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  <front>
    <journal-meta>
      <journal-id journal-id-type="nlm-ta">Energy Mater.</journal-id>
      <journal-id journal-id-type="publisher-id">ENERGYMATER</journal-id>
      <journal-title-group>
        <journal-title>Energy Materials</journal-title>
      </journal-title-group>
      <issn pub-type="epub">2770-5900</issn>
      <publisher>
        <publisher-name>OAE Publishing Inc.</publisher-name>
      </publisher>
    </journal-meta>
    <article-meta>
	<article-id pub-id-type="doi">10.20517/energymater.2026.217</article-id>
      <article-categories>
        <subj-group>
          <subject>Article</subject>
        </subj-group>
      </article-categories>
      <title-group>
        <article-title>Robust CoRuO<sub>x</sub> oxide catalysts with broad electrolyte compatibility toward superior hydrogen evolution</article-title>
      </title-group>
      <contrib-group>
        <contrib contrib-type="author">
          <name>
            <surname>Zheng</surname>
            <given-names>Qianqian</given-names>
          </name>
          <xref ref-type="aff" rid="I1">
            <sup>1</sup>
          </xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Li</surname>
            <given-names>Yang</given-names>
          </name>
          <xref ref-type="aff" rid="I1">
            <sup>1</sup>
          </xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Lu</surname>
            <given-names>Chunling</given-names>
          </name>
          <xref ref-type="aff" rid="I1">
            <sup>1</sup>
          </xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Maubane-Nkadimeng</surname>
            <given-names>Manoko S.</given-names>
          </name>
          <xref ref-type="aff" rid="I3">
            <sup>3</sup>
          </xref>
        </contrib>
        <contrib contrib-type="author" corresp="yes">
          <name>
            <surname>Feng</surname>
            <given-names>Tao</given-names>
          </name>
          <xref ref-type="aff" rid="I2">
            <sup>2</sup>
          </xref>
          <xref ref-type="aff" rid="I*">
            <sup>*</sup>
          </xref>
          <xref ref-type="corresp" rid="cor1" />
        </contrib>
        <contrib contrib-type="author" corresp="yes">
          <name>
            <surname>Niu</surname>
            <given-names>Bingbing</given-names>
          </name>
          <xref ref-type="aff" rid="I1">
            <sup>1</sup>
          </xref>
          <xref ref-type="aff" rid="I*">
            <sup>*</sup>
          </xref>
          <xref ref-type="corresp" rid="cor1" />
        </contrib>
      </contrib-group>
      <aff id="I1">
        <sup>1</sup>School of Science, University of Science and Technology Liaoning, Anshan 114051, Liaoning, China.</aff>
      <aff id="I2">
        <sup>2</sup>Department of Materials Science and Engineering, Southern University of Science and Technology, Shenzhen 518055, Guangdong, China.</aff>
      <aff id="I3">
        <sup>3</sup>Microscopy and Microanalysis Unit, School of Chemistry, University of Witwatersrand, Johannesburg 2050, South Africa.</aff>
      <author-notes>
        <corresp id="cor1">*Correspondence to: Dr. Tao Feng, Department of Materials Science and Engineering, Southern University of Science and Technology, Shenzhen 518055, Guangdong, China. E-mail: <email>fengt@sustech.edu.cn</email>; Dr. Bingbing Niu, School of Science, University of Science and Technology Liaoning, Anshan 114051, Liaoning, China. E-mail: <email>niubb@ustl.edu.cn</email></corresp>
      <fn fn-type="other">
          <p>
            <bold>Received:</bold> 9 Jul 2026 | <bold>First Decision:</bold> 23 Jul 2026 | <bold>Revised:</bold> 29 Aug 2026 | <bold>Accepted:</bold> 3 Sep 2026 | <bold>Published:</bold> 22 Sep 2026</p>
        </fn>
        <fn fn-type="other">
          <p>
            <bold>Academic Editor:</bold> Ho Won Jang | <bold>Copy Editor:</bold> Fangling Lan |  <bold>Production Editor:</bold> Fangling Lan</p>
        </fn>
      </author-notes>
	  <pub-date pub-type="ppub">
        <year>2026</year>
      </pub-date>
      <pub-date pub-type="epub">
        <day>22</day>
        <month>9</month>
        <year>2026</year>
      </pub-date>
      <volume>6</volume>
	  <issue>9</issue>
	 <elocation-id>600122</elocation-id>
	 
	 
	 
      <permissions>
        <copyright-statement>© The Author(s) 2026.</copyright-statement>
        <license xlink:href="https://creativecommons.org/licenses/by/4.0/">
          <license-p>© The Author(s) 2026. <bold>Open Access</bold> This article is licensed under a Creative Commons Attribution 4.0 International License (<uri xlink:href="https://creativecommons.org/licenses/by/4.0/">https://creativecommons.org/licenses/by/4.0/</uri>), which permits unrestricted use, sharing, adaptation, distribution and reproduction in any medium or format, for any purpose, even commercially, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.</license-p>
        </license>
      </permissions>
      <abstract>
        <p>Developing hydrogen evolution reaction (HER) electrocatalysts that combine high activity with reliable operation in different electrolytes remains important for clean-hydrogen and electrochemical-energy technologies. In this study, CoRu composite oxides with adjustable Co/Ru molar ratios were formed in situ on nickel foam through co-precipitation and subsequent high-temperature calcination, and their HER behavior was examined in alkaline, neutral, and near-neutral media. Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> showed the good activity and durability. In 1 M KOH, current densities of 100, 300, and 700 mA cm<sup>-2</sup> were obtained at overpotentials of 78, 127, and 196 mV, respectively; the corresponding Tafel slope was 21.64 mV dec<sup>-1</sup>. The electrode also operated for 200 h in both 1 and 6 M KOH. When incorporated into a membrane electrode assembly electrolyzer, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>||NF sustained overall water splitting at 100 mA cm<sup>-2</sup> for 200 h. In 1 M phosphate buffer solution, only 16 mV was needed to deliver 10 mA cm<sup>-2</sup>, and stable operation was again maintained for 200 h. High-current HER activity was also obtained in saturated KHCO<sub>3</sub>, while a Zn-CO<sub>2</sub> cell using this catalyst reached a maximum power density of 9.6 mW cm<sup>-2</sup>. Collectively, these findings identify <InlineParagraph>Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub></InlineParagraph> as a multifunctional HER electrode suited to several electrochemical environments.</p>
      </abstract>
      <kwd-group>
        <kwd>Hydrogen evolution reaction</kwd>
        <kwd>stability</kwd>
        <kwd>electrolyte adaptability</kwd>
        <kwd>overpotential</kwd>
      </kwd-group>
    </article-meta>
  </front>
  <body>
