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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem.</journal-id>
<journal-title>Frontiers in Chemistry</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem.</abbrev-journal-title>
<issn pub-type="epub">2296-2646</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1071274</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2022.1071274</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemistry</subject>
<subj-group>
<subject>Review</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Recent progress in noble-metal-free electrocatalysts for alkaline oxygen evolution reaction</article-title>
<alt-title alt-title-type="left-running-head">Tan et al.</alt-title>
<alt-title alt-title-type="right-running-head">
<ext-link ext-link-type="uri" xlink:href="https://doi.org/10.3389/fchem.2022.1071274">10.3389/fchem.2022.1071274</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Tan</surname>
<given-names>Deming</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1880728/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Xiong</surname>
<given-names>Hao</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Zhang</surname>
<given-names>Tao</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Fan</surname>
<given-names>Xuelin</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1823752/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Wang</surname>
<given-names>Junjie</given-names>
</name>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<xref ref-type="aff" rid="aff5">
<sup>5</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Xu</surname>
<given-names>Fei</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>School of Mechanical Engineering</institution>, <institution>Chengdu University</institution>, <addr-line>Chengdu</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>School of Materials Science and Engineering</institution>, <institution>Northwestern Polytechnical University</institution>, <addr-line>Xi&#x2019;an</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Institute of Process Engineering</institution>, <institution>Chinese Academy of Sciences</institution>, <addr-line>Beijing</addr-line>, <country>China</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>Institute of Botany</institution>, <institution>Jiangsu Province and Chinese Academy of Sciences</institution>, <addr-line>Nanjing</addr-line>, <country>China</country>
</aff>
<aff id="aff5">
<sup>5</sup>
<institution>Jiangsu Key Laboratory for the Research and Utilization of Plant Resources</institution>, <addr-line>Jiangsu</addr-line>, <country>China</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/578335/overview">Xiaopeng Han</ext-link>, Tianjin University, China</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1858927/overview">Jingqi Chi</ext-link>, Qingdao University of Science and Technology, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1868593/overview">Zhaohui Xiao</ext-link>, Hainan University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Deming Tan, <email>tandeming@cdu.edu.cn</email>; Fei Xu, <email>feixu@nwpu.edu.cn</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Electrochemistry, a section of the journal Frontiers in Chemistry</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>08</day>
<month>12</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>1071274</elocation-id>
<history>
<date date-type="received">
<day>16</day>
<month>10</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>17</day>
<month>11</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Tan, Xiong, Zhang, Fan, Wang and Xu.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Tan, Xiong, Zhang, Fan, Wang and Xu</copyright-holder>
<license xlink:href="http://creativecommons.org/licenses/by/4.0/">
<p>This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.</p>
</license>
</permissions>
<abstract>
<p>The practical application of splitting water to generate hydrogen is to a large extent hindered by an oxygen evolution reaction (OER) process. Electrocatalysts with low-cost, high activity, and durability are essential for the low kinetic threshold of the OER. Despite the high active performances of noble metal compound electrocatalysts like IrO<sub>2</sub> and RuO<sub>2</sub>, they are heavily restricted by the high cost and scarcity of noble metal elements. In this context, noble-metal-free electrocatalysts have acquired increasing significance in recent years. So far, a broad spectrum of noble-metal-free electrocatalysts has been developed for improved OER performance. In this review, three types of electrolysis and some evaluation criteria are introduced, followed by recent progress in designing and synthesizing noble-metal-free alkaline OER electrocatalysts, with the classification of metal oxides/(oxy)hydroxides, carbon-based materials, and metal/carbon hybrids. Finally, perspectives are also provided on the future development of the alkaline OER on active sites and stability of electrocatalysts.</p>
</abstract>
<kwd-group>
<kwd>OER electrocatalyst</kwd>
<kwd>electrochemical water splitting</kwd>
<kwd>noble-metal-free electrocatalyst</kwd>
<kwd>water electrolysis</kwd>
