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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem.</journal-id>
<journal-title>Frontiers in Chemistry</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem.</abbrev-journal-title>
<issn pub-type="epub">2296-2646</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">895198</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2022.895198</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemistry</subject>
<subj-group>
<subject>Mini Review</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Reductive Upgrading of Biomass-Based Levulinic Acid to &#x3b3;-Valerolactone Over Ru-Based Single-Atom Catalysts</article-title>
<alt-title alt-title-type="left-running-head">Meng et al.</alt-title>
<alt-title alt-title-type="right-running-head">Single-Atom Catalysts</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Meng</surname>
<given-names>Ye</given-names>
</name>
<uri xlink:href="https://loop.frontiersin.org/people/1722922/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Jian</surname>
<given-names>Yumei</given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Chen</surname>
<given-names>Dandan</given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Huang</surname>
<given-names>Jinshu</given-names>
</name>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhang</surname>
<given-names>Heng</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1551723/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Li</surname>
<given-names>Hu</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/743130/overview"/>
</contrib>
</contrib-group>
<aff>
<institution>State Key Laboratory Breeding Base of Green Pesticide and Agricultural Bioengineering</institution>, <institution>Key Laboratory of Green Pesticide and Agricultural Bioengineering</institution>, <institution>Ministry of Education</institution>, <institution>State-Local Joint Laboratory for Comprehensive Utilization of Biomass</institution>, <institution>Center for R&#x26;D of Fine Chemicals</institution>, <institution>Guizhou University</institution>, <addr-line>Guiyang</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/789529/overview">Xianxiang Liu</ext-link>, Hunan Normal University, China</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/766206/overview">Ping Zhu</ext-link>, Technical University of Denmark, Denmark</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/635634/overview">Fumin Zhang</ext-link>, Zhejiang Normal University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Heng Zhang, <email>hzhang23@gzu.edu.cn</email>; Hu Li, <email>hli13@gzu.edu.cn</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Catalytic Reactions and Chemistry, a section of the journal Frontiers in Chemistry</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>01</day>
<month>04</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>895198</elocation-id>
<history>
<date date-type="received">
<day>13</day>
<month>03</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>18</day>
<month>03</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Meng, Jian, Chen, Huang, Zhang and Li.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Meng, Jian, Chen, Huang, Zhang and Li</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>With the great adjustment of world industrialization and the continuous improvement of energy consumption requirements, the selective conversion of biomass-based platform molecules to high-value chemicals and biofuels has become one of the most important topics of current research. Catalysis is an essential approach to achieve energy-chemical conversion through the &#x201c;bond breaking-bond formation&#x201d; principle, which opens a broad world for the energy sector. Single-atom catalysts (SACs) are a new frontier in the field of catalysis in recent years, and exciting achievements have been made in biomass energy chemistry. This mini-review focuses on catalytic conversion of biomass-based levulinic acid (LA) to &#x3b3;-valerolactone (GVL) over SACs. The current challenges and future development directions of SACs-mediated catalytic upgrading of biomass-based LA to produce value-added GVL, and the preparation and characterization of SACs are analyzed and summarized, aiming to provide theoretical guidance for further development of this emerging field.</p>
</abstract>
<kwd-group>
<kwd>biomass</kwd>
<kwd>value-added chemicals</kwd>
<kwd>&#x3b3;-Valerolactone</kwd>
