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<article article-type="research-article" dtd-version="2.3" xml:lang="EN" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">
<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">983778</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2022.983778</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemistry</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Bimetallic Cu-Bi catalysts for efficient electroreduction of CO<sub>2</sub> to formate</article-title>
<alt-title alt-title-type="left-running-head">Li 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.2022.983778">10.3389/fchem.2022.983778</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Li</surname>
<given-names>Le</given-names>
</name>
<xref ref-type="fn" rid="fn1">
<sup>&#x2020;</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1893677/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Jin</surname>
<given-names>Xuan</given-names>
</name>
<xref ref-type="fn" rid="fn1">
<sup>&#x2020;</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Yu</surname>
<given-names>Xiaohan</given-names>
</name>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhong</surname>
<given-names>Miao</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
</contrib>
</contrib-group>
<aff>
<institution>National Laboratory of Solid State Microstructures</institution>, <institution>Jiangsu Key Laboratory of Artificial Functional Materials</institution>, <institution>College of Engineering and Applied Sciences</institution>, <institution>Nanjing University</institution>, <addr-line>Nanjing</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/1552919/overview">David Raciti</ext-link>, National Institute of Standards and Technology (NIST), United States</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/1749648/overview">Carla Casadevall Serrano</ext-link>, University of Cambridge, United Kingdom</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1016712/overview">Jiajun Wang</ext-link>, Tianjin University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Miao Zhong, <email>miaozhong@nju.edu.cn</email>
</corresp>
<fn fn-type="equal" id="fn1">
<label>
<sup>&#x2020;</sup>
</label>
<p>These authors have contributed equally to this work</p>
</fn>
<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>03</day>
<month>10</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>983778</elocation-id>
<history>
<date date-type="received">
<day>01</day>
<month>07</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>15</day>
<month>09</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Li, Jin, Yu and Zhong.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Li, Jin, Yu and Zhong</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>Electrochemical CO<sub>2</sub> reduction offers an effective means to store renewable electricity in value-added chemical feedstocks. Much effort has been made to develop catalysts that achieve high Faradaic efficiency toward Formate production, but the catalysts still need high operating potentials to drive the CO<sub>2</sub>&#x2013;to&#x2013;formate reduction. Here we report physical vapor deposition to fabricate homogeneously alloyed, compositionally controlled Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> bimetallic catalysts over a large area with excellent electrical conductivity. Operating electrochemical studies in Ar-saturated and CO<sub>2</sub>-saturated electrolytes identified that Cu&#x2013;Bi catalysts notably suppress the competing H<sub>2</sub> evolution reaction and enhance CO<sub>2</sub>&#x2013;to&#x2013;formate selectivity. We reported a formate Faradaic efficiency of &#x3e;95% at an improved cathodic potential of &#x223c;&#x2212;0.72&#xa0;V vs. RHE and a high formate cathodic energy efficiency of &#x223c;70%. The electrochemical reaction is stable over 24&#xa0;h at a current density of 200&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>. The work shows the advantages of bimetallic catalysts over single metal catalysts for increased reaction activity and selectivity.</p>
