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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Environ. Sci.</journal-id>
<journal-title>Frontiers in Environmental Science</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Environ. Sci.</abbrev-journal-title>
<issn pub-type="epub">2296-665X</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1467797</article-id>
<article-id pub-id-type="doi">10.3389/fenvs.2024.1467797</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Environmental Science</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Fe(II)-loaded goat manure biochar efficiently activated peroxymonosulfate for tetracycline degradation in groundwater</article-title>
<alt-title alt-title-type="left-running-head">Fan 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/fenvs.2024.1467797">10.3389/fenvs.2024.1467797</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Fan</surname>
<given-names>Lianjie</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>
<uri xlink:href="https://loop.frontiersin.org/people/2797838/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
<role content-type="https://credit.niso.org/contributor-roles/data-curation/"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Xie</surname>
<given-names>Qinglin</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
<role content-type="https://credit.niso.org/contributor-roles/data-curation/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Li</surname>
<given-names>Yanhong</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/formal-analysis/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Zou</surname>
<given-names>Shengzhang</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/investigation/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Lu</surname>
<given-names>Haiping</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/data-curation/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Li</surname>
<given-names>Su Ling</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
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<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Li</surname>
<given-names>Xiaoxiao</given-names>
</name>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2797248/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>College of Environmental Science and Engineering</institution>, <institution>Guilin University of Technology</institution>, <addr-line>Guilin</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Guangxi Karst Resources and Environment Research Center of Engineering Technology</institution>, <institution>Institute of Karst Geology</institution>, <institution>Chinese Academy of Geological Sciences</institution>, <addr-line>Guilin</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>International Research Centre on Karst under the Auspices of UNESCO</institution>, <institution>National Center for International Research on Karst Dynamic System and Global Change</institution>, <addr-line>Guilin</addr-line>, <country>China</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>College of Environment</institution>, <institution>Hohai University</institution>, <addr-line>Nanjing</addr-line>, <country>China</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2290905/overview">Xiao Huang</ext-link>, Chongqing University of Science and Technology, 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/1683928/overview">Ting Yang</ext-link>, Minzu University of China, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1940203/overview">V. N. Meena Devi</ext-link>, Noorul Islam University, India</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Qinglin Xie, <email>992896002@qq.com</email>; Xiaoxiao Li, <email>lixiaoxiao19970305@163.com</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>20</day>
<month>12</month>
<year>2024</year>
</pub-date>
<pub-date pub-type="collection">
<year>2024</year>
</pub-date>
<volume>12</volume>
<elocation-id>1467797</elocation-id>
<history>
<date date-type="received">
<day>20</day>
<month>07</month>
<year>2024</year>
</date>
<date date-type="accepted">
<day>03</day>
<month>12</month>
<year>2024</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2024 Fan, Xie, Li, Zou, Lu, Li and Li.</copyright-statement>
<copyright-year>2024</copyright-year>