<kwd>anion exchange membrane electrolysis</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Splitting water to generate H<sub>2</sub> and O<sub>2</sub>, through the hydrogen evolution reaction (HER) and oxygen evolution reaction (OER), is regarded as an ideal solution to the energy shortage and climate problems. (<xref ref-type="bibr" rid="B8">Doyle and Lyons, 2016</xref>; <xref ref-type="bibr" rid="B35">Liu et al., 2018</xref>; <xref ref-type="bibr" rid="B40">Lyu et al., 2019</xref>) Benefitting from its high-density energy and non-polluting nature, H<sub>2</sub> is usually acknowledged to be the ultimate clean energy. (<xref ref-type="bibr" rid="B27">Hunter et al., 2016</xref>; <xref ref-type="bibr" rid="B75">Zuo et al., 2019</xref>; <xref ref-type="bibr" rid="B46">Park et al., 2022</xref>) However, the realization of large-scale production of H<sub>2</sub> is heavily dependent on the development of low-cost alternative technologies. Steam reforming of natural gas can be used for large-scale production of H<sub>2</sub> (<xref ref-type="bibr" rid="B62">Wu et al., 2020</xref>; <xref ref-type="bibr" rid="B9">&#x10e;urovi&#x10d; et al., 2021</xref>), but this method is unsustainable and harmful to the environment. Alternatively, the water electrolysis produces hydrogen gas in a renewable and potentially cost-effective way, which utilizes electric power to split the oxygen and hydrogen bond in a water molecule. It is an especially attractive solution for H<sub>2</sub> production compared to the use of steam reforming of natural gas. (<xref ref-type="bibr" rid="B29">Jamesh and Harb, 2021</xref>) According to the type of ions transporting through the electrolyte and operating temperature, three main types (<xref ref-type="bibr" rid="B49">Plevov&#xe1; et al., 2021</xref>) of the water electrolysis process are distinguished: high-temperature solid oxide steam electrolysis, proton exchange membrane (PEM) electrolysis, and anion exchange membrane (AEM) electrolysis (<xref ref-type="bibr" rid="B5">Carmo et al., 2013</xref>; <xref ref-type="bibr" rid="B47">Peng et al., 2016</xref>; <xref ref-type="bibr" rid="B50">Reier et al., 2017</xref>; <xref ref-type="bibr" rid="B64">Xu et al., 2018</xref>; <xref ref-type="bibr" rid="B55">Todoroki and Wadayama, 2019</xref>; <xref ref-type="bibr" rid="B33">Li et al., 2021</xref>).</p>
<sec id="s1-1">
<title>1.1 High-temperature solid oxide steam electrolysis</title>
<p>Solid oxide steam electrolysis exhibits high performance in the absence of noble-metal catalysts like platinum. Nevertheless, this is at the cost of the high energy consumption and strict material requirements, thus becoming the least-used technology among the three types mentioned in this study. (<xref ref-type="bibr" rid="B22">Hauch et al., 2008</xref>)</p>
</sec>
<sec id="s1-2">
<title>1.2 PEM water electrolysis</title>
<p>PEM electrolyzers use proton exchange membranes to separate the gas products. (<xref ref-type="bibr" rid="B5">Carmo et al., 2013</xref>) It is a highly flexible, intensive, and compact technology with higher current density, lower Ohmic losses, and a larger partial load range in comparison to alkaline electrolyzers. Nevertheless, the high cost of PEM and the narrow choice of available catalysts hinder its widespread application. (<xref ref-type="bibr" rid="B10">Eftekhari, 2017a</xref>)</p>
</sec>
<sec id="s1-3">
<title>1.3 AEM water electrolysis</title>
<p>In contrast to the PEM process, the AEM process performs in an alkaline environment (<xref ref-type="fig" rid="F1">Figure 1</xref>), which could circumvent the limitations of the PEM system and enable the use of cheap catalysts like metal oxides. (<xref ref-type="bibr" rid="B64">Xu et al., 2018</xref>) Consequently, AEM is by far the most prevailing technology because of its low cost and a variety of available catalysts, making it an attractive candidate for large-scale commercial applications, e.g., in hydrogen production. (<xref ref-type="bibr" rid="B48">Pletcher and Li, 2011</xref>)</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Schematic diagram of an AEM process system. (<xref ref-type="bibr" rid="B64">Xu et al., 2018</xref>) Copyright 2018, American Chemical Society.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g001.tif"/>
</fig>
<p>AEM is an attractive option because of its well-matured technology in the hydrogen economy scheme, which however AEM technology needs further improvement to become competitive with the PEM process. This goal creates some important research fields of AEM and leads to the development of increasingly more active catalysts. (<xref ref-type="bibr" rid="B9">&#x10e;urovi&#x10d; et al., 2021</xref>) Therefore, this review specifically focuses on the catalysts for an OER in the AEM process. In the following section, fundamental electrochemistry and evaluation criteria of an OER in the AEM process will be discussed.</p>
</sec>
<sec id="s1-4">
<title>1.4 Fundamental electrochemistry of an OER in alkaline environments</title>
<p>Under alkaline conditions, the overall water oxidation reaction is (<xref ref-type="bibr" rid="B34">Liang et al., 2021</xref>)<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:mn>4</mml:mn>
<mml:msup>
<mml:mrow>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mi mathvariant="normal">H</mml:mi>
</mml:mrow>
<mml:mo>&#x2212;</mml:mo>
</mml:msup>
<mml:mo>&#x2192;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mn>2</mml:mn>
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<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">g</mml:mi>
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</mml:mrow>
<mml:mo>&#x2b;</mml:mo>
<mml:mn>2</mml:mn>
<mml:msub>
<mml:mi mathvariant="normal">H</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">l</mml:mi>
