi is merely 0.734 V. Considering the ORR efficiency, Zn–air batteries (ZABs) were assembled using the CrMnFeCoNi HEA as the air cathode and zinc foil as the anode. These assembled cells exhibited an open-circuit voltage of 1.489 V, which was 90% of its theoretical limit (1.66 V), a peak power density of 116.5 mW cm−2, and a specific capacity of 836 mA h g−1 and remained stable for over 10 days of continuous cycling, corresponding to 720 cycles at 8 mA cm−2, and 16.6 days of continuous cycling, corresponding to 1200 cycles at 5 mA cm−2 (Fig. 20a and b). A flexible ZAB was assembled using a polished Zn plate (anode) and hydrophilic carbon paper coated with the CrMnFeCoNi HEA as the cathode, with polyvinyl alcohol-KOH-H2O gel as the electrolyte. CrMnFeCoNi-based ZABs could power a red LED while bent at various angles, demonstrating their flexibility during operation (Fig. 20c).
| Electrode | Synthesis | Electrolyte | Performance | Key points | Reference |
|---|---|---|---|---|---|
| np-PtRuCuOsIr | Chemical dealloying | 0.1 M HClO4 | E 1/2 = 0.9 V, ΔE = 36 mV | 1.8- and 3.8-times mass and specific activity than those of Pt/C | 319 |
| Mn70Ni7.5Cu7.5Co4.2V4.2Fe2Mo2Pd0.5Pt0.5Au0.5Ru0.5Ir0.5 | One-step dealloying | Alkaline | E 1/2 = 0.875 V, ΔE = 15 mV | Nanoporous structure, distribution of elements, and strong interaction of mixed-metal elements | 272 |
| AlNiCoRuMo | Dealloying | 1 M KOH | E 1/2 = 0.9 V, ΔE = 50 mV, electron transfer = 3.9 | Ru and Mo enhance activity | 273 |
| PdCuPtNiCo HEAs/C | Seed-mediated co-reduction, heating, and quenching | 0.1 M KOH | E onset = 1.06 V, E1/2 = 0.83 V | Atomic-level mixing creates high interfacial strain | 279 |
| PtFeCoNiCu | Reduction method | 0.1 M HClO4 | E 1/2 = 0.88 V, ΔE = 50 mV, b = 68 mV dec−1, electron transfer = 4 | d-band center of Pt monitors the ORR | 312 |
| rGO@OHEA-mNC nanosheets | Wet chemical | 1 M KOH | E 1/2 = 0.9 V | HEA phase increases mass transfer and electron conductivity | 313 |
| PtPdFeCoNi | Wet chemical | 0.1 M HClO4 | E 1/2 = 0.920 V, ΔE = 50 mV | Core effect improves the ORR | 314 |
FeCoNiMnCu-1000 (1 : 1) |
Solid-state thermal reaction method | 0.1 M KOH | E onset = 0.92 V, E1/2 = 0.78 V | Nanoparticles increase activity | 315 |
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| Fig. 20 (a) Specific capacity comparisons between a CrMnFeCoNi- and Pt/C-based Zn–air battery (ZAB). Photograph of a red LED screen powered by a CrMnFeCoNi-based ZAB is also shown. (b) Galvanostatic discharge–charge curves. (c) Solid and flexible ZAB schematic diagram. Reproduced with permission.311 Copyright 2023, Elsevier Ltd. (d and e) TEM image of a HEA, (f) in situ Raman spectra of a HEA system, and (g and h) ORR performance of a HEA. Reproduced with permission.315 Copyright 2023, The Royal Chemical Society. | ||
In another report PtFeCoNiCu HEA NPs exhibited ORR catalytic mass activity that was 15.8 times higher than that of a Pt/C catalyst.312 DFT results confirmed that multi-element alloying lowered the activation barriers for O–O bond cleavage and changed the binding energy of OOH* intermediates to improve the reaction rate by combining metals with different oxygen affinities. This approach may be promising in the development of ORR catalysts for industrial application. A structurally ordered HEA (OHEA) NP was synthesized on a novel 2D nitrogen-rich mesoporous carbon sandwich framework (OHEA-mNC) via a combination of ligand-assisted interfacial assembly and NH3 annealing.313 XRD spectral analysis and atomic-resolution chemical mapping via TEM confirmed that the HEA was formed in a chemically ordered L12 phase, exhibiting superior activity with a large half-wave potential (0.90 eV). The Pd and Cu atoms promote electron transfer on the HEA surfaces, while Co sites alleviate the eg–t2g splitting effect, enhancing the electron transfer process. Both experimental and theoretical findings indicate that the superior performance stems from the well-designed spatial structure and presence of the stable chemically ordered HEA phase, facilitating fast mass transfer and modulating active sites for adsorbing reaction species and electron transfer during the ORR process. The electrochemical kinetics and stability of Pt-based catalysts are still far from meeting the requirements in practical applications, although progress has been made in this respect. HEA NPs of PtPdFeCoNi were fabricated using a high-temperature injection method by Yu et al.314 which exhibited superior catalytic activity and stability for the ORR owing to the high-entropy, lattice distortion, and slow-diffusion effects of the HEA. Therefore, it can be argued that increasing the minimum concentration of the noble metal enhances the mass transport process, thereby resulting in an enhancement of peak power density.
However, only transition metal-based HEA FeCoNiMnCu NPs encapsulated in N-doped graphitized hollow carbon tubes potentially prevent alloy particle aggregation during the ORR (Fig. 20d and e).315 The in situ XRD technique provided insights into the evolution of HEAs, identifying their formation point at approximately 908 K during the carbonization process (Fig. 20f). The catalyst exhibited superior catalytic activity, demonstrating ideal ORR performance in an alkaline solution. This high performance can be attributed to the synergistic effect of HEAs, high specific surface area, and graphite-encapsulated hollow carbon layer structure. The optimized catalyst demonstrated significant stability due to the carbonaceous scaffolds, outperforming commercial 20 wt% Pt/C–RuO2 in an assembled ZAB (Fig. 20f and h). A peak power density of 81 mW cm−2 and lower voltage gap between charge and discharge diagrams suggests the commercial applicability of the HEA in the ORR. The most critical challenge with non-noble metal-based electrode materials often lies in their lower mass transport efficiency and durability at the cathode in commercial fuel cells. Furthermore, while the highest activities based on rotating disk electrode (RDE) evaluations have been observed with shape-controlled Pt alloys and core–shell structures, whether these highly active ORR electrocatalysts can demonstrate the same enhancement factor in real fuel cells remains an open question. Significant efforts are needed to demonstrate their feasibility in fuel cell applications, ensuring desired performance and durability. Previous discussions have suggested that HEAs, comprising transition metals or a combination of transition metals and noble metals, with promising morphological and electronic properties, have the potential to replace Pt dominance in fuel cells commercially.