</abstract>
<kwd-group>
<kwd>electrocatalysis</kwd>
<kwd>Cu-Bi</kwd>
<kwd>bimetal</kwd>
<kwd>CO<sub>2</sub>R</kwd>
<kwd>formate</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>Introduction</title>
<p>With the rapid development of modern society, the excessive burning of fossil fuels has led to huge amounts of CO<sub>2</sub> emissions, breaking the ecological carbon cycle and causing the growing greenhouse effect (<xref ref-type="bibr" rid="B14">Singh et al., 2016</xref>; <xref ref-type="bibr" rid="B21">Xiao et al., 2017</xref>; <xref ref-type="bibr" rid="B5">Garza et al., 2018</xref>; <xref ref-type="bibr" rid="B1">Birdja et al., 2019</xref>; <xref ref-type="bibr" rid="B8">Li et al., 2020</xref>). Renewably powered CO<sub>2</sub> conversion to value-added fuels or chemical raw materials, such as CO, HCOO<sup>&#x2212;</sup>, C<sub>2</sub>H<sub>4</sub>, C<sub>2</sub>H<sub>5</sub>OH, etc., is becoming an important way to maintain energy and environmental sustainability (<xref ref-type="bibr" rid="B7">Kortlever et al., 2015</xref>; <xref ref-type="bibr" rid="B16">Wang et al., 2021a</xref>; <xref ref-type="bibr" rid="B18">Wang et al., 2021b</xref>; <xref ref-type="bibr" rid="B17">Wang et al., 2022</xref>). For example, the electroreduction of CO<sub>2</sub> using renewable electricity has attracted great research attention (<xref ref-type="bibr" rid="B19">Wang et al., 2021c</xref>). Among the commonly reported CO<sub>2</sub>R products, formic acid or formate stands out as a promising liquid chemical due to its high energy value in the techno-economic analysis and high volumetric mass density (53.4&#xa0;g&#xa0;L<sup>&#x2212;1</sup>) for easy storage and transport (<xref ref-type="bibr" rid="B23">Yoo et al., 2016</xref>; <xref ref-type="bibr" rid="B3">Chi et al., 2021</xref>).</p>
<p>Conventionally, p block metals such as Bi, Pb, and In have appropriate &#x2a;OCHO binding energy, favoring the CO<sub>2</sub>&#x2013;to&#x2013;formate conversion. However, the electrical conductivity of these metals is not satisfactory, causing a large potential loss at high current densities. Cu is naturally abundant and has good electrical conductivity, possible for practical use (<xref ref-type="bibr" rid="B6">Huang et al., 2018</xref>). Cu-based materials are widely investigated as electrocatalysts for CO<sub>2</sub>R to multi-carbon (C<sub>2&#x2b;</sub>) production (<xref ref-type="bibr" rid="B12">Mistry et al., 2016a</xref>; <xref ref-type="bibr" rid="B11">Mistry et al., 2016b</xref>; <xref ref-type="bibr" rid="B4">Gao et al., 2019</xref>; <xref ref-type="bibr" rid="B24">Zaza et al., 2022</xref>). However, due to the modest binding to H, C, and O (<xref ref-type="bibr" rid="B13">Qin et al., 2019</xref>; <xref ref-type="bibr" rid="B29">Zheng et al., 2021</xref>; <xref ref-type="bibr" rid="B25">Zhang et al., 2022</xref>), Cu shows poor selectivity to one specific product which leads to an increased product separation cost.</p>
<p>Bimetallic catalysts have been reported to increase the activity and selectivity of electrocatalytic CO<sub>2</sub>R by taking the advantage of both metals. Zeng et al. improved the formate production by fabricating single atom Pb anchored Cu catalysts (<xref ref-type="bibr" rid="B29">Zheng et al., 2021</xref>); Thomas J. Meyer et al. enhanced selectivity for methane production by forming Cu-Pd bimetal alloys (<xref ref-type="bibr" rid="B28">Zhang et al., 2015</xref>); Douglas R. MacFarlane et al. improved the electrocatalytic reduction of CO<sub>2</sub> to CO by loading Au on Cu (<xref ref-type="bibr" rid="B2">Chen et al., 2017</xref>); <xref ref-type="bibr" rid="B20">Wang et al. (2010)</xref> prepared novel silver-coated nanoporous copper composite electrocatalysts for CO<sub>2</sub>R to produce dimethyl carbonate. As for formate