<copyright-holder>Fan, Xie, Li, Zou, Lu, Li 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>Poultry manure is one of the important sources of antibiotic pollution in agricultural soil and groundwater. Recently, the excessive discharge of goat manure has resulted in groundwater environmental challenges and negative impacts. It is of practical significance that such wastes can be converted into functional materials to promote the resource utilization of waste and reduce the risk of antibiotic contamination. In this study, Fe (&#x2161;)-loaded goat manure biochar (Fe-GMC) was prepared by pyrolyzing goat manure and iron salts and used to activate peroxymonosulfate (PMS) for tetracycline (TC) degradation in groundwater. The as-prepared Fe-GMC exhibited good catalytic performance for PMS activation due to its porous surface and rich oxygen-containing groups. Under the conditions of catalyst dosage of 0.2&#xa0;g/L, PMS dosage of 1.0&#xa0;mM, and pH of 3.0, TC was removed 81.3% within 60&#xa0;min. In addition, the TC degradation efficiency was inhibited to different extents by inorganic anions (HCO<sub>3</sub>
<sup>&#x2212;</sup>&#x3e;Cl<sup>&#x2212;</sup>&#x3e;NO<sub>3</sub>
<sup>&#x2212;</sup>) in water. Furthermore, the quenching experiments, electron paramagnetic resonance (EPR) experiments, and X-ray photoelectron spectroscopy (XPS) spectra analysis indicated that the generation of hydroxyl radicals (<sup>&#x2022;</sup>OH) was responsible for TC degradation. Particularly, Fe-GMC produces a strong oxidizing agent. This study provides an efficient and environmentally friendly tetracycline degradation catalyst, which offers a new theoretical basis for water environmental remediation.</p>
</abstract>
<abstract abstract-type="graphical">
<title>Graphical Abstract</title>
<p>
<graphic xlink:href="FENVS_fenvs-2024-1467797_wc_abs.tif"/>
</p>
</abstract>
<kwd-group>
<kwd>goat manure</kwd>
<kwd>tetracycline degradation</kwd>
<kwd>waste utilization</kwd>
<kwd>Fe(III)</kwd>
<kwd>peroxymonosulfate</kwd>
</kwd-group>
<contract-num rid="cn001">AB21220044</contract-num>
<contract-sponsor id="cn001">Guangxi Key Research and Development Program<named-content content-type="fundref-id">10.13039/501100017691</named-content>
</contract-sponsor>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Toxicology, Pollution and the Environment</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Antibiotics are chemical agents used to treat microbial infectious diseases and are widely used in human and animal healthcare and aquaculture. Due to their long stability and extensive distribution characteristics, antibiotics have become a worldwide pollutant (<xref ref-type="bibr" rid="B16">Jiang L. B. et al., 2018</xref>; <xref ref-type="bibr" rid="B56">Zhang et al., 2019</xref>). Tetracyclines (TCs) are widely used for treating and preventing animal diseases, promoting animal growth, and improving animal husbandry productivity. They represent the largest class of veterinary antibiotics used in China&#x2019;s livestock and poultry industry, accounting for approximately 37% of the total antibiotic use. However, TC antibiotics cannot be completely absorbed by the animal body and are excreted in the form of maternal or metabolites with livestock and poultry manure. Antibiotics discharged from livestock feedlots through wastewater could disseminate into surrounding groundwater environments (<xref ref-type="bibr" rid="B48">Xiao et al., 2018</xref>, <xref ref-type="bibr" rid="B46">Watanabe et al., 2010</xref>). Thermophilic composting has proven to be a cost-effective technology for recovering animal manure resources and mitigating TC-related hazards, but there are problems with higher costs and incomplete removal (<xref ref-type="bibr" rid="B45">Wanying et al., 2023</xref>). Thus, TC is detected in large quantities in environmental media such as water, sediments, and soil. Therefore, there is an urgent need to develop an economical and environmentally friendly approach to control TC pollution (<xref ref-type="bibr" rid="B57">Zhijie et al., 2018</xref>; <xref ref-type="bibr" rid="B40">Wang and Wang, 2018</xref>).</p>
<p>To date, adsorption (<xref ref-type="bibr" rid="B29">Rahmat and Ahmadi, 2019</xref>), biological treatment (<xref ref-type="bibr" rid="B49">Xiaodong et al., 2021</xref>), advanced oxidation processes (AOPs), and other techniques have been employed to treat TC (<xref ref-type="bibr" rid="B8">Dong et al., 2017</xref>; <xref ref-type="bibr" rid="B13">Hussain et al., 2017</xref>). AOPs have attracted widespread attention because of their high efficiency in the degradation of TC (<xref ref-type="bibr" rid="B53">Yangju et al., 2021</xref>). Therein, PMS-based AOPs are regarded as optimized means to remove refractory contaminants, benefiting from the strong oxidation ability, excellent stability, and convenient transportation (<xref ref-type="bibr" rid="B4">Chang-Mao et al., 2016</xref>; <xref ref-type="bibr" rid="B19">Luo et al., 2020</xref>). Moreover, PMS could be activated to produce radicals (sulfate radical SO<sub>4</sub>
