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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="doi">10.3389/fchem.2020.00293</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>Effect of CeH<sub>2.73</sub>-CeO<sub>2</sub> Composites on the Desorption Properties of Mg<sub>2</sub>NiH<sub>4</sub></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name><surname>Wu</surname> <given-names>Kaiyao</given-names></name>
</contrib>
<contrib contrib-type="author">
<name><surname>Cai</surname> <given-names>Daqian</given-names></name>
</contrib>
<contrib contrib-type="author">
<name><surname>Shao</surname> <given-names>Kaimei</given-names></name>
</contrib>
<contrib contrib-type="author">
<name><surname>Xue</surname> <given-names>Tuguang</given-names></name>
</contrib>
<contrib contrib-type="author">
<name><surname>Zhang</surname> <given-names>Peng</given-names></name>
</contrib>
<contrib contrib-type="author">
<name><surname>Li</surname> <given-names>Wei</given-names></name>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name><surname>Lin</surname> <given-names>Huai-Jun</given-names></name>
<xref ref-type="corresp" rid="c001"><sup>&#x0002A;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/787714/overview"/>
</contrib>
</contrib-group>
<aff><institution>Institute of Advanced Wear and Corrosion Resistant and Functional Materials, Jinan University</institution>, <addr-line>Guangzhou</addr-line>, <country>China</country></aff>
<author-notes>
<fn fn-type="edited-by"><p>Edited by: Yongfeng Liu, Zhejiang University, China</p></fn>
<fn fn-type="edited-by"><p>Reviewed by: Yao Zhang, Southeast University, China; Rapee Utke, Suranaree University of Technology, Thailand</p></fn>
<corresp id="c001">&#x0002A;Correspondence: Huai-Jun Lin <email>hjlin&#x00040;jnu.edu.cn</email></corresp>
<fn fn-type="other" id="fn001"><p>This article was submitted to Inorganic Chemistry, a section of the journal Frontiers in Chemistry</p></fn></author-notes>
<pub-date pub-type="epub">
<day>15</day>
<month>04</month>
<year>2020</year>
</pub-date>
<pub-date pub-type="collection">
<year>2020</year>
</pub-date>
<volume>8</volume>
<elocation-id>293</elocation-id>
<history>
<date date-type="received">
<day>22</day>
<month>02</month>
<year>2020</year>
</date>
<date date-type="accepted">
<day>24</day>
<month>03</month>
<year>2020</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#x000A9; 2020 Wu, Cai, Shao, Xue, Zhang, Li and Lin.</copyright-statement>
<copyright-year>2020</copyright-year>
<copyright-holder>Wu, Cai, Shao, Xue, Zhang, Li and Lin</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>A series of CeH<sub>2.</sub>73/CeO<sub>2</sub> composites with different ratios of hydride and oxide phases are prepared from the pure cerium hydride via oxidation treatments in the air at room temperature, and they are subsequently doped into Mg<sub>2</sub>NiH<sub>4</sub> by ball milling. The desorption properties of the as-prepared Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B;CeH<sub>2.73</sub>/CeO<sub>2</sub> composites are studied by thermogravimetry and differential scanning calorimetery. Microstructures are studied by scanning electron microscopy and transmission electron microscopy, and the phase transitions during dehydrogenation are analyzed through <italic>in situ</italic> X-ray diffraction. Results show that the initial dehydrogenation temperature and activation energy of Mg<sub>2</sub>NiH<sub>4</sub> are maximally reduced by doping the CeH<sub>2.73</sub>/CeO<sub>2</sub> composite with the same molar ratio of cerium hydride and oxide. In this case, the CeH<sub>2.73</sub>/CeO<sub>2</sub> composite has the largest density of interface among them, and the hydrogen release effect at the interface between cerium hydride and oxide plays an efficient catalytic role in enhancing the hydrogen desorption properties of Mg<sub>2</sub>NiH<sub>4</sub>.</p></abstract>
<kwd-group>
<kwd>Hydrogen storage materials</kwd>
<kwd>dehydrogenation</kwd>