The electrocatalytic CO2RR is a multistep process that involves a number of electron and proton transfer reactions.151,189,226 However, high potential and low selectivity often hinder the reaction, leading to a limited reduction product yield. Multiple active sites are essential for facilitating the sequential coupling steps of the electrocatalytic reduction of CO2 that can convert simple molecules into more complex chemicals. The complexity of CO2 reduction arises from the large number of surface–bound reaction intermediates involved, and a variety of reduction products can be generated. As multi-electron reduction reactions require extensive proton and electron transfers through a variety of intermediates, alloys of different metal elements and compositions can significantly affect the types of products that are formed. Because different active sites promote different reactions, further study is required to fully understand the influence of alloys on the CO2RR, especially multi-element alloys (Table 12). Theoretical and experimental understanding suggests that most of the effective catalysts contain Cu or Ag owing to their effective interaction with the intermediate products. Nellaiappan et al. used a cast-cum-cryomilling process to synthesis the nanocrystalline equiatomic AuAgPtPdCu HEA for the efficient electrochemical reduction of CO2 to hydrocarbon (Fig. 21a).189 Although five elements were used, the electrocatalytic activity was primarily associated with the presence of redox-active Cu metal (Cu2+/Cu0), and other metals only provided a synergistic effect. The first-principles-based DFT analysis showed the reversal in adsorption trends for two out of the total eight intermediates of *OCH3 and *O on Cu (111) and HEA surfaces and also confirmed that the conversion of CO2 to gaseous products was low. In a similar approach, Rossmeisl et al. theoretically screened two HEA systems, CoCuGaNiZn and AgAuCuPdPt for the CO2RR.227 Their studies again confirmed that the Cu (111) plane of the FCC HEAs of CoCuGaNiZn and AgAuCuPdPt favored the selective reduction of CO2 to highly reduced products. They also proposed that the selectivity of the CO2RR/CO reduction reaction (CORR) and activity of the CORR are expected to change as the HEA catalysts vary in composition (Fig. 21b). Hence, the conversion efficiency is highly influenced by the specific metallic composition, as well as its variations. This underscores the ability of a model to predict promising catalyst candidates even without prior knowledge of their catalytic properties or the composition of disordered alloys for optimal catalytic performance.
| Electrode | Synthesis | Electrolyte | Performance & key points | Reference |
|---|---|---|---|---|
| (MoWVNbTa)S2 | Chemical vapor deposition method | Aq. 1 M KOH: 1 M choline chloride | Current density: −353, η: −0.76 V vs. RHE (631 mV), TOF: 209 885 h−1, CO Fe: 72% |
151 |
| AuAgPdPtCu NP | Cryomilling | 0.5 M K2SO4 | CH4: 38.2%; C2H4: 29.5%; CO: 4.9%; H2: 27.5%; potential: −0.3 V RHE | 189 |
| Pr0.5Ba0.5Mn0.2Fe0.2Co0.2Ni0.2Cu0.2O3−δ | Sol–gel method | — | CO Fe: 95% | 317 |
| PdCuAuAGBiIn HEA aerogel | Freeze–thaw method | 0.5 M KHCO3 | C1 Fe: 100% at −0.7 to −1.1 VRHE; HCOOH FE: 87.5% | 318 |
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| Fig. 21 (a) Free energy diagram of the CO2 reduction reaction (CO2RR) on the HEA surface. Reproduced with permission.189 Copyright 2020, American Chemical Society. (b) Activity and selectivity plot of theoretically designed HEAs. Reproduced with permission.227 Copyright 2019, Wiley VCH. (c) Faradaic efficiency of the designed HEA for the CO2RR. Reproduced with permission.151 Copyright 2021, Wiley VCH. (d) Schematic CO2 electrolysis procedure. Reproduced with permission.317 Copyright 2023, Elsevier B.V. (e) Faradaic efficiency of the HEA for CO2 reduction. Reproduced with permission.318 Copyright 2023, Wiley VCH. | ||
Roy et al. conducted HT screening of HEA-based (Cu, Co, Ni, Zn, and Sn) catalysts through ML for CO2 hydrogenation to methanol.226 The designed CuCoNiZnSn-catalyst exhibited satisfactory performance in all possible combinations, where different elemental, compositional, and surface microstructural features were used as input parameters. Several theoretical studies have successfully designed HEAs for the CO2RR; however, these HEAs have not yet been experimentally verified. An extensive experimental study should be performed to achieve an effective HEA design, so that the HEAs can be used as industrial electrode materials for the CO2RR.316 Cavin et al. synthesized and tested five high-entropy 2D transition-metal dichalcogenide alloys containing four or five transition metals, and identified that the alloy with the highest configurational entropy, that is, (MoWVNbTa)S2, exhibited promising performance for CO2 electroreduction (Fig. 21c).151 Zhang et al. demonstrated that high-entropy perovskite oxide Pr0.5Ba0.5Mn0.2Fe0.2Co0.2Ni0.2Cu0.2O3−δ effectively catalyzes CO2 electrolysis in SOECs. The in situ formation of Fe–Co–Ni–Cu quaternary alloy nanocatalysts exhibited enhanced catalytic activity for the CO2RR, as evidenced by the significantly lower polarizing resistance and higher electrolytic current density (Fig. 21d).317 Li et al. developed highly active and durable CO2RR catalysts by fabricating PdCuAgBiIn HEA aerogels (HEAAs) which demonstrated superior CO2RR activity for selectively producing HCOOH over a wide potential range. In a flow cell device with 0.5 M KHCO3, the HEAAs achieved a current density of nearly 200 mA cm−2 and a faradaic efficiency of HCOOH of 87%.318 This remarkable performance is attributed to the strong interactions between different metals and surface unsaturated sites in the HEAAs, which optimize the electronic structures and HCOO* interfacial adsorption, suppressing CO poisoning and competitive H2 production to favor HCOOH formation (Fig. 21e).
