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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">1106426</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2022.1106426</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>Advancement in utilization of magnetic catalysts for production of sustainable biofuels</article-title>
<alt-title alt-title-type="left-running-head">Zhang 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.2022.1106426">10.3389/fchem.2022.1106426</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhang</surname>
<given-names>Yutao</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1985947/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Li</surname>
<given-names>Weihua</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Wang</surname>
<given-names>Jialu</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1024046/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Jin</surname>
<given-names>Jiaxing</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Zhang</surname>
<given-names>Yixi</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Cheng</surname>
<given-names>Jingsong</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhang</surname>
<given-names>Qiuyun</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/766393/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>Engineering Technology Center of Control and Remediation of Soil Contamination of Guizhou Science and Technology Department</institution>, <institution>Anshun University</institution>, <addr-line>Anshun</addr-line>, <addr-line>Guizhou</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>School of Chemistry and Chemical Engineering</institution>, <institution>Anshun University</institution>, <addr-line>Anshun</addr-line>, <addr-line>Guizhou</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>College Rural Revitalization Research Center of Guizhou</institution>, <institution>Anshun University</institution>, <addr-line>Anshun</addr-line>, <addr-line>Guizhou</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/743130/overview">Hu Li</ext-link>, Guizhou 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/995005/overview">Jian He</ext-link>, Jishou University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1312687/overview">Hu Pan</ext-link>, Jiaxing University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Yutao Zhang, <email>zyt0516@126.com</email>; Qiuyun Zhang, <email>sci_qyzhang@126.com</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Green and Sustainable Chemistry, a section of the journal Frontiers in Chemistry</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>10</day>
<month>01</month>
<year>2023</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>1106426</elocation-id>
<history>
<date date-type="received">
<day>23</day>
<month>11</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>06</day>
<month>12</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2023 Zhang, Li, Wang, Jin, Zhang, Cheng and Zhang.</copyright-statement>
<copyright-year>2023</copyright-year>
<copyright-holder>Zhang, Li, Wang, Jin, Zhang, Cheng and Zhang</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>In this study, we summarize recent advances in the synthesis of magnetic catalysts utilized for biodiesel production, particularly focusing on the physicochemical properties, activity, and reusability of magnetic mixed metal oxides, supported magnetic catalysts, ionic acid-functionalized magnetic catalysts, heteropolyacid-based magnetic catalysts, and metal&#x2013;organic framework-based magnetic catalysts. The prevailing reaction conditions in the production of biodiesel are also discussed. Lastly, the current limitations and challenges for future research needs in the magnetic catalyst field are presented.</p>
</abstract>
<kwd-group>
<kwd>magnetic</kwd>
<kwd>heterogeneous catalysis</kwd>
<kwd>reusability</kwd>
<kwd>esterification</kwd>
<kwd>transesterification</kwd>
<kwd>biodiesel</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>With the rapidly expanding economy and high energy demand, the over-consumption of fossil fuels and fossil fuel usage has led to severe effects on the environment (e.g., global warming), creating wide attention among researchers (<xref ref-type="bibr" rid="B36">Li et al., 2023</xref>; <xref ref-type="bibr" rid="B45">Pan et al., 2022a</xref>; <xref ref-type="bibr" rid="B79">Zhang et al., 2022a</xref>; <xref ref-type="bibr" rid="B46">Pan et al., 2022b</xref>). Thus, seeking a sustainable energy resource is a high priority. To date, various types of biofuels, such as biodiesel, bioethanol, and aviation biofuels, have been considered as fossil fuel replacements. Among them, biodiesel (fatty acid alkyl ester, FAME) has been getting significant interest as an alternative fuel because of its safety, biodegradability, and carbon-neutrality (<xref ref-type="bibr" rid="B77">Zhang et al., 2020</xref>; <xref ref-type="bibr" rid="B26">Hoang et al., 2021</xref>). Currently, biodiesel is synthesized from free fatty acids (FFAs) and various oils mixed with short-chain alcohols, using homogeneous, heterogeneous, or enzymatic catalysts to promote the reaction (<xref ref-type="fig" rid="F1">Figure 1</xref>) (<xref ref-type="bibr" rid="B81">Zhang et al., 