<sup>&#x2022;-</sup>), hydroxyl radical (<sup>&#x2022;</sup>OH), superoxide radical (O<sub>2</sub>
<sup>&#x2022;&#x2212;</sup>), and singlet oxygen (<sup>1</sup>O<sub>2</sub>) (<xref ref-type="bibr" rid="B60">Zou et al., 2019</xref>; <xref ref-type="bibr" rid="B42">Wang et al., 2017</xref>). Therefore, compared with the Fenton reaction, the PMS activation process has a stronger mineralization capacity. Fe<sup>2&#x2b;</sup> is the best reagent for PMS activation because Fe<sup>2&#x2b;</sup> is inexpensive, environmentally friendly, and non-biotoxic (<xref ref-type="bibr" rid="B58">Zhu et al., 2022</xref>). In addition, a non-radical pathway occurs during the reaction, and the intermediate reactant, high-valent iron (Fe(IV)), has attracted widespread attention due to its strong oxidation potential (<xref ref-type="bibr" rid="B52">Xingyu et al., 2022</xref>).</p>
<p>PMS could be activated by UV, heat, ultrasound, and transition metals. Although UV is an efficient method to activate PMS, its low economic benefits limit its widespread application (<xref ref-type="bibr" rid="B41">Wang et al., 2018</xref>). Thus, ferrous iron (Fe (&#x2161;)) was commonly chosen as the activator for SO<sub>4</sub>
<sup>&#x2022;-</sup> generation from PMS due to its advantages of environmental friendliness, cost-effectiveness, and high activity (<xref ref-type="bibr" rid="B38">Uthirakrishnan et al., 2020</xref>). At present, carbon matrices such as graphene and carbon nanotubes are widely used (<xref ref-type="bibr" rid="B48">Xiao et al., 2018</xref>). However, their development costs are more expensive. Consequently, low-cost carbon materials should be developed. Biochar provides new active points for PMS due to its huge specific surface area, abundant oxygen-containing functional groups, and hybrid carbon structure, which can be considered sustainable and promising catalyst support (<xref ref-type="bibr" rid="B3">Bolan et al., 2022</xref>).</p>
<p>With the development of animal husbandry, the excessive discharge of animal manure has placed a severe burden on the environment (<xref ref-type="bibr" rid="B59">Zhu et al., 2013</xref>). Research has explored biochar-loaded Fe-based activation of PMS to generate free radicals for pollutant removal from water. Studies such as those by <xref ref-type="bibr" rid="B47">Wu et al. (2023)</xref> and <xref ref-type="bibr" rid="B9">Fang et al. (2024)</xref> have shown that this approach can generate SO<sub>4</sub>&#x2022;<sup>-</sup> and &#xb7;&#x2022;OH free radicals, which effectively remove pollutants from water. However, limited research has focused on &#x201c;Waste for Waste&#x201d; methods to produce biochar. The &#x201c;Waste for Waste&#x201d; paradigm represents an ecologically sound and sustainable developmental ideology, accentuating the conversion of waste into valuable resources. Goat manure is a valuable option as a carbon matrix for the removal of tetracycline by activating PMS. On one hand, this approach can reduce antibiotic contamination of goat manure itself. On the other hand, we can make full use of the small number of inherent heteroatoms in goat manure to avoid additional doping, thereby contributing to antibiotic removal from the environment (<xref ref-type="bibr" rid="B43">Wang et al., 2021</xref>; <xref ref-type="bibr" rid="B24">Miguel et al., 2022</xref>). Therefore, the resource utilization of goat manure not only reduces environmental pollution but also offers practical advantages. Goat manure is widely available, has low price, and can be produced on a large scale. In this study, a novel Fe-GMC material was synthesized using goat manure and FeSO<sub>4</sub>.7H<sub>2</sub>O as feedstocks and was used to activate PMS for TC degradation. The key factors affecting the degradation of TC in the Fe-GMC/PMS system, such as initial pH, PMS dosage, Fe-GMC dosage, inorganic ions, and reaction temperature, were also investigated. Finally, the oxidation pathways and mechanism of the Fe-GMC/PMS system were elucidated through scavenging tests and electron paramagnetic resonance (EPR).</p>
</sec>
<sec id="s2">
<title>2 Experimental</title>
<sec id="s2-1">
<title>2.1 Materials</title>
<p>The raw goat manure was obtained from the local farm in Yunnan. The collected goat manure was rinsed with deionized water and dried at 60&#xb0;C for subsequent use. Ferrous sulfate (FeSO<sub>4</sub>&#xb7;7H<sub>2</sub>O) and tetracycline (TC) were purchased from Aladdin Chemistry Co. Ltd., China. Other compounds including 2KHSO<sub>5</sub>&#xb7;K<sub>2</sub>SO<sub>4</sub>&#xb7;K<sub>2</sub>SO<sub>4</sub> (PMS), sodium chloride (NaCl), sodium bicarbonate (NaHCO<sub>3</sub>), sodium nitrate (NaNO<sub>3</sub>), ethanol (Et-OH), and tert-butanol (TBA) were supplied by Sinopharm Chemical Reagent Co. Ltd. (Shanghai, China). All reagents were of analytical grade and used directly without further purification. The aqueous solution involved in the experiments was prepared with deionized water produced in the laboratory (<xref ref-type="bibr" rid="B17">Jianghui et al., 2022</xref>).</p>