The literature survey highlights the extensive use of metal species such as Cu, Ag, Au, and Sn as catalysts for CO2 electroreduction. To facilitate electroreduction, it is imperative that the charged intermediate CO2˙− actively participates, necessitating the development of new electrodes for better stabilization of this molecule. Metals exhibit differing tendencies to temporarily bind intermediates and products to the electrocatalyst surface, leading to their classification into three classes. The first class comprises metals such as Cu, where the most stable bonds are formed between the intermediate and the surface. Cu, being a representative metal of this class, forms highly stable bonds with the charged intermediate CO2˙−, enabling the production of very reduced products such as alcohols (e.g., CH3OH) and hydrocarbons (e.g., CH4). The second class includes metals that create weaker bonds compared to Cu, resulting in the predominant production of CO as the main product. Noble metals such as Pd, Au, and Ag, along with others such as Zn, fall into this category. Lastly, the third class consists of metals where HCOO− is the main product due to the weak binding of the intermediate to the catalyst surface. Metals such as Sn, In, Pb, and Hg are examples of this class.
In conclusion, strategic design and the use of high-entropy alloys (HEAs) with active metals can aid in achieving the desired electrode materials tailored for specific value-added products. Additionally, computational studies and the trial-and-error method can concurrently contribute to the design of HEA-based electrode materials for the CO2RR process. Overall, these three classes of catalysts yield higher value-added products such as hydrocarbons or alcohols, CO, and HCOO (or HCOOH depending on the acidity). However, it's essential to consider the competitive process of the hydrogen evolution reaction (HER) in CO2 electroreduction in aqueous solutions. In the first class of metals (Cu), where the partially reduced intermediate CO2˙− is strongly adsorbed, the HER tends to occur predominantly on metals from the other two classes, such as Pt, Ti, Fe, and Ni. Therefore, fine-tuning the binding energies of key reaction intermediates is crucial for achieving selectivity in desired HEA based products and minimizing the specific energy consumption of CO2 electroreduction.
Finally, HEAs can be designed to have multiple types of active sites, each with a specific function. For example, a HEA can be designed to have active sites for alcohol adsorption, C
C bond cleavage, and oxidation of toxic substances. This can result in more efficient and selective AOR catalysts (Table 13). The coordination environment of the metal surface sites can be changed by changing the composition of the HEA alloy. This results in metal sites that balance the adsorption energies of reactants, reactors, and intermediates at the adsorption sites, ultimately achieving high activity.
| Electrode | Synthesis | Electrolyte | Performance and key points | Reference |
|---|---|---|---|---|
| Pd40Ni60 | Melt spinning technique | 1.0 M KOH + 0.5 M methanol | E onset: −0.83 V, If/Ib: 9.3 | 74 |
| Pd40Ni60 | Melt spinning technique | 1.0 M KOH + 0.5 M ethanol | E onset: −0.81 V | 74 |
| Pt52Fe11Co10Ni11Cu10Ag8 NPs | Radio-frequency sputter depositions | 0.5 M H2SO4 + 1.0 M CH3OH | Mass activity: 462–504 mA mg−1; Eonset = 0.222 V, E at If: 0.676, E at Ib: 0.518, If/Ib: 1.02 | 186 |
| PtRuCuOsIr Nps | Dealloying | 0.5 M H2SO4 + 0.5 M CH3OH | Mass activity: 857.5 mA mgPt−1, specific activity: 3.0 mA cm−2, If/Ib: 1.2 | 319 |
| Pt18Ni26Fe15Co14Cu27 NPs | Mechanical method | 1 M KOH + 1 M CH3OH | Mass activity: 15.04 mA mgPt−1 | 295 |
| PdNiCoCuFe nanotube | Template-assisted electrodeposition | 0.5 M CH3OH + 0.5 M NaOH | Current density of the forward scan of PdNiCoCuFe alloy NTAs is two-times higher than that of Pd NTAs | 319 |
| PtFeCoNiCu (HEA-700) | Calcination and annealing | 0.1 M HClO4+ 0.1 M CH3OH | Specific activity: 3.29 mA cm−2 (1.40A mg−1), If/Ib: 1.21 | 320 |
| PdPtCuAgAu nanowires | One-pot solution-phase route | 1 M KOH+ 1 M ethanol | Mass activity: 7.7 A mg(Pd+Pt)−1, If/Ib: 3.4 | 322 |
| PdAgSn/PtBi HEA NPs | Wet chemical method | 1.0 M KOH + 1 M methanol | Mass activity: 2874 mA mg(Pd+Pt)−1, 5.9- and 4.8-fold higher than that of commercial Pd/C and Pt/C | 323 |
| PdAgSn/PtBi HEA NPs | Wet chemical method | 1 M KOH + 1 M ethanol | Mass activity: 3386 mA mg(Pd+Pt)−1, 5.4- and 4.9-times higher than that of commercial Pd/C and Pt/C | 323 |
A template-assisted electrodeposition method was employed to fabricate PdNiCoCuFe alloy nanotube arrays (NTAs), exhibiting enhanced methanol oxidation capability achieved by the synergistic interaction between Pd, Ni, Co, Cu, and Fe, which facilitates C–H bond cleavage and hydroxyl species generation (Fig. 22a).319 The compositional integrity, geometric arrangement, and strong electronic interaction within the metal provide a synergistic effect and ultimately contribute to the catalytic activity by altering the electronic state of Pd. Therefore, the quinary PdNiCoCuFe alloy NTAs are highly desirable as low-Pd-content catalysts in DAFCs.