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</mml:mrow>
<mml:mo>&#x2b;</mml:mo>
<mml:mn>4</mml:mn>
<mml:msup>
<mml:mi mathvariant="normal">e</mml:mi>
<mml:mo>&#x2212;</mml:mo>
</mml:msup>
<mml:mo>,</mml:mo>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>where (g) refers to the gas phase and (l) the liquid phase.</p>
<p>The OER process in an alkaline medium is considered to proceed as the following steps (<xref ref-type="bibr" rid="B73">Zhou et al., 2017</xref>):<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
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<mml:mo>,</mml:mo>
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<label>(2)</label>
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<disp-formula id="e3">
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<label>(3)</label>
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</p>
<p>where <sup>&#x2217;</sup> represents the catalyst active site and <sup>&#x2217;</sup>OH, <sup>&#x2217;</sup>O, and <sup>&#x2217;</sup>OOH represent the species adsorbed on the active site.</p>
</sec>
<sec id="s1-5">
<title>1.5 Evaluation criteria of OER catalysts</title>
<p>It is essentially important to establish standards for evaluating the performance of OER electrocatalysts. Here, we summarized some well-established criteria including overpotential (&#x3b7;), onset potential, turnover frequency (TOF), Faradic efficiency, Tafel slope (b), stability, and activity. (<xref ref-type="bibr" rid="B54">Tahir et al., 2017</xref>; <xref ref-type="bibr" rid="B40">Lyu et al., 2019</xref>)</p>
<sec id="s1-5-1">
<title>1.5.1 Overpotential</title>
<p>The overpotential critically determines the extra energy consumption and energy conversion efficiencies. Low overpotential is a noteworthy quality of OER catalysts for reducing these parameters. (<xref ref-type="bibr" rid="B60">Wei and Xu, 2018</xref>)<disp-formula id="e6">
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<mml:mi mathvariant="normal">o</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>,</mml:mo>
</mml:mrow>
</mml:math>
<label>(7)</label>
</disp-formula>
<disp-formula id="e8">
<mml:math id="m8">
<mml:mrow>
<mml:mi>b</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mo>&#x2212;</mml:mo>
<mml:mn>2.303</mml:mn>
<mml:mo>&#x2219;</mml:mo>
<mml:mi mathvariant="normal">R</mml:mi>
<mml:mi mathvariant="normal">T</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>&#x3b1;</mml:mi>
<mml:mi mathvariant="normal">F</mml:mi>
</mml:mrow>
</mml:mfrac>
<mml:mo>.</mml:mo>
</mml:mrow>
</mml:math>
<label>(8)</label>
</disp-formula>
</p>
<p>Here, j represents the corresponding current density, j<sub>o</sub> represents the exchange current density, and <italic>&#x3b1;</italic> represents exchange coefficients, and generally, <italic>&#x3b1;</italic> &#x2248; 1/2. (<xref ref-type="bibr" rid="B43">Naimi and Antar, 2018</xref>)</p>
</sec>
<sec id="s1-5-2">
<title>1.5.2 Tafel slope</title>
<p>Another significant parameter is the Tafel slope (b), which can be calculated from the equation (<xref ref-type="bibr" rid="B46">Park et al., 2022</xref>). A high Tafel slope means a rapid increase of overpotential with the current density, indicating inferior OER kinetics of the electrocatalysts.</p>
</sec>
<sec id="s1-5-3">
<title>1.5.3 Faradic efficiency</title>
<p>Faradic efficiency (FE) is the ratio of the amount of target gas detected in the experiment to the amount of gas calculated. (<xref ref-type="bibr" rid="B53">Sun et al., 2022</xref>) Faradic efficiency can be calculated as follows:<disp-formula id="e9">
<mml:math id="m9">
<mml:mrow>
<mml:mi mathvariant="normal">F</mml:mi>
<mml:mi mathvariant="normal">E</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mn>4</mml:mn>
<mml:mi mathvariant="normal">F</mml:mi>
<mml:msub>
<mml:mi mathvariant="normal">n</mml:mi>
<mml:msub>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
</mml:msub>
</mml:mrow>
<mml:mrow>
<mml:mi mathvariant="normal">I</mml:mi>
<mml:mi mathvariant="normal">t</mml:mi>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
<mml:mo>%</mml:mo>
<mml:mo>,</mml:mo>
</mml:mrow>
</mml:math>
<label>(9)</label>
</disp-formula>where F represents Faraday&#x2019;s constant, <inline-formula id="inf1">
<mml:math id="m10">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">n</mml:mi>
<mml:msub>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula> represents the amount of produced O<sub>2</sub>, I represents the constant current applied, and t represents the reaction time.</p>
</sec>
<sec id="s1-5-4">
<title>1.5.4 Turnover frequency</title>
<p>The TOF for the OER is the average number of moles of O<sub>2</sub> evolved per active site and time unit. (<xref ref-type="bibr" rid="B9">&#x10e;urovi&#x10d; et al., 2021</xref>) It is also an important parameter to estimate the OER catalysts. The calculation of TOF is demonstrated as follows:<disp-formula id="e10">
<mml:math id="m11">
<mml:mrow>
<mml:mi mathvariant="normal">T</mml:mi>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mi mathvariant="normal">F</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mi mathvariant="normal">j</mml:mi>
<mml:mi mathvariant="normal">S</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mn>4</mml:mn>
<mml:mi mathvariant="normal">n</mml:mi>
<mml:mi mathvariant="normal">F</mml:mi>
</mml:mrow>
</mml:mfrac>
<mml:mo>.</mml:mo>
</mml:mrow>
</mml:math>
<label>(10)</label>
</disp-formula>
</p>