    <sec id="sec1">
      <title>INTRODUCTION</title>
      <p>Rising energy consumption and worsening environmental pollution have intensified interest in hydrogen as a clean energy vector because it has a high mass-specific energy content and produces only water upon combustion<sup>[<xref ref-type="bibr" rid="B1">1</xref>-<xref ref-type="bibr" rid="B3">3</xref>]</sup>. Water electrolysis powered by renewable electricity can generate high-purity hydrogen through a sustainable pathway<sup>[<xref ref-type="bibr" rid="B4">4</xref>]</sup>. During the hydrogen evolution reaction (HER), water adsorbs and dissociates before hydrogen intermediates form and subsequently desorb. Catalysts that retain both activity and stability across dissimilar electrolytes are therefore required for efficient hydrogen production and practical energy-conversion systems<sup>[<xref ref-type="bibr" rid="B5">5</xref>]</sup>.</p>
      <p>Platinum catalysts provide fast HER kinetics at small overpotentials, but their broader use is limited by the scarcity and high cost of Pt<sup>[<xref ref-type="bibr" rid="B4">4</xref>,<xref ref-type="bibr" rid="B6">6</xref>]</sup>. Prolonged operation can also promote particle agglomeration and the loss of active sites, thereby compromising durability and impeding large-scale electrochemical hydrogen production<sup>[<xref ref-type="bibr" rid="B7">7</xref>,<xref ref-type="bibr" rid="B8">8</xref>]</sup>. Ruthenium is a less expensive platinum-group metal with considerable HER activity and has consequently been studied as an alkaline-media substitute for Pt<sup>[<xref ref-type="bibr" rid="B9">9</xref>,<xref ref-type="bibr" rid="B10">10</xref>]</sup>. Even so, single-phase Ru catalysts may use the noble metal inefficiently and may lack structural robustness. Combining Ru with cobalt oxides offers a route to lower Ru loading while exploiting cooperative effects to improve activity and stability<sup>[<xref ref-type="bibr" rid="B11">11</xref>-<xref ref-type="bibr" rid="B13">13</xref>]</sup>. The benefits of such Ru-Co oxides in alkaline HER have been demonstrated previously. Zhang <italic>et al</italic>., for example, derived the Ru-Co<sub>3</sub>O<sub>4</sub>-NiO-NF heterostructure from a metal-organic framework<sup>[<xref ref-type="bibr" rid="B12">12</xref>]</sup>. In 1 M KOH, this catalyst required 44 mV at 10 mA cm<sup>-2</sup> and 115 mV at 100 mA cm<sup>-2</sup>. It outperformed most reported Ru-Co catalysts and commercial Pt/C in that study and remained stable during a 60 h test at high current density. Ren <italic>et al.</italic> later prepared a MOF-derived RuO<sub>2</sub>-Co<sub>3</sub>O<sub>4</sub> bimetallic oxide in which interactions between the two oxide components modified the local electronic structure and promoted interfacial charge redistribution<sup>[<xref ref-type="bibr" rid="B13">13</xref>]</sup>.</p>
      <p>Although Ru-Co-based oxides have demonstrated promising HER performance in alkaline media<sup>[<xref ref-type="bibr" rid="B13">13</xref>]</sup>, recent studies have begun to explore their activity under broader pH conditions, highlighting the additional kinetic challenges posed by neutral and near-neutral electrolytes<sup>[<xref ref-type="bibr" rid="B14">14</xref>,<xref ref-type="bibr" rid="B15">15</xref>]</sup>. Nevertheless, systematic investigations of Ru-Co-based oxides across distinct electrolyte environments, particularly buffered and bicarbonate-containing media, remain limited. In neutral or buffered media, HER kinetics are governed by water dissociation, buffer-assisted proton transfer, local pH variation, and interfacial mass transport and differ markedly from those in strongly alkaline electrolytes<sup>[<xref ref-type="bibr" rid="B16">16</xref>-<xref ref-type="bibr" rid="B18">18</xref>]</sup>. Therefore, evaluating catalysts beyond conventional alkaline KOH is essential for clarifying their adaptability to different proton-transfer and interfacial reaction environments<sup>[<xref ref-type="bibr" rid="B18">18</xref>,<xref ref-type="bibr" rid="B19">19</xref>]</sup>. Kim <italic>et al</italic>. proposed aqueous Zn/Al-CO<sub>2</sub> systems that exploit CO<sub>2</sub>-induced acidity to achieve simultaneous electricity generation and H<sub>2</sub> production, using a separated alkaline anodic compartment and a saturated KHCO<sub>3</sub> cathodic environment<sup>[<xref ref-type="bibr" rid="B20">20</xref>]</sup>. In this metal-CO<sub>2</sub> configuration, a saturated KHCO<sub>3</sub> electrolyte creates a bicarbonate-rich cathodic environment, where local acidity is generated by continuous CO<sub>2</sub> feeding. The HER catalyst at the cathode must not only accelerate proton reduction for efficient H<sub>2</sub> generation but also maintain catalytic activity and interfacial stability during the accompanying CO<sub>2</sub> mineralization process. This process involves HCO<sub>3</sub><sup>-</sup>/CO<sub>3</sub><sup>2-</sup> interconversion, local pH fluctuation, competitive adsorption, and carbonate precipitation at the reactive interface. Therefore, the half-cell tests in saturated KHCO<sub>3</sub> provide a more realistic assessment of the catalyst under metal-CO<sub>2</sub> cathodic conditions. Integration into a full metal-CO<sub>2</sub> cell further verifies the catalyst's ability to promote hydrogen production and enhance the overall power output.</p>
      <p>Here, a multifunctional Ru-Co oxide catalyst was fabricated on nickel foam (NF) by co-precipitation and heat treatment. We then assessed its electrochemical response in 1 M KOH, 6 M KOH, saturated KHCO<sub>3</sub>, and 1 M phosphate buffer solution (PBS). The catalyst showed strong and durable HER activity in both KOH concentrations; it also performed well in PBS and showed utility for a metal-CO<sub>2</sub> configuration in saturated KHCO<sub>3</sub>. These properties reflect cooperation between the Ru and Co oxide components, rapid mass and charge transfer through the three-dimensional conductive NF scaffold, and the availability of numerous surface sites. Beyond alkaline testing, the study establishes how the HER behavior of Ru-Co oxides changes with electrolyte environment. Relating activity to interfacial water activation, charge-transfer behavior, and electrolyte-controlled proton delivery provides a basis for designing durable HER catalysts with broad electrolyte tolerance.</p>
    </sec>
    <sec id="sec2">
      <title>EXPERIMENTAL</title>
      <sec id="sec2-1">
        <title>Chemicals</title>
        <p>Analytical-grade ruthenium chloride hydrate (RuCl<sub>3</sub>·xH<sub>2</sub>O), cobalt(II) chloride hexahydrate (CoCl<sub>2</sub>·6H<sub>2</sub>O), potassium bicarbonate (KHCO<sub>3</sub>), anhydrous ethanol (C<sub>2</sub>H<sub>5</sub>OH), urea (CO(NH<sub>2</sub>)<sub>2</sub>), 1 M PBS (pH 7.0), ethylene glycol (C<sub>2</sub>H<sub>6</sub>O<sub>2</sub>), hydrochloric acid (HCl, 36-38 wt%), and potassium hydroxide (KOH) were obtained from Aladdin. NF was obtained from Shanghai Jiaqingyuan Co., Ltd. Each chemical was employed as received, without an additional purification step.</p>