<kwd>Mg<sub>2</sub>NiH<sub>4</sub></kwd>
<kwd>CeH<sub>2.73</sub>/CeO<sub>2</sub></kwd>
<kwd>catalysts</kwd>
</kwd-group>
<contract-num rid="cn001">51601090</contract-num>
<contract-num rid="cn002">21619415</contract-num>
<contract-sponsor id="cn001">National Natural Science Foundation of China<named-content content-type="fundref-id">10.13039/501100001809</named-content></contract-sponsor>
<contract-sponsor id="cn002">Fundamental Research Funds for the Central Universities<named-content content-type="fundref-id">10.13039/501100012226</named-content></contract-sponsor>
<contract-sponsor id="cn003">Guangdong Science and Technology Department<named-content content-type="fundref-id">10.13039/501100007162</named-content></contract-sponsor>
<counts>
<fig-count count="7"/>
<table-count count="1"/>
<equation-count count="2"/>
<ref-count count="44"/>
<page-count count="7"/>
<word-count count="4315"/>
</counts>
</article-meta>
</front>
<body>
<sec sec-type="intro" id="s1">
<title>Introduction</title>
<p>With the advantages of abundant natural resources and no pollution to the environment, hydrogen has been widely considered as an ideal carbon-free energy carrier. Hydrogen energy storage technology is a prerequisite for the large-scale utilization of hydrogen energy. Light-weight solid-state hydrogen storage materials have been considered to be ideal candidates for hydrogen storage because of the high hydrogen storage density and security consideration (Mohtadi and Orimo, <xref ref-type="bibr" rid="B26">2016</xref>; Wang et al., <xref ref-type="bibr" rid="B38">2016</xref>). Among the existing solid-state hydrogen storage materials, Mg-based hydrogen storage materials are widely studied and considered as promising solid-state hydrogen storage materials due to the high hydrogen storage capacity, abundance on the earth and low production cost (Ouyang et al., <xref ref-type="bibr" rid="B29">2013</xref>, <xref ref-type="bibr" rid="B27">2017</xref>; Rusman and Dahari, <xref ref-type="bibr" rid="B32">2016</xref>; Shao et al., <xref ref-type="bibr" rid="B34">2018</xref>).</p>
<p>MgH<sub>2</sub> and Mg<sub>2</sub>NiH<sub>4</sub> are two typical Mg-based hydrogen storage materials with hydrogen densities of 7.6 wt and 3.6 wt%, respectively (Reilly and Wiswall, <xref ref-type="bibr" rid="B31">1968</xref>; Bogdanovi&#x00107;, <xref ref-type="bibr" rid="B3">1984</xref>; Liu et al., <xref ref-type="bibr" rid="B21">2016</xref>, <xref ref-type="bibr" rid="B22">2019</xref>; Zhan et al., <xref ref-type="bibr" rid="B41">2016</xref>; Chen et al., <xref ref-type="bibr" rid="B5">2018</xref>; Ding et al., <xref ref-type="bibr" rid="B6">2019</xref>). Nevertheless, the stable thermodynamics and slow kinetics of hydrogen storage properties of Mg-based materials lead to harsh conditions for dehydrogenation (Bogdanovi&#x00107; et al., <xref ref-type="bibr" rid="B4">2010</xref>; Jain et al., <xref ref-type="bibr" rid="B12">2010</xref>). The hydrogen desorption temperatures of MgH<sub>2</sub> and Mg<sub>2</sub>NiH<sub>4</sub> are usually as high as 250&#x02013;350C. Many efforts have been made by researchers to improve the kinetics and reduce the desorption temperatures of MgH<sub>2</sub> and Mg<sub>2</sub>NiH<sub>4</sub>. The commonly conducted methods include mechanical alloying, doping catalysts, nanostructuring, surface modification and so on (Terashita et al., <xref ref-type="bibr" rid="B36">1999</xref>; Lin et al., <xref ref-type="bibr" rid="B17">2012a</xref>, <xref ref-type="bibr" rid="B20">2016</xref>; Shao et al., <xref ref-type="bibr" rid="B35">2012</xref>; Eleskandarany et al., <xref ref-type="bibr" rid="B7">2016</xref>; Zhang et al., <xref ref-type="bibr" rid="B42">2017</xref>; Khan et al., <xref ref-type="bibr" rid="B13">2018</xref>; Xu et al., <xref ref-type="bibr" rid="B40">2019</xref>).</p>