</sec>
<sec id="s2-2">
<title>2.2 Catalyst synthesis</title>
<p>Fe-GMC was prepared as follows: first, 20&#xa0;g of goat manure was immersed in the Fe<sup>2&#x2b;</sup> solution (0.05&#xa0;M) under continuous stirring overnight, followed by washing twice with deionized water and drying at 60&#xb0;C (<xref ref-type="bibr" rid="B19">Luo et al., 2020</xref>). Afterward, the obtained samples were placed in the quartz boat and carbonized in a tube furnace at 800&#xb0;C (at a rate of 5&#xb0;C/min) for 2&#xa0;h under the continuous nitrogen atmosphere. The furnace was allowed to cool, and the sample was removed and placed inside a sample bag. The prepared sample was referred to as Fe-GMC. Raw goat manure (GMC) was prepared without iron.</p>
</sec>
<sec id="s2-3">
<title>2.3 Catalyst characterization</title>
<p>X-ray diffraction (XRD, Bruker D8) was conducted to confirm the crystal structure of Fe-GMC and GMC. The morphologies and structural features of Fe-GMC and GMC were determined via scanning electron microscopy (SEM; Zeiss Sigma HD, Germany) with an X-ray energy dispersive spectrometer (EDS). High-resolution transmission electron microscopy (TEM, FEI Talos F200x, United States) tests were utilized to observe the micro shape on catalyst surface. The surface elements of the Fe-GMC were recorded by X-ray photoelectron spectroscopy (XPS; ESCALAB250Xi, Thermo Fisher). Fourier transform infrared spectroscopy (FT-IR) was utilized to monitor the functional groups of the composites. Electron paramagnetic resonance (EPR, JEOL JES-FA200) examined the main active species. Brunauer&#x2013;Emmett&#x2013;Teller (BET) surface area was employed to obtain the specific surface area.</p>
</sec>
<sec id="s2-4">
<title>2.4 Catalytic activity experiment</title>
<p>Fe-GMC was ground into powder and used in the batch catalytic experiments. In brief, the reactions were carried out in the 125&#xa0;mL serum bottle TC (10&#xa0;mg/L, 50&#xa0;mL) and PMS (1.0&#xa0;mM), which were initiated by adding 0.1&#xa0;g of catalyst into the TC solution, which was shaken by a thermostatic reciprocating shaker at 150&#xa0;rpm and 30&#xb0;C. All serum bottles were covered with tin foil. At different elapsed times, a 2&#xa0;mL sample was collected from each flask using a 10&#xa0;mL syringe. After that, the remaining concentration of TC was measured using a UV&#x2013;Vis spectrophotometer at 357&#xa0;nm. The reaction kinetics of TC was simulated using the pseudo-first kinetic model. Details related to the model are provided as Text S1 in Supporting Information.</p>
<p>The key factors affecting the degradation of TC in the Fe-GMC/PMS system, such as initial pH, PMS dosage, Fe-GMC dosage, inorganic ions, and reaction temperature, were determined and detailed in SI (Supporting Information, see Text S2). In quenching experiments, Et-OH (SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> and <sup>&#x2022;</sup>OH), TBA (SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup>), and L-histidine (<sup>1</sup>O<sub>2</sub>) were selected as quenchers to scavenge corresponding active species. Afterward, the process was monitored using the UV&#x2013;Vis spectrophotometer.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Material characterization</title>
<p>
<xref ref-type="fig" rid="F1">Figure 1A</xref> shows that the surface morphologies and structure of materials were confirmed via SEM. The SEM results determined that goat manure without supported iron exhibited a smooth surface with an irregular multilayer lamellar structure and some stripes (<xref ref-type="fig" rid="F1">Figure 1A</xref>). In contrast, for Fe-GMC, some pores and ridges can be seen in <xref ref-type="fig" rid="F1">Figure 1B</xref>, which increases the active sites and is more conducive to the adsorption of TC (<xref ref-type="bibr" rid="B25">Mingfei et al., 2021</xref>). The detailed elemental distribution and content of Raw goat manure and Fe-GMC were determined by EDS (<xref ref-type="fig" rid="F1">Figures 1C, D</xref>). The element Fe was detected, which indicated the successful introduction of Fe species. Uniformly distributed Fe nanoparticles can be seen in <xref ref-type="fig" rid="F1">Figure 1E</xref>, demonstrating that Fe particles are encapsulated within the GMC. As indicated by the high-magnification TEM image (<xref ref-type="fig" rid="F1">Figure 1F</xref>), a thin layered structure of carbon nanoflakes could be observed, with a lattice spacing of 0.25&#xa0;nm attributed to Fe<sub>3</sub>O<sub>4</sub>, similar to previous studies (<xref ref-type="bibr" rid="B39">Wang et al., 2020</xref>). In addition, the layered nanoflake structures are highly porous and become gradually thinner toward the edges of the material. Moreover, these uniformly distributed Fe<sub>3</sub>O<sub>4</sub> particles onto the biochar carrier corroborated the results of SEM images of <xref ref-type="fig" rid="F1">Figure 1B</xref>, and this study demonstrates the successful synthesis of Fe-GMC composites.