production, Bi is extensively studied as a promising CO<sub>2</sub>R&#x2013;to&#x2013;formate catalyst due to its abundance on Earth, low cost, and environmental-benign properties. Jiang and collaborators reported that a Bi nanostructured catalyst electrochemically reduced by BiOCl nanosheets obtained 92% FE<sub>HCOOH</sub> at &#x2212;1.5&#xa0;V vs. SCE at room temperature (<xref ref-type="bibr" rid="B26">Zhang et al., 2014</xref>); Zhong et al. achieved over 95% formate selectivity with ultra-long stability of more than 100&#xa0;days (<xref ref-type="bibr" rid="B10">Li et al., 2021</xref>); <xref ref-type="bibr" rid="B9">Li et al. (2019)</xref> achieved nearly 100% formate selectivity using Bi/Bi<sub>2</sub>O<sub>3</sub> with abundant grain boundaries as catalysts. Yet the Bi-based catalysts still require a high potential to conduct electrocatalytic reduction of CO<sub>2</sub> (<xref ref-type="bibr" rid="B15">Tian et al., 2021</xref>).</p>
<p>Herein, we present the large-area fabrication of Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) catalysts using controllable thermal evaporation. We evaluated the CO<sub>2</sub>R and also the competing hydrogen evolution reaction (HER) performance in flow cells in CO<sub>2</sub>-saturated and Ar-saturated electrolytes. We obtained a formate selectivity of 95% and a cathode energy efficiency of 70% at &#x2212;0.72&#xa0;V vs. RHE with Cu<sub>0.8</sub>Bi<sub>0.2</sub>. The CO<sub>2</sub>R can proceed stably and efficiently at a current density of 200&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup> over 24&#xa0;h. We conclude that the bimetallic Cu<sub>0.8</sub>Bi<sub>0.2</sub> improves formate selectivity and enhances the CO<sub>2</sub>R activity and cathodic energy efficiency, which may offer new perspectives for future design and synthesis of bimetallic CO<sub>2</sub>R catalysts.</p>
</sec>
<sec id="s2">
<title>Experimental section</title>
<sec id="s2-1">
<title>Synthesis of Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25), Cu and Bi catalyst</title>
<p>Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25), Cu, and Bi catalysts were synthesized by using the thermal evaporation (SKY-RH400) method. To prepare the Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) catalyst, the precursors Cu and Bi particles are evaporated onto the PTFE gas diffusion electrodes by thermal evaporation. In brief, 2&#xa0;g of Bi metal particles and 2&#xa0;g of Cu metal particles were put into the tungsten boats in the deposition chamber. The metal powder was slowly melted in a vacuum environment below 5&#x2a;10<sup>&#x2013;4</sup>&#xa0;Pa. The evaporation rate of Bi was set to 0.03, 0.04, and 0.05&#xa0;nm&#xa0;s<sup>&#x2212;1</sup> and Cu was set to 0.07, 0.06, and 0.05&#xa0;nm&#xa0;s<sup>&#x2212;1</sup> to obtain Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) samples. The thickness of the as-deposited Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) films was about 500&#xa0;nm as measured by a thickness meter placed inside the evaporation chamber. Uniform bimetallic films were obtained. To prepare the pure Bi and Cu films with the same thickness as control samples, we evaporated both Bi and Cu at 0.1&#xa0;nm&#xa0;s<sup>&#x2212;1</sup> under the same conditions.</p>
</sec>
<sec id="s2-2">
<title>Characterization</title>
<p>Field Emission Scanning Electron Microscope (FESEM) images were taken on a SU8100 Scanning Electron Microscope. SEM-EDX test voltage is 20&#xa0;kV. Powder X-ray diffraction (XRD) was performed using a Bruker D8 Advance X-ray diffractometer using Cu K&#x3b1; radiation (<italic>&#x3bb;</italic> &#x3d; 0.15418&#xa0;nm) in the 2&#x3b8; range of 20&#xb0;&#x2013;80&#xb0; at a scan rate of 7&#xb0;/min. X-ray photoelectron spectroscopy (XPS) studies were performed using PHI5000 VersaProbe. The binding energy data were calibrated relative to the C 1s signal at 284.6&#xa0;eV.</p>
</sec>
<sec id="s2-3">
<title>Electrochemical measurements</title>