<p>Here, j is the current density, S represents the electrode area, and n represents the number of active sites.</p>
<p>Active sites normally originate from the surface self-reconstruction during the dynamic catalysis process. (<xref ref-type="bibr" rid="B13">Fabbri et al., 2017</xref>) However, it is difficult to determine the precise number of active sites in practice. The evaluation of the number of active sites by measuring the total active species often leads to overestimated results as inert species are not excluded. Despite the advances in the current understanding of reaction mechanisms, the exact mechanism involved in a catalysis process is still insubstantial. A combination of various <italic>in situ</italic> techniques and theoretical calculations may be helpful to better understand the reaction mechanism and the true active sites.</p>
</sec>
<sec id="s1-5-5">
<title>1.5.5 Electrolyte</title>
<p>Acidity and basicity of the electrolyte exert considerable influence on the performance of OER electrocatalysts. So far, as reported in literatures, alkaline electrolytes are the most favorable for most OER electrocatalysts, followed by neutral electrolytes, and the least favorable for acidic electrolytes. (<xref ref-type="bibr" rid="B54">Tahir et al., 2017</xref>; <xref ref-type="bibr" rid="B4">Cai et al., 2019</xref>; <xref ref-type="bibr" rid="B68">Zeradjanin et al., 2021</xref>; <xref ref-type="bibr" rid="B32">Kim et al., 2022</xref>) At present, most researchers focus on designing and synthesizing electrocatalysts which are stable in an alkaline electrolyte. Nevertheless, most of these catalysts cannot resist the high oxidative potential under acidic conditions. Therefore, it is of great importance to develop OER electrocatalysts that can perform over a wide pH range.</p>
</sec>
<sec id="s1-5-6">
<title>1.5.6 Stability</title>
<p>It is essential to evaluate the stability of electrocatalysts toward practical applications. An electrolyte plays an important role in the stability of catalysts as most catalysts are apt to be corrupted in an acidic medium but can perform well in a basic medium. The stability of catalysts is also affected by a working electrode in most cases, and typically catalysts fabricated on the working electrode directly show higher stability. It is questionable whether the reported stability in the literature meets the requirements of real devices. The recently developed techniques which employed <italic>ex situ</italic> and <italic>in situ</italic> XRD, TEM, SEM, and XPS for monitoring the structure evolution of catalysts might be the answer to the problem.</p>
<p>The OER is a key step in the AEM process, but it is kinetically sluggish due to its four-electron transfer process. (<xref ref-type="bibr" rid="B63">Xie et al., 2022</xref>) In order to maintain the momentum of future advances of water splitting, the development of high-performance OER electrocatalysts is necessary. RuO<sub>2</sub> and IrO<sub>2</sub> are at present the ideal OER catalysts because of their high catalytic activity both in an acidic and alkaline environment. Nevertheless, the scarcity of Ir and Ru elements inducing the large-scale production of RuO<sub>2</sub> and IrO<sub>2</sub> in an OER runs into bottlenecks. (<xref ref-type="bibr" rid="B9">&#x10e;urovi&#x10d; et al., 2021</xref>) For the last few years, the search for more abundant and lower cost alternatives to the noble-metal-based catalysts has stimulated an influx of research into this field and leads to significant advances. (<xref ref-type="bibr" rid="B8">Doyle and Lyons, 2016</xref>; <xref ref-type="bibr" rid="B11">Eftekhari, 2017b</xref>; <xref ref-type="bibr" rid="B52">Stelmachowski et al., 2021</xref>) For instance, some noble-metal-free-based OER electrocatalysts like transition metal-based materials (<xref ref-type="bibr" rid="B28">Huynh et al., 2015</xref>; <xref ref-type="bibr" rid="B15">Gao et al., 2021</xref>; <xref ref-type="bibr" rid="B57">Wang et al., 2021</xref>; <xref ref-type="bibr" rid="B58">Wang et al., 2022</xref>) and carbon-based materials (<xref ref-type="bibr" rid="B16">Gao et al., 2019</xref>) are recently reported to perform well in both acidic and alkaline conditions. The encouraging results shows that some noble-metal-free-based electrocatalysts exhibit a remarkable catalytic activity in alkaline conditions and sometimes are superior to noble-metal-based electrocatalysts (<xref ref-type="bibr" rid="B38">Lu et al., 2017</xref>; <xref ref-type="bibr" rid="B37">Lu et al., 2019</xref>). For this reason, this review aims to briefly summarize the recent advances in noble-metal-free electrocatalysts for an alkaline OER process.</p>
</sec>
</sec>
</sec>
<sec id="s2">
<title>2 Noble-metal-free electrocatalysts for the OER in an alkaline electrolyte</title>
<sec id="s2-1">
<title>2.1 Non-precious metal oxide/(oxy)hydroxide materials</title>
<p>Noble-metal-free metal oxides/(oxy)hydroxides attracted great interest due to their outstanding stability and abundance (<xref ref-type="bibr" rid="B41">Marschall and Wang, 2014</xref>). They can be prepared and/or obtained directly from metal X-ides (X-: sulf-, nitr-, carb-, chalcogen-, etc.) during an OER process. (<xref ref-type="bibr" rid="B7">Ding et al., 2019</xref>; <xref ref-type="bibr" rid="B26">Huang et al., 2019</xref>; <xref ref-type="bibr" rid="B75">Zuo et al., 2019</xref>; <xref ref-type="bibr" rid="B63">Xie et al., 2022</xref>) In alkaline electrolytes, iron oxides/hydroxides, cobalt oxides/hydroxides, and nickel oxides/hydroxides have been studied extensively among the earth-abundant metals, which thus will be emphasized in the following.</p>