      </sec>
      <sec id="sec2-2">
        <title>Synthesis of CoRuO<sub>x</sub></title>
        <p>CoRuO<sub>x</sub> electrocatalysts were deposited directly on NF by co-precipitation and then calcined. Before deposition, a 1 cm × 2 cm NF piece was sonicated for 10 min in 40 mL of 3 M HCl to strip the native oxide layer. It was subsequently sonicated in 40 mL of anhydrous ethanol for 3 min, washed repeatedly with deionized water until neutral, and dried at ambient temperature.</p>
        <p>RuCl<sub>3</sub>·xH<sub>2</sub>O and CoCl<sub>2</sub>·6H<sub>2</sub>O were used as the Ru and Co sources, respectively. To prepare Co<sub>1</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, 0.0414 g (0.2 mmol) of RuCl<sub>3</sub>·xH<sub>2</sub>O, 0.0476 g (0.2 mmol) of CoCl<sub>2</sub>·6H<sub>2</sub>O, and 0.012 g (0.2 mmol) of urea were dispersed in 40 mL of ethylene glycol by sonication. The same protocol was applied to <InlineParagraph>Co<sub>2</sub>Ru<sub>1</sub>(OH)<sub>x</sub>,</InlineParagraph> Co<sub>3</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co<sub>4</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, and Co<sub>5</sub>Ru<sub>1</sub>(OH)<sub>x</sub>. In these syntheses, the Ru precursor was kept at 0.0414 g <InlineParagraph>(0.2 mmol),</InlineParagraph> whereas the mass of CoCl<sub>2</sub>·6H<sub>2</sub>O was set to 0.0952, 0.143, 0.1903, and 0.238 g to obtain Co/Ru molar ratios of 2:1, 3:1, 4:1, and 5:1. A Co-only solution was prepared by sonicating CoCl<sub>2</sub>·6H<sub>2</sub>O (0.1903 g, <InlineParagraph>0.8 mmol)</InlineParagraph> and urea (0.012 g, 0.2 mmol) in 40 mL of ethylene glycol, corresponding to the CoO<sub>x</sub> sample. The corresponding Ru-only solution contained RuCl<sub>3</sub>·xH<sub>2</sub>O (0.0414 g, 0.2 mmol) and urea (0.012 g, <InlineParagraph>0.2 mmol)</InlineParagraph> in the same volume of ethylene glycol, corresponding to the RuO<sub>x</sub> sample.</p>
        <p>The cleaned NF was placed vertically in each precursor solution, which was maintained at 95 °C for 12 h. The recovered specimens were alternately rinsed three times with anhydrous ethanol and deionized water to eliminate residual ions and weakly adsorbed material, followed by air drying at room temperature. The hydroxide intermediates were labeled Co<sub>1</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co<sub>2</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co<sub>3</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co<sub>4</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co<sub>5</sub>Ru<sub>1</sub>(OH)<sub>x</sub>, Co(OH)<sub>x</sub>, and Ru(OH)<sub>x</sub>. They were placed in a crucible, heated at 2 °C min<sup>-1</sup> to 300 °C, and calcined for 2 h. The products were denoted Co<sub>1</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>2</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>3</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>5</sub>Ru<sub>1</sub>O<sub>x</sub>, CoO<sub>x</sub>, and RuO<sub>x</sub>, respectively. For electrochemical testing, a 1 cm × 1 cm catalyst-coated region was exposed to the electrolyte; the other 1 cm × 1 cm region was insulated and attached to the electrode clip. Reported current densities were normalized to the 1.0 cm<sup>2</sup> exposed geometric area.</p>
      </sec>
      <sec id="sec2-3">
        <title>Material characterizations</title>
        <p>Sample morphology was examined by scanning electron microscopy (SEM, JSM-6701F, JEOL, Japan) at <InlineParagraph>5 kV.</InlineParagraph> Transmission electron microscopy and high-resolution TEM (TEM/HRTEM, JEM-2100F, JEOL, Japan; 200 kV) were used to resolve the nanoscale and crystallographic features, while associated energy-dispersive X-ray spectroscopy (EDS) maps provided elemental distributions. Surface composition and chemical states were analyzed by X-ray photoelectron spectroscopy (XPS, AXIS ULTRA DLD, Kratos Analytical, UK) using monochromatic Al Kα radiation (hυ = 1,486.6 eV) at 15 kV and 10 mA. Binding energies were referenced to the C 1s signal at 284.8 eV. Raman measurements employed a LabRAM HR Evolution system (HORIBA Scientific, France), a 473 nm laser, and a 600 grooves mm<sup>-1</sup> grating. X-ray absorption fine-structure (XAFS) data spanning 4.5-20 keV were acquired on a SuperXAFS-H3000 benchtop hard X-ray absorption spectrometer (Shanghai Institute of Applied Physics, CAS, China). Fourier-transform infrared spectra were collected with a Vertex 80 Fourier Transform Infrared Spectroscopy (FTIR) instrument (Bruker, Germany).</p>
      </sec>
      <sec id="sec2-4">
        <title>Electrocatalytic measurements</title>
        <p>Electrochemical measurements were performed using a CS350M workstation from CH Instruments. Catalyst-coated NF with a 1 cm<sup>2</sup> exposed area was the working electrode for HER testing in KOH; Hg/HgO and graphite were used as the reference and counter electrodes, respectively. Except for the potentials monitored directly during durability experiments, all measured potentials were converted to the reversible hydrogen electrode (RHE) scale. For a Hg/HgO electrode filled with 1 M KOH, the conversion followed Ref.<sup>[<xref ref-type="bibr" rid="B21">21</xref>]</sup>:</p>
        
		<p><disp-formula> <label>(1)</label> <tex-math id="E1"> $$ \begin{equation}  \begin{aligned} E_{{vs. } R H E}=E_{v s . H g / H g O}+E_{H g / H g O}^{\theta}+0.059 \times p H  \end{aligned} \end{equation} $$ </tex-math>
</disp-formula></p>
		
        <p>Potentials measured with an Ag/AgCl reference electrode containing saturated KCl were converted as described in Ref.<sup>[<xref ref-type="bibr" rid="B22">22</xref>]</sup>:</p>
        
		
		<p><disp-formula> <label>(2)</label> <tex-math id="E2"> $$ \begin{equation}  \begin{aligned} E_{{vs. } R H E}=E_{v s . A g / A g C l}+E_{A g / A g C l}^{\theta}+0.059 \times p H  \end{aligned} \end{equation} $$ </tex-math>
</disp-formula></p>
		
        <p>The measured pH values were 14, 7, and 8 for 1 M KOH, 1 M PBS, and saturated KHCO<sub>3</sub>, respectively.</p>
        <p>Linear sweep voltammograms were collected at 5 mV s<sup>-1</sup> with 90% iR compensation. To estimate the electrochemical double-layer capacitance (C<sub>dl</sub>), cyclic voltammograms in 1 M KOH were obtained at 10, 20, 40, 60, 80, 100, and 120 mV s<sup>-1</sup>. The electrochemical surface area (ECSA) was then determined from C<sub>dl</sub> using:</p>
       
	   
	   <p><disp-formula> <label>(3)</label> <tex-math id="E3"> $$ \begin{equation}  \begin{aligned}  \mathrm{ECSA}=\left(\frac{\mathrm{C}_{\mathrm{dl} \times \mathrm{S}}}{\mathrm{C}_{\mathrm{s}}}\right) \end{aligned} \end{equation} $$ </tex-math>