<p>The electrochemical CO<sub>2</sub>R experiments were carried out in a flow cell setup of a three-electrode system. The CO<sub>2</sub>R catalysts, Ag/AgCl electrodes, and foamed nickel films were used as working electrodes, reference electrodes, and counter electrodes, respectively. 1&#xa0;M KOH electrolytes were used as both catholyte and anolyte. An anion exchange membrane (Fumasep FAB-PK-130) was used to separate the catholyte and anolyte. All measurements were performed by using an electrochemical workstation (AOTU-Lab). All experiments were performed under the standard conditions with a CO<sub>2</sub> gas flow rate of 25 standard cubic centimeter per minute (sccm) at the flow cell outlet. The potential range of linear sweep voltammetry (LSV) is 0 to &#x2212;1.2 V<sub>RHE</sub>, with a sweep speed of 50&#xa0;mV&#xa0;s<sup>&#x2212;1</sup>. The electrode potentials were converted to the RHE potentials using V<sub>RHE</sub> &#x3d; V<sub>Ag/AgCl</sub> &#x2b; 0.197 &#x2b; 0.059 &#xd7; pH. Electrochemical impedance spectroscopy (EIS) was measured at open circuit potential with amplitudes of 10&#xa0;mV over the frequency range of 1&#xa0;MHz to 1&#xa0;Hz. The liquid products of CO<sub>2</sub> reduction were quantitatively analyzed by ion chromatography (Shenghan ICS-1000). Gaseous products were analyzed by gas chromatography (PE GC9790). <sup>1</sup>H nuclear magnetic resonance (NMR) spectroscopy was used to identify other liquid products other than formate. All measurements were made at room temperature and ambient pressure.</p>
<p>The Faradaic Efficiency (FE) of formate is calculated as follows:<disp-formula id="equ1">
<mml:math id="m1">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi mathvariant="normal">F</mml:mi>
<mml:mi mathvariant="normal">E</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>f</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>m</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>t</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mi>n</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>F</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>V</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>c</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="italic">1000</mml:mn>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>M</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>Q</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
</disp-formula>where <italic>n</italic> is the number of electrons transferred (<italic>n</italic> &#x3d; 2). <italic>F</italic> is Faraday&#x2019;s constant (96,485&#xa0;C&#xa0;mol<sup>&#x2212;1</sup>). <italic>c</italic> is the mass concentration of formate produced by the reaction (mg&#xa0;L<sup>&#x2212;1</sup>). <italic>V</italic> is the volume of catholyte (L). <italic>M</italic> is the molar mass of formate (46.03&#xa0;g&#xa0;mol<sup>&#x2212;1</sup>). Q is the total amount of charge consumed by the entire reaction monitored by the electrochemical workstation (C).</p>
<p>The FE of the gas product is calculated according to the following equation:<disp-formula id="equ2">
<mml:math id="m2">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi mathvariant="normal">F</mml:mi>
<mml:mi mathvariant="normal">E</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>g</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>s</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mi>n</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>F</mml:mi>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>V</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="italic">1000</mml:mn>
<mml:mo>&#x2217;</mml:mo>
<mml:mn mathvariant="italic">22.4</mml:mn>
<mml:mo>&#x2217;</mml:mo>
<mml:mi>Q</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