2023</xref>). However, the homogeneous catalysis system exhibits numerous disadvantages, such as the fact that homogeneous catalysts (e.g., NaOH, KOH, H<sub>2</sub>SO<sub>4</sub>, etc.) are non-recyclable and cause pollution (<xref ref-type="bibr" rid="B78">Zhang et al., 2021</xref>; <xref ref-type="bibr" rid="B37">Liu et al., 2022</xref>). In contrast, heterogeneous catalysts (e.g., zeolites, heteropolyacids, metal oxides, etc.) have attracted growing interest owing to their low pollution and easy recovery (<xref ref-type="bibr" rid="B59">Woo et al., 2021</xref>; <xref ref-type="bibr" rid="B80">Zhang et al., 2022b</xref>; <xref ref-type="bibr" rid="B44">Paiva et al., 2022</xref>; <xref ref-type="bibr" rid="B54">Ul Islam et al., 2022</xref>). However, high-efficiency separation of the catalyst from the liquid phase and reduction of catalyst loss remain challenges. The use of magnetic separation techniques is an interesting approach to solving these problems (<xref ref-type="bibr" rid="B12">Chen et al., 2022</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Classification of catalysts for biodiesel production.</p>
</caption>
<graphic xlink:href="fchem-10-1106426-g001.tif"/>
</fig>
<p>In recent times, magnetic solid acid/base catalysts have been widely applied for esterification and transesterification reactions as compared to other heterogeneous catalysts because they are environmentally friendly and cheap, and their highly magnetic nature allows efficient separation with an external magnetic field (<xref ref-type="bibr" rid="B52">Shylesh et al., 2010</xref>; <xref ref-type="bibr" rid="B76">Zhang et al., 2014</xref>). The present work reviews recent applications of different types of magnetic catalysts and their functionalized magnetic composites employed in biodiesel production, including magnetic mixed metal oxides, supported magnetic catalysts, ionic acid-functionalized magnetic catalysts, heteropolyacid-based magnetic catalysts, and MOF-based magnetic catalysts, among others. The physicochemical properties, activity, and reusability of these magnetic catalysts are evaluated and discussed. Lastly, a brief conclusion and summary on the outlook for designing magnetic catalysts with high catalytic activity is presented.</p>
</sec>
<sec id="s2">
<title>2 Magnetic catalysts</title>
<p>In general, Fe-, Co-, and Ni-based catalysts exhibit permanent magnetism and can be used as magnetic materials; Fe-based catalysts have been especially widely studied. According to their characteristics, magnetic catalysts can be roughly classified into five types, namely, magnetic mixed metal oxides, supported magnetic catalysts, ionic acid-functionalized magnetic catalysts, heteropolyacid-based magnetic catalysts, and MOF-based magnetic catalysts.</p>
<sec id="s2-1">
<title>2.1 Magnetic mixed metal oxides</title>
<p>Recently, spinel ferrites, MFe<sub>2</sub>O<sub>4</sub> (where <italic>M</italic> indicates a transition metal atom of Cu, Zn, Mo, Co, or Mn) have been widely researched for applications as heterogeneous catalysts due to their thermal stability and ease of separation by using an external magnet. <xref ref-type="bibr" rid="B38">Luadthong et al. (2016)</xref> investigated the transesterification of palm oil using a copper ferrite spinel oxide (CuFe<sub>2</sub>O<sub>4</sub>) catalyst. The characterization results revealed that the major active species of CuFe<sub>2</sub>O<sub>4</sub> were the Cu<sup>2&#x2b;</sup> and Fe<sup>2&#x2b;</sup>. Optimal reaction conditions of 220&#xb0;C, 1&#xa0;g of catalyst, a methanol:oil molar ratio of 1:18, and a high FAME content of &#x3e;90% were determined. A similar study was conducted by <xref ref-type="bibr" rid="B3">Ali et al. (2020)</xref>, in which a cuprospinel CuFe<sub>2</sub>O<sub>4</sub> catalyst was used for the transesterification of waste frying oil with methanol at 60&#xb0;C, giving a 90.24% yield. Kinetic results showed that the transesterification reaction followed pseudo-first-order kinetics, and the activation energy was found to be 37.64&#xa0;kJ/mol. <xref ref-type="bibr" rid="B4">AlKahlaway et al. (2021)</xref> prepared ferric molybdate, Fe<sub>2</sub>(MoO<sub>4</sub>)<sub>3</sub>, nanoparticles for biodiesel synthesis and the catalytic conversion of oleic acid was 90.5%.</p>
<p>In addition, some magnetic mixed metal oxides including MoO<sub>3</sub>/SrFe<sub>2</sub>O<sub>4</sub> (<xref ref-type="bibr" rid="B21">Gon&#xe7;alves et al., 2021</xref>), MnFe<sub>2</sub>O<sub>4</sub>/GO (<xref ref-type="bibr" rid="B7">Bai et al., 2021</xref>), MgFe<sub>2</sub>O<sub>4</sub>@OA@CRL (<xref ref-type="bibr" rid="B27">Iuliano et al., 2020</xref>), NaFeTiO<sub>4</sub>/Fe<sub>2</sub>O<sub>3</sub>&#x2013;FeTiO<sub>3</sub> (<xref ref-type="bibr" rid="B23">Gutierrez-Lopez et al., 2021</xref>), Mg<sup>2&#x2b;</sup>-doped ZnFe<sub>2</sub>O<sub>4</sub> (<xref ref-type="bibr" rid="B6">Ashok et al., 2021</xref>), and waste chalk/CoFe<sub>2</sub>O<sub>4</sub>/K<sub>2</sub>CO<sub>3</sub> (<xref ref-type="bibr" rid="B19">Foroutan et al., 2022</xref>) have been explored for their application largely due to their unique magnetism. <xref ref-type="bibr" rid="B21">Gon&#xe7;alves et al. (2021)</xref> prepared a magnetic catalyst, MoO<sub>3</sub>/SrFe<sub>2</sub>O<sub>4</sub>, for the transesterification of waste