</disp-formula></p>
	   
        <p>Here, S is the geometric area of the working electrode, and C<sub>s</sub> is the specific capacitance assigned to an ideally smooth surface. A C<sub>s</sub> value of 40 μF cm<sup>-2</sup>, selected from prior electrochemical reports, was used in this study<sup>[<xref ref-type="bibr" rid="B23">23</xref>]</sup>. For 1 M PBS and saturated KHCO<sub>3</sub>, CV data were collected at 20, 40, 60, 80, and 100 mV s<sup>-1</sup>.</p>
        <p>The durability of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> was evaluated using a direct-current power supply for 200 h. The starting current density was -100 mA cm<sup>-2</sup> in 1 and 6 M KOH and -10 mA cm<sup>-2</sup> in 1 M PBS. Overall water splitting was evaluated in a membrane electrode assembly (MEA) containing Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> as the cathode and NF as the anode; its linear sweep voltammetry (LSV) curve was recorded at 50 mV s<sup>-1</sup>. For Zn-CO<sub>2</sub> testing, Zn foil and Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> served as the anode and cathode, respectively, under continuous CO<sub>2</sub> supply. Polarization data were acquired at 50 mV s<sup>-1</sup>, and the overpotentials were derived from RHE-converted potentials.</p>
      </sec>
    </sec>
    <sec id="sec3">
      <title>RESULTS AND DISCUSSION</title>
      <sec id="sec3-1">
        <title>Evaluation of HER performance</title>
        <p>Alkaline HER activity was first compared for the prepared CoRuO<sub>x</sub> electrodes in 1 M KOH. Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> was the most active composition: overpotentials of 78, 127, and 196 mV produced 100, 300, and 700 mA cm<sup>-2</sup>, respectively. At 100 and 300 mA cm<sup>-2</sup>, these values were lower than those of Co<sub>1</sub>Ru<sub>1</sub>O<sub>x</sub> (262 and 340 mV), Co<sub>5</sub>Ru<sub>1</sub>O<sub>x</sub> (127 and 225 mV), and commercial Pt/C (115 and 250 mV) [<xref ref-type="fig" rid="fig1">Figure 1A</xref> and <xref ref-type="fig" rid="fig1">B</xref>]. Its advantage over Pt/C increased further at 700 mA cm<sup>-2</sup>, supporting its suitability for high-current alkaline operation<sup>[<xref ref-type="bibr" rid="B9">9</xref>,<xref ref-type="bibr" rid="B24">24</xref>]</sup>. The Tafel plot in <xref ref-type="fig" rid="fig1">Figure 1C</xref> gave a slope of 21.64 mV dec<sup>-1</sup> for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>, smaller than those of the other prepared electrodes and Pt/C, and therefore indicative of faster HER kinetics<sup>[<xref ref-type="bibr" rid="B25">25</xref>]</sup>.</p>
        <fig id="fig1" position="float">
          <label>Figure 1</label>
          <caption>
            <p>HER characterization of Co<sub>x</sub>Ru<sub>1</sub>O<sub>x</sub> and reference catalysts in 1 M KOH: (A) LSV responses; (B) overpotentials at selected current densities; (C) Tafel plots; (D) C<sub>dl</sub>; (E) ECSA; and (F) 200 h chronopotentiometry of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> at -100 mA cm<sup>-2</sup>. (G) HER polarization of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> in 1 and 6 M KOH, together with Pt/C in 1 M KOH. (H) A 200 h stability trace for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> at -100 mA cm<sup>-2</sup> in 6 M KOH.</p>
          </caption>
          <graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="em60217.fig.1.jpg" />
        </fig>
        <p>Cyclic voltammetry was used to probe the origin of the high HER activity. Co<sub>1</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>2</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>3</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>, Co<sub>5</sub>Ru<sub>1</sub>O<sub>x</sub>, and Pt/C were scanned from 10 to 120 mV s<sup>-1</sup> [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 1</inline-supplementary-material>]. As presented in <xref ref-type="fig" rid="fig1">Figure 1D</xref>, the C<sub>dl</sub> of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> was 20.9 mF cm<sup>-2</sup>, exceeding the values for Co<sub>5</sub>Ru<sub>1</sub>O<sub>x</sub> (3.51 mF cm<sup>-2</sup>), Co<sub>1</sub>Ru<sub>1</sub>O<sub>x</sub> (15.44 mF cm<sup>-2</sup>), and Pt/C (13.2 mF cm<sup>-2</sup>; <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 2</inline-supplementary-material>). The calculated ECSA values are summarized in <xref ref-type="fig" rid="fig1">Figure 1E</xref>. Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> reached 523 cm<sup>2</sup>, compared with 330 cm<sup>2</sup> for Pt/C, consistent with a larger number of accessible sites. Chronopotentiometry in 1 M KOH was then used to assess durability. At -100 mA cm<sup>-2</sup>, the potential of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> changed negligibly over 200 h [<xref ref-type="fig" rid="fig1">Figure 1F</xref>], demonstrating robust alkaline stability.</p>
        <p>The polarization response in 6 M KOH was compared with that in 1 M KOH in <xref ref-type="fig" rid="fig1">Figure 1G</xref>. Larger overpotentials, especially at high current, were observed in the more concentrated electrolyte. The greater viscosity and lower water activity of 6 M KOH can impede ion diffusion, transport near the electrode, and detachment of gas bubbles<sup>[<xref ref-type="bibr" rid="B26">26</xref>,<xref ref-type="bibr" rid="B27">27</xref>]</sup>. A smaller population of free water molecules may also slow water dissociation, an important kinetic step in alkaline HER<sup>[<xref ref-type="bibr" rid="B28">28</xref>,<xref ref-type="bibr" rid="B29">29</xref>]</sup>. Thus, any conductivity gain at higher KOH concentration is offset by less favorable mass transfer and interfacial reaction conditions. Nevertheless, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> needed only 121, 162, and 223 mV to reach 100, 300, and 700 mA cm<sup>-2</sup> in 6 M KOH. In addition, operation at <InlineParagraph>-100 mA cm<sup>-2</sup></InlineParagraph> was maintained for 200 h [<xref ref-type="fig" rid="fig1">Figure 1H</xref>]. These observations demonstrate catalytic activity and long-term durability over a wide range of alkaline concentrations.</p>
      </sec>
      <sec id="sec3-2">
        <title>Morphologies and structures of CoRuO<sub>x</sub></title>