<p>Doping catalysts by ball milling is a commonly-used and efficient method to enhance the hydrogenation/dehydrogenation kinetics of Mg-based materials (Ouyang et al., <xref ref-type="bibr" rid="B30">2014a</xref>,<xref ref-type="bibr" rid="B28">b</xref>; Wang and Wang, <xref ref-type="bibr" rid="B39">2017</xref>). To date, many additives have been explored, including oxides (Barkhordarian et al., <xref ref-type="bibr" rid="B1">2003</xref>), transition metals (Hanada et al., <xref ref-type="bibr" rid="B10">2005</xref>), hydrides (Ma et al., <xref ref-type="bibr" rid="B25">2017</xref>), carbon-based materials (Lototskyy et al., <xref ref-type="bibr" rid="B24">2013</xref>) and so on. It has been demonstrated that compounds with higher valences show higher catalytic effect on the hydrogen storage performances of Mg-based materials than that of the lower valence compounds (Bobet et al., <xref ref-type="bibr" rid="B2">2002</xref>). Because of the unique 4<italic>f</italic> electron of the Ce element, Ce-based compounds are widely used in the catalysis field (Trovarelli, <xref ref-type="bibr" rid="B37">1996</xref>). Long et al. (<xref ref-type="bibr" rid="B23">2013</xref>) reported Mg-Ce oxide powders produced by an arc plasma evaporation method. As a result, enthalpies of hydrogenation and dehydrogenation for Mg/MgH<sub>2</sub> reduce to &#x02212;71.0 and 75.4 kJ/mol H<sub>2</sub>, respectively. Moreover, the hydrogenation activation energy is reduced to only 47.75 kJ/mol. The composite can absorb 4.07 wt%-H at 323 K in 10 h. Their study indicates that minor addition of Ce oxide can remarkably improve the hydrogenation kinetics of Mg/MgH<sub>2</sub>. We previously reported that CeF<sub>4</sub> was an efficient catalyst to enhance the hydrogen storage properties of MgH<sub>2</sub> (Lin et al., <xref ref-type="bibr" rid="B16">2015</xref>), which can lead to reduced dehydrogenation temperature and activation energy because of the formation of new Mg-Ce-F species on the surface of MgH<sub>2</sub>. Gulicovski (Gulicovski et al., <xref ref-type="bibr" rid="B9">2012</xref>) et al. prepared MgH<sub>2</sub>-CeO<sub>2</sub> composite by ball milling of MgH<sub>2</sub> and nano-CeO<sub>2</sub> particles. The dehydrogenation activation energy is reduced to 60 &#x000B1; 10 kJ/mol, indicating that the activation energy is sufficiently decreased by the catalytic effect of vacant CeO<sub>2</sub> particles. We also developed a new symbiotic CeH<sub>2.73</sub>/CeO<sub>2</sub> nano-catalyst, which was <italic>in-situ</italic> produced by controlling hydrogenation and oxidation treatments upon the amorphous Mg-Ce-Ni alloys (Lin et al., <xref ref-type="bibr" rid="B18">2014</xref>), leading to significantly improved dehydrogenation performance of MgH<sub>2</sub>-based composite. Moreover, <italic>in situ</italic> TEM and DFT study show that the remarkable catalysis effect is attributed to the spontaneous hydrogen release effect at the interface between cerium oxide and hydride. Because the composite contains only major MgH<sub>2</sub> but also minor Mg<sub>2</sub>NiH<sub>4</sub>, the effect of CeH<sub>2.73</sub>/CeO<sub>2</sub> composite on the dehydrogenation properties of Mg<sub>2</sub>NiH<sub>4</sub> has not been well-understood.</p>
<p>In order to clarify the effect of cerium hydride/oxide composites on the dehydrogenation properties of Mg<sub>2</sub>NiH<sub>4</sub>, in the present study, a series of CeH<sub>2.73</sub>/CeO<sub>2</sub> composites with different ratios of cerium oxide and hydride were synthesized from pure cerium hydride via controlled oxidation treatments in the air at room temperature, and then they were doped into Mg<sub>2</sub>NiH<sub>4</sub> by ball milling. The dehydrogenation properties of cerium hydride and cerium oxide-doped Mg<sub>2</sub>NiH<sub>4</sub> were studied, and the initial dehydrogenation temperature and activation energy were characterized by TG-DSC and a Kissinger&#x00027;s method. Moreover, the phase transitions during dehydrogenation were analyzed through <italic>in situ</italic> XRD experiments.</p>
</sec>
<sec id="s2">
<title>Experimental Details</title>
<sec>
<title>Materials</title>