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| Fig. 22 (a) XPS diagram of a PdNiCoCuFe alloy nanotube. Reproduced with permission.319 Copyright 2014, Elsevier B.V. (b) Fourier transform of the extended X-ray absorption fine structure spectra of the PtFeCoNiCu HEA for the Pt L3-edge. Reproduced with permission.244 Copyright 2021, Spinger Nature. (c and d) Intrinsic methanol oxidation reaction (MOR) and ethanol oxidation reaction (EOR) activities of the designed HEA NPs and (e and f) comparison of the activities of the HEA NPs towards the EOR and MOR. Reproduced with permission.323 Copyright 2023, Wiley VCH. | ||
The electrochemical AOR process using a HEA-based electrode material involves linear electron and proton transfer processes with critical intermediate orbitals, promoting effective oxidation and bond strength. HEAs provide a suitable electronic environment with multiple surface-active sites, promoting effective electron transfer, facilitating adsorption, and maximizing surface electrical activity, thus facilitating effective conversion.320 For example, the MOR activity of the FCC crystalline PtFeCoNiCu HEA was improved by the surface strain strategy.244 EXAFS analysis revealed that the shortening of the Pt–Pt bond distance and developed compressive strain significantly improved MOR electrocatalytic performance by downshifting the d-band center (Fig. 22b). Furthermore, DFT calculations indicate that the compressive strain shifts the d-band center away from the Fermi energy, resulting in weaker adsorption of CO on the HEA surface, which improved the MOR performance.
The development of highly efficient direct ethanol fuel cells (DEFCs) faces a challenge in enhancing ethanol C–C bond cleavage through the complete 12-electron EOR. Modern catalysts struggle with incomplete pathways due to CO poisoning, affecting power performance and efficiency. A separated PtPdFeCoNiSnMn HEA (PtPd HEA) was designed to address this issue.321 The PtPd HEA exhibited superior activity and stability against the EOR and ORR, respectively, and achieved record performance with a maximum power density of 0.72 W cm−2 and stable operation for over 1200 h in DEFCs. Interestingly, Sn was also introduced to promote CO oxidation and C–C bond cleavage; Pt and Pd served as active sites to catalyze the EOR, and the reaction barrier for C–C bond cleavage was significantly reduced at the Pd site of the PtPd HEA because of the synergistic and electronic effects with other elements. Fan et al. synthesized PdPtCuAgAu nanowire networks using carboxyl-functionalized surfactants as soft templates. These alloy-based electrocatalysts exhibited enhanced performance in ethanol oxidation, with high mass activity, anti-poisoning ability, superior stability/durability, and fine electrocatalytic kinetics, along with advantages such as anisotropic and thin nanowires.321,322
Despite significant advancements in the field of HEAs, controlling their morphology and structure remains a challenge because of the complexities involved in balancing precise HEA surface control with extreme synthesis conditions. Guo et al. employed a simple low-temperature synthesis method under atmospheric pressure to fabricate Pd-enriched-HEA-core and Pt-enriched-HEA-shell NPs with a single-phase FCC structure.323 Interestingly, both the Pd-enriched-HEA-core and Pt-enriched-HEA-shell NPs exhibited lattice expansion during HEA formation, resulting in tensile strain within the HEA core and shell (Fig. 22c and d). The synthesized PdAgSn/PtBi HEA NPs demonstrated superior electrocatalytic activity and durability for both the MOR and EOR. The specific (mass) activity of PdAgSn/PtBi HEA NPs for the MOR surpassed that of commercial Pd/C and Pt/C catalysts (Fig. 2e and f). Integrating high-entropy elements (HEEs) with Pt and Pd sites at the HEA interface synergistically facilitates a multistep process for the AOR. Consequently, noble metal-based HEA electrodes exhibit enhanced activity compared to their non-noble metal-based counterparts. This is attributed to the structural, electronic, and morphological modifications induced by the addition of noble metals. However, achieving cost-effectiveness through non-noble metal-based HEAs for the AOR remains a challenge, limiting the full potential of this technology in industrial applications.
N triple bonds in N2 and competitive HER. A heterogeneous catalytic pathway was observed, with the adsorption of N2 molecules on the electrocatalyst surface, hydrogenation, and desorption of NH3 (Fig. 23a).287 Understanding the mechanisms of association and dissociation are crucial for designing efficient and selective electrocatalysts for N2 to NH3 conversion. The activation energy required to break the stable N2 triple bond is a major challenge. To improve catalytic capacity, surface control, defect engineering, strain engineering, alloying, composition tuning, and blending strategies are needed. HEAs are also promising for the NRR because of their tunability, which enables the designing of specific NRR catalysts. Proper compositional tuning with early transition metals such as Sc, Y, Ti, and Zr can be a good choice for selective designing of active NRR materials. Yu et al. utilized DFT calculations to screen the optimal performance of a FeCoNiCuPd HEA for the NRR. Their findings revealed that the varying metal ratios of HEAs significantly influence the d-band center, consequently affecting the catalytic activity across the HEA surface. Theoretical studies have demonstrated that Ni0.3(FeCoCuPd)0.175 with an exposed (111) crystal plane exhibits significant NRR activity, achieving an overpotential of 0.34 eV. This assessment was based on the measurements of the adsorption energy of the initial N2 and the free energy of intermediates along different pathways. Notably, the bridge site of Fe–Co on the surface emerged as the optimal site for N2 adsorption and activation, contributing to the superior NRR catalytic performance. Electronic calculation results indicated that the atomic ratios of HEAs play a crucial role in positioning the d-band center, thereby enhancing the interaction between the metal site and the adsorbate and influencing the catalytic activity. Compared to the secondary HER, the Ni0.3(FeCoCuPd)0.175 catalyst exhibits a superior selectivity of 99%. This high selectivity is attributed to the stronger adsorption of H, which favors the NRR over the HER. Regardless of the element ratio in HEAs, the PDOS results consistently reveal that optimal N2 adsorption configurations involve Fe or Co atoms. These atoms facilitate electron transfer to N2 molecules during their reduction to NH3 (Table 14).324