        <p>Morphological, structural, and elemental data for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> are compiled in <xref ref-type="fig" rid="fig2">Figure 2</xref>. Before the durability experiment, the SEM image in <xref ref-type="fig" rid="fig2">Figure 2A</xref> shows an interconnected, comparatively uniform porous network. This architecture increases access to reaction sites and supports electrolyte infiltration and reactant transport, which benefit HER<sup>[<xref ref-type="bibr" rid="B30">30</xref>]</sup>. The pre-test EDS maps [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 3</inline-supplementary-material>] show broadly even distributions of Co, Ru, Ni, and O. After 200 h of HER operation, most of the porous skeleton remains visible, although limited reconstruction and small surface particles appear [<xref ref-type="fig" rid="fig2">Figure 2B</xref>]. The post-test maps in <InlineParagraph><inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 4</inline-supplementary-material></InlineParagraph> continue to show well-retained distributions of all four elements, with no clear sign of migration. These observations support the structural and compositional durability of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>. TEM, HRTEM, and local EDS mapping were additionally used to resolve the catalyst structure. Lattice fringes are evident in the TEM image and in enlarged HRTEM views in <xref ref-type="fig" rid="fig2">Figure 2C</xref>. Spacings of approximately 0.318 and <InlineParagraph>0.204 nm</InlineParagraph> correspond to the RuO<sub>2</sub> (110) and Co<sub>3</sub>O<sub>4</sub> (400) planes, respectively, confirming RuO<sub>x</sub>- and CoO<sub>x</sub>-related oxide domains<sup>[<xref ref-type="bibr" rid="B31">31</xref>,<xref ref-type="bibr" rid="B32">32</xref>]</sup>. The TEM image in <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 5</inline-supplementary-material> and EDS maps in <xref ref-type="fig" rid="fig2">Figure 2D</xref> further demonstrate good dispersion of Co, Ru, Ni, and O in the chosen region. Accordingly, the material combines locally crystalline oxide domains with homogeneous elemental dispersion.</p>
        <fig id="fig2" position="float">
          <label>Figure 2</label>
          <caption>
            <p>Morphology and elemental distribution of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>: SEM images obtained (A) before and (B) after a 200 h HER durability experiment in 1 M KOH; (C) TEM image with magnified HRTEM regions; and (D) associated EDS maps.</p>
          </caption>
          <graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="em60217.fig.2.jpg" />
        </fig>
        <p>XPS was used to compare the surface states of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> before and after the 200 h HER test in 1 M KOH [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 6</inline-supplementary-material>]. The survey spectra in <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 6A</inline-supplementary-material> contain signals from Co, Ru, O, C, and Ni in both specimens, showing that the principal surface elements persist after extended operation. In the Co 2p spectra [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 6B</inline-supplementary-material>], the initial Co 2p<sub>3/2</sub> and Co 2p<sub>1/2</sub> components occur at 780.9 and 796.9 eV, with satellites at 789.5 and 801.2 eV<sup>[<xref ref-type="bibr" rid="B33">33</xref>,<xref ref-type="bibr" rid="B34">34</xref>]</sup>. Following the durability test, the principal components were observed at 781.1 and 797.3 eV, and the satellites at 787.6 and 801.6 eV. The modest changes in position and line shape indicate that the Co-containing surface species remain largely intact. The O 1s spectra in <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 6C</inline-supplementary-material> contain surface-oxygen and lattice-oxygen contributions. Their initial positions, 531.9 and 530.9 eV, shift to 531.4 and 530.7 eV after testing<sup>[<xref ref-type="bibr" rid="B34">34</xref>,<xref ref-type="bibr" rid="B35">35</xref>]</sup>, while the two-component profile is preserved. This response is consistent with a stable oxygen environment and oxide framework. <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 6D</inline-supplementary-material> covers the overlapping C 1s/Ru 3d region. Before testing, the 284.8 eV feature arises from C-C/C=C bonds, and the 280.2 and 286.6 eV components are associated with Ru 3d<sup>[<xref ref-type="bibr" rid="B36">36</xref>]</sup>. Ru-related signals remain readily observable after 200 h without an obvious loss in overall intensity, confirming retention of surface Ru.</p>
        <p>The electronic states and short-range coordination of Co and Ru were probed by XPS and XAFS to understand the superior HER activity of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>. The high-resolution spectra indicate appreciable Co-Ru electronic coupling [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 7</inline-supplementary-material>]. Relative to RuO<sub>x</sub>, the Ru 3d<sub>5/2</sub> component shifts by about <InlineParagraph>0.5 eV,</InlineParagraph> from 280.7 to 280.2 eV, in Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>. The Co 2p<sub>3/2</sub> and Co 2p<sub>1/2</sub> components likewise move from 781.4 and 797.5 eV in CoO<sub>x</sub> to 780.9 and 796.9 eV in the mixed oxide, decreases of approximately 0.5 and <InlineParagraph>0.6 eV<sup>[<xref ref-type="bibr" rid="B37">37</xref>]</sup>.</InlineParagraph> The correlated shifts support electron-density redistribution between the two metals and the formation of modified surface electronic and chemical environments after Ru is introduced<sup>[<xref ref-type="bibr" rid="B38">38</xref>]</sup>.</p>
        <p>Differences between the Co K-edge XANES spectra of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> and CoO<sub>x</sub> [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 8</inline-supplementary-material>] provide further evidence that the electronic environment of Co is altered. Fourier-transformed EXAFS also reveals a change in local coordination. CoO<sub>x</sub> displays a principal contribution near 2.6 Å that is assigned to Co-O-Co coordination<sup>[<xref ref-type="bibr" rid="B39">39</xref>]</sup>, whereas Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> has a feature near 1.9 Å associated with Co-M (M = Co or Ru) scattering and a weaker Co-O-Co signal. Ru addition therefore reconstructs the local environment of Co and electronically tunes the cobalt-oxide framework. Taken together, the XPS and XAFS data show that Ru changes both the electronic state and coordination of Co, producing catalytic centers with favorable interfacial electronic properties. This reconstruction promotes interfacial electron transfer and regulates the interaction between the active sites and hydrogen intermediates, which helps explain the high HER activity of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>.</p>
      </sec>
      <sec id="sec3-3">
        <title>Evaluation of MEA performance</title>