<kwd>single-atom catalysts (SACs)</kwd>
<kwd>levulinic acid (LA)</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>Introduction</title>
<p>With advances in research and industrial technology, biomass is now increasingly deemed as one of the most valuable renewable resources that can be converted into a variety of platform molecules, fine chemicals, biofuels, and solid biochars (<xref ref-type="bibr" rid="B28">Li et al., 2015</xref>; <xref ref-type="bibr" rid="B34">Liu et al., 2015</xref>; <xref ref-type="bibr" rid="B29">Li et al., 2017</xref>; <xref ref-type="bibr" rid="B27">Li H et al., 2019</xref>; <xref ref-type="bibr" rid="B26">Li H et al., 2020</xref>; <xref ref-type="bibr" rid="B39">Meng and Li, 2021</xref>; <xref ref-type="bibr" rid="B40">Meng et al., 2022</xref>). &#x3b3;-Valerolactone (GVL) is an important platform molecule and green solvent, which can be used to produce liquid fuels, polymers, intermediates for fine chemicals synthesis, and seasonings (<xref ref-type="bibr" rid="B56">Wright and Palkovits, 2012</xref>; <xref ref-type="bibr" rid="B72">Zhang, 2016</xref>; <xref ref-type="bibr" rid="B63">Ye et al., 2020</xref>). Catalytic hydrogenation of biomass-based levulinic acid (LA) is one of the most effective methods to produce GVL, which has attracted increasing attention in recent years. Homogeneous catalysts can be uniformly dispersed in the catalytic system, which can effectively promote LA hydrogenation to produce GVL. However, due to the high boiling point of GVL (207&#x2013;208&#xb0;C), the product/catalyst separated by distillation is not economical, resulting in a homogeneous system not suitable for the target production of GVL (<xref ref-type="bibr" rid="B72">Zhang, 2016</xref>). Therefore, the large-scale production of GVL almost certainly depends on heterogeneous catalysts, because heterogeneous catalysts are easier to be separated from nonvolatile GVL (<xref ref-type="bibr" rid="B72">Zhang, 2016</xref>; <xref ref-type="bibr" rid="B66">Zhang et al., 2019</xref>).</p>
<p>Metal sites play an important role in the hydrogenation, intramolecular (trans) esterification or dehydration of LA to obtain GVL (<xref ref-type="bibr" rid="B11">Dutta et al., 2019</xref>). Therefore, improving the utilization rate of metal atoms is the key step to reduce the production cost and obtain high efficiency in the whole catalytic process. Single-atom catalysts (SACs) are supported catalysts containing only isolated active centers (<xref ref-type="bibr" rid="B6">Chen et al., 2018</xref>; <xref ref-type="bibr" rid="B21">Ji et al., 2020</xref>), in which a strong interaction or considerable charge transfer between highly dispersed single metal atoms and solid supports. This unique structure allows single-metal atoms of the SACs to have a desired electronic structure and carry specific electrical charges different from those of conventional metal nanoparticles (<xref ref-type="bibr" rid="B10">Ding et al., 2019</xref>; <xref ref-type="bibr" rid="B58">Xue et al., 2022</xref>). It seems one of the most promising materials for rational utilization of metal resources and atomic economy. In theory, all the involved metal atoms could behave as homogeneously as homogeneous catalysts, with an atomic efficiency of 100% (<xref ref-type="bibr" rid="B10">Ding et al., 2019</xref>). SACs have shown excellent catalytic performance, with respect to activity, selectivity, and stability, in catalytic conversion of various biomass-derived feedstocks into target value-added chemicals (<xref ref-type="bibr" rid="B9">De et al., 2022</xref>).</p>
<p>Some excellent reviews have depicted the catalytic production of GVL from biomass-based platform molecule LA in different perspectives (<xref ref-type="bibr" rid="B56">Wright and Palkovits, 2012</xref>; <xref ref-type="bibr" rid="B72">Zhang, 2016</xref>; <xref ref-type="bibr" rid="B63">Ye et al., 2020</xref>), while SACs applied in this field have not been comprehensively discussed till now. This mini-review focuses on the preparation and characterization of SACs and their application in the conversion of LA to GVL. The advantages and disadvantages of SACs, and the catalytic activity of LA over SACs are introduced emphatically.</p>
</sec>
<sec id="s2">
<title>Catalytic Conversion of LA to GVL</title>