<p>The Mg<sub>2</sub>NiH<sub>4</sub> used in this experiment was prepared by a method of hydrogenation combustion synthesis method (HCS), which was carried out in Prof. Yunfeng Zhu&#x00027;s group in Nanjing Tech University (Gu et al., <xref ref-type="bibr" rid="B8">2009</xref>; Zhu et al., <xref ref-type="bibr" rid="B44">2017</xref>). CeH<sub>2.73</sub> (purity &#x0003E;99%) was purchased from Hunan Research Institute of Non-ferrous metals. About 0.1 g CeH<sub>2.73</sub> powder was located in a plastic bottle of 3 ml, in the Ar glove-box. Then it was transferred into the small side box of glove-box. The door of side box was then open to let air in for different time: 0.5, 1.5, 3, 10, and 60 min. The oxidized CeH<sub>2.73</sub> became CeH<sub>2.73</sub>/CeO<sub>2</sub> composites, and 2 mol% of CeH<sub>2.73</sub>/CeO<sub>2</sub> composites were then doped into Mg<sub>2</sub>NiH<sub>4</sub> by ball milling at 400 rpm for 4 h.</p>
</sec>
<sec>
<title>Characterizations</title>
<p>The phase structures were analyzed by X-ray diffraction (XRD), and the phase transition during dehydrogenation was analyzed by <italic>in situ</italic> XRD analysis. The XRD analysis was carried out by an X-ray diffractometer apparatus (UItima IV, Rigaku, Japan) with Cu-K &#x003B1; (&#x003BB; = 0.15405 nm). The tube voltage and tube current were 40 kV and 40 mA, respectively. Thermogravimetry (TG) and Differential Scanning Calorimetery (DSC) were used to study the hydrogen desorption behaviors at different heating rates on a METTLER TGA/DSC 3<sup>&#x0002B;</sup> synchronous thermal analyzer. The microstructures of the Mg<sub>2</sub>NiH<sub>4</sub>-Ce<sub>2.73</sub>/CeO<sub>2</sub> composites were observed by backscattered electron imaging using scanning electron microscope (SEM) and transition electronic microscopy (TEM).</p>
</sec>
</sec>
<sec id="s3">
<title>Results and Discussion</title>
<sec>
<title>Preparation of the CeH<sub>2.73</sub>/CeO<sub>2</sub> Catalysts</title>
<p>Six sets of CeH<sub>2.73</sub>/CeO<sub>2</sub> composites prepared by oxidation treatments for different durations were analyzed by XRD. The CeH<sub>2.73</sub>/CeO<sub>2</sub> composites are marked as S1, S2, S3, S4, S5, and S6, according to the oxidation duration of CeH<sub>2.73</sub> of 0, 0.5, 1.5, 3, 10, and 60 min, respectively. The diffraction patterns are shown in <xref ref-type="fig" rid="F1">Figure 1</xref>. With the increase of oxidation time, CeH<sub>2.73</sub> gradually transforms into CeO<sub>2</sub>. After oxidation of 60 min, no CeH<sub>2.73</sub> has left. The obtained XRD patterns were refined by a Jade 6.0 software and the phase contents were calculated by the K value (RIR) method. The relative contents of the CeO<sub>2</sub> phase as increase of the oxidation time are shown in <xref ref-type="fig" rid="F2">Figure 2</xref>. The oxidation data can be fitted by the Avrami&#x02013;Erofeev equation deduced from the nucleation and growth process:</p>
<disp-formula id="E1"><label>(1)</label><mml:math id="M1"><mml:mtable class="eqnarray" columnalign="left"><mml:mtr><mml:mtd><mml:mi>&#x003B1;</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn><mml:mo>-</mml:mo><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mi>p</mml:mi><mml:mrow><mml:mo stretchy="false">(</mml:mo><mml:mrow><mml:mo>-</mml:mo><mml:mi>B</mml:mi><mml:msup><mml:mrow><mml:mi>t</mml:mi></mml:mrow><mml:mrow><mml:mi>m</mml:mi></mml:mrow></mml:msup></mml:mrow><mml:mo stretchy="false">)</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<p>where &#x003B1; is the ratio of reacted material to total material, m and B are constants. The fitted m is 1.085, which is very close to 1.07, indicating the oxidation of CeH<sub>2.73</sub> at room temperature is a three-dimensional interface reaction process (Lin et al., <xref ref-type="bibr" rid="B19">2012b</xref>). For the S4 sample, the relative content of CeH<sub>2.73</sub> is 54.2 wt%, and the relative content of CeO<sub>2</sub> phase is 45.8 wt%, indicating almost the same molar ratio of cerium hydride and oxide when the oxidation time is around 3 min. After the oxidation treatments, the samples were doped into Mg<sub>2</sub>NiH<sub>4</sub> by ball milling.</p>