cooking oil, and results confirmed the success of MoO<sub>3</sub> anchorage of the SrFe<sub>2</sub>O<sub>4</sub> material. The activity test showed that a biodiesel yield of 95.4% was obtained in 4&#xa0;h at 164&#xb0;C. The MoO<sub>3</sub>/SrFe<sub>2</sub>O<sub>4</sub> catalyst could be easily separated by a permanent magnet and showed high stability with a yield of 84% after five cycles. <xref ref-type="bibr" rid="B7">Bai et al. (2021)</xref> investigated the catalytic performance of a MnFe<sub>2</sub>O<sub>4</sub>/graphene oxide catalyst for biodiesel production from waste edible oil. The MnFe<sub>2</sub>O<sub>4</sub>/graphene oxide catalyst had a high basicity of 3978.6&#xa0;mmol/g, and in transesterification reactions, a high biodiesel yield of 96.47% was achieved. Moreover, the physical properties of the synthetic biodiesel were within the ASTM D6751 and EN 14214 standard range. A K<sub>2</sub>CO<sub>3</sub> modification to the waste chalk/CoFe<sub>2</sub>O<sub>4</sub> was developed by <xref ref-type="bibr" rid="B19">Foroutan et al. (2022)</xref>, and the characterization results showed that the composite catalyst had a lower surface area due to the introduction of K<sub>2</sub>CO<sub>3</sub>. The highest biodiesel yield of 98.87% was obtained under optimized conditions, and the activation energy and frequency factor of the reaction system was found to be 11.8&#xa0;kJ/mol and 0.78 min<sup>&#x2212;1</sup>, respectively.</p>
<p>
<xref ref-type="bibr" rid="B48">Rezania et al. (2021)</xref> synthesized a heterogeneous magnetic MGO@MMO nanocatalyst via the ultra-sonication procedure for biodiesel production from waste frying oil. From the results, a high biodiesel yield of 94% was achieved with a 1.5&#xa0;h reaction at 60&#xb0;C; the catalyst could be separated and recycled four times, achieving an 86% biodiesel yield. However, after the eighth cycle, the biodiesel yield decreased significantly, possibly due to leaching of the active components or active site blocking. In a more recent study by <xref ref-type="bibr" rid="B24">Hanif et al. (2022)</xref>, a magnetic Fe/SnO nanocatalyst supported on feldspar was synthesized for the transesterification of various non-edible oils. The magnetic catalyst exhibited a high catalytic activity with more than 97% yield for all the tested non-edible oils. A highly active bifunctional Na&#x2013;Fe&#x2013;Ca nanocatalyst was developed by <xref ref-type="bibr" rid="B57">Wang et al. (2022)</xref>. The catalytic activity of the magnetic Na&#x2013;Fe&#x2013;Ca nanocatalyst in biodiesel production was evaluated at low temperatures. Interestingly, with a 500&#xb0;C calcination temperature, the catalyst reached a 95.84% biodiesel yield with 16 cycles via magnetic separation. In conclusion, magnetic mixed metal oxides have been used successfully as acid/base catalysts or supports in the catalysis industry, and the design and composition of cheap, magnetic composite nanocatalysts is a highly desirable goal in the future.</p>
</sec>
<sec id="s2-2">
<title>2.2 Supported magnetic catalysts</title>
<p>Apart from magnetic spinel ferrite catalysts, supported magnetic acid/base catalysts have also attracted significant interest for biofuels production in recent years. At present, Fe<sub>3</sub>O<sub>4</sub> magnetic particles do not commonly exhibit good catalytic activity, although they are easily separated and reused. Magnetic Fe<sub>3</sub>O<sub>4</sub> is often used as a carrier, and the catalytic system is cost-effective and environment-friendly. <xref ref-type="bibr" rid="B28">Joorasty et al. (2021)</xref> prepared NaOH/clinoptilolite&#x2013;Fe<sub>3</sub>O<sub>4</sub> for the transesterification reaction of <italic>Amygdalus scoparia</italic> oil, and the highest biodiesel yield by the catalyst was 91%. The kinetics of NaOH/clinoptilolite&#x2013;Fe<sub>3</sub>O<sub>4</sub>-catalyzed transesterification were also explored, and the activation energy was determined to be 9.21&#xa0;kJ/mol. <xref ref-type="bibr" rid="B64">Xia et al. (2022)</xref> prepared bifunctional Co-doped Fe<sub>2</sub>O<sub>3</sub>&#x2013;CaO nanocatalysts (Co/Fe<sub>2</sub>O<sub>3</sub>&#x2013;CaO) and studied their catalytic performance in soybean oil transesterification. It was reported that the Co/Fe<sub>2</sub>O<sub>3</sub>&#x2013;CaO catalyst had good ferromagnetism (26.2&#xa0;emu/g) after the Co doping, and could be efficiently separated. In another study by <xref ref-type="bibr" rid="B43">Nizam et al. (2022)</xref>, magnetic Fe<sub>2</sub>O<sub>3</sub> immobilized on microporous molecular sieves (Fe<sub>2</sub>O<sub>3</sub>/MS) was developed using a plant extract-mediated method. In the catalytic reaction, the Fe<sub>2</sub>O<sub>3</sub>/MS catalyst exhibited excellent applicability in the esterification, transesterification, and photodegradation reactions. <xref ref-type="bibr" rid="B39">Mohamed et al. (2020)</xref> and <xref ref-type="bibr" rid="B40">Mohamed and El-Faramawy. (2021)</xref> used a newly developed <italic>&#x3b1;</italic>-Fe<sub>2</sub>O<sub>3</sub>/AlOOH(&#x3b3;-Al<sub>2</sub>O<sub>3</sub>) nanocatalyst to produce biodiesel from waste oil. The <italic>&#x3b1;</italic>-Fe<sub>2</sub>O<sub>3</sub>/AlOOH(&#x3b3;-Al<sub>2</sub>O<sub>3</sub>) catalyst presented the highest FAME yield and recyclability due to its large surface area of 323.3&#xa0;m<sup>2</sup>/g, high acidity of 0.45&#xa0;mmol/g, and exposed active site planes. Furthermore, thermal analyses showed that the catalytic reaction system was endothermic.</p>