        <p>Practical HER behavior was examined in a MEA electrolyzer<sup>[<xref ref-type="bibr" rid="B40">40</xref>,<xref ref-type="bibr" rid="B41">41</xref>]</sup>. The cathode consisted of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> on NF, and uncoated NF was used as the anode; this device is denoted Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>||NF. <xref ref-type="fig" rid="fig3">Figure 3A</xref> depicts its cathode-membrane-anode arrangement. <xref ref-type="fig" rid="fig3">Figure 3B</xref> shows polarization curves for a 1 × 1 cm<sup>2</sup>||1 × 1 cm<sup>2</sup> cell at several temperatures. Increasing the temperature from 30 to 70 °C continuously increased current density, consistent with accelerated interfacial kinetics, ion transport, and gas-bubble removal. At 2.0 V, the current density rose from 0.43 A cm<sup>-2</sup> at 30 °C to 1.59 A cm<sup>-2</sup> at 70 °C [<xref ref-type="fig" rid="fig3">Figure 3C</xref>]. During a <InlineParagraph>200 h</InlineParagraph> chronopotentiometric experiment at 100 mA cm<sup>-2</sup>, the cell voltage remained close to 1.8 V with only small variations [<xref ref-type="fig" rid="fig3">Figure 3D</xref>]. The stable response demonstrates the promise of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>||NF for membrane-electrolyzer operation.</p>
        <fig id="fig3" position="float">
          <label>Figure 3</label>
          <caption>
            <p>Performance of a Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>||NF membrane electrolyzer: (A) device configuration; (B) polarization at 30-70 °C; (C) current density at 2.0 V as a function of temperature; and (D) a 200 h chronopotentiometric trace collected at 100 mA cm<sup>-2</sup>.</p>
          </caption>
          <graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="em60217.fig.3.jpg" />
        </fig>
      </sec>
      <sec id="sec3-4">
        <title>Electrochemical performance in neutral and near-neutral electrolytes</title>
        <p>Catalyst response in neutral and near-neutral media was assessed in 1 M PBS and saturated KHCO<sub>3</sub> <InlineParagraph>[<xref ref-type="fig" rid="fig4">Figure 4</xref>].</InlineParagraph> PBS measurements used a three-electrode arrangement with graphite and Ag/AgCl as the counter and reference electrodes. In <xref ref-type="fig" rid="fig4">Figure 4A</xref> and <xref ref-type="fig" rid="fig4">B</xref>, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> reaches 10, 100, and 300 mA cm<sup>-2</sup> at 16, 217, and <InlineParagraph>554 mV,</InlineParagraph> whereas Pt/C requires 17, 371, and 667 mV. The two electrodes are comparable at low current, but the mixed oxide needs substantially less overpotential at higher current<sup>[<xref ref-type="bibr" rid="B17">17</xref>]</sup>. The Tafel slopes are <InlineParagraph>99.51 mV dec<sup>-1</sup></InlineParagraph> for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> and 169.55 mV dec<sup>-1</sup> for Pt/C [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 9</inline-supplementary-material>], again favoring the oxide catalyst. CV and C<sub>dl</sub> analyses in <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figures 10-13</inline-supplementary-material> give 7.36 mF cm<sup>-2</sup> for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> and <InlineParagraph>12.21 mF cm<sup>-2</sup></InlineParagraph> for Pt/C. Because superior high-current activity is obtained despite the smaller C<sub>dl</sub>, the advantage in PBS is attributed primarily to faster reaction kinetics, more effective use of surface sites, and porous-structure-assisted mass transport. The potential remained nearly constant over 200 h at -10 mA cm<sup>-2</sup> <InlineParagraph>[<xref ref-type="fig" rid="fig4">Figure 4C</xref>],</InlineParagraph> confirming durability in the phosphate buffer.</p>
		
		 <fig id="fig4" position="float">
          <label>Figure 4</label>
          <caption>
            <p>Neutral and near-neutral electrochemical behavior of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>: (A) HER polarization, (B) selected overpotentials, and (C) a 200 h stability trace at -10 mA cm<sup>-2</sup> in 1 M PBS; (D) polarization and (E) selected overpotentials in saturated KHCO<sub>3</sub>; and (F) discharge polarization/power-density profiles for Zn-CO<sub>2</sub> cells containing Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> or Pt/C cathodes.</p>
          </caption>
          <graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="em60217.fig.4.jpg" />
        </fig>
		
		
        <p>Saturated KHCO<sub>3</sub> was also examined in a three-electrode cell using graphite as the counter electrode and Hg/HgO as the reference. In this electrolyte, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> again outperformed Pt/C. The oxide catalyst required 173, 262, and 325 mV to produce 100, 300, and 500 mA cm<sup>-2</sup>, respectively, compared with 212, 388, and <InlineParagraph>532 mV</InlineParagraph> for Pt/C [<xref ref-type="fig" rid="fig4">Figure 4D</xref> and <xref ref-type="fig" rid="fig4">E</xref>]. These values demonstrate effective HER operation in a near-neutral bicarbonate medium. Tafel slopes from <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 14</inline-supplementary-material> were 51.85 and <InlineParagraph>53.88 mV dec<sup>-1</sup></InlineParagraph> for Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> and Pt/C, indicating similar kinetics with a small advantage for the former. <InlineParagraph><inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figures 15-17</inline-supplementary-material></InlineParagraph> yield C<sub>dl</sub> values of 20.41 and 38.51 mF cm<sup>-2</sup>, respectively. Thus, the lower overpotentials of <InlineParagraph>Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub></InlineParagraph> cannot be explained by a larger electrochemical area; more efficient active-site utilization and reaction kinetics are the more likely origins.</p>
        <p>Device-level utility was investigated by using Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> as the cathode catalyst in a Zn-CO<sub>2</sub> cell<sup>[<xref ref-type="bibr" rid="B42">42</xref>,<xref ref-type="bibr" rid="B43">43</xref>]</sup>. In the mechanism described by Kim <italic>et al</italic>.<sup>[<xref ref-type="bibr" rid="B20">20</xref>]</sup>, hydration of dissolved CO<sub>2</sub> generates carbonic acid and produces a mildly acidic cathodic environment favorable for HER. Simultaneously, Zn oxidation at the anode supplies electrons, allowing hydrogen and electricity to be generated together. The Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>-based cell attained <InlineParagraph>9.6 mW cm<sup>-2</sup>,</InlineParagraph> <italic>vs.</italic> 6.6 mW cm<sup>-2</sup> for the Pt/C cell [<xref ref-type="fig" rid="fig4">Figure 4F</xref>]. These results extend the favorable neutral and near-neutral response observed in PBS and KHCO<sub>3</sub> to a complete Zn-CO<sub>2</sub> device.</p>
        <p>