<fig id="F1" position="float">
<label>Figure 1</label>
<caption><p>XRD images of six groups of CeH<sub>2.73</sub>/CeO<sub>2</sub> composite catalysts obtained by oxidation of CeH<sub>2.73</sub> for different durations: <bold>(A)</bold> 0 min, S1, <bold>(B)</bold> 0.5 min, S2, <bold>(C)</bold> 1.5 min, S3, <bold>(D)</bold> 3 min, S4, <bold>(E)</bold> 10 min, S5, <bold>(F)</bold> 60 min, S6.</p></caption>
<graphic xlink:href="fchem-08-00293-g0001.tif"/>
</fig>
<fig id="F2" position="float">
<label>Figure 2</label>
<caption><p>Relative content of the CeO<sub>2</sub> composites phase as increase of oxidation time.</p></caption>
<graphic xlink:href="fchem-08-00293-g0002.tif"/>
</fig>
<p>In order to understand the morphologies of the CeH<sub>2.73</sub>/CeO<sub>2</sub> composite doped Mg<sub>2</sub>NiH<sub>4</sub>, back scattering scanning electron microscopy (BSEM) was carried out. Because the S1&#x02013;S4 sample will continue to oxidize in the air, the S5 doped Mg<sub>2</sub>NiH<sub>4</sub> sample was selected as the experimental material. The morphologies of the as-prepared CeH<sub>2.73</sub>/CeO<sub>2</sub> composite (S5 sample) and the ball-milled Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5 sample are shown in <xref ref-type="fig" rid="F3">Figure 3</xref>. It could be clearly seen that the particle size of the as-prepared CeH<sub>2.73</sub>/CeO<sub>2</sub> composite is about 200&#x02013;400 nm. After ball milling, the particle size of the CeH<sub>2.73</sub>/CeO<sub>2</sub> composite is greatly reduced to below 30&#x02013;100 nm. <xref ref-type="fig" rid="F3">Figure 3B</xref> shows that the CeH<sub>2.73</sub>/CeO<sub>2</sub> composites, which are brighter particles, are uniformly distributed in the Mg<sub>2</sub>NiH<sub>4</sub> matrix. The homogeneous CeH<sub>2.73</sub>/CeO<sub>2</sub> composites could be beneficial for catalyzing hydrogen storage properties for the Mg-based materials (Hong et al., <xref ref-type="bibr" rid="B11">2009</xref>; Shao et al., <xref ref-type="bibr" rid="B33">2011</xref>; Li et al., <xref ref-type="bibr" rid="B15">2018</xref>).</p>
<fig id="F3" position="float">
<label>Figure 3</label>
<caption><p>BSEM image of <bold>(A)</bold> the as-oxidized CeH<sub>2.73</sub>/CeO<sub>2</sub> composite (S5) and <bold>(B)</bold> the ball-milled Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5 sample.</p></caption>
<graphic xlink:href="fchem-08-00293-g0003.tif"/>
</fig>
</sec>
<sec>
<title>Dehydrogenation of Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; CeH<sub>2.73</sub>/CeO<sub>2</sub> Composites</title>
<p>The decomposition behaviors of the ball-milled Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B;CeH<sub>2.73</sub>/CeO<sub>2</sub> composites are studied by TG-DSC synchronous thermal analyzer as shown in <xref ref-type="fig" rid="F4">Figure 4</xref>. The DSC study of Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; CeH<sub>2.73</sub>/CeO<sub>2</sub> composites are at a heating rate of 20 K/min, showing the dehydrogenation initial temperature of Mg<sub>2</sub>NiH<sub>4</sub> decreases after addition of CeH<sub>2.73</sub>/CeO<sub>2</sub> composites. Among the six sets of catalysts, the S4 sample obtained by oxidation of CeH<sub>2.73</sub> for 3 min, exhibits the highest catalytic effect on reducing the dehydrogenation temperature of Mg<sub>2</sub>NiH<sub>4</sub>. The dehydrogenation temperature is decreased to 267&#x000B0;C, which is about 17&#x000B0;C lower than the that of as-milled Mg<sub>2</sub>NiH<sub>4</sub> (284&#x000B0;C).</p>
<fig id="F4" position="float">
<label>Figure 4</label>
<caption><p><bold>(A)</bold> DSC and <bold>(B)</bold> TG curves of the ball-milled Mg<sub>2</sub>NiH<sub>4</sub>-CeH<sub>2.73</sub>/CeO<sub>2</sub> composites materials, at a heating rate of 20 K/min.</p></caption>