<p>In a study conducted by <xref ref-type="bibr" rid="B10">Changmai et al. (2021a)</xref>, a recoverable Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>&#x2013;SO<sub>3</sub>H core@shell magnetic catalyst was successfully prepared by a stepwise co-precipitation, coating, and functionalization method. The obtained magnetic Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>-SO<sub>3</sub>H had a magnetic saturation of 30.94&#xa0;emu/g, a relatively large surface area of 32.88&#xa0;m<sup>2</sup>/g, and a high acidity of 0.76&#xa0;mmol/g. The Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>&#x2013;SO<sub>3</sub>H catalyst achieved a high conversion of <italic>Jatropha curcas</italic> oil of 98 &#xb1; 1% under optimal reaction conditions. <xref ref-type="bibr" rid="B41">Mohammadpour and Safaei (2022</xref>) developed a novel sulfonated carbon-coated magnetic catalyst (Fe<sub>3</sub>O<sub>4</sub>@C@OSO<sub>3</sub>H), which was used for the Pechmann condensation of phenol derivatives and &#x3b2;-ketoesters. The resulting yield values were as high as 98%, and the catalyst could be reused fifteen times with no significant loss in activity. <xref ref-type="table" rid="T1">Table 1</xref> shows a summary of supported magnetic catalysts utilized for the synthesis of biodiesel.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Recent findings on green biodiesel production using supported magnetic catalysts.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Entry</th>
<th align="center">Feedstock/oil</th>
<th align="center">Catalyst</th>
<th align="center">Conditions (time, temperature, catalyst amount, and molar ratio of acid or oil to alcohol</th>
<th align="center">Yield (<italic>Y</italic>/%) or conversion(<italic>C</italic>/%)</th>
<th align="center">Times catalyst reused; yield</th>
<th align="center">
<italic>E</italic>a (KJ/mol)</th>
<th align="center">Reference</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">1</td>
<td align="center">Jatropha oil &#x2b; methanol</td>
<td align="center">CaSO<sub>4</sub>/Fe<sub>2</sub>O<sub>3</sub>&#x2013;SiO<sub>2</sub>
</td>
<td align="center">4&#xa0;h, 120&#xb0;C, 12%, 1:9</td>
<td align="center">Y &#x3d; 94%</td>
<td align="center">9 cycles; Y &#x3d; 83%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B53">Teo et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="center">2</td>
<td align="center">Rapeseed oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>-CeO<sub>2</sub>-25K</td>
<td align="center">2&#xa0;h, 65&#xb0;C, 4.5%, 1:7</td>
<td align="center">Y &#x3d; 96.13%</td>
<td align="center">5 cycles; Y &#x3d; 80.94%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B5">Ambat et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="center">3</td>
<td align="center">
<italic>Amygdalus scoparia</italic> oil &#x2b; methanol</td>
<td align="center">NaOH/clinoptilolite&#x2013;Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">2.5&#xa0;h, 65&#xb0;C, 0.5%, 1:10.43</td>
<td align="center">Y &#x3d; 91%</td>
<td align="center">4 cycles; Y &#x3d; 82%</td>
<td align="center">9.21</td>
<td align="center">
<xref ref-type="bibr" rid="B28">Joorasty et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="center">4</td>
<td align="center">Fat &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>/Cs<sub>2</sub>O</td>
<td align="center">5&#xa0;h, 65&#xb0;C, 7%, 1:21</td>
<td align="center">Y &#x3d; 97.1%</td>
<td align="center">9 cycles; Y &#x3d; 78%</td>
<td align="center">43.8</td>
<td align="center">
<xref ref-type="bibr" rid="B8">Booramurthy et al. (2020)</xref>
</td>
</tr>
<tr>
<td align="center">5</td>
<td align="center">
<italic>Pongamia pinnata</italic> raw oil &#x2b; methanol</td>
<td align="center">CES-Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">2&#xa0;h, 65&#xb0;C, 2%, 1:12</td>
<td align="center">Y &#x3d; 98%</td>
<td align="center">7 cycles; Y &#x3d; 98%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B14">Chingakham et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="center">6</td>
<td align="center">
<italic>Chlorella vulgaris</italic> oil &#x2b; ethanol</td>
<td align="center">KF/KOH-Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">6&#xa0;h, 25&#xb0;C, 1.5%, 1:6</td>
<td align="center">Y &#x3d; 80%</td>
<td align="center">Not reported</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B17">Farrokheh et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="center">7</td>
<td align="center">Used cooking oil &#x2b; methanol</td>
<td align="center">CaO-ZSM-5/Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">4&#xa0;h, 65&#xb0;C, 3%, 1:5</td>
<td align="center">C &#x3d; 83%</td>
<td align="center">4 cycles; Y &#x3d; 85%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B32">Lani and Nagi, (2022)</xref>
</td>
</tr>
<tr>
<td align="center">8</td>
<td align="center">Soybean oil &#x2b; methanol</td>
<td align="center">Co/Fe<sub>2</sub>O<sub>3</sub>-CaO</td>
<td align="center">2.5&#xa0;h, 70&#xb0;C, 3%, 1:16</td>
<td align="center">Y &#x3d; 98.2%</td>