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| Fig. 23 (a) Schematic illustration of different mechanisms for the nitrogen reduction reaction (NRR). Reproduced with permission.324 Copyright 2022 Elsevier B.V. (b) d-band centers in the designed high-entropy perovskite oxides. (c) Faradaic efficiency of the designed HEA perovskite toward the NRR, Reproduced with permission.325 Copyright 2022 Springer Nature. (d) Mechanism of the HEA for the NRR. Reproduced with permission.326 Copyright 2021 Wiley VCH. | ||
| Electrode | Synthesis | Electrolyte | Performance and key points | Reference |
|---|---|---|---|---|
| B-doped FeCoNiCuPd | Electrospinning | 0.5 M K2SO4 | NH3 yield of 24.8 μmol h−1 cm−2, NH3 FE of 39.2% | 287 |
| Ni0.3(FeCoCuPd)0.175 | — | — | Ni increases NRR activity | 324 |
| RuFeCoNiCuNps | Wet chemical | 1 M KOH | NH3 yield of 11.4 μg h−1 cm−2, NH3 FE of 39.2% | 325 |
Chu et al. synthesized high-entropy perovskite oxides, Bax(FeCoNiZrY)0.2O3−δ (Bx(FCNZY)0.2) (x = 0.9, 1) (where FCNZY represents Fe, Co, Ni, Zr, and Y, respectively) using a modified sol–gel method.325 By modifying the non-stoichiometric metal elements at the A site and introducing oxygen vacancies, the NRR activity of the high-entropy perovskite oxide was significantly enhanced. Employing the d-band center theory, the catalytically active center at the B site was theoretically predicted, identifying Ni as the primary catalytic site. Moreover, Ni, Co, and Fe also served as catalytically active sites in the bulk B(FCNZY)0.2, as their energy levels approach the Fermi level, as confirmed via the d-band center analysis (Fig. 23b). The free energy values of the intermediate states in the optimal distal pathway reveal that the third protonation step (*NNH2 → *NNH3) is the rate-determining step, and the increased oxygen vacancies in the high-entropy perovskite facilitate nitrogen adsorption and reduction. The enhanced NRR activity of B0.9(FCNZY)0.2 is attributed to the additional oxygen vacancies and the synergistic effect between different metal elements at the B site, as corroborated by DFT calculations (Fig. 23c).
High-voltage requirements, low-NH3 yield, and poor stability of electrode materials pose significant challenges for the NRR. To address these issues, RuFeCoNiCu HEA NPs were synthesized in an oil phase at atmospheric pressure and low temperature (≤250 °C), demonstrating NRR activity in 0.1 M KOH, 0.1 M Li2SO4, 0.1 M Na2SO4, and 0.1 M HCl electrolytes.326 The designed HEA NPs exhibited a high NH3 yield of 57.1 μg h−1 mgcat−1 at 0.05 V versus the reversible hydrogen electrode in 0.1 M KOH, with a corresponding faradaic efficiency of 38.5%. Monte Carlo and DFT calculations suggested that Fe in the alloy is the most favorable site for N2 adsorption and activation, whereas Co–Cu and Ni–Ru pairs exhibit excellent surface hydrogenation ability at low overpotential, forming H* on their surfaces. Specifically, t-Fe, b-Fe-Fe, h-Co-Ni-Ni, and s-Ni–Ru are identified as four promising active sites, and t-Fe was identified to be the most effective for the NRR (Fig. 23d). This investigation introduces a novel method for HEA synthesis and demonstrates the application of HEAs in the NRR under various pH conditions. These findings shed light on a new NRR mechanism with potential for commercial applications. While the strategic design of HEA-based electrode materials is still in its early stages, significant progress can be made towards achieving commercially viable performance through selective metal choices, design, and optimization. Additionally, computational studies offer a valuable tool to bridge the gap between current experimental limitations and the efficient evaluation of potential HEAs.
| Electrode | Synthesis | Electrolyte | Performance & key points | Reference |
|---|---|---|---|---|
| (FeCoNiCrMn)3O4 | Calcination | 1 M LiPF6 + ethylene carbonate (EC)/ethyl methyl carbonate (EMC)/dimethyl carbonate (DEC) (1 : 1 : 1) |
Coulombic efficiency: 61.6%, discharge/charge specific capacities: 1034 mA h g−1/680 mA h g−1 | 129 |
| (FeNiCrMnZn)3O4 | Ball milling | 1 M LiPF6 + ethylene carbonate/dimethyl carbonate (1 : 1) |
Discharge capacity (386.7 mA h g−1) at 0.5 A g−1 after 185 cycles | 327 |
| (Co0.2Cu0.2Mg0.2Ni0.2Zn0.2)O | Spray pyrolysis | — | Coulombic efficiency: 99.4–99.95% | 329 |
| Li1.3Mn0.1Co0.1Mn0.1Cr0.1Ti0.1Nb0.2O1.7F0.3 | Solid state method | 1 M LiPF6 + ethylene carbonate/dimethyl carbonate (1 : 1) |
Specific energy: 307 mA h g−1 (955 W h kg−1) | 330 |
| Fe0.24Co0.26Ni0.10Cu0.15Mn0.25 | Lithium nitrate (LiNO3, 0.2 M) lithium bis(trifluoromethanesulfonyl)imide (LiTFSI, 1 M) in DME/DOL (1 : 1) |
Specific capacity: 1079.5 mA h gcathode−1 | 331 | |
| (FeCoNiCrMn)3O4 | Arc melting and dealloying | 2 M KOH | Specific capacitance of 639 F g−1 at 1 A g−1 and retention of 80.77% at 10 A g−1 | 332 |
| (FeCoCrMnNi)3O4 | Sol–gel method | 1 M KOH | Capacitance: 332.2 F g−1 at 0.3 A g−1, energy density: 103.8 W h kg−1, potential window: −1 to 0.6 | 333 |
| Fe–Co–Ni–Cu–Zn | Ball milling | 3 M KOH | Gravimetric capacitance of 325.17 F g−1 at 1 A g−1, energy density: 3.82 W h kg−1, power density: 325 W kg−1 | 334 |
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| Fig. 24 (a) Ex situ XRD patterns of high-entropy oxide (HEO) at different states of charge. (b) Kinetics analysis of HEO in Li-ion batteries. Reproduced with permission.129 Copyright 2022, Elsevier B.V. (c) Electrochemical performance of HEAs as an anode material. Reproduced with permission.327 Copyright 2021, Elsevier Ltd. (d) Schematics of the proposed de-/lithiation mechanism during the conversion reaction of transition-metal-based HEO. M in the figure denotes only the cations in the high-entropy system. Reproduced with permission.329 Copyright 2018, Nature Spinger. | ||