<p>Iron oxides are promising electrocatalysts due to the low cost and abundance of iron and have been studied extensively. (<xref ref-type="bibr" rid="B27">Hunter et al. 2016</xref>) found that OER activity of Fe<sub>2</sub>O<sub>3</sub> nanostructures depends on the number of Fe edge-site atoms. (<xref ref-type="bibr" rid="B31">Kauffman et al., 2019</xref>) Edge-site located Fe atoms were recognized as the main reaction centers, and the OER turnover frequencies produced by an edge-site located Fe is approximately 150 times greater than that of Fe atoms on the surface (<xref ref-type="fig" rid="F2">Figure 2</xref>). Furthermore, by using DFT calculations, more advantageous edge site-based OERs were revealed, which have lower predicted overpotentials benefited from the modification of intermediate binding. Boettcher et al. reported a new OER catalytic model of iron (oxy) hydroxide in alkaline media. (<xref ref-type="bibr" rid="B74">Zou et al., 2015</xref>) The catalyst dissolution rate is low at overpotentials of about 350&#xa0;mV. Mass loading influences the OER current density to a great extent, and the AuOx/Au substrate can greatly improve the catalytic activity. The choice of the substrate has little influence on the activity, and a linear relationship between the current density and loading is identified. (<xref ref-type="bibr" rid="B74">Zou et al., 2015</xref>) J. Xu and co-workers designed and successfully synthesized ferromagnetic Co<sub>3</sub>&#x2212;xFe<sub>x</sub>O<sub>4</sub> spinels using sulfurization. (<xref ref-type="bibr" rid="B61">Wu et al., 2021</xref>) Benefitting from limited oxyhydroxide layer and the stable configuration of Co<sub>3</sub>&#x2212;xFe<sub>x</sub>O<sub>4</sub>/Co(Fe)O<sub>x</sub>H<sub>y</sub>, the reconstructed Co(Fe)O<sub>x</sub>H<sub>y</sub> owns an order of magnitude higher catalytic activity than the directly synthesized Co (Fe) oxyhydroxides. (<xref ref-type="bibr" rid="B61">Wu et al., 2021</xref>)</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>
<bold>(A)</bold> OER voltammograms of 2L-Fe<sub>2</sub>O<sub>3</sub>/Au under different loadings in N<sub>2</sub> purged 0.1&#xa0;M KOH (<xref ref-type="bibr" rid="B31">Kauffman et al., 2019</xref>). <bold>(B)</bold> TOF and mass activity <italic>versus</italic> the relative population of edge-site located Fe atoms (<xref ref-type="bibr" rid="B31">Kauffman et al., 2019</xref>). Copyright 2019, American Chemical Society.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g002.tif"/>
</fig>
<p>Cobalt oxides have been used as water oxidation catalysts for more than 70 years. (<xref ref-type="bibr" rid="B27">Hunter et al., 2016</xref>; <xref ref-type="bibr" rid="B67">Yu et al., 2022</xref>) Co<sub>2</sub>O<sub>3</sub>, CoO<sub>2</sub>, and CoO were first found feasible under anodic bias by initial electrochemical characterization in alkaline conditions. (<xref ref-type="bibr" rid="B12">El Wakkad and Hickling, 1950</xref>) Some newly developed structures have shown greater prospects, such as Co<sub>3</sub>O<sub>4</sub>. (<xref ref-type="bibr" rid="B6">Dangwal Pandey et al., 2012</xref>) Dismukes and co-workers synthesized lithium cobalt oxide having two polymorphs. The results revealed that the existence of a cubic core of Co<sub>4</sub>O<sub>4</sub> indicates the activity of water oxidation. (<xref ref-type="bibr" rid="B17">Gardner et al., 2012</xref>) The synthesized pure cubic 400-Li<sub>2</sub>Co<sub>2</sub>O<sub>4</sub> per bulk cobalt atom has a TOF value of 1.0 &#xd7; 10<sup>&#x2212;3</sup> s<sup>&#x2212;1</sup> (<xref ref-type="fig" rid="F3">Figures 3A,B</xref>). The TOF has reached 1.9 &#xd7; 10<sup>&#x2212;3</sup> s<sup>&#x2212;1</sup> after normalization to the amount of cobalt that is accessible on the surface. The electrochemical characterization of membrane electrode assemblies (MEAs) reveals that the current density of the MEA containing cubic 400-Li<sub>2</sub>Co<sub>2</sub>O<sub>4</sub> is 50 times higher than of the current for the MEA only with Nafion (<xref ref-type="fig" rid="F3">Figure 3C</xref>). Wang et al. successfully synthesized Co<sub>3</sub>O<sub>4</sub> nanoparticles with controllable size and found that the absence of ligands can lead to high activity. (<xref ref-type="bibr" rid="B20">Grzelczak et al., 2013</xref>) The tendency that the activity increases with the decrease in particle size reported in the article explicitly demonstrated that water oxidation was primarily dependent on the availability of the surface cobalt atoms. (<xref ref-type="bibr" rid="B20">Grzelczak et al., 2013</xref>) M&#xfc;ller et al. successfully synthesized composition- and size-controlled Co<sub>3</sub>O<sub>4</sub> nanoparticles without surfactants. (<xref ref-type="bibr" rid="B2">Blakemore et al., 2013</xref>) The obtained cobalt oxide nanoparticles delivered the highest TOF (0.21&#xa0;mol O<sub>2</sub> (mol Co<sub>surface</sub>)<sup>&#x2212;1</sup> s<sup>&#x2212;1</sup>), and the overpotential of their Co<sub>3</sub>O<sub>4</sub> nanoparticles obtained is 314&#xa0;mV at 0.5&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>. Meanwhile, the mass activity of 10 A m<sup>&#x2212;2</sup>g<sup>&#x2212;1</sup> is achieved at 500&#xa0;mV overpotential. (<xref ref-type="bibr" rid="B2">Blakemore et al., 2013</xref>) More recently, Yeo et al. reported an iron (III) ion-adsorbed amorphous cobalt oxide as high-efficient OER catalysts. (<xref ref-type="bibr" rid="B19">Gong et al., 2017</xref>) The synergetic effect of Fe<sup>3&#x2b;</sup> and CoO<sub>x</sub> reduces the overpotential of up to 69&#xa0;mV at 10&#xa0;mAcm<sup>&#x2212;2</sup>. The catalyst has a low overpotential of only 309&#xa0;mV and can catalyze the OER process at 10&#xa0;mAcm<sup>&#x2212;2</sup>. The stability of the obtained catalyst was enhanced compared with that of the CoO<sub>x</sub> catalyst, and the Tafel slope of the synthesized catalyst was 27.6&#xa0;mVdec<sup>&#x2212;1</sup>. (<xref ref-type="bibr" rid="B19">Gong et al., 2017</xref>)</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>