<td align="center">5 cycles; Y &#x3d; 78.8%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B64">Xia et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">9</td>
<td align="center">Waste cooking oil &#x2b; methanol</td>
<td align="center">KOH/Fe<sub>3</sub>O<sub>4</sub>@MCM-41</td>
<td align="center">3&#xa0;h, 65&#xb0;C, 8%, 1:40</td>
<td align="center">Y &#x3d; 93.95%</td>
<td align="center">3 cycles; C&#x3e;80%</td>
<td align="center">115.79</td>
<td align="center">
<xref ref-type="bibr" rid="B30">Khakestarian et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">10</td>
<td align="center">Soybean oil &#x2b; methanol</td>
<td align="center">Na<sub>2</sub>CO<sub>3</sub>&#x22c5;H<sub>2</sub>O@BFD</td>
<td align="center">2&#xa0;h, 65&#xb0;C, 7%, 1:15</td>
<td align="center">Y &#x3d; 100.0%</td>
<td align="center">12 cycles; Y &#x3d; 92.56%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B58">Wang et al. (2022b)</xref>
</td>
</tr>
<tr>
<td align="center">11</td>
<td align="center">Sunflower oil &#x2b; methanol</td>
<td align="center">Fe<sub>2</sub>O<sub>3</sub>/MS</td>
<td align="center">4&#xa0;h, 70&#xb0;C, 0.03 g, 1:10(volume)</td>
<td align="center">Y &#x3d; 84.5%</td>
<td align="center">Not reported</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B43">Nizam et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">12</td>
<td align="center">Glyceryl trioleate &#x2b; methanol</td>
<td align="center">Sulfamic acid-functionalized Fe/Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">20&#xa0;h, 100&#xb0;C, &#x2014;, &#x2014;</td>
<td align="center">C &#x3d; 100%</td>
<td align="center">5 cycles; C &#x3d; 95%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B56">Wang et al. (2015)</xref>
</td>
</tr>
<tr>
<td align="center">13</td>
<td align="center">Adipic acid &#x2b; <italic>n</italic>-butanol</td>
<td align="center">Sulfonated magnetic SiO<sub>2</sub>
</td>
<td align="center">4&#xa0;h, 105&#xb0;C, 2.95%, 1:3</td>
<td align="center">C &#x3d; 99%</td>
<td align="center">6 cycles; C &#x3d; 85.61%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B29">Ke et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="center">14</td>
<td align="center">Acetic acid &#x2b; methanol</td>
<td align="center">Fe<sub>2</sub>O<sub>3</sub>&#x2013;MCM-48&#x2013;SO<sub>4</sub>
</td>
<td align="center">4.5&#xa0;h, 60&#xb0;C, 15&#xa0;g/L, 1:10</td>
<td align="center">C &#x3d; 90%</td>
<td align="center">5 cycles; C &#x3d; 44.4%</td>
<td align="center">29.077</td>
<td align="center">
<xref ref-type="bibr" rid="B51">Sharma et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="center">15</td>
<td align="center">Waste cooking oil &#x2b; methanol</td>
<td align="center">CSPA@Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="center">3&#xa0;h, 65&#xb0;C, 6%, 1:6</td>
<td align="center">Y &#x3d; 98%</td>
<td align="center">9 cycles; Y &#x3d; 91%</td>
<td align="center">34.41</td>
<td align="center">
<xref ref-type="bibr" rid="B11">Changmai et al. (2021b)</xref>
</td>
</tr>
<tr>
<td align="center">16</td>
<td align="center">Oleic acid &#x2b; methanol</td>
<td align="center">EFB-MCC/&#x3b3;-Fe<sub>2</sub>O<sub>3</sub>
</td>
<td align="center">2&#xa0;h, 60&#xb0;C, 9%, 1:12</td>
<td align="center">Y &#x3d; 92.1%</td>
<td align="center">5 cycles; Y &#x3d; 77.6%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B31">Krishnan et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">17</td>
<td align="center">Yeast oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>-CHO</td>
<td align="center">10&#xa0;h, 55&#xb0;C, 2.5 g, &#x2014;</td>
<td align="center">Y &#x3d; 98.12%</td>
<td align="center">10 cycles; Y &#x3d; 90%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B9">Cao et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="center">18</td>
<td align="center">Cottonseed oil &#x2b; methanol</td>
<td align="center">&#x3b1;-Fe<sub>2</sub>O<sub>3</sub>/AlOOH(&#x3b3;-Al<sub>2</sub>O<sub>3</sub>)</td>
<td align="center">3&#xa0;h, 60&#xb0;C, 3%, 1:6</td>
<td align="center">Y &#x3d; 100%</td>
<td align="center">3 cycles; Y &#x3d; 95%</td>
<td align="center">57.4</td>
<td align="center">
<xref ref-type="bibr" rid="B39">Mohamed et al. (2020)</xref>
</td>
</tr>
<tr>
<td align="center">19</td>
<td align="center">Waste cooking oil &#x2b; methanol</td>
<td align="center">&#x3b1;-Fe<sub>2</sub>O<sub>3</sub>/AlOOH</td>
<td align="center">3&#xa0;h, 60&#xb0;C, 3%, 1:6</td>
<td align="center">Y &#x3d; 95%</td>
<td align="center">4 cycles; Y &#x3d; 91.3%</td>
<td align="center">51.54</td>
<td align="center">
<xref ref-type="bibr" rid="B40">Mohamed and El-Faramawy, (2021)</xref>
</td>
</tr>
<tr>
<td align="center">20</td>
<td align="center">Soybean oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>-poly(GMA-co-MAA)@ lipase</td>
<td align="center">60&#xa0;h, 40&#xb0;C, 20%, 1:4</td>
<td align="center">Y &#x3d; 92.8%</td>
<td align="center">5 cycles; Y &#x3d; 79.4%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B67">Xie and Huang, (2020)</xref>
</td>
</tr>
<tr>
<td align="center">21</td>
<td align="center">Soybean oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>-poly(AGE-DVB-GMA)</td>
<td align="center">8&#xa0;h, 65&#xb0;C, 7%, 1:20</td>
<td align="center">Y &#x3d; 92.6%</td>
<td align="center">4 cycles; no significant decrease</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B72">Xie et al. (2021a)</xref>