<graphic xlink:href="fchem-08-00293-g0004.tif"/>
</fig>
<p>To further elucidate the dehydrogenation activation energy of the Mg<sub>2</sub>NiH<sub>4</sub>-CeH<sub>2.73</sub>/CeO<sub>2</sub> composites, DSC experiments for the Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; CeH<sub>2.73</sub>/CeO<sub>2</sub> composites at heating rates of 10 K/min and 50 K/min were carried out (results not shown). The activation energy of the dehydrogenation process was calculated by using the Kissinger&#x00027;s method (Kissinger, <xref ref-type="bibr" rid="B14">1957</xref>),</p>
<disp-formula id="E2"><label>(2)</label><mml:math id="M2"><mml:mtable class="eqnarray" columnalign="left"><mml:mtr><mml:mtd><mml:mtext>ln</mml:mtext><mml:mrow><mml:mo stretchy="true">(</mml:mo><mml:mrow><mml:mfrac><mml:mrow><mml:mi>&#x003B2;</mml:mi></mml:mrow><mml:mrow><mml:msubsup><mml:mrow><mml:mi>T</mml:mi></mml:mrow><mml:mrow><mml:mi>m</mml:mi></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup></mml:mrow></mml:mfrac></mml:mrow><mml:mo stretchy="true">)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:msub><mml:mrow><mml:mi>E</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>s</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:mi>R</mml:mi><mml:msub><mml:mrow><mml:mi>T</mml:mi></mml:mrow><mml:mrow><mml:mi>m</mml:mi></mml:mrow></mml:msub></mml:mrow></mml:mfrac><mml:mo>&#x0002B;</mml:mo><mml:mi>C</mml:mi></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<p>where <italic>E</italic><sub><italic>des</italic></sub> is the dehydrogenation activation energy, <italic>T</italic><sub><italic>m</italic></sub>, &#x003B2;, R, and C are the peak temperature, heating rate of DSC experiments, gas constant and another constant, respectively. The relation between <italic>T</italic><sub><italic>m</italic></sub> and &#x003B2; is linearly fitted as plotted in <xref ref-type="fig" rid="F5">Figure 5</xref>, and the activation energy was summarized in <xref ref-type="table" rid="T1">Table 1</xref>. Results show that the S4 sample by oxidation of CeH<sub>2.73</sub> for 3 min exhibits the best catalytic effect on reducing the dehydrogenation activation energy of Mg<sub>2</sub>NiH<sub>4</sub> (from 76.3 kJ/mol to 62.6 kJ/mol). Zhang (Zhang et al., <xref ref-type="bibr" rid="B43">2018</xref>) et al. suggested that alloying Mg<sub>2</sub>Ni with Ti, V, Fe, or Si could reduce the hydrogenation and dehydrogenation activation energies to 60&#x02013;70 kJ/mol. Our study suggests that the CeH<sub>2.73</sub>/CeO<sub>2</sub> composites are also efficient to reduce the dehydrogenation activation energy of Mg<sub>2</sub>NiH<sub>4</sub>.</p>
<fig id="F5" position="float">
<label>Figure 5</label>
<caption><p>Kissinger&#x00027;s Plot of Mg<sub>2</sub>NiH<sub>4</sub>-CeH<sub>2.73</sub>/CeO<sub>2</sub> composite system.</p></caption>
<graphic xlink:href="fchem-08-00293-g0005.tif"/>
</fig>
<table-wrap position="float" id="T1">
<label>Table 1</label>
<caption><p>Initial temperature, peak temperature and activation energy of dehydrogenation for the ball-milled Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; CeH<sub>2.73</sub>/CeO<sub>2</sub> composites (20 K/min).</p></caption>
<table frame="hsides" rules="groups">
<thead><tr>
<th valign="top" align="left"><bold>Materials</bold></th>
<th valign="top" align="center"><bold>Initial temperature (<sup><bold>&#x000B0;</bold></sup>C)</bold></th>
<th valign="top" align="center"><bold>Peak temperature (<sup><bold>&#x000B0;</bold></sup>C)</bold></th>
<th valign="top" align="center"><bold>Activation energy (kJ/mol)</bold></th>
</tr>
</thead>
<tbody>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub></td>
<td valign="top" align="center">284</td>
<td valign="top" align="center">320</td>
<td valign="top" align="center">76.3</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S1</td>
<td valign="top" align="center">283</td>
<td valign="top" align="center">317</td>