<p>LA is an important platform molecule, which can be easily and economically produced from lignocellulose <italic>via</italic> a simple and high-yield acid-catalyzed hydrolysis process (<xref ref-type="fig" rid="F1">Figure 1</xref>) (<xref ref-type="bibr" rid="B47">Rackemann and Doherty, 2011</xref>; <xref ref-type="bibr" rid="B48">Ruppert et al., 2012</xref>; <xref ref-type="bibr" rid="B24">Khan et al., 2018</xref>). The condensation ability of LA is related to hydrogenation, and the generation of GVL may be realized through the hydrogenation of unsaturated carbon-carbon or carbon-oxygen bonds. Therefore, GVL can be synthesized by hydrogenation of LA through following two reaction mechanisms. <italic>1</italic>) Hydrogenation of ketone group of LA to produce unstable intermediate 4-hydroxy-pentanoic acid (HPA), and subsequent dehydration followed by an intramolecular esterification, resulting in the ring closure to yield GVL. <italic>2</italic>) LA is directly dehydrated to produce &#x3b1;-angelica lactone and then hydrogenated to produce GVL (<xref ref-type="bibr" rid="B72">Zhang, 2016</xref>; <xref ref-type="bibr" rid="B11">Dutta et al., 2019</xref>; <xref ref-type="bibr" rid="B63">Ye et al., 2020</xref>). In these two pathways, the hydrogenation step depends on the metal active sites of the catalyst, and the dehydration and cyclization steps are affected by the acidic conditions of the reaction system (<xref ref-type="bibr" rid="B16">Galletti et al., 2012</xref>; <xref ref-type="bibr" rid="B33">Lin et al., 2018</xref>; <xref ref-type="bibr" rid="B3">Cai et al., 2019</xref>). In this regard, improving the utilization rate of metal atoms is a key step to reducing the cost and obtaining high efficiency for the overall catalytic process.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>The schematic of reductive upgrading of biomass-based LA (levulinic acid) to GVL (&#x3b3;-valerolactone) over single-atom catalysts.</p>
</caption>
<graphic xlink:href="fchem-10-895198-g001.tif"/>
</fig>
<p>In recent years, SACs have opened up a vast field of catalysis because of their advantages of high atomic utilization rate, high activity, high stability, and high selectivity. Many different active phases, including noble and non-noble metals, have been tested to catalyze the conversion of LA to GVL (<xref ref-type="bibr" rid="B59">Yan et al., 2013</xref>; <xref ref-type="bibr" rid="B65">Yuan et al., 2013</xref>; <xref ref-type="bibr" rid="B37">Mai et al., 2014</xref>). Ruthenium-based catalysts remain preferred because they are usually the most active and selective catalysts. Using metal-organic framework (MOF) NH<sub>2</sub>-MIL-125 as the precursor, Zhang et al. prepared Ru single-atom catalyst (Ru/TiO<sub>2</sub>@CN) by loading anatase and rutile mixed-phase TiO<sub>2</sub> on nitrogen-doped amorphous carbon through high-temperature calcination (<xref ref-type="bibr" rid="B68">Zhang et al., 2021</xref>). At room temperature, the conversion of LA and selectivity of GVL could reach 100% through hydrogenation and dehydration reactions. The turnover frequency (TOF) of the catalyst was about 35 times higher than that of the industrial Ru/C catalyst, also with superior selectivity toward GVL. In addition, the mechanism study showed that LA is first converted to HPA through the hydrogenation process, and then HPA is rapidly dehydrated to GVL. The stability of 0.85&#xa0;wt% Ru/ZrO<sub>2</sub>@C catalyst prepared by wet impregnation method for the conversion of LA to GVL was significantly improved (<xref ref-type="bibr" rid="B5">Cao et al., 2017</xref>). ZrO<sub>2</sub>@C support, with a nano t-ZrO<sub>2</sub> (3.3&#xa0;nm) structure embedded in amorphous carbon, was obtained by thermal decomposition of UiO-66 material (Zr-MOF). The catalytic performance of Ru/ZrO<sub>2</sub>@C in LA-to-GVL conversion was tested under 10&#xa0;bar H<sub>2</sub> at 150&#xb0;C in an aqueous solution, and compared with that of commercial 5&#xa0;wt% Ru/C. Both catalysts could achieve the full conversion of LA and the quantitative yield of GVL, while 5&#xa0;wt% Ru/C exhibited poor deactivation resistance after the first operation. Inductively coupled plasma optical emission spectroscopy (ICP), X-ray photoelectron spectroscopy (XPS), high-resolution transmission electron microscopy (HR-TEM), aberration-corrected scanning transmission electron microscopy (AC-STEM), temperature-programmed reduction (TPR), and physical adsorption data showed that the rapid deactivation of Ru/C was mainly due to the leaching of Ru and the loss of surface area caused by carbon deposition in micropores (<xref ref-type="bibr" rid="B5">Cao et al., 