</td>
</tr>
<tr>
<td align="center">22</td>
<td align="center">Jatropha oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>&#x2013;SO<sub>3</sub>H</td>
<td align="center">3.5&#xa0;h, 80&#xb0;C, 8%, 1:9</td>
<td align="center">C &#x3d; 98%</td>
<td align="center">9 cycles; C &#x3d; 81%</td>
<td align="center">37.0</td>
<td align="center">
<xref ref-type="bibr" rid="B10">Changmai, et al. (2021a)</xref>
</td>
</tr>
<tr>
<td align="center">23</td>
<td align="center">Oleic acid &#x2b; methanol</td>
<td align="center">SC-F-Plg-3</td>
<td align="center">4&#xa0;h, 65&#xb0;C, 0.02&#xa0;g, 1:55</td>
<td align="center">C &#x3d; 88.69%</td>
<td align="center">5 cycles; C &#x3d; 70.31%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B60">Wu et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">24</td>
<td align="center">Cooking oil &#x2b; methanol</td>
<td align="center">Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>-APTES-L<sup>AE</sup>-Mo<sup>VI</sup>O<sub>2</sub>
</td>
<td align="center">0.75&#xa0;h, RT, 0.04&#xa0;g, 1:3</td>
<td align="center">C &#x3d; 99%</td>
<td align="center">12 cycles; C &#x3d; 92%</td>
<td align="center">\</td>
<td align="center">
<xref ref-type="bibr" rid="B41">Mohammadpour and Safaei, (2022)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s2-3">
<title>2.3 Magnetic catalysts functionalized with ionic liquids (ILs)</title>
<p>Recently, due to their highly tunable nature, low volatility, and strong chemical and thermal stability, ionic liquids (ILs) have been widely reported for use in the catalysis field (<xref ref-type="bibr" rid="B50">Sharma et al., 2022</xref>). Among these, many IL-functionalized magnetic catalysts have been tested for the production of biodiesel because of their unique properties and commercial availability. <xref ref-type="bibr" rid="B18">Fauzi et al. (2014)</xref> used oleic acid as raw material and 1-butyl-3-methylimidazolium tetrachloroferrate ([BMIM][FeCl<sub>4</sub>]) as a magnetic catalyst to prepare biodiesel by esterification, with a yield of methyl oleate of 83.4% under optimum conditions. In addition, the [BMIM][FeCl<sub>4</sub>] catalyst was reused for six runs with little loss; the activation energy of the esterification system was 17.97&#xa0;kJ/mol.</p>
<p>A novel IL-functionalized magnetic catalyst was fabricated by covalent bonding of [SO<sub>3</sub>H-PIM-TMSP]HSO<sub>4</sub> ILs onto mesoporous silica-modified Fe<sub>3</sub>O<sub>4</sub> nanoparticles (FSS&#x2013;IL) (<xref ref-type="bibr" rid="B63">Wu et al., 2014</xref>; <xref ref-type="bibr" rid="B55">Wan et al., 2015</xref>). The characterization results revealed that the FSS&#x2013;IL catalyst possessed a uniform core&#x2013;shell structure and high specific surface area. In the process of preparing biodiesel, the conversion was 93.5% after 4&#xa0;h using oleic acid as a raw material. More importantly, this FSS&#x2013;IL catalytic system remained active for six cycles. In another study, magnetically hydrophobic acidic polymeric ionic liquids (FnmS-PILs) were prepared and exhibited good activity and reusability (<xref ref-type="bibr" rid="B74">Zhang et al., 2018</xref>). <xref ref-type="bibr" rid="B70">Xie and Wang. (2020a)</xref> prepared a magnetic Fe<sub>3</sub>O<sub>4</sub>/SiO<sub>2</sub>-supported polymeric sulfonated ionic liquid (Fe<sub>3</sub>O<sub>4</sub>/SiO<sub>2</sub>-PIL) for simultaneous transesterification and esterification of low-cost oils, and the highest conversion obtained under optimal conditions was 93.3%. Additionally, the reusability study showed that the Fe<sub>3</sub>O<sub>4</sub>/SiO<sub>2</sub>-PIL could be recycled and reused five times. The higher activity and excellent reusability were attributed to the polymeric acidic ILs and porous magnetic nanoparticles. An immobilized dual acidic-ionic liquid on core&#x2013;shell-structured magnetic silica was also prepared, and the as-prepared magnetic acid catalyst exhibited a large surface acidity of 3.93 meq H<sup>&#x2b;</sup>/g, a strong magnetism of 27.5&#xa0;emu/g, and achieved the highest conversion of biodiesel at 94.2%. The catalyst was reused for five runs, and the conversion still reached 86% (<xref ref-type="bibr" rid="B65">Xie et al., 2021</xref>).</p>
<p>Similar catalysts [NiFe<sub>2</sub>O<sub>4</sub>@BMSI]Br, Fe<sub>3</sub>O<sub>4</sub>@GO@PBIL, Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>@[C4mim]HSO<sub>4</sub>, Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>@PIL, and [BSO<sub>3</sub>HMIm][HSO<sub>4</sub>]@IRMOF-3 were also studied (<xref ref-type="bibr" rid="B16">Ding et al., 2021</xref>; <xref ref-type="bibr" rid="B42">Naushad et al., 2021</xref>; <xref ref-type="bibr" rid="B73">Yu et al., 2021</xref>; <xref ref-type="bibr" rid="B82">Zhao et al., 2021</xref>; <xref ref-type="bibr" rid="B13">Cheng et al., 2022</xref>). Among them, the magnetic [NiFe<sub>2</sub>O<sub>4</sub>@BMSI]Br catalyst was synthesized by an ion-exchange process, and the resulting catalyst had a BET surface area of 89.21&#xa0;m<sup>2</sup>/g. Moreover, the [NiFe<sub>2</sub>O<sub>4</sub>@BMSI]Br catalyst attained a maximum yield of 86.4% for the transesterification of palm oil, and the catalytic activity was retained up to six cycles without obvious loss of yield (<xref ref-type="bibr" rid="B42">Naushad et al., 2021</xref>). Based on recent literature projections, ILs are expected to develop as potential acid materials for the synthesis of functionalized composite magnetic catalysts in the future.</p>