<bold>(A)</bold> Concentration of dissolved O<sub>2</sub> measured by a Clark-type electrode at 23&#xb0;C, pH 5.8 for lithium cobalt oxides synthesized at <bold>(A)</bold> 400&#xb0;C, <bold>(B)</bold> 500&#xb0;C, <bold>(C)</bold> 600&#xb0;C, and <bold>(D)</bold> 700&#xb0;C, and <bold>(B)</bold> the total surface area of a synthesized catalyst. <bold>(C)</bold> Bulk electrolysis of the Nafion-only control (solid gray line), 700-LiCoO<sub>2</sub> (dashed gray line), and 400-Li<sub>2</sub>Co<sub>2</sub>O<sub>4</sub> (solid black line). (<xref ref-type="bibr" rid="B17">Gardner et al., 2012</xref>) Copyright 2012, Wiley-VCH.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g003.tif"/>
</fig>
<p>In 1966, nickel oxides were first identified as water oxidation catalysts by <xref ref-type="bibr" rid="B3">Bode et al. (1966</xref>). Also, further deep studies were made in the following two&#xa0;decades (<xref ref-type="bibr" rid="B44">Oliva et al., 1982</xref>). Owing to the high OER catalytic activity in alkaline media, the application of nickel oxides in electrocatalysis has attracted great attention recently (<xref ref-type="bibr" rid="B67">Yu et al., 2022</xref>) (<xref ref-type="bibr" rid="B42">M&#x142;ynarek et al., 1984</xref>). A detailed study of iron-doped nickel oxides by Boettcher et al. <xref ref-type="bibr" rid="B56">Trotochaud et al. (2014</xref>) underscored the essentiality of impurity influences on the performance of electrocatalysts (<xref ref-type="fig" rid="F4">Figure 4</xref>). (<xref ref-type="bibr" rid="B56">Trotochaud et al., 2014</xref>) Lyons and co-workers investigated the mechanisms of nickel oxide electrodes and revealed the importance of Ni (III) or Ni (IV) species and proposed a more general physisorbed peroxide mechanism. (<xref ref-type="bibr" rid="B39">Lyons and Brandon, 2008</xref>) They used the electrode as the hole acceptor throughout instead of invoking multiple oxidation states of nickel. (<xref ref-type="bibr" rid="B39">Lyons and Brandon, 2008</xref>) Ma et al. reported a high catalytic active single-atom W<sup>6&#x2b;</sup>-doped &#x3b1;-Ni(OH)<sub>2</sub> OER electrocatalyst. (<xref ref-type="bibr" rid="B66">Yan et al., 2019</xref>) Overpotential values of 237&#xa0;mV and 267&#xa0;mV were obtained at 10&#xa0;mAcm<sup>&#x2212;2</sup> and 80&#xa0;mAcm<sup>&#x2212;2</sup>, respectively. Also, a low Tafel slope of 33&#xa0;mVdec<sup>&#x2212;1</sup> was obtained in a 1&#xa0;M KOH electrolyte. (<xref ref-type="bibr" rid="B66">Yan et al., 2019</xref>)</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>SEM images of synthesized Ni(OH)<sub>2</sub> (left) and Ni<sub>0.75</sub>Fe<sub>0.25</sub>(OH)<sub>2</sub> (right) catalysts as-deposited and after 24&#xa0;h of aging in 40&#xb0;C 1&#xa0;M KOH. (<xref ref-type="bibr" rid="B56">Trotochaud et al., 2014</xref>) Copyright 2014, American Chemical Society.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g004.tif"/>
</fig>
</sec>
<sec id="s2-2">
<title>2.2 Metal-free carbon-based materials</title>
<p>Carbon-based metal-free electrocatalysts have been considered promising OER catalysts because of their intriguing properties like nature abundance and chemical stability. (<xref ref-type="bibr" rid="B1">An et al., 2022</xref>) In 2009, carbon nanotubes doped with nitrogen were found to have excellent OER catalytic activity without fuel crossover and poisoning in alkaline media. (<xref ref-type="bibr" rid="B18">Gong et al., 2009</xref>) More recently, these new types of catalysts were discovered to be superior to metal catalysts for the OER. (<xref ref-type="bibr" rid="B70">Zhang et al., 2015</xref>)</p>
<p>Dai and co-workers successfully synthesized a high-efficiency electron-acceptor by absorbing buckminsterfullerene (C<sub>60</sub>) onto single-walled carbon nanotubes (SWCNTs). (<xref ref-type="bibr" rid="B16">Gao et al., 2019</xref>) The obtained metal-free C<sub>60</sub>-SWCNT electrocatalysts were shown to be excellent for the OER process over a wide pH range from acidic to alkaline. (<xref ref-type="bibr" rid="B16">Gao et al., 2019</xref>) The current density (10&#xa0;mAcm<sup>&#x2212;2</sup>) of C<sub>60</sub>-SWCNT is 50, 5.3, and 1.2 times higher than that of the pure C<sub>60</sub>, SWCNTs and commercial RuO<sub>2</sub> at 1.69&#xa0;V potential, respectively. (<xref ref-type="bibr" rid="B16">Gao et al., 2019</xref>) Wu et al. synthesized a carbon quantum dot/graphene composite electrocatalyst with a simple novel two-step procedure (<xref ref-type="fig" rid="F5">Figure 5A</xref>). (<xref ref-type="bibr" rid="B71">Zhao et al., 2019a</xref>) The corresponding Tafel slope of the obtained hybrid is 44&#xa0;mV dec<sup>&#x2212;1</sup>. Moreover, the stability test of obtained hybrids was carried out by CV scanning for 