</disp-formula>where <italic>n</italic> is the number of electrons transferred (<italic>n</italic> &#x3d; 2). <italic>F</italic> is Faraday&#x2019;s constant (96,485&#xa0;C&#xa0;mol<sup>&#x2212;1</sup>). <italic>V</italic> is the volume of catholyte (L). <italic>Q</italic> is the total amount of charge consumed by the entire reaction monitored by the electrochemical workstation (C).</p>
<p>Cathode Energy Efficiency (CEE) Calculation Formula:<disp-formula id="equ3">
<mml:math id="m3">
<mml:mrow>
<mml:msub>
<mml:mrow>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">E</mml:mi>
<mml:mi mathvariant="normal">E</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>f</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>m</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>t</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mrow>
<mml:mo>(</mml:mo>
<mml:mrow>
<mml:mn mathvariant="italic">1.23</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi>E</mml:mi>
<mml:mrow>
<mml:mi>f</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>m</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>t</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
<mml:mo>)</mml:mo>
</mml:mrow>
<mml:mo>&#x2217;</mml:mo>
<mml:msub>
<mml:mrow>
<mml:mi>F</mml:mi>
<mml:mi>E</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>f</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>r</mml:mi>
<mml:mi>m</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>t</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="italic">1.23</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi>E</mml:mi>
<mml:mrow>
<mml:mi>c</mml:mi>
<mml:mi>a</mml:mi>
<mml:mi>t</mml:mi>
<mml:mi>h</mml:mi>
<mml:mi>o</mml:mi>
<mml:mi>d</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
</disp-formula>where <italic>E</italic>
<sub>
<italic>formate</italic>
</sub> of &#x2212;0.199&#xa0;V vs. RHE is the standard potential of the formate formation. <italic>FE</italic>
<sub>
<italic>formate</italic>
</sub> is the measured formate Faradaic efficiency. <italic>E</italic>
<sub>
<italic>cathode</italic>
</sub> is the applied potential vs. RHE.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>Results and discussion</title>
<p>We prepared a series of Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) bimetallic materials, pure Cu, and pure Bi samples on a large area by thermal evaporation. As shown in <xref ref-type="fig" rid="F1">Figures 1A,B</xref> and <xref ref-type="sec" rid="s10">Supplementary Figure S1</xref>, the as-prepared Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) catalysts were all tightly wrapped on the PTFE fibers and formed uniformly distributed Cu and Bi nanoparticles with a size of 100&#x2013;200&#xa0;nm. It can be seen from <xref ref-type="fig" rid="F2">Figure 2A</xref> and <xref ref-type="sec" rid="s10">Supplementary Figure S1</xref> that with the increase of Bi content, the particles gradually form nanocrystals, and the particle size of Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25) is about 100&#x2013;200&#xa0;nm, and the Cu-Bi bimetallic distribution is uniform. The particle sizes of Bi and Cu are 200&#xa0;nm and 50&#x2013;100&#xa0;nm, respectively. Then we measured the element distribution using SEM-EDX. As shown in the mapping spectrum, Cu and Bi elements were uniformly distributed on the catalyst surfaces (<xref ref-type="fig" rid="F2">Figures 2B,C</xref>; <xref ref-type="sec" rid="s10">Supplementary Figure S2</xref>). Through SEM-EDX and XPS analysis, the element ratio of our prepared Cu-Bi was 0.8:0.2 (<xref ref-type="sec" rid="s10">Supplementary Figure S3</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>
<bold>(A)</bold> A schematic illustration of the synthetic process of Cu-Bi catalyst on polytetrafluoroethylene (PTFE). <bold>(B)</bold> The insert optical image shows a 5&#xa0;cm<sup>2</sup> &#xd7; 5&#xa0;cm<sup>2</sup> sample of Cu<sub>0.8</sub>Bi<sub>0.2</sub> on the PTFE substrate.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g001.tif"/>
</fig>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>