</sec>
<sec id="s2-4">
<title>2.4 Magnetic catalysts based on heteropolyacids</title>
<p>Heteropolyacids are inorganic compounds with a Keggin structure that acts as a strong Br&#xf8;nsted acid. Heteropolyacids have a low surface area and easily dissolve in polar solvents, so researchers bonded them to magnetic supports to overcome these problems. <xref ref-type="bibr" rid="B62">Wu et al. (2016a)</xref> investigated the application of magnetic material grafted onto a poly(phosphotungstate)-based acidic ionic liquid as a heterogeneous catalyst for the esterification of oleic acid. Under optimal conditions, the conversion of oleic acid reached 93.4%. More specifically, the catalyst exhibited good reusability after six runs using an external magnetic field.</p>
<p>As reported by <xref ref-type="bibr" rid="B25">Helmi et al. (2021)</xref>, phosphomolybdic acid was supported on clinoptilolite&#x2013;Fe<sub>3</sub>O<sub>4</sub>, and the prepared catalyst showed excellent activity (80% yield in 8&#xa0;h at 75&#xb0;C) and reusability in the production of biodiesel from <italic>Salvia mirzayanii</italic> oil. The HPA/clinoptilolite&#x2013;Fe<sub>3</sub>O<sub>4</sub> catalyst was able to recycle up to four times with minimal loss in activity. A magnetic heteropolyanion-based ionic liquid (MNP@HPAIL) was synthesized by <xref ref-type="bibr" rid="B15">Dadhania et al. (2021)</xref>, and was evaluated for the esterification of oleic acid under ultrasonic irradiation. The maximum oleic acid conversion of 58% was reached, and the catalyst could be reused for six consecutive cycles.</p>
<p>On the same note, <xref ref-type="bibr" rid="B75">Zhang et al. (2021)</xref> immobilized a 12-tungstophosphoric acid (HPW)-based magnetic catalyst (Fe<sub>3</sub>O<sub>4</sub>@SBA-15@HPW and Fe<sub>3</sub>O<sub>4</sub>@SBA-15-NH<sub>2</sub>-HPW) for the production of biodiesel from palm oil with methanol. The synthesized magnetic catalysts have a high content of Br&#xf8;nsted acid sites due to the induction of HPW. In particular, the Fe<sub>3</sub>O<sub>4</sub>@SBA-15-NH<sub>2</sub>-HPW exhibited a high biodiesel yield of 91% under optimal reaction conditions, and also exhibited high reusability. <xref ref-type="bibr" rid="B20">Ghasemzadeh et al. (2022)</xref> adapted a cotton/Fe<sub>3</sub>O<sub>4</sub>@SiO<sub>2</sub>@H<sub>3</sub>PW<sub>12</sub>O<sub>40</sub> magnetic nanocomposite to catalyze the transesterification of sunflower oil. The catalyst had an excellent magnetism of 45&#xa0;emu/g and demonstrated a high FAME yield of 95.3% under optimum conditions. After four cycles of transesterification, the FAME yield was still relatively high at 85.5%. In addition, the physical properties of the synthetic biodiesel meet the ASTM and EU standards. According to the reported literature, heteropolyacids grafted onto magnetic supports can be an effective solution to overcome the loss of heteropolyacids.</p>
</sec>
<sec id="s2-5">
<title>2.5 MOF-based magnetic catalysts</title>
<p>Recently, metal&#x2013;organic frameworks (MOFs), as a newly emergent type of stable and tunable material, have become promising magnetic catalysts and supports, and MOF derivatives have been used for heterogeneous catalysis. <xref ref-type="bibr" rid="B61">Wu et al. (2016b)</xref> investigated the ability of the Fe<sub>3</sub>O<sub>4</sub>@NH<sub>2</sub>-MIL-88B(Fe) catalyst to perform the esterification of oleic acid with ethanol. The Fe<sub>3</sub>O<sub>4</sub>@NH<sub>2</sub>-MIL-88B(Fe) catalyst had an acidity of 1.76&#xa0;mmol/g and achieved a high yield of 93.2% at 90&#xb0;C. Moreover, the Fe<sub>3</sub>O<sub>4</sub>@NH<sub>2</sub>-MIL-88B(Fe) catalyst could be recycled six times without significant loss of activity.</p>
<p>Xie&#x2019;s group (<xref ref-type="bibr" rid="B68">Xie and Wan, 2018</xref>; <xref ref-type="bibr" rid="B66">Xie and Huang, 2019</xref>; <xref ref-type="bibr" rid="B71">Xie and Wang, 2020</xref>; <xref ref-type="bibr" rid="B65">Xie et al., 2021b</xref>) has studied biodiesel production from soybean oil and low-quality oils using magnetic Fe<sub>3</sub>O<sub>4</sub>@HKUST-1-ABILs, Fe<sub>3</sub>O<sub>4</sub>@MIL-100(Fe)/<italic>Candida rugosa</italic> lipase, CoFe<sub>2</sub>O<sub>4</sub>/MIL-88B(Fe)-NH<sub>2</sub>/(Py-Ps)PMo, and H<sub>6</sub>PV<sub>3</sub>MoW<sub>8</sub>O<sub>40</sub>/Fe<sub>3</sub>O<sub>4</sub>/ZIF-8 catalysts. Their results revealed that all magnetic catalysts exhibited good catalytic performance and excellent reusability. Thus, these MOF-based magnetic catalysts comprise an excellent potential alternative for processing low-quality oils into biofuels. In another study by Zhou&#x2019;s group (<xref ref-type="bibr" rid="B83">Zhou et al., 2019</xref>; <xref ref-type="bibr" rid="B84">Zhou et al., 2023</xref>), a MIL-100(Fe) was embedded in magnetic Fe<sub>3</sub>O<sub>4</sub> nanoparticles (Fe<sub>3</sub>O<sub>4</sub>/MIL-100(Fe), and the Fe<sub>3</sub>O<sub>4</sub>/MIL-100(Fe) composite exhibited unexpectedly high catalytic activity with a rosin conversion of 94.8% at 240&#xb0;C. Furthermore, the Fe<sub>3</sub>O<sub>4</sub>/MIL-100(Fe) composite showed good stability and recyclability over six cycles. An annealed Fe<sub>3</sub>O<sub>4</sub>/MOF-5 was also synthesized and used to catalyze rosin esterification with glycerol. The highest conversion of 94.1% was attained in 2.5&#xa0;h at 240&#xb0;C, and the annealed catalyst showed excellent reusability.</p>