          <xref ref-type="table" rid="t1">Table 1</xref> benchmarks Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> against recent Ru- and Ru-Co-containing HER electrocatalysts in terms of overpotential, Tafel slope, electrolyte, test current, and durability. In 1 M KOH, Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> combines an overpotential of 78 mV at -100 mA cm<sup>-2</sup>, a 21.64 mV dec<sup>-1</sup> Tafel slope, and 200 h of continuous operation. This balance of activity and durability compares favorably with many reported Ru-based and Ru-Co-based materials and is consistent with cooperative Co/Ru oxide effects and a tuned surface electronic environment. Unlike most alkaline-centered reports, the present catalyst also remains active in neutral PBS and bicarbonate media, demonstrating compatibility with distinct proton-transfer environments.</p>
        <table-wrap id="t1">
          <label>Table 1</label>
          <caption>
            <p>Comparison of HER performance of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> with representative Ru-based and Co-Ru-based electrocatalysts</p>
          </caption>
          <table frame="hsides" rules="groups">
            <thead>
              <tr>
                <td style="border-bottom:1;">
                  <bold>Electrocatalysts</bold>
                </td>
                <td style="border-bottom:1;">
                  <bold>Overpotential</bold> </td>
                <td style="border-bottom:1;">
                  <bold>Tafel slope</bold>
                </td>
                <td style="border-bottom:1;">
                  <bold>Stability</bold>
                </td>
                <td style="border-bottom:1;">
                  <bold>Reference</bold>
                </td>
              </tr>
            </thead>
            <tbody>
              <tr>
                <td>Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub></td>
                <td>ղ<sub>100</sub> = 78 mV<break />(1 M KOH)</td>
                <td>21.64 mV dec<sup>-1</sup></td>
                <td>@-100 mA cm<sup>-2</sup><break />200 h</td>
                <td>This work</td>
              </tr>
              <tr>
                <td>RuCo<sub>3</sub>O<sub>4</sub>-NiO-NF</td>
                <td>ղ<sub>100</sub> = 115 mV<break />(1 M KOH)</td>
                <td>53.9 mV dec<sup>-1</sup></td>
                <td>@-100 mA cm<sup>-2</sup><break />60 h</td>
                <td>[<xref ref-type="bibr" rid="B12">12</xref>]</td>
              </tr>
              <tr>
                <td>Ru/Co<sub>4</sub>N/NF</td>
                <td>ղ<sub>100</sub> = 145 mV<break />(1 M KOH)</td>
                <td>25 mV dec<sup>-1</sup></td>
                <td>@-100 mA cm<sup>-2</sup><break />120 h</td>
                <td>[<xref ref-type="bibr" rid="B44">44</xref>]</td>
              </tr>
              <tr>
                <td>Ru-Co@Ti<sub>2</sub>AlC</td>
                <td>ղ<sub>100</sub> = 95 mV<break />(1 M KOH)</td>
                <td>105 mV dec<sup>-1</sup></td>
                <td>@-20 mA cm<sup>-2 </sup> <break />48 h</td>
                <td>[<xref ref-type="bibr" rid="B45">45</xref>]</td>
              </tr>
              <tr>
                <td>Ru-O-Ru clusters</td>
                <td>ղ<sub>100</sub> = 86 mV<break />(1 M KOH)</td>
                <td>29.2 mV dec<sup>-1</sup></td>
                <td>@-100 mA cm<sup>-2</sup><break />50 h</td>
                <td>[<xref ref-type="bibr" rid="B46">46</xref>]</td>
              </tr>
              <tr>
                <td>NiRuO<sub>x</sub>-Ar</td>
                <td>ղ<sub>100</sub> = 94 mV<break />(1 M KOH)</td>
                <td>52.73 mV dec<sup>-1</sup></td>
                <td>@-50 mA cm<sup>-2</sup><break />100 h</td>
                <td>[<xref ref-type="bibr" rid="B47">47</xref>]</td>
              </tr>
              <tr>
                <td>Ru/Ni<sub>3</sub>N-Ni</td>
                <td>ղ<sub>100</sub> = 135 mV<break />(1 M KOH)</td>
                <td>32.4 mV dec<sup>-1</sup></td>
                <td>1,000  cycles</td>
                <td>[<xref ref-type="bibr" rid="B48">48</xref>]</td>
              </tr>
              <tr>
                <td> Ru-NiO/CNTs</td>
                <td>ղ<sub>100</sub> = 98 mV<break />(1 M KOH)</td>
                <td>56.5 mV dec<sup>-1</sup></td>
                <td>@-10 mA cm<sup>-2</sup><break />100 h</td>
                <td>[<xref ref-type="bibr" rid="B49">49</xref>]</td>
              </tr>
              <tr>
                <td>RuO<sub>2</sub>−Ti<sub>3</sub>C<sub>2</sub>/NF</td>
                <td>ղ<sub>100</sub> = 85 mV<break />(1 M KOH)</td>
                <td>127.5 mV dec<sup>-1</sup></td>
                <td>@-20 mA cm<sup>-2</sup><break />40 h</td>
                <td>[<xref ref-type="bibr" rid="B50">50</xref>]</td>
              </tr>
              <tr>
                <td>cRu-Ni<sub>3</sub>N/NF</td>
                <td>ղ<sub>100</sub> = 99 mV<break />(1 M KOH)</td>
                <td>26.2 mV dec<sup>-1</sup></td>
                <td>5,000 cycles</td>
                <td>[<xref ref-type="bibr" rid="B51">51</xref>]</td>
              </tr>
              <tr>
                <td>Ru-Ni<sub>3</sub>N@NC</td>
                <td>ղ<sub>50</sub> = 101 mV<break />(1 M KOH)</td>
                <td>70 mV dec<sup>-1</sup></td>
                <td>@-10 mA cm<sup>-2</sup><break />10 h</td>
                <td>[<xref ref-type="bibr" rid="B52">52</xref>]</td>
              </tr>
              <tr>
                <td>Ru NRs/TiN</td>
                <td>ղ<sub>100</sub> = 150 mV<break />(1 M KOH)</td>
                <td>27.08 mV dec<sup>-1</sup></td>
                <td>1,000 cycles</td>
                <td>[<xref ref-type="bibr" rid="B53">53</xref>]</td>
              </tr>
              <tr>
                <td>Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub></td>
                <td>ղ<sub>10</sub> = 16 mV<break />ղ<sub>100</sub> = 217 mV<break />(1 M PBS)</td>
                <td>99.51 mV dec<sup>-1</sup></td>
                <td>@-10 mA cm<sup>-2</sup><break />200 h</td>
                <td>This work</td>
              </tr>
              <tr>
                <td>Ru-WO<sub>3-x</sub>/CP</td>
                <td>ղ<sub>10</sub> = 19 mV<break />(1 M PBS)</td>
                <td>41 mV dec<sup>-1</sup></td>
                <td>@-20 mA cm<sup>-2</sup><break />30 h</td>
                <td>[<xref ref-type="bibr" rid="B54">54</xref>]</td>
              </tr>
              <tr>
                <td>CoRu/CoRuP</td>
                <td>ղ<sub>10</sub> = 31 mV<break />(1 M PBS)</td>
                <td>53.09 mV dec<sup>-1</sup></td>
                <td>@-10 mA cm<sup>-2</sup><break />40 h</td>
                <td>[<xref ref-type="bibr" rid="B55">55</xref>]</td>
              </tr>
            </tbody>
          </table>
        </table-wrap>