2017</xref>). In contrast, the self-made Ru/ZrO<sub>2</sub>@C catalyst could be repeatedly recycled in water and high proton aqueous solution, with no significant decrease in catalytic performance. Yang et al. reported a single-atom catalyst (SAC) with a core-shell structure synthesized by core-shell bistability strategy using amine-modified Ru<sub>1</sub>/Fe<sub>3</sub>O<sub>4</sub> as the core and periodic mesoporous organic silicon (PMO) as the shell (<xref ref-type="bibr" rid="B61">Yang et al., 2021</xref>). The Ru atom (0.76&#xa0;wt%) was inserted into the oxygen vacancy of Fe<sub>3</sub>O<sub>4</sub> spheres and stabilized by the amine group of 1,6-hexanediamine. Hollow PMO spheres are hydrophobic, which provides a strong barrier for the core of internal Ru<sub>1</sub>/Fe<sub>3</sub>O<sub>4</sub>, while the mesopores of the shell (4.2&#xa0;nm) together with the cavity enhance the porosity of the catalyst. The conversion rate of LA was up to 99% with the GVL selectivity of up to 98.9%, while the high catalyst stability was still maintained after seven cycles. Regulating the electronic structure of metal catalysts can improve the catalyst performance, but it is very challenging work to regulate the electronic structure of atom-level catalysts. Fortunately, a RuCo single-atom alloy (SAA) catalyst was recently reported, in which precisely tailored electron-rich Ru atoms were confined to Co lattices, and ZIF-67 containing Ru was prepared by pyrolysis (<xref ref-type="bibr" rid="B49">Shao et al., 2021</xref>). The experimental study and calculation simulation showed that its activity was derived from the intrinsic active site of RuCo SAA. It was further illustrated that the electron-rich Ru single atom promoted the adsorption of C&#x3d;O/H<sub>2</sub> and the dissociation of H<sub>2</sub> to H atom, especially beneficial to hydrogenation of the unsaturated &#x3b3;-C of LA, which is the rate-determining step of LA hydrogenation. The more Ru content, the better the reaction activity of RuCo is for LA-to-GVL, and the TOF value could reach 3500&#xa0;h<sup>&#x2212;1</sup>, which is 27 times higher than that of commercial 5&#xa0;wt% Ru/C catalyst. Han et al. also reported a strategy using notched polyoxomtalate (N-POM) to immobilize Ru atoms, which could prevent the aggregation of Ru during pyrolysis and obtain atom-dispersed Ru catalysts anchored onto uniform subsupporter WO<sub>
<italic>x</italic>
</sub> clusters on carbon-nitrogen (Ru<sub>1</sub>@WO<sub>
<italic>x</italic>
</sub>/CN) (<xref ref-type="bibr" rid="B18">Han et al., 2021</xref>). The synthesized Ru<sub>1</sub>@WO<sub>
<italic>x</italic>
</sub>/CN catalyst had good catalytic activity for the hydrogenation of LA to GVL under solvent-free conditions (99% conversion, and 100% selectivity). Properly regulating the active center of the Ru electronic structure can promote the formation and dehydration of HPA intermediates to form GVL. The N-POM strategy is also excellent in preparing a series of atom-dispersed noble metal atoms, which provides an opportunity to find SACs. The stability of the catalyst in polar solvents is also a very important indicator in the catalytic upgrading of the biomass platform molecules. The activity, selectivity, and stability of Ru-based catalysts supported on TiO<sub>2</sub>, ZrO<sub>2</sub>, and C in the conversion of GVL from LA at 30&#xa0;bar H<sub>2</sub> and 150&#xb0;C were investigated (<xref ref-type="bibr" rid="B15">Ftouni et al., 2016</xref>). All the tested catalysts showed good GVL yield in fresh use, but only Ru/ZrO<sub>2</sub> catalyst could maintain high yield in multiple cycles. Surprisingly, the widely used Ru/TiO<sub>2</sub> catalyst showed rapid deactivation after the first catalytic test. The characterization structure showed that the partial deactivation of Ru was attributed to the reduction of Ti support and the coating of Ru nanoparticles, namely the interaction of harmful strong metal supports, rather than the sintering or coking of Ru. In contrast, the Zr support showed no signs of activity reduction after five cycles and had high morphological and structural stability. It is worth noting that in the fresh Ru/ZrO<sub>2</sub> catalyst, even if the Ru loading is 1&#xa0;wt%, Ru can still be completely dispersed on the fresh catalyst, and some Ru nanoparticles can be observed after recycling. Further studies on Ru/ZrO<sub>2</sub> catalysts showed that the dioxane was easily replaced by milder