<p>A novel TiO<sub>2</sub>-decorated magnetic ZIF-8 nanocomposite (Fe<sub>3</sub>O<sub>4</sub>@ZIF-8/TiO<sub>2</sub>) was synthesized by <xref ref-type="bibr" rid="B49">Sabzevar et al. (2021)</xref>. The as-prepared nanocomposite demonstrated excellent performance in the esterification of oleic acid (92.25% yield), which was mainly attributed to its acidic properties and large surface area. After five cycles, the yield of biodiesel was still 77.22%. <xref ref-type="bibr" rid="B2">Abdelmigeed et al. (2021a)</xref>, <xref ref-type="bibr" rid="B1">Abdelmigeed et al. (2021b)</xref> prepared NaOH/magnetized ZIF-8 catalysts for the production of high-quality biodiesel from a blend of sunflower and soybean oil with ethanol. The transesterification reaction with the blended oil produced 70% biodiesel in 1.5&#xa0;h at 75&#xb0;C. The ethanolysis reaction followed a pseudo-second-order kinetic model, and the activation energy was calculated as 77.27&#xa0;kJ/mol.</p>
<p>In another important area of catalyst research, MOFs were pyrolized at various temperatures to act as self-sacrificial templates for the synthesis of structured nanoporous metal oxides (<xref ref-type="bibr" rid="B47">Reddy et al., 2020</xref>). <xref ref-type="bibr" rid="B33">Li et al. (2019)</xref>, <xref ref-type="bibr" rid="B35">Li et al. (2020)</xref>, <xref ref-type="bibr" rid="B34">Li et al. (2021)</xref> reported on a series of magnetic catalysts based on MOF derivatives (MM&#x2013;SrO, magnetic CaO-based catalyst, carbonized MIL-100(Fe) supporting ammonium sulfate), and the physical, chemical, and thermal properties of the MOF-derived magnetic catalysts were evaluated. The researchers discovered that these catalysts exhibited strong magnetism and excellent catalytic activity and could be easily separated by an external magnetic field after each cycle. In another study, a bifunctional magnetic catalyst with various coordination states of Co and non-coordinated N sites was developed by <xref ref-type="bibr" rid="B22">Guo et al. (2022).</xref> The prepared bifunctional magnetic catalyst (550&#x2013;30) was evaluated for biodiesel production from microalgal lipids. It had a high conversion efficiency of 96.0%, owing to the generated structural defects that formed a mesopore-dominated structure in the bifunctional magnetic catalyst. Also, the catalyst could be magnetically separated and reused for six cycles with a conversion efficiency of 89.7%.</p>
</sec>
</sec>
<sec id="s3">
<title>3 Summary and outlook</title>
<p>In the field of catalysis, magnetic catalysts promote catalytic reactions efficiently and their strong magnetic properties allow them to be easily reused, which make magnetic catalysts more cost-effective and efficient when used in industrial catalysis. The current mini-review highlights recent applications of magnetic catalysts and their functionalized magnetic materials utilized for biodiesel production. Although remarkable progress has been achieved in the area of magnetic catalyst research, there are still some limitations that need to be overcome by continuing design improvements. The catalytic mechanisms and deactivation processes are not well understood, supported magnetic catalysts show weak interactions between active ingredients and magnetic supports, and the complex synthesis processes for some magnetic catalysts need to be simplified. Thus, future investigation into the preparation methods, performance, mechanisms, and economics of the magnetic catalyst is essential to correct the present issues. In light of the current evidence, however, we strongly believe that the integrated development of novel magnetic catalysts will play a key role in further developing a cost-effective biorefinery industry.</p>
</sec>
</body>
<back>
<sec id="s4">
<title>Author contributions</title>
<p>YTZ conceived the article, discussed the outline, and wrote the manuscript; WL, JW, JJ, YXZ, and JC made preliminary revisions to the manuscript; YTZ and QZ coordinated the entire content of the manuscript and made detailed revisions; QZ was in charge of project administration.</p>
</sec>
<sec id="s5">
<title>Funding</title>
<p>This work was financially supported by the Anshun Science and Technology Planning Project ((2021)1), National Natural Science Foundation of China (22262001), Creative Research Groups Support Program of Guizhou Education Department (KY (2017)049), Youth Growth Science and Technology Personnel Foundation of Guizhou Education Department (KY (2019)147), Guizhou Province Key Laboratory of Ecological Protection and Restoration of Typical Plateau Wetlands ((2020) 2002), and Project of Anshun University supporting Doctors Research ((2021)asxybsjj01).</p>
</sec>
<sec sec-type="COI-statement" id="s6">
<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="s7">
<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>
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