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>SEM images of <bold>(A)</bold> raw goat manure and <bold>(B)</bold> Fe-GMC and <bold>(C)</bold> raw goat manure and <bold>(D)</bold> Fe-GMC EDS. <bold>(E)</bold> TEM and HRTEM <bold>(F)</bold> images of Fe-GMC.</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g001.tif"/>
</fig>
<p>The surface functional groups were investigated by FT-IR. As observed in <xref ref-type="fig" rid="F2">Figure 2A</xref>, the stretching vibration of C&#x3d;O and C&#x3d;C bonds transformed from aromatic rings results in a signal at 1,623&#xa0;cm<sup>&#x2212;1</sup> (<xref ref-type="bibr" rid="B28">Pu et al., 2021</xref>). The C&#x2013;C stretching vibration was observed at 1,172&#xa0;cm<sup>&#x2212;1</sup>, and the band at 1,084&#xa0;cm<sup>&#x2212;1</sup> corresponded to the C&#x2013;O stretching vibration (<xref ref-type="bibr" rid="B36">Tianyi et al., 2020</xref>). The pyrolysis of organic to obtain the biochar played an important role in increasing oxygen-containing surface functional groups, and this might enhance the biochar activation effect (<xref ref-type="bibr" rid="B8">Dong et al., 2017</xref>). In addition, there was an obvious vibration at approximately 570&#xa0;cm<sup>&#x2212;1</sup> for Fe-GMC, which indicated the existence of an Fe-O characteristic peak in Fe-GMC, which also suggested that Fe<sup>2&#x2b;</sup> was successfully synthesized on the GMC (<xref ref-type="bibr" rid="B15">Jayaselvan L et al., 2020</xref>). In summary, the Fe-GMC had abundant oxygen-containing functional groups and oxides of Fe (II)/Fe (III). Furthermore, the crystal phase composition of the composite was determined by XRD (<xref ref-type="bibr" rid="B32">Shuzhao et al., 2020</xref>). <xref ref-type="fig" rid="F2">Figure 2B</xref> shows a diffraction peak of Fe-GMC with a 2&#x3b8; value of 43.74, 44.76, and 45.1, which corresponds to Fe<sub>3</sub>C (<xref ref-type="bibr" rid="B35">Tang et al., 2021</xref>; <xref ref-type="bibr" rid="B5">Chen et al., 2022</xref>). In addition, the dominant Fe<sub>3</sub>O<sub>4</sub> diffraction peaks were detected at 2&#x3b8; values of approximately 35.49 plane (<xref ref-type="bibr" rid="B14">Ikramullah and Zulkarnain, 2019</xref>). This result indicated that Fe-GMC may be loaded Fe<sub>3</sub>O<sub>4</sub>. The diffraction peaks at 26&#xb0; and 60&#xb0; are assigned to Fe<sub>2</sub>SiO<sub>4</sub> and magnetite, respectively, and the inorganic mineral composition Fe<sub>2</sub>SiO<sub>4</sub> was detected in Fe-GMC. This might be due to the redox reaction between Fe and Si components during high-temperature pyrolysis, and there is a significant increase in the XRD peak after the composite, indicating the successful composite of Fe<sub>3</sub>O<sub>4</sub> (<xref ref-type="bibr" rid="B33">Song et al., 2022</xref>).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Fourier transform-infrared (FITR) data <bold>(A)</bold> and X-ray diffraction (XRD) patterns <bold>(B)</bold> of GMC and Fe-GMC.</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g002.tif"/>
</fig>
<p>Similarly, we analyzed the specific surface area of the loaded material, as shown in <xref ref-type="sec" rid="s10">Supplementary Figure S1</xref>, and the Fe-GMC composites exhibit type IV adsorption curves and H3 type hysteresis loops, indicative of mesoporous attributes. In addition, the material has a good specific surface area and pore structure, with experimental results indicating a specific surface area of 416.248&#xa0;m<sup>2</sup>/g. This finding summarizes the physical properties of the material, making it suitable for adsorption, catalysis, and composite superiority of the material.</p>