2000 cycles, and negligible change was observed. Such good electrocatalytic performance is attributed to various defect sites exposed by small-sized graphene flakes and carbon quantum dots, as well as the fast charge transfer rate and high active surface area. (<xref ref-type="bibr" rid="B71">Zhao et al., 2019a</xref>) Dai et al. reported an easy method with mass production to synthesize N and P co-doped 3D mesoporous carbon foams as bifunctional electrocatalysts for oxygen reduction and OER (<xref ref-type="fig" rid="F5">Figure 5B</xref>). (<xref ref-type="bibr" rid="B70">Zhang et al., 2015</xref>) The obtained catalyst demonstrated lower onset potentials and higher currents than those of the Pt/C electrode. Furthermore, the material exhibits a lower onset potential than the RuO<sub>2</sub> nanoparticle reference. Wang et al. successfully introduced the sp-hybridized nitrogen (sp-N) into graphdiyne, which exhibits potential for the OER. (<xref ref-type="bibr" rid="B72">Zhao et al., 2019b</xref>) In their research, heteroelements N and S were introduced into few-layer acetylenic groups in graphdiyne by a one-pot facile method, and the ratios of the N atoms and the S atoms were able to be tuned. (<xref ref-type="bibr" rid="B72">Zhao et al., 2019b</xref>) The heteroelement co-doped sample exhibits catalytic activity to those individually doped (either N or S doping) samples and most reported metal-free catalysts. (<xref ref-type="bibr" rid="B72">Zhao et al., 2019b</xref>) L. Xin and co-workers built a large library of single-atom catalysts by characterization and analysis of 37 monometallic elements. (<xref ref-type="bibr" rid="B21">Han et al., 2022</xref>) By employing an <italic>in situ</italic> method, they presented a unified set of principles on the state of oxidization, the number of coordinates, the length of the bond, and the coordination element of single atoms for the preparation of single-atom catalysts. They utilized the built single-atom-catalyst library to create complex multi-metallic single-atom phases with up to 12 different elements. (<xref ref-type="bibr" rid="B21">Han et al., 2022</xref>) The synthesized 12-metal single-atom catalyst exhibits higher current density, mass activity, and turnover frequency than those of the mixed and individual monometallic single-atom catalysts at the same potentials. (<xref ref-type="bibr" rid="B21">Han et al., 2022</xref>) OER catalysis of the 12-metal single-atom catalyst was performed at a constant current of 10&#xa0;mAcm<sup>&#x2212;2</sup> for 130&#xa0;h, and no appreciable potential change was observed.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>
<bold>(A)</bold> Probable formation route of the carbon quantum dot/graphene heterostructure. (<xref ref-type="bibr" rid="B71">Zhao et al., 2019a</xref>) Copyright 2019, the Royal Society of Chemistry. <bold>(B)</bold> Preparation of porous carbon co-doped with N and P electrocatalysts. (<xref ref-type="bibr" rid="B70">Zhang et al., 2015</xref>) Copyright 2015, Macmillan Publishers Limited.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g005.tif"/>
</fig>
</sec>
<sec id="s2-3">
<title>2.3 Non-precious metal and carbon hybrids</title>
<p>The poor stability and low conductivity of transition metals (TMs) have severely impeded their use in large-scale H<sub>2</sub> production. As is known, carbon nanotubes and graphites have remarkable conductivity and good chemical/thermal stability. The integration of carbon nanomaterials with TM could, therefore, circumvent the aforementioned issues on TM-based electrocatalysts (<xref ref-type="fig" rid="F6">Figure 6</xref>). (<xref ref-type="bibr" rid="B24">Hou et al., 2015</xref>; <xref ref-type="bibr" rid="B59">Wang et al., 2015</xref>; <xref ref-type="bibr" rid="B30">Jiang et al., 2018</xref>; <xref ref-type="bibr" rid="B25">Hu et al., 2019</xref>) Therefore, TM/carbon hybrids are emerging as new efficient OER electrocatalysts. Usually, these composites demonstrated both the attributes of the respective components (e.g., TM or carbon) and novel promising properties achieved through the combination of carbon nanomaterials and TM, such as Ni@ nitrogen-doped graphene [Mo<sub>3</sub>S<sub>13</sub>]<sup>2-</sup>@ graphene. (<xref ref-type="bibr" rid="B65">Xu et al., 2017</xref>; <xref ref-type="bibr" rid="B45">Ouyang et al., 2018</xref>) The new attributes of these hybrids make them promising alternatives for the next-generation, low-cost, and efficient OER catalysts rather than a precious metal electrochemical catalyst.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Schematic diagram of the synergistic effect of TMs and carbon nanomaterials.</p>
</caption>
<graphic xlink:href="fchem-10-1071274-g006.tif"/>
</fig>