        <p>Electrochemical impedance spectroscopy was used to clarify why Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> remains highly active even though its C<sub>dl</sub> is lower than that of Pt/C in PBS and saturated KHCO<sub>3</sub> (Nyquist plots, <InlineParagraph><inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 18</inline-supplementary-material>).</InlineParagraph> The solution resistances (R<sub>s</sub>) of Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> and Pt/C are 1.44 and 1.92 Ω in 1 M KOH, 4.06 and 5.83 Ω in <InlineParagraph>1 M PBS,</InlineParagraph> and 1.52 and 2.25 Ω in saturated KHCO<sub>3</sub>, respectively. Although R<sub>s</sub> varies with electrolyte conductivity, its consistently smaller value for the mixed oxide indicates lower ohmic losses under each HER condition.</p>
        <p>Operando Raman spectra were next collected in 1 M KOH, 1 M PBS, and saturated KHCO<sub>3</sub> to probe the HER interface [<inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 19</inline-supplementary-material>]. Similar potential-dependent changes in the broad O-H stretching envelope near 3,500 cm<sup>-1</sup> appear in all three media, showing that interfacial water activation is retained. The elementary HER sequence is comparable, but its rate is shaped by electrolyte-specific proton donors, conductivity, and interfacial solvation. In KOH, water dissociation precedes formation of adsorbed hydrogen. The near-neutral PBS environment supplies fewer protons and normally slows proton transfer; nevertheless, effective water activation at Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> supports proton delivery and HER<sup>[<xref ref-type="bibr" rid="B54">54</xref>]</sup>. In saturated KHCO<sub>3</sub>, bands near 1,015 and 1,064 cm<sup>-1</sup> are assigned to HCO<sub>3</sub><sup>-</sup> and CO<sub>3</sub><sup>2-</sup>, respectively<sup>[<xref ref-type="bibr" rid="B56">56</xref>,<xref ref-type="bibr" rid="B57">57</xref>]</sup>, evidencing a dynamic interfacial bicarbonate/carbonate equilibrium that buffers local proton transfer. The absence of new bands associated with heavy carbonate or bicarbonate accumulation suggests that these species do not substantially obstruct the active interface. FTIR spectra in <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Figure 20</inline-supplementary-material> show hydroxyl-stretching and water-bending bands near 3,404 and 1,630 cm<sup>-1</sup>, respectively, for both RuO<sub>x</sub> and <InlineParagraph>Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub><sup>[<xref ref-type="bibr" rid="B58">58</xref>]</sup>.</InlineParagraph> The stronger hydroxyl-related absorption of the mixed oxide indicates greater interaction with interfacial water. Its electrolyte tolerance therefore derives from maintained water activation together with effective charge and proton transport, rather than from identical kinetics in every electrolyte.</p>
      </sec>
    </sec>
    <sec id="sec4">
      <title>CONCLUSIONS</title>
      <p>A porous Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub> electrode was prepared on three-dimensional NF by co-precipitation and calcination and evaluated under several HER conditions. Tuning the Co/Ru ratio enhanced activity, kinetics, and durability through cooperative Co/Ru oxide chemistry, efficient electron and ion transport within the NF network, and ready access to surface sites. After prolonged electrolysis, the porous architecture and homogeneous elemental distribution were largely retained, demonstrating structural and compositional resilience. A MEA containing Co<sub>4</sub>Ru<sub>1</sub>O<sub>x</sub>||NF operated continuously for 200 h at 100 mA cm<sup>-2</sup>, supporting its use in practical water splitting. In addition to strong alkaline performance, the catalyst responded effectively and stably in PBS and saturated KHCO<sub>3</sub>, confirming adaptability to neutral and near-neutral media. Its promising power output in a Zn-CO<sub>2</sub> cell further broadens the potential applications beyond water electrolysis. Overall, the findings connect composition control and porous-electrode design with multi-environment operation and provide a route toward versatile, high-performance Ru-Co oxide electrocatalysts.</p>
    </sec>
  </body>
  <back>
  <sec>
      <title>DECLARATIONS</title>
      <sec>
        <title>Authors' contributions</title>
        <p>Investigation, formal analysis, writing - original draft: Zheng, Q.</p>
        <p>Data curation, investigation: Li, Y.</p>
        <p>Validation, formal analysis: Lu, C.</p>
        <p>Writing - review &amp; editing: Maubane-Nkadimeng, M. S.</p>
        <p>Supervision, funding acquisition, writing - review &amp; editing: Feng, T.</p>
        <p>Conceptualization, project administration, resources: Niu, B.</p>
        <p>All authors read and approved the final manuscript.</p>
      </sec>
      <sec>
        <title>Availability of data and materials</title>
        <p>The data supporting the findings of this study are available in the article and its <inline-supplementary-material content-type="local-data" mimetype="application/pdf" xlink:href="em60217-SupplementaryMaterials.pdf">Supplementary Materials</inline-supplementary-material>. Additional raw data are available from the corresponding author upon reasonable request.</p>
      </sec>
      <sec>
        <title>AI and AI-assisted tools statement</title>
        <p>During the preparation of this manuscript, the AI tool ChatGPT (GPT-5.5 Instant, released 2026-05-05) was used to assist with language editing and manuscript refinement. In addition, ChatGPT Images 2.0 (released 2026-04-21) was used to assist in creating the graphical abstract. After using this tool/service, the authors carefully reviewed and edited the generated content as needed and take full responsibility for the content of the published article.</p>
      </sec>
      <sec>
        <title>Financial support and sponsorship</title>
        <p>This work was supported by the National Natural Science Foundation of China (No. W2441008) and the Natural Science Foundation of Liaoning (LJ212510146025).</p>
      </sec>
      <sec>
        <title>Conflicts of interest</title>
        <p>All authors declared that there are no conflicts of interest.</p>
      </sec>
      <sec>
        <title>Ethical approval and consent to participate</title>
        <p>Not applicable.</p>
      </sec>
      <sec>
        <title>Consent for publication</title>
        <p>Not applicable.</p>
      </sec>
	  <sec>
        <title>Copyright</title>
        <p>© The Author(s) 2026.</p>
      </sec>
	  
	   <sec sec-type="supplementary-material">
        <title>Supplementary Materials</title>
        <supplementary-material content-type="local-data">
          <media xlink:href="em60217-SupplementaryMaterials.pdf" mimetype="application/pdf">
            <caption>
              <p>Supplementary Materials</p>
            </caption>
          </media>
        </supplementary-material>
      </sec>
	  
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