The superior electrochemical performance of (FeCoNiCrMn)3O4 can be ascribed to the optimized electron configurations, smooth ion diffusion paths and abundant active storage sites derived from the unique structure of HEO with multiple metal elements of mixed valence states and different cation radii. The cathodic peak located at 0.25 V is attributed to the stepwise reduction of transition-metal oxides (containing M4+/M3+ toM2+ and further M2+ to M0) and the formation of an inert solid electrolyte interface layer, indicating HEA-based redox behavior and a battery-type electrode material (Fig. 24b).327 This HEO amorphous structure is good for achieving an anode with superior electrochemical performance. The defects in amorphous HEO not only provide more possible active sites for Li+ storage, but also open sufficient diffusion paths for Li+ through the electrode and regulate electron configurations to accelerate the transport of electrons, giving rise to increased capacity. Furthermore, the disordered structure provides more space for buffer volume changes during the repeated lithiation and delithiation. In another report, Dai et al. confirmed that Zn improved the content of trivalent Mn in HEOs, thereby increasing the voltage range of the reaction process, which then enhances the Li storage performance. The comparison between (FeNiCrMnZn)3O4 and (FeNiCrMnMg)3O4 suggested that, when compared to Mg, the introduction of Zn improved the diffraction peak intensity and crystallinity of the XRD spectra, which was then reflected in their Li storage performance (Fig. 24c).327 Apart from the anodic electrode performance, HEO has received considerable attention as the most promising cathode material for next-generation LIBs.328
Sarkar et al. demonstrated the reversible lithium storage properties of HEOs, underlying mechanism, and influence of entropy stabilization on the electrochemical behavior. It was found that the stabilization effect of entropy brings significant benefits for the storage capacity retention of HEOs and significantly improves the cycling stability of the proposed lithiation or delithiation mechanism during the conversion reaction of (Co0.2Cu0.2Mg0.2Ni0.2Zn0.2)O HEO. The as-prepared transition-metal-based HEO (TM-HEO) was composed of poly-/nanocrystallites, exhibiting an ordered structure; moreover, during lithiation, some of the divalent metals of TM-HEO reacted with Li to form nano-Li2O and nano-M nuclei via a conversion reaction (Fig. 24d).329 The rock-salt structure was preserved in this state and nanosized nuclei grew inside the rock-salt host structure, causing the buildup of stresses, thus resulting in the introduction of defects. Consequently, the participating ions remained trapped inside the host matrix and could easily diffuse back into the crystal structure in the subsequent oxidation process. Hence, the parent HEO structure was restored after the delithiation process. Therefore, the charge–discharge process is reversible and rapid in the rock-salt-like HEO system. Lun et al. demonstrated a cation-disordered rock-salt-type HEO for LIBs where cathode compound, composed of six different transition-metal species, was approximately 40% larger than the capacity of the conventional compound. The incorporation of a large number of TM species into the lattice could reduce the extent of short-range order and significantly improve Li transport.330 Gao et al. developed a novel sulfur cathode comprising Fe0.24Co0.26Ni0.10Cu0.15Mn0.25 HEA nanocrystallites embedded on nitrogen-doped carbon.331 This unique architecture enabled the cathode to exhibit remarkable electrocatalytic activity in converting solid sulfur into solid discharged products, bypassing the soluble intermediate lithium polysulfide phase. Consequently, the cathode achieved a superior reversible capacity of 1079.5 mA h gcathode−1, corresponding to a high utilization of 89.4%, with the entire cathode serving as the active material instead of solely the sulfur element. Notably, even under challenging conditions involving a lean electrolyte (3 μL mg−1) and ultrahigh sulfur loading (27.0 mg cm−2), the cathode retained an impressive discharge capacity of 868.2 mA h gcathode−1. This groundbreaking approach paves the way for exploring catalytic host materials that can effectively enhance sulfur utilization in lithium–sulfur batteries. Sui et al. synthesized (FeCoNiCrMn)3O4 by dealloying the FeCoNiCrMnAl95 alloy in 3 M NaOH, achieving superior supercapacitor characteristics as an anode material, with a specific capacitance of 639 F g−1 at 1 A g−1 and retention of 80.77% at 10 A g−1.332 The reduction peak occurs at 0.3 V, which is predominantly caused by the transition-metal oxide reduction (M4+/M3+ to M2+, M2+ to M0), indicating that the materials rely on noticeable redox reactions for energy storage. The better capacitive performance can be compared with that of CoCr2O4 (Fig. 25a and b). Ma et al. fabricated spinel-phase (FeCoCrMnNi)3O4 at a low calcination temperature of 450 °C, achieving a high specific surface area of 63.1 m2 g−1 in an alkaline medium. The specific capacitance was observed to be 332.2 F g−1 at a current density of 0.3 A g−1 in 1 M KOH electrolyte with a wide potential window of (−1, 0.6). The HEO electrode achieved an energy density of 103.8 W h kg−1 by maintaining the designed microstructural arrangement.333
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| Fig. 25 (a–c) Capacitive contribution, separations of diffusion-controlled and capacitive charges at different scan rates, and cycling performances of (FeCoNiCrMn)3O4/NF and CoCr2O4/NF. Reproduced with permission.332 Copyright 2023, American Chemical Society. (d) Plots of density of states for d-states of Fe, Co, Ni, Cu, and Zn in the FeCoNiCuZn HEA, which is actively used as electrode materials in supercapacitor devices. Reproduced with permission.334 Copyright 2023, Elsevier Ltd. | ||
Tiwary et al. successfully synthesized a Fe–Co–Ni–Cu–Zn HEA using a ball milling method.334 This HEA exhibited multivalent quinary characteristics and favorable intermediate intercalation/deintercalation kinetics, making it a promising candidate for supercapacitor applications. The asymmetric liquid device performance was attributed to the presence of multivalent elements with surface oxidation and the availability of d-states near the Fermi level. The device demonstrated stable performance over long-term (up to 5000 cycles) charging–discharging cycles in a voltage window of 1.5 V. It achieved a maximum specific capacitance of approximately 105 F g−1 at a scan rate of 5 mV s−1. The fabricated liquid-state device exhibited a superior specific energy of 23.82 W h kg−1 and specific power of 375 W kg−1. The enhanced electronic conductivity and electron transport properties of the HEA alloy contributed to the reduction and formation of split energy levels, as confirmed via DFT calculations. The d-band center of the quinary Fe–Co–Ni–Cu–Zn HEA was significantly closer to the Fermi level as compared to that of individual atom nanoclusters, resulting in increased chemical affinity toward oxygen absorbability on the surface of the mesoporous HEA (Fig. 25c). This tailored surface chemistry led to improved chemical stability, enhanced reaction kinetics, and reduced ion diffusion barriers.