<p>To further analyze the material&#x2019;s surface chemical compositions, XPS analysis was conducted. As shown in <xref ref-type="fig" rid="F3">Figure 3</xref>, the XPS full-spectrum and the spectra of Fe 2p, C 1&#xa0;s and O 1&#xa0;s in the Fe-GMC sample were obtained. The XPS spectra (<xref ref-type="fig" rid="F3">Figure 3A</xref>) confirmed the presence of C (284.8&#xa0;eV) and O (531.8&#xa0;eV). Compared with the full spectrum of GMC, Fe-GMC exhibited a distinct characteristic peak at 724.6&#xa0;ev, which is the characteristic peak of Fe, consistent with the results of EDS characterization (<xref ref-type="fig" rid="F1">Figure 1C</xref>). In <xref ref-type="fig" rid="F3">Figure 3B</xref>, Fe 2p spectrum shows peaks at 710.45&#xa0;eV and 724.1&#xa0;eV (due to Fe 2p<sub>3/2</sub>) and 711.85&#xa0;eV and 726.3&#xa0;eV (corresponded to Fe 2p<sub>1/2</sub>), while the peaks at 718.5&#xa0;eV and 733.0&#xa0;eV were the satellite peaks of Fe 2p<sub>3/2</sub> to Fe 2p<sub>1/2</sub>, respectively (<xref ref-type="bibr" rid="B26">Mohammadi and Saied Saeed Hosseiny, 2020</xref>). The peak area ratio of Fe<sup>2&#x2b;</sup> to Fe<sup>3&#x2b;</sup> obtained from the XPS analysis was close to 1:2. This result was also consistent with the abovementioned XRD analysis results, which verify the presence of Fe<sub>3</sub>O<sub>4</sub> particles on the surface of Fe-GMC.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>High-resolution X-ray photoelectron spectra (XPS) of GMC and Fe-GMC, <bold>(A)</bold> full spectrum, <bold>(C)</bold> C 1s region and O 1s region <bold>(D)</bold>, and <bold>(B)</bold> Fe 2p region of Fe-GMC.</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g003.tif"/>
</fig>
<p>To facilitate the differentiation of the materials prior to and following the composite formation for further study, C 1&#xa0;s and O 1&#xa0;s spectra of biochar and the composites are separated into several fine peaks. From <xref ref-type="fig" rid="F3">Figures 3C,D</xref>, it can be concluded that with the addition of Fe<sub>3</sub>O<sub>4</sub>, the positions of the peaks of the oxygen-containing functional groups in the composites are generally to the left, and the binding energy increases. It can also be observed from <xref ref-type="fig" rid="F3">Figure 3D</xref> that the relative area of C-OH in Fe-GMC decreases, while the relative area of Fe-O increases, indicating that the oxygen-containing functional groups on the GMC play important roles in the composite of Fe<sub>3</sub>O<sub>4</sub>. These findings are similar to those of previous studies (<xref ref-type="bibr" rid="B34">Song et al., 2019</xref>). At the same time, the electron-rich groups C&#x3d;C and C&#x3d;O can favor the activation of PMS to produce free radicals, and these free radicals may facilitate TC removal (<xref ref-type="bibr" rid="B6">Chen et al., 2020</xref>; <xref ref-type="bibr" rid="B19">Luo et al., 2020</xref>; <xref ref-type="bibr" rid="B60">Zou et al., 2019</xref>). These conclusions can be a good proof of the success of the material composite.</p>
</sec>
<sec id="s3-2">
<title>3.2 Catalytic activity of Fe-GMC</title>
<sec id="s3-2-1">
<title>3.2.1 Performance of Fe-GMC catalytic degradation of TC</title>
<p>TC was selected as the target pollutant to measure the catalytic activity of Fe-GMC. The results of the degradation of the TC solution are shown in <xref ref-type="fig" rid="F4">Figure 4A</xref> and <xref ref-type="sec" rid="s10">Supplementary Table S1</xref>. It is evident that the addition of Fe-GMC resulted in a significant increase in TC removal. In the reaction system containing GMC, the removal rate of TC by PMS was determined to be 31.3%. In the GMC system with Fe<sup>2&#x2b;</sup>, the maximum removal rate of TC due to pure adsorption is only 37.5% in the absence of PMS. When PMS was added, the degradation rate of TC reached 81.3% in 60&#xa0;min. In addition, the reaction kinetics of the Fe-GMC systems was analyzed according to a pseudo-first order reaction model (<xref ref-type="fig" rid="F4">Figure 4B</xref>; <xref ref-type="sec" rid="s10">Supplementary Table S2</xref>). The apparent rate constants were calculated to be 0.0092&#xa0;min<sup>&#x2212;1</sup> for control, 0.0479&#xa0;min<sup>&#x2212;1</sup> for the GMC/PMS system, and 1.2198&#xa0;min<sup>&#x2212;1</sup> for the Fe-GMC/PMS system. It was clear that Fe-GMC/PMS showed the highest apparent degradation rate constant, about 25.95 times higher than GMC-PMS. It has been previously reported that the synergic effect between Fe and biochar resulted in high catalytic performance via producing radicals and non-free radicals in the presence of PMS (<xref ref-type="bibr" rid="B54">Zang et al., 2020</xref>).</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>TC removal in different systems <bold>(A)</bold> and the pseudo-first order kinetic fitting curves <bold>(B)</bold> (experiment conditions: 0.20&#xa0;g/L catalyst, 1&#xa0;mM PMS, initial pH &#x3d; 3.01, and 30&#xb0;C).</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g004.tif"/>
</fig>
</sec>
<sec id="s3-2-2">