solvents, including GVL itself. Recently, in addition to the SACs constructed with Ru as the active center, which shows excellent catalytic performance in the research system of LA-to-GVL conversion, Ir-based SACs have also come into the vision of researchers. Cao et al. first reported an ultra-stable Ir-based SAC (0.6&#xa0;wt% Ir@ZrO<sub>2</sub>@C) (<xref ref-type="bibr" rid="B4">Cao et al., 2019</xref>). In polar and proton reaction media (pH &#x3d; 3 and pH &#x3d; 1) under harsh conditions (T &#x3d; 155&#xb0;C, P<sub>H2</sub> &#x3d; 40&#xa0;bar), 2.7&#xa0;wt% Ir/C and 0.6&#xa0;wt% Ir/ZrO<sub>2</sub> nanocatalysts showed significant deactivation in recycling experiments, mainly due to the leaching of Ir into acidic reaction media. In contrast, Ir@ZrO<sub>2</sub>@C SAC catalyst showed advantages in selectivity and unprecedented stability toward GVL, which could be recycled continuously seven times (pH &#x3d; 3) and six times (pH &#x3d; 1) in aqueous solution without deactivation and metal sintering or leaching. It is thus can be observed that the <italic>in-situ</italic> synthesis process that limits the entry of a single atom into the metal-organic framework by space proves to be an effective method for preparing acid-resistant solid catalysts.</p>
</sec>
<sec id="s3">
<title>Preparation and Characterization</title>
<p>The catalytic performance of SACs with a good structure and coordination environment is greatly improved, which is helpful for the identification of active sites and the study of catalytic mechanisms at an atomic level. Although SACs have made proud achievements in various catalytic fields such as thermal catalysis, photo-catalysis, electro-catalysis, and photoelectron-catalysis, the preparation of highly dispersed SACs still presents some challenges (<xref ref-type="bibr" rid="B21">Ji et al., 2020</xref>). Here, the synthesis strategies of SACs are summarized for a better understanding of the construction process of SACs to promote the application of SACs for LA-to-GVL (e.g., impregnation, co-precipitation, spatial confinement, coordination, and defect strategy) (<xref ref-type="fig" rid="F1">Figure 1</xref>). As a typical preparation method, the impregnation and co-precipitation methods are of great significance for the preparation of SACs by controlling metal loadings and selecting suitable high surface area supports (<xref ref-type="bibr" rid="B55">Wei et al., 2014</xref>; <xref ref-type="bibr" rid="B71">Zhang X et al., 2018</xref>; <xref ref-type="bibr" rid="B62">Ye et al., 2019</xref>). For example, Ftouni et al. prepared two 1&#xa0;wt% Ru catalysts supported on TiO<sub>2</sub> and monoclinic ZrO<sub>2</sub> by wet impregnation method (<xref ref-type="bibr" rid="B15">Ftouni et al., 2016</xref>). The spatial confinement strategy is to disperse single atoms in space using porous materials such as zeolites (<xref ref-type="bibr" rid="B38">Masoumifard et al., 2018</xref>; <xref ref-type="bibr" rid="B36">Liu L et al., 2020</xref>), metal-organic frameworks (MOFs) (<xref ref-type="bibr" rid="B22">Jiao and Jiang, 2019</xref>), and covalent organic frameworks (COFs) (<xref ref-type="bibr" rid="B64">Yi et al., 2018</xref>; <xref ref-type="bibr" rid="B73">Zhong et al., 2019</xref>). N-POM was used to confine Ru atoms to prepare highly dispersed Ru1@WO<sub>
<italic>x</italic>
</sub>/CN catalysts for producing GVL (<xref ref-type="bibr" rid="B18">Han et al., 2021</xref>). The coordination usually takes the target single atom as the coordination center, which then coordinates with the ligand containing lone pair electrons to form highly dispersed SACs. Ligands commonly used are polymers and polymer-derived materials with abundant heteroatoms (<xref ref-type="bibr" rid="B43">Pan et al., 2018</xref>; <xref ref-type="bibr" rid="B20">He et al., 2019</xref>), MOFs and their derivatives (<xref ref-type="bibr" rid="B67">Zhang et al., 2016</xref>; <xref ref-type="bibr" rid="B60">Yang et al., 2019</xref>), carbon-based materials (<xref ref-type="bibr" rid="B31">Li X et al., 2020</xref>), and C<sub>3</sub>N<sub>4</sub> and graphdiyne (<xref ref-type="bibr" rid="B53">Tan et al., 2017</xref>). The defect strategy is to prepare materials with dispersed defect sites from relatively intact materials, followed by introducing single atoms into the defect sites to form highly dispersed SACs (<xref ref-type="bibr" rid="B1">Beniya and Higashi, 2019</xref>). These materials usually include oxides, hydroxides (<xref