Developing and optimizing industrial electrocatalysts pose a significant challenge for the scientific community. Industrial electrode materials must adhere to a set of fundamental requirements that are not typically considered for laboratory-scale or research-based development and synthesis. Generally, electrode materials for industrial applications must meet specific criteria, including (a) a straightforward synthesis approach, (b) a product-efficient synthesis route, (c) environmentally friendly technology, (d) cost effectiveness, and (e) high catalytic efficiency, stability, and selectivity. The feasibility of employing HEAs as industrial electrode materials compared to conventional electrode materials hinges on systematically addressing these criteria. The introduction of HEAs and their derivatives has revolutionized the field by introducing an entirely new class of materials, finding applications in a range of electrochemical processes. HEAs, therefore, stand as promising candidates for revolutionizing catalytic research and, with the right design strategy and understanding of structure–property relationships, can potentially transition into industrial applications. The intrinsic properties of HEAs result in unique characteristics such as high mechanical strength, superior fracture toughness, and corrosion resistance. Utilizing these HEAs in catalytic reactions is a relatively new area of research.
| Electrochemical process | Traditional materials | Property/aspect of high-entropy materials (HEMs) | Advantages of HEMs | Challenges of HEMs |
|---|---|---|---|---|
| HER | Pt, Ni, Mo, MoS2, and NiFe | (a) Synergistic effects and a tunable electronic structure and (b) high stability under harsh conditions | (a) Improved activity and durability compared to pure metals. (b) Can be tuned for specific pH conditions | (a) Synthesis complexity and cost. (b) Limited understanding of structure–property relationships |
| OER | Ir, Ru, Co, RuO2, IrO2, and LaMnO3 | (a) Improvement through compositional tuning and (b) high stability, especially in an acidic medium | (a) Enhanced activity and lower overpotential compared to traditional oxides. (b) Potential for cost reduction compared to noble metals | (a) Difficulty in controlling surface composition during synthesis. (b) Long-term stability concerns |
| ORR | Pt, Ag, and Pt alloy | (a) Comparable or superior activity. (b) High stability with potential for improvement through alloying | (a) Exhibit comparable activity to Pt at significantly lower cost. (b) Potential for improved durability compared to Pt | (a) Achieving high selectivity towards O2 reduction (avoiding H2O production). (b) Difficulty in fine-tuning activity and selectivity |
| CO2RR | Cu, Sn, Ag, and Cu alloy | (a) Competitive activity through synergistic effects, (b) tunable selectivity towards the desired product, and (c) high stability, especially in aqueous solutions | (a) Tunable product selectivity (CO, HCOOH, CH4, etc.) based on the composition. (b) Potential for enhanced activity and improved conversion efficiency | (a) Identifying optimal compositions for the desired products. (b) Difficulty in controlling morphology and active sites |
| NRR | Fe, Mo, and MoS2 | (a) Tunable electronic structure and (b) tunable selectivity | (a) Achieve high ammonia selectivity and activity at lower overpotentials. (b) Potential for cost-effective alternatives to noble metal catalysts | (a) Identifying optimal compositions for N2 activation and H2 dissociation. (b) Long-term stability issues for some HEMs |
| AOR | Pt and Pd | (a) Stability for compositional complexity and (b) the initial cost may be higher but potential for cost reduction with optimization | (a) Potential for lower cost and improved CO poisoning tolerance compared to Pt. (b) Tunable activity and selectivity for specific alcohols | (a) Difficulty in achieving high activity and selectivity simultaneously. (b) Long-term stability needs further investigation |
| Battery | LiCoO2, LiFePO4, and carbonaceous material | (a) Potential for high capacity and long cycle life and (b) cost-effectiveness may vary depending on the specific application | (a) High energy density and tunable capacity based on the composition. (b) Potential for improved cycling stability and safety | (a) Understanding complex phase transformations during operation. (b) Optimizing synthesis methods for achieving the desired morphologies |
| Supercapacitor | Carbonaceous materials and MnO2 | (a) Potential for high capacitance and fast charge–discharge rates and (b) high stability under cycling conditions | (a) High capacitance and potential for fast charge/discharge rates. (b) Tailoring the pore structure and surface area for enhanced performance | (a) Identifying cost-effective and scalable synthesis methods. (b) Exploring strategies for improving long-term cycling stability |
Despite the promising potential of HEA-based electrode materials, several challenges need to be addressed before they can be widely adopted in industrial processes. Fabricating HEAs for industrial applications requires the utilization of suitable synthesis approaches that adhere to moderate reaction conditions that are compatible with industrial requirements. Alongside reaction conditions, product percentage and purity are also crucial design factors for selecting a specific synthesis route that enables controlled composition, size, and uniformity. The catalytic performance of the HEA system is significantly influenced by factors such as crystal structure, phase, morphology, counter anions, and exposed active planes. Various designing techniques and engineering approaches (defect, strain, bandgap, d-band, active crystal plane, etc.) are available to control these parameters and facilitate the development of electrode materials that are suitable for industrial processes. During synthesis, the judicious adjustment of reaction conditions, including metal precursors, growth control agents, reducing agents, solvents, surfactants, masking agents, and others, offers flexibility for tailoring the structure and morphology of HEAs. Notably, although numerous studies have explored the impact of the phase structure on the mechanical, magnetic, and corrosion properties of HEAs, research on how the phase structures of HEAs with identical compositions affect their electrocatalytic behavior remains limited. Therefore, further investigation into this area is of paramount importance for future research.