<title>3.2.2 Influence of different parameters on TC degradation</title>
<p>Different experimental parameters, including catalyst and PMS concentration, reaction temperature, initial solution pH, and inorganic anions, are analyzed to explore the catalytic properties of the Fe-GMC/PMS system (<xref ref-type="fig" rid="F5">Figure 5</xref>, <xref ref-type="sec" rid="s10">Supplementary Table S3</xref>, <xref ref-type="sec" rid="s10">Supplementary Figure S2</xref>). The effect of catalyst dose on TC degradation was displayed in <xref ref-type="fig" rid="F5">Figure 5A</xref> and <xref ref-type="sec" rid="s10">Supplementary Table S3</xref>. The removal efficiency of TC increased from 78.1% to 81.3% when the catalyst dose increased from 0.05 to 0.20&#xa0;g/L in 60&#xa0;min, which could be because increasing the catalyst dosage could offer more active sites to activate PMS and lead to the generation of more radicals (<xref ref-type="bibr" rid="B2">Alireza et al., 2015</xref>). However, as the dosage of the catalyst continued to increase to 0.25&#xa0;g/L, TC degradation decreased from 81.3% to 79.5%. Further increases in the biochar dose may overproduce oxidizing free radicals, promoting interactions between free radicals and leading to reduced pollutant decomposition (<xref ref-type="bibr" rid="B27">Nguyen et al., 2019</xref>). The abovementioned difference in TC removal from 78.1% to 81.3% was too slight because of the excessive generation of reactive oxygen radicals by Fe-GMC/PMS. For this reason, we increased the initial concentration of TC and the reaction time to identify the optimal concentration of catalyst addition, which can be observed in <xref ref-type="sec" rid="s10">Supplementary Figure S3</xref>. When the TC concentration was 15&#xa0;mg/L, the 0.2&#xa0;mg/L catalyst could remove 66% of the TC in 120&#xa0;min, which was much more than the other catalyst additions, and for this reason, the 0.2&#xa0;mg/L catalyst was chosen for the following experiments.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Effect of experimental conditions on TC removal in the Fe-GMC/PMS system. <bold>(A)</bold> Catalyst dosage (0.05&#xa0;g/L&#x2013;0.25&#xa0;g/L), <bold>(B)</bold> PMS dosage (0.5&#x2013;2.0&#xa0;mM), <bold>(C)</bold> reaction temperature (10&#xb0;C&#x2013;60&#xb0;C), and <bold>(D)</bold> initial pH (3&#x2013;11).</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g005.tif"/>
</fig>
<p>The impact of the PMS concentration on TC removal is illustrated in <xref ref-type="fig" rid="F5">Figure 5B</xref>. The removal rate of TC increases correspondingly as the initial PMS concentration increases. At an initial PMS concentration of 0.5&#xa0;mM, the removal rate of TC is low, and only 48.8% of TC is removed over 60&#xa0;min. When PMS concentration increased to 1&#xa0;mM, the removal rate increased to 81.3%. However, when 2&#xa0;mM of PMS was added, the degradation efficiency was not improved. The results may be attributed to the significant self-quenching effect (<xref ref-type="bibr" rid="B12">Haitao et al., 2020</xref>). The degradation efficiencies were increased from 71.2% to 81.3% with the increase in reaction temperatures from 10&#xb0;C to 30&#xb0;C (<xref ref-type="fig" rid="F5">Figure 5C</xref>), which indicated that a higher reaction temperature accelerates the decomposition of PMS, generating more free radicals <sup>&#x2022;</sup>OH and SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> for TC degradation. However, excessively high temperatures (60&#xb0;C) can destroy free radical activity (<xref ref-type="bibr" rid="B30">Ruan et al., 2019</xref>).</p>
<p>The initial pH can affect the release of ferrous ions and the activity of oxidants in Fe-GMC (<xref ref-type="bibr" rid="B22">Ma et al., 2021</xref>). Therefore, it is necessary to explore the effect of different initial pH values on TC removal. <xref ref-type="fig" rid="F5">Figure 5D</xref> illustrates that the degradation efficiencies for TC were 81.3%, 66.5%, 47.5%, and 37.1% within the Fe-GMC/PMS system when the initial pH values were 3.0, 5.0, 7.0, and 11.0, respectively. Since the surface charge of biochar is positive when the initial pH value is 3.0, it is conducive to the approach of PMS to the surface of biochar (<xref ref-type="bibr" rid="B7">Da et al., 2019</xref>). However, as the initial pH gradually increases (pH 5&#x2013;11), the negative charge on the surface of biochar increases, hindering its reaction with PMS (<xref ref-type="bibr" rid="B1">Ahmadi and Farshid, 2019</xref>).</p>
<p>Usually, many anions are ubiquitous in the real water environment, and their presence can affect catalytic activity. Therefore, the effects of Cl<sup>&#x2212;</sup>, NO<sub>3</sub>