ref-type="bibr" rid="B12">Dvorak et al., 2016</xref>; <xref ref-type="bibr" rid="B52">Sun et al., 2019</xref>), graphene, and other deficiency-rich materials (<xref ref-type="bibr" rid="B14">Fei et al., 2019</xref>). The strategy of direct conversion of metal nanoparticles into SACs is to create suitable synthesis conditions to break the metal bond of nanoparticles and form a new bond between the single metal atom and the anchor chain of the support (<xref ref-type="bibr" rid="B41">Moliner et al., 2016</xref>). The &#x201c;top-down&#x201d; strategy is to directly convert metal block materials and metal oxide powers materials into SACs (<xref ref-type="bibr" rid="B46">Qu et al., 2018</xref>). Single-atom alloy strategy is dependent on the dispersion of metal single-atom sites into another metal nanomaterial (<xref ref-type="bibr" rid="B17">Greiner et al., 2018</xref>; <xref ref-type="bibr" rid="B30">Li M et al., 2019</xref>; <xref ref-type="bibr" rid="B49">Shao et al., 2021</xref>). Chemical etching strategies include direct etching of bulk metals and nanoparticles (<xref ref-type="bibr" rid="B45">Qiu et al., 2015</xref>), and indirect template-assisted etching into SACs (<xref ref-type="bibr" rid="B19">Han et al., 2017</xref>; <xref ref-type="bibr" rid="B51">Sun et al., 2018</xref>). Atomic layer deposition (ALD) technology has a good ability to control the deposition of single atom or cluster on the support, so it is one of the powerful methods to accurately prepare ideal single-atom materials (<xref ref-type="bibr" rid="B50">Sun et al., 2013</xref>; <xref ref-type="bibr" rid="B69">Zhang L et al., 2018</xref>). In addition, other preparation strategies that are not commonly used include photochemistry method (<xref ref-type="bibr" rid="B23">Karkas et al., 2016</xref>), electrochemistry method (<xref ref-type="bibr" rid="B70">Zhang et al., 2017</xref>), freezing-assisted method (<xref ref-type="bibr" rid="B54">Wei et al., 2017</xref>), microwave-assisted method (<xref ref-type="bibr" rid="B2">Bilecka and Niederberger, 2010</xref>), ball-milling method (<xref ref-type="bibr" rid="B8">Cui et al., 2016</xref>), ionic-liquid-assisted method (<xref ref-type="bibr" rid="B57">Xi and Sun, 2019</xref>), and so on.</p>
<p>With continuous efforts in recent years, researchers have developed a variety of effective synthesis strategies, as discussed above. In connection to this, how to reveal the isolated reactive centers and overall structural information of SACs is also a very important link. In this mini-review paper, the structural characterization of isolated reactive centers in SACs (especially the Ru-based SACs for LA-to-GVL conversion) was disclosed by using advanced technologies such as electron microscopy and spectroscopy (<xref ref-type="fig" rid="F1">Figure 1</xref>) (<xref ref-type="bibr" rid="B58">Xue et al., 2022</xref>). Transmission electron microscopy (TEM) with the atomic resolution has been developed as an effective method to study the detailed structural information of isolated reaction centers and their interactions with supports. The additional energy dispersive X-ray (EDX) detector of scanning transmission electron microscopy (STEM) can further provide element mappings, clarify the atomic dispersion of metal atoms on supports, and further evaluate the dispersion degree of single atoms. In addition, aberration-corrected high-angle annular dark-field scanning transmission electron microscopy (AC-HAADF-STEM) can easily confirm the existence of isolated reaction centers on the supports, as long as the metal atoms exhibit a much higher atomic number than the supporting elements (<xref ref-type="bibr" rid="B25">Lee et al., 2019</xref>; <xref ref-type="bibr" rid="B7">Chen et al., 2020</xref>). Although electron microscope images provide effective information to identify the structural information of the catalysts, it should be noted that there are some limitations in its application in structural characterization. Due to the limited electron penetration ability of microscopic technology, it is difficult to observe the isolated metal atoms modified in the bulk phase or cavities, rather than the surface structure. In addition, the electron microscope can only image the local structure, and cannot provide the overall structure information of the SACs (<xref ref-type="bibr" rid="B35">Liu J et al., 2020</xref>). Therefore, some additional spectral methods are needed to provide supplementary data and support the