The structure–activity relationship is a crucial parameter in designing more effective electrode materials. In this context, a thorough understanding and in-depth study of individual HEAs are essential for elucidating the mechanism and identifying active intermediates. Advanced physicochemical studies can provide valuable insights into these aspects and inform the design and development of potential electrode materials for specific electrochemical processes. Although the multi-element nature of HEAs can introduce complexity, this can be mitigated through in situ studies during electrochemical and HEA design processes. In situ studies enable the monitoring and tuning of catalytically active sites, growth processes, morphological changes, composition, chemical valence states, and electronic structures of elements in HEAs. Electrochemical operando studies are expected to be particularly useful in measuring structural evolution and identifying the actual active sites of catalysts. Therefore, developing a more comprehensive and sophisticated set of in situ techniques is crucial for achieving a profound understanding of HEA-based catalysts during electrocatalytic processes that help to tune optimized electrode materials for industrial processes such as PEMWEs, PEMFCs, energy storage devices, etc.
As HEAs are composed of multiple elements with various compositional possibilities, thereby the structure and activity can alter significantly with compositional and elemental variations of the constituent elements. The most efficient compositional and elemental combination can be effectively assessed using theoretical and computational modelling. Moreover, the desired electrochemical performance may not always match the expected results. Therefore, a comprehensive theoretical study is crucial for designing and developing efficient electrode materials for industrial applications. The involvement of novel computational methods, such as DFT, molecular dynamics, ML, NNs, and HT screening, has facilitated the evaluation of a larger number of active sites and accelerated the understanding of the potential for adjusting adsorption energies for a specific electrochemical process. The identity of the active intermediate in the designed electrode materials can be predicted using theoretical calculations. These advanced techniques have aided in the design of potential electrode materials with improved catalytic performance. However, the theoretical understanding may not always align perfectly with experimental findings. While these models can provide valuable guidance, their predictions must be interpreted with caution and validated experimentally. Therefore, a collaborative approach seamlessly integrating theoretical calculations with experimental verification is crucial for advancing HEAs as efficient electrocatalysts and realizing tangible industrial benefits.
The vast composition space and unique high-entropy structure of HEAs offer promising opportunities for catalyzing various reactions. However, further research efforts are required to fully unlock their potential. HEA-based heterogeneous catalysts offer four core effects that provide distinct advantages compared to mono- or bimetallic electrode materials or electrocatalysts. Numerous electrochemical processes utilize HEA systems that exhibit superior electrochemical performance when compared to other state-of-the-art materials. However, there remains significant scope for designing new HEA-based electrode materials with low cost and robust performance. Prior to utilizing any HEA-based electrode material in an industrial process, its activity, selectivity, and stability must be carefully evaluated. The selection of appropriate elements and the maintenance of compositional integrity are crucial factors in designing efficient electrode materials. The applicability of the HEA system is determined by the suitable choice and optimization of these parameters. In addition to pristine HEAs, their derivatives also hold immense potential for various electrochemical processes. In some cases, these derivatives have demonstrated superior electrochemical activity when compared to pristine HEAs. Therefore, through proper tuning and optimization, HEA-based materials can be designed to serve as highly effective electrode materials in industrial electrochemical processes. Likewise, the formation of pre-catalysts can be an effective approach to enhance electrochemical performance and achieve optimal results. Furthermore, there remains a gap between industry and academia. Extensive research and development efforts are needed to realize the goal of utilizing HEAs in industrial electrochemical processes. The following approach can offer a pathway to achieve this goal (Fig. 26).
One of the main challenges is the design of HEAs for electrochemical processes. In addition, it is important to develop a cost-effective and scalable manufacturing process while maintaining the desired composition and properties of the HEA. To address this issue, a thorough literature review of electrochemical processes should be conducted. After understanding the process mechanisms using specific benchmark materials, potential HEA materials can be identified. In addition, modern computational science would also be helpful in supporting and assisting in the design of the most efficient electrode materials. The most compositionally active materials can be identified through thorough theoretical studies and optimization of synthetic pathways using trial-and-error methods. It is accurate to conclude that computational studies alone cannot be used to choose the most suitable HEA for industrial electrochemical applications. Tuning the composition and structure of HEAs to maximize their performance in a particular electrochemical process is another challenge. This requires a deep understanding of the relationship between composition, microstructure, and electrochemical properties. Ensuring the long-term stability and durability of HEAs under realistic operating conditions is essential for their industrial adoption; HEAs must withstand the harsh environments and cyclic stresses encountered in electrochemical processes without significant degradation.
Therefore, all the designed and optimized HEAs should be tested under real operating conditions in the device and prototype levels. In order to calculate the efficiency of the designed HEA, appropriate stability tests should be performed on the HEA system. Moreover, physicochemical study helps to evaluate the proper mechanistic routes to find out the active intermediate of the materials. An improved electrode performance can be achieved by the modifying the electronic structure, morphology, crystal face, lattice structure, the composition, etc. In addition, HEAs need to be compatible with existing industrial processes and technologies, including electrode fabrication methods and device integration. It is crucial that HEAs can be seamlessly integrated into existing systems without compromising performance; HEAs offer promising properties, but their commercial feasibility depends on their cost-effectiveness when compared to conventional materials. Optimizing manufacturing processes to reduce production costs and improve material efficiency is essential to transfer the technology from the lab to the industry level. Addressing these challenges will require interdisciplinary efforts involving materials scientists, electrochemists, engineers, and industry partners. Collaboration between academia and industry can facilitate the translation of fundamental research findings into practical applications. Moreover, continued investment in research and development, along with advancements in manufacturing and characterization techniques, will be essential for unlocking the full potential of HEAs as industrial electrode materials across a wide range of electrochemical applications.
This study intends to offer a comprehensive overview of the strengths and limitations of HEA-based electrode materials in electrochemical applications. Through critical evaluation of current state-of-the-art research, the study aims to guide future research directions and contribute to the development of more effective HEA-based electrode materials for industrial purposes. With ongoing advancements, HEA-based electrode materials are anticipated to showcase significant potential for diverse industrial applications in the near future, thereby generating economic and environmental benefits.
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