<bold>(A)</bold> SEM images of the synthesized Cu<sub>0.8</sub>Bi<sub>0.2</sub> by thermal evaporation. <bold>(B)</bold> EDX spectrum of the Cu<sub>0.8</sub>Bi<sub>0.2</sub>. <bold>(C)</bold> EDX Mapping results of the Cu<sub>0.8</sub>Bi<sub>0.2</sub>.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g002.tif"/>
</fig>
<p>The chemical states of the synthesized Cu, Cu<sub>0.8</sub>Bi<sub>0.2</sub>, and Bi catalysts were studied by the high-resolution XPS spectra of Bi 4f and Cu 2p, respectively (<xref ref-type="fig" rid="F3">Figures 3A,B</xref>). We observed that the strong peaks at 158.7 and 164.0&#xa0;eV corresponded to Bi<sup>3&#x2b;</sup> 4f<sub>7/2</sub> and Bi<sup>3&#x2b;</sup> 4f<sub>5/2</sub>, and the peaks at 157.0&#xa0;eV, 162.3&#xa0;eV corresponded to Bi<sup>0</sup> 4f<sub>7/2</sub> and Bi<sup>0</sup> 4f<sub>5/2</sub>. From the high-resolution XPS spectrum of Cu 2p, the peaks at 932.0 and 951.8&#xa0;eV corresponded to Cu<sup>0, 1&#x2b;</sup>, while the peaks at 933.9 and 953.6&#xa0;eV were consistent with Cu<sup>2&#x2b;</sup>. It should be explained that both Cu and Bi are easily oxidized in air, the positively charged Bi<sup>3&#x2b;</sup> and Cu<sup>2&#x2b;</sup> are detected, probably because the oxidation occurred during the storage of the sample in air. Compared with Cu, the d-band center of Cu<sub>0.8</sub>Bi<sub>0.2</sub> moved more positively after the introduction of Bi species (<xref ref-type="fig" rid="F3">Figure 3C</xref>). As reported, the positively shifted d-band center likely increases the electron donation from the catalysts to the adsorbed &#x2a;OCHO intermediate, strengthening the &#x2a;OCHO surface binding (<xref ref-type="bibr" rid="B22">Xin et al., 2014</xref>; <xref ref-type="bibr" rid="B27">Zhang et al., 2018</xref>). This is consistent with our electrochemical CO<sub>2</sub>R test that Cu-Bi catalysts show improved performance.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>
<bold>(A)</bold> Cu 2p XPS spectra of Cu<sub>0.8</sub>Bi<sub>0.2</sub>. <bold>(B)</bold> Bi 4f XPS spectra of Cu<sub>0.8</sub>Bi<sub>0.2</sub>. <bold>(C)</bold> Surface valence band photoemission spectra of Cu and Cu<sub>0.8</sub>Bi<sub>0.2</sub>. The white bar in <bold>(C)</bold> highlights the <italic>d</italic>-band center of various materials.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g003.tif"/>
</fig>
<p>The CO<sub>2</sub>R electrochemical performance of the Cu<sub>
<italic>1-x</italic>
</sub>Bi<sub>
<italic>x</italic>
</sub> (<italic>x</italic> &#x3d; 0.1, 0.2, 0.25), pure Cu, and pure Bi catalysts were tested in a flow cell with a three-electrode system (<xref ref-type="fig" rid="F4">Figure 4</xref>). The anode was Ni, the reference electrode was an Ag/AgCl electrode, and the electrolyte was 1&#xa0;M KOH solution (pH &#x3d; 14). From the linear sweep voltammetry (LSV), we can intuitively see that the reaction overpotential of Cu-Bi bimetal was reduced significantly (<xref ref-type="fig" rid="F5">Figure 5A</xref>; <xref ref-type="sec" rid="s10">Supplementary Figure S4</xref>). As shown in <xref ref-type="fig" rid="F3">Figure 3B</xref>, the overpotential (520&#xa0;mV) of the Cu<sub>0.8</sub>Bi<sub>0.2</sub> catalyst is significantly smaller than that of the Bi catalyst (660&#xa0;mV) at the same current density (100&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>). The overpotential for Cu is the best (400&#xa0;mV), but the product selectivity is poor (<xref ref-type="fig" rid="F5">Figure 5B</xref>). The cathodic current density on Cu, Cu<sub>0.8</sub>Bi<sub>0.2</sub>, and Bi electrodes was largely reduced when N<sub>2</sub> was passing through (<xref ref-type="fig" rid="F5">Figure 5A</xref>). In the presence of N<sub>2</sub>, the current density started to increase slowly at &#x2212;0.70&#xa0;V vs. RHE, which was mainly caused by the hydrogen evolution reaction (HER). It is also clear that HER on the Cu electrode is worse than CO<sub>2</sub>R on the Bi electrode, indicating that the introduction of Bi into Cu can suppress HER In the presence of CO<sub>2</sub>, which is more beneficial to CO<sub>2</sub>R.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Schematic of Cu-Bi electrocatalyst on PTFE for electroreduction of CO<sub>2</sub> in a flow cell.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g004.tif"/>