<td valign="top" align="center">82.4</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B; S2</td>
<td valign="top" align="center">283</td>
<td valign="top" align="center">323</td>
<td valign="top" align="center">77.8</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B; S3</td>
<td valign="top" align="center">276</td>
<td valign="top" align="center">315</td>
<td valign="top" align="center">66.9</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B; S4</td>
<td valign="top" align="center">267</td>
<td valign="top" align="center">308</td>
<td valign="top" align="center">62.6</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B; S5</td>
<td valign="top" align="center">276</td>
<td valign="top" align="center">317</td>
<td valign="top" align="center">75.7</td>
</tr>
<tr>
<td valign="top" align="left">Mg<sub>2</sub>NiH<sub>4</sub>&#x0002B; S6</td>
<td valign="top" align="center">275</td>
<td valign="top" align="center">314</td>
<td valign="top" align="center">82.3</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Combining XRD and TG-DSC study, it indicates clearly that the initial dehydrogenation temperature and activation energy of Mg<sub>2</sub>NiH<sub>4</sub> are maximally reduced as the cerium hydride and cerium oxide are in the same amount. These results well-accord with our previous finding on the effect of CeH<sub>2.73</sub>/CeO<sub>2</sub> composites on the dehydrogenation properties of MgH<sub>2</sub> (Lin et al., <xref ref-type="bibr" rid="B18">2014</xref>), which means the CeH<sub>2.73</sub>/CeO<sub>2</sub> composite with the same molar ratio of cerium hydride and oxide could be a good catalyst for the dehydrogenation properties of Mg-based hydrogen storage materials, including both MgH<sub>2</sub> and Mg<sub>2</sub>NiH<sub>4</sub>.</p>
</sec>
<sec>
<title>Microstructures of the Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; CeH<sub>2.73</sub>/CeO<sub>2</sub> Composite</title>
<p>The morphology and microstructure of Mg<sub>2</sub>NiH<sub>4</sub> and as-oxidized 10 min CeH<sub>2.73</sub>/CeO<sub>2</sub> composite (S5) are shown in <xref ref-type="fig" rid="F6">Figure 6a</xref>. From the HRTEM images in <xref ref-type="fig" rid="F6">Figure 6b</xref>, it could be found that the composite matrix is Mg<sub>2</sub>NiH<sub>4</sub>, which lattice fringe corresponds to the lattice plane of (111) and (220). Particle sizes of the CeO<sub>2</sub> nanoparticles are in a large range from 50&#x02013;200 to 5&#x02013;10 nm, which have been clearly shown in <xref ref-type="fig" rid="F6">Figures 6a,d</xref>, respectively. Moreover, it could be seen that the <italic>in-situ</italic> generated CeO<sub>2</sub> particles are embedded homogeneously in the Mg<sub>2</sub>NiH<sub>4</sub> matrix after ball milling. The interfaces between Mg<sub>2</sub>NiH<sub>4</sub> and CeO<sub>2</sub> composite, as shown in <xref ref-type="fig" rid="F6">Figures 6c,d</xref>, are contacted closely with each other. The homogeneously distributed catalysts can lead to high catalysis effect, and thus be beneficial for the hydrogenation/dehydrogenation properties of Mg<sub>2</sub>NiH<sub>4</sub>. Because of the too small amount of CeH<sub>2.73</sub>, we could not clarify their microstructures in the TEM study.</p>
<fig id="F6" position="float">
<label>Figure 6</label>
<caption><p><bold>(a)</bold> TEM and <bold>(b&#x02013;d)</bold> HRTEM images of the Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5 composite. <bold>(b)</bold> shows the Mg<sub>2</sub>NiH<sub>4</sub> matrix, <bold>(c)</bold> shows the magnified interface between Mg<sub>2</sub>NiH<sub>4</sub> and CeO<sub>2</sub>, <bold>(d)</bold> shows a CeO<sub>2</sub> particle with size of 5&#x02013;10 nm.</p></caption>
<graphic xlink:href="fchem-08-00293-g0006.tif"/>
</fig>
</sec>
<sec>
<title><italic>In situ</italic> XRD of Dehydrogenation</title>