existence of isolated metal sites in SACs. For example, X-ray photoelectron spectroscopy (XPS) is widely used to reveal the surface valence structure of SACs. Compared with pure metal, the obvious change of binding energy may explain the oxidation state of isolated metal atoms and exclude the existence of nanoparticles (<xref ref-type="bibr" rid="B18">Han et al., 2021</xref>; <xref ref-type="bibr" rid="B49">Shao et al., 2021</xref>). In addition, X-ray absorption spectroscopy (XAS) is one of the most commonly used and powerful tools to characterize SACs, including X-ray absorption near-edge structure (XANES) spectroscopy and the extended X-ray absorption fine structure (EXAFS) (<xref ref-type="bibr" rid="B42">Pan et al., 2019</xref>; <xref ref-type="bibr" rid="B44">Qiao et al., 2022</xref>). XANES can provide local electronic state information of the detected elements, while EXAFS can provide a high-resolution coordination environment and local geometry details of isolated metal sites. As site-specific characterization techniques, Fourier transform infrared spectroscopy (FTIR) and Raman spectroscopy are also widely used to evaluate the existence of isolated metal sites (<xref ref-type="bibr" rid="B32">Li et al., 2016</xref>; <xref ref-type="bibr" rid="B13">Fang et al., 2018</xref>), because they have obvious displacement relative to clusters or nanoparticles. The theoretical calculation also is one of the most important research methods (<xref ref-type="bibr" rid="B18">Han et al., 2021</xref>), state density, wave function &#x7c;&#x3a8;&#x7c;<sup>2</sup>, and modeling can verify each other with electron microscopy and spectroscopy. Taking together, the above characterization methods are conducive to revealing the role of SACs in the LA-to-GVL conversion system, which provides an effective basis for the visualization of the system in the future.</p>
</sec>
<sec id="s4">
<title>Conclusion and Perspectives</title>
<p>The over-exploitation of fossil resources has caused serious social and environmental problems, and the high-value conversion of renewable resources has gradually become a global research upsurge. This mini-review focuses on the conversion of LA to GVL over SACs, and also extends to the involved reaction mechanism (e.g., hydrogenation, cyclization, and dehydration), synthesis methods (e.g., impregnation, co-precipitation, spatial confinement, self-assembling, and defect sites), and structural characterization methods (e.g., electron microscopy, and spectroscopy) of SACs. Both SACs and traditional heterogeneous catalysts show high activity and selectivity in the catalytic conversion of LA to GVL. However, traditional heterogeneous catalysts tend to lose activity after reaction, while SACs show excellent stability. At present, the SACs in this field mainly use Ru species as the active sites. Therefore, the development of SCAs with cheap transition metals as the active sites is one of the major tasks for LA-to-GVL, which is conducive to reducing the catalyst cost and promoting the commercialization of this field. In addition, the development of cleaner and more sustainable catalytic systems for LA-to-GVL is also a hot topic for future research, such as single-atom electro- and photocatalytic systems. In conclusion, SACs have great potential in large-scale catalytic production of GVL from LA. Further development of facile preparation methods of SACs and eco-friendly catalytic processes, as well as elucidation of the single-atom active center is challenging but an unprecedented opportunity to promote the industrialization of SACs for biomass valorization.</p>
</sec>
</body>
<back>
<sec id="s5">
<title>Author Contributions</title>
<p>YM organized and prepared this manuscript; YJ made preliminary revisions to the manuscript; DC and JH participated in literature collection and collation; HZ and HL supervised and contributed to reviewing the manuscript.</p>
</sec>
<sec id="s6">
<title>Funding</title>
<p>The study was funded by the National Natural Science Foundation of China (21908033), Guizhou Provincial S&#x0026;T Project (ZK(2022)011, ZK(2022)141), the Fok Ying-Tong Education Foundation (161030), and GZU (Guizhou University) Found for Cultivation ((2020)73).</p>
</sec>
<sec sec-type="COI-statement" id="s7">
<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="s8">
<title>Publisher&#x2019;s Note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
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