</fig>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>
<bold>(A)</bold> The LSV curves under CO<sub>2</sub> or N<sub>2</sub> conditions of Cu<sub>0.8</sub>Bi<sub>0.2</sub>, Cu, and Bi. <bold>(B)</bold> The particular current density of formate of Cu<sub>0.8</sub>Bi<sub>0.2</sub>, Cu, and Bi. <bold>(C,E)</bold> The faradaic efficiency of formate and H<sub>2</sub> of Cu<sub>0.8</sub>Bi<sub>0.2</sub>, Cu, and Bi at current densities of 100, 200, and 300&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>. <bold>(D)</bold> The cathode energy efficiency of formate at current densities of Cu<sub>0.8</sub>Bi<sub>0.2</sub>, Cu, and Bi of 100, 200, and 300&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>. <bold>(F)</bold> The EIS curve of Cu, Cu<sub>0.8</sub>Bi<sub>0.2</sub>, and Bi.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g005.tif"/>
</fig>
<p>To investigate the product selectivity of CO<sub>2</sub>R with Cu<sub>0.8</sub>Bi<sub>0.2</sub>, Cu, and Bi catalysts, chronopotentiometry tests were performed at current densities of 100, 200, and 300&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>, respectively (<xref ref-type="sec" rid="s10">Supplementary Figure S5</xref>). The products were quantitatively analyzed by gas chromatography (GC), ion chromatography (IC), and nuclear magnetic resonance (NMR). As shown in <xref ref-type="fig" rid="F5">Figures 5C-E</xref>, and <xref ref-type="sec" rid="s10">Supplementary Figure S6</xref>, the Cu<sub>0.8</sub>Bi<sub>0.2</sub> catalyst achieved over 90% selectivity to formate at all current densities, in particular, the selectivity for formate reached 95% at a current density of 100&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>, with a cathode energy efficiency reaching about 70%. Although the single-metal Bi catalyst has a formate selectivity close to that of Cu<sub>0.8</sub>Bi<sub>0.2</sub>, its cathode energy efficiency is much lower than that of Cu<sub>0.8</sub>Bi<sub>0.2</sub> at all current densities due to its high reaction potential. In the case of the Cu catalyst, the formate selectivity is very low. Considering both the selective and energy efficiency, Cu<sub>0.8</sub>Bi<sub>0.2</sub> outperforms Bi and Cu in the electroreduction of CO<sub>2</sub> to formate.</p>
<p>As shown in <xref ref-type="fig" rid="F5">Figure 5E</xref>, we found that the introduction of Bi into Cu can significantly reduce HER, which is consistent with the LSV results under N<sub>2</sub> environment. To explain the reason for the excellent performance of Cu<sub>0.8</sub>Bi<sub>0.2</sub> catalysts, we performed EIS tests on the three samples. As is shown in <xref ref-type="fig" rid="F5">Figure 5F</xref>, Cu<sub>0.8</sub>Bi<sub>0.2</sub> shows a smaller semicircle diameter than Bi in the impedance spectrum, suggesting that the charge transfer resistance of Cu<sub>0.8</sub>Bi<sub>0.2</sub> is lower than that of Bi, ensuring a faster electron transfer during the reaction. The conductivity of Cu is 58.13953&#xa0;S/m, and that of Bi is 0.95238&#xa0;S/m. The conductivity of Cu is significantly better than that of Bi. Therefore, we analyze that the loading of Cu metal increases the conductivity of the material and reduces the charge transfer resistance, also the HER is greatly suppressed in the presence of CO<sub>2</sub>, as a result, Cu<sub>0.8</sub>Bi<sub>0.2</sub> can reduce the reaction overpotential and maintain high CO<sub>2</sub>R catalytic activity and selectivity.</p>