<p>Zhang and co-workers successfully achieved a mesoporous polyhedral structure of graphite carbon enclosing CoTe<sub>2</sub> nanocrystals based on a single heat treatment involving tellurizing and carbonizing simultaneously. (<xref ref-type="bibr" rid="B36">Liu et al., 2017</xref>) The texture of the hybrid provides a simple path for the OER with increased activity and strong stability. The hybrid showed an overpotential of 300&#xa0;mV at 10&#xa0;mAcm<sup>&#x2212;2</sup>. Moreover, the graphitic carbon matrix provides a high electrical conductivity and rich access to active sites besides interfacing with the confined nanocrystalline CoTe<sub>2</sub> in an intensive way for the enhancement of the OER. (<xref ref-type="bibr" rid="B36">Liu et al., 2017</xref>) Huang and co-workers proposed a general and rational strategy for a group of monodispersed TMs embedded in graphene. (<xref ref-type="bibr" rid="B14">Fei et al., 2018</xref>) They have established that the resulting M@graphene (M &#x3d; Fe, Co, Ni) hybrids lead to minimum distortion of the 2D graphene lattice. More importantly, the existence of the well-defined MN<sub>4</sub>C<sub>4</sub> moieties in different holey graphene frameworks provides a desirable model system for determining and quantifying the relationship between the atomistic structure of the metal centers and its catalytic properties. Owing to the high activity of the intrinsic activity of Ni embedded in nitrogen-doped holey graphene frameworks, the density of the active sites increases as the metal loading increases. (<xref ref-type="bibr" rid="B14">Fei et al., 2018</xref>) Zhu et al. developed an effective bifunctional electrocatalyst based on porphyra-derived S-doped Fe-N-C. (<xref ref-type="bibr" rid="B69">Zhang et al., 2019</xref>) The resultant hybrid exhibits a low Tafel slope of 59&#xa0;mV dec<sup>&#x2212;1</sup> and an overpotential of 410&#xa0;mV at 10&#xa0;mAcm<sup>&#x2212;2</sup> in a 0.1&#xa0;M KOH medium. Further investigation revealed that S-doping could optimize the charge and spin distribution of the Fe&#x2013;N&#x2013;C hybrid, resulting in good activities in the OER, which mainly attributes to the Fe-Nx and Fe-N<sub>3</sub>&#x7c;S sites individually. (<xref ref-type="bibr" rid="B69">Zhang et al., 2019</xref>) G. Gomes and co-workers designed an easy one-step sustainable protocol to synthesize nickel/nickel oxide@carbon bifunctional electrocatalysts from the wastes of cauliflower leaves. The electrocatalytic performance of the resultant hybrid was found dependent on the pyrolysis temperature. (<xref ref-type="bibr" rid="B23">Hoang et al., 2020</xref>) At 10&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>, the obtained hybrids require overpotentials of 346&#xa0;mV and moderate Tafel slopes of 70&#xa0;mV dec<sup>&#x2212;1</sup> for an OER in a 0.1&#xa0;M KOH electrolyte. The synthesized electrocatalyst needs only 1.688&#xa0;V to reach a current density of 10&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup> when incorporated into a two-electrode water electrolyzer. Medeiros et al. reported on the synthesis, structural, morphological, and electrochemical characterization of Ni-NiO/carbon nanofibers for an OER catalytic process by solution blow spinning. (<xref ref-type="bibr" rid="B51">Silva et al., 2021</xref>) The XPS analysis demonstrated that a small fraction of the species of nickel present in the fiber surface is sufficient to promote a good performance in the OER process. The performance of the Ni-NiO/C_An electrode was not affected although the size of the nanoparticles slightly exceeds that of the electrode. (<xref ref-type="bibr" rid="B51">Silva et al., 2021</xref>) Also, the active species of Ni<sup>3&#x2b;</sup> were found to be the main factor affecting the catalysis performance.</p>
</sec>
</sec>
<sec id="s3">
<title>3 Summary and perspectives</title>
<p>It is essential to identify the active sites and their coordination structure for OER catalysts as those attributes are closely associated with the catalyst activity and stability. Several major types of active sites are classified: defects, electron deficient site, metal center, etc. The debate over the active site of electrocatalysts underlines the complication of recognizing the real active sites despite various experimental techniques and computational methods being employed. One possibility is to use an <italic>in situ</italic> technique to monitor catalyst evolution during the OER to provide significant insight into active sites.</p>
<p>Material instability and operational instability are considered the two main types of catalyst instability that occurred in the catalytic system and have great influences on the stable catalytic action. Material instability is usually caused by material corrosion regardless of the test conditions. Future OER catalyst applications require the development of materials that can be operated under severe working conditions. For metal oxides, material stability can be improved through structure design and composition adjustment. For carbon-based catalysts, material stability can possibly be improved by increasing the degree of graphitization. Operational instability arises during electrochemical tests and is usually caused by potential-induced element dissolution and/or structure damage. One possible way to increase the operational instability is to use lower operation potential. However, low operation potential needs substantial improvements in the catalyst activity; hence, the design of a high active OER is highly desirable for the future commercial development of water electrolysis.</p>
</sec>
</body>
<back>
<sec id="s4">
<title>Author contributions</title>
<p>DT and FX contributed to the conception and design of the manuscript. DT and HX organized the database. DT wrote the whole draft of the manuscript. All authors contributed to manuscript revision, read, and approved the submitted version.</p>
</sec>
<sec sec-type="COI-statement" id="s5">
<title>Conflict of interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s6">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors, and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
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