<p>The phase transition of the Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5 sample during dehydrogenation was further studied by <italic>in situ</italic> XRD. The obtained <italic>in situ</italic> XRD patterns are shown in <xref ref-type="fig" rid="F7">Figure 7</xref>. The XRD pattern of Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5 sample at room temperature contains the diffraction peaks of Mg<sub>2</sub>NiH<sub>4</sub> and CeO<sub>2</sub> because the XRD intensity of CeH<sub>2.73</sub> is too weak. The diffraction peaks of CeO<sub>2</sub> do not obviously change during the whole dehydrogenation process, indicating that the CeO<sub>2</sub> phase might act as a catalyst of Mg<sub>2</sub>NiH<sub>4</sub> dehydrogenation. When the temperature was raised to 250&#x000B0;C, the diffraction peak of Mg<sub>2</sub>NiH<sub>0.3</sub>/Mg<sub>2</sub>Ni phase appears, which means the dehydrogenation of Mg<sub>2</sub>NiH<sub>4</sub> starts. As temperature increases, the intensity of Mg<sub>2</sub>NiH<sub>0.3</sub>/Mg<sub>2</sub>Ni phase gradually enhances, and that of the Mg<sub>2</sub>NiH<sub>4</sub> peaks decreases. As temperature reaches about 330&#x000B0;C, the diffraction peaks of CeO<sub>2</sub> remains unchanged and no MgO is found.</p>
<fig id="F7" position="float">
<label>Figure 7</label>
<caption><p><italic>In situ</italic> XRD patterns of dehydrogenation of the ball-milled Mg<sub>2</sub>NiH<sub>4</sub> &#x0002B; S5.</p></caption>
<graphic xlink:href="fchem-08-00293-g0007.tif"/>
</fig>
<p>The <italic>in situ</italic> XRD patterns are then refined using Jade 6.0, and the relative contents of phases are calculated by the RIR method. At 270&#x000B0;C, the relative content of Mg<sub>2</sub>NiH<sub>0.3</sub> phase is 47.1 wt%, and the relative content of Mg<sub>2</sub>NiH<sub>4</sub> phase is 52.9 wt%. After heating to 290&#x000B0;C, the relative content of the two phases changes rapidly, and the relative content of Mg<sub>2</sub>NiH<sub>0.3</sub> phase increases to 81.8 wt% and Mg<sub>2</sub>NiH<sub>4</sub> The relative content of the phase was reduced to 18.2 wt%. Subsequently, the rate of phase change during the heating process was significantly slowed down. The relative content of Mg<sub>2</sub>NiH<sub>0.3</sub> phase was 89.1 wt% at 400&#x000B0;C, and the relative content of Mg<sub>2</sub>NiH<sub>4</sub> phase reduces to about 10.9 wt%.</p>
</sec>
</sec>
<sec sec-type="conclusions" id="s4">
<title>Conclusion</title>
<p>In summary, CeH<sub>2.73</sub>/CeO<sub>2</sub> composites with different proportions of cerium hydride and oxide are synthesized from pure cerium hydride via oxidation treatments in the air at room temperature. Oxidation time of 3 min leads to formation of CeH<sub>2.73</sub>/CeO<sub>2</sub> composite with the same molar ratio of cerium hydride and oxide, which maximally reduces the initial dehydrogenation temperature and activation energy of Mg<sub>2</sub>NiH<sub>4</sub>. The CeH<sub>2.73</sub>/CeO<sub>2</sub> composite with the same molar ratio is a good catalyst for reducing dehydrogenation temperatures of Mg-based materials.</p>
</sec>
<sec sec-type="data-availability-statement" id="s5">
<title>Data Availability Statement</title>
<p>The raw data supporting the conclusions of this article will be made available by the authors, without undue reservation, to any qualified researcher.</p>
</sec>
<sec id="s6">
<title>Author Contributions</title>
<p>KW and DC: methodology and writing - original draft. KS and TX: methodology and formal analysis. PZ: resources and supervision. WL: supervision and project administration. H-JL: conceptualization, resources, writing - review and editing, supervision, and funding acquisition.</p>
<sec>
<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>
</body>
<back>
<ack><p>We thank Prof. Yunfeng Zhu for providing the Mg<sub>2</sub>NiH<sub>4</sub>. Financial supports from National Natural Science Foundation of China (No. 51601090), Guangdong Basic and Applied Basic Research Foundation (No. 2019A1515011985) and the Fundamental Research Funds for the Central Universities (No. 21619415) are appreciated.</p>
</ack>
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