<p>To verify the stability of the Cu<sub>0.8</sub>Bi<sub>0.2</sub> catalyst, we performed the stability test at a current density of 200&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>, and SEM characterization of the reacted sample was performed. It can be seen from <xref ref-type="fig" rid="F6">Figure 6</xref> that during the reaction process of the 24&#xa0;h CO<sub>2</sub> reduction, the reaction potential did not change significantly, and the selectivity of HCOO<sup>&#x2212;</sup> was maintained above 90%. We also carried out SEM, SEM-EDX, and XRD analyses of the sample after 24&#xa0;h of reaction. From <xref ref-type="sec" rid="s10">Supplementary Figure S7</xref>, we can observe that the morphology and structure of the Cu<sub>0.8</sub>Bi<sub>0.2</sub> bimetallic catalyst did not change after the reaction. The XRD characterizations also showed that the catalyst did not change significantly after the reaction, indicating that good stability with Cu<sub>0.8</sub>Bi<sub>0.2</sub> for CO<sub>2</sub>R.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>The stability test of Cu<sub>0.8</sub>Bi<sub>0.2</sub> in 1&#xa0;M KOH at 200&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>.</p>
</caption>
<graphic xlink:href="fchem-10-983778-g006.tif"/>
</fig>
</sec>
<sec sec-type="conclusion" id="s4">
<title>Conclusion</title>
<p>In conclusion, we developed a simple, controllable, and large-area preparation method for the synthesis of Cu<sub>0.8</sub>Bi<sub>0.2</sub> catalysts. Cu<sub>0.8</sub>Bi<sub>0.2</sub> exhibited excellent formate selectivity and cathode energy efficiency under all current densities. Specifically, it exhibited a formate selectivity of 95% and a cathode energy efficiency of 70% at a potential of &#x2212;0.72&#xa0;V vs. reversible hydrogen electrode and maintained the CO<sub>2</sub>R durability for over 24&#xa0;h at a current density of 200&#xa0;mA&#xa0;cm<sup>&#x2212;2</sup>. The excellent catalytic performance of Cu<sub>0.8</sub>Bi<sub>0.2</sub> is attributed to the following factors: 1) CuBi alloy likely has a favorable work function to improve CO<sub>2</sub> adsorption for formate production; 2) CuBi alloy improves electron transport. We expect that the bimetal Cu<sub>0.8</sub>Bi<sub>0.2</sub> electrocatalyst may offer a material foundation for the improved catalytic CO<sub>2</sub>R to formate conversion.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The original contributions presented in the study are included in the article/<xref ref-type="sec" rid="s10">Supplementary Material</xref>, further inquiries can be directed to the corresponding author.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>MZ supervised the project. MZ conceived the idea and designed the experiments. LL and XJ conducted the synthesis, characterizations, and flow-cell tests. LL, XJ, XY, and MZ discussed the experiment results. MZ, XY, and LL wrote the manuscript. All authors discussed the results and assisted during manuscript preparation.</p>
</sec>
<sec id="s7">
<title>Funding</title>
<p>This work was supported by the National Key R&#x26;D Program of China (No. 2020YFA0406102), the National Natural Science Foundation of China (grant numbers 22272078 and 91963121), the Frontiers Science Center for Critical Earth Material Cycling of Nanjing University, and the &#x201c;Innovation and Entrepreneurship of Talents plan&#x201d; of Jiangsu Province.</p>
</sec>
<ack>
<p>The authors also acknowledge the support from Jiangsu Key Laboratory of nanotechnology, Nanjing University</p>
</ack>
<sec sec-type="COI-statement" id="s8">
<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="s9">
<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>
<sec id="s10">
<title>Supplementary material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/fchem.2022.983778/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fchem.2022.983778/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="DataSheet1.PDF" id="SM1" mimetype="application/PDF" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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