<sup>&#x2212;</sup>, and HCO<sub>3</sub>
<sup>&#x2212;</sup> on TC degradation were studied. As demonstrated in <xref ref-type="sec" rid="s10">Supplementary Table S3</xref> and <xref ref-type="sec" rid="s10">Supplementary Figure S2</xref>, it was found that three typical inorganic anions had an inhibitory effect on TC removal, and the removal efficiencies of TC were 52.2%, 60.3%, and 44.9% within 60&#xa0;min, respectively. At the same time, we explored the effect of different concentrations of inorganic anions on the removal of TC from the system (<xref ref-type="sec" rid="s10">Supplementary Figure S4</xref>), and the results demonstrated that the inhibition of TC removal remained relatively consistent when the concentration of inorganic anions was increased from the low-concentration condition, which was attributed to the fact that &#x2022;OH was replaced by the reactive species with much smaller redox potentials. NO<sub>3</sub>
<sup>&#x2212;</sup> and Cl-have a slight inhibition on TC removal, which is due to the fact that these anions could scavenge free radicals and form weak radical species [<xref ref-type="disp-formula" rid="e1">Equations (1</xref>&#x2013;<xref ref-type="disp-formula" rid="e5">5)</xref>] (<xref ref-type="bibr" rid="B23">Masoumeh et al., 2018</xref>). However, HCO<sub>3</sub>
<sup>&#x2212;</sup> had a serious inhibitory effect on TC degradation, which could scavenge <sup>&#x2022;</sup>OH and SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> with high rates [<xref ref-type="disp-formula" rid="e1">Equations (1</xref>&#x2013;<xref ref-type="disp-formula" rid="e8">8)</xref>]. According to the abovementioned results, different anions have a certain influence on the free radical oxidation process. Hence, studying the influence of anions on TC degradation is conducive to providing a theoretical basis for practical applications.</p>
<p>Dissolved organic matter, particularly humic acid (HA), was widely present in natural water bodies. The effect of different concentrations of HA on the removal of TC by Fe-GMC/PMS was explored (<xref ref-type="sec" rid="s10">Supplementary Figure S4D</xref>). The ability of carbon materials to catalyze PMS and free radical generation is reduced because HA occupies the active sites on the carbon materials. Furthermore, HA formed stable complexes with Fe<sup>2&#x2b;</sup> ions. This complexation hampered the release of Fe<sup>2&#x2b;</sup>, thereby impeding electron transfer and radical generation pathways (<xref ref-type="bibr" rid="B18">Li et al., 2024</xref>).<disp-formula id="e1">
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</p>
<p>The reusability of a catalyst is a crucial element in the overall assessment of its efficacy in practical applications, particularly when the financial implications are taken into account. The objective of this study was to conduct five recycling experiments under optimal conditions to further explore the stability of Fe-GMC. <xref ref-type="fig" rid="F6">Figure 6A</xref> demonstrates that following five cycles of recycling, the Fe-GMC composites exhibit a residual TC removal rate of approximately 75%, indicative of exceptional material stability and recycling performance. This provides a robust economic foundation for practical applications. <xref ref-type="fig" rid="F6">Figure 6B</xref> illustrates the leaching rate of Fe ions across each cycle of the experiment. It can be observed that the leaching of each cycle is less than 0.6&#xa0;mg/L, a figure that is considerably lower than the European standard of 2&#xa0;mg/L. Moreover, the Fe-GMC/PMS catalyst was evaluated in comparison to other catalysts, and the system demonstrated remarkable stability and catalytic efficacy (<xref ref-type="table" rid="T1">Table 1</xref>). Moreover, the mineralization rate of TC by the system was examined. As illustrated in <xref ref-type="sec" rid="s10">Supplementary Figure S5</xref>, the total organic carbon (TOC) of TC remained at 1.6&#xa0;mg/L after 60&#xa0;min, and the mineralization rate was 73.37%, indicating an effective TC removal rate.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>
<bold>(A)</bold> Reusability of Fe-GMC/PMS for TC removal over five cycles and <bold>(B)</bold> Fe ion leakage during each cycle.</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g006.tif"/>
</fig>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Comparison of Fe-GMC with other reported catalysts for contaminant degradation in different systems.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Catalyst</th>
<th align="left">Pollutant</th>
<th align="left">Property</th>
<th align="left">Recyclability</th>
<th align="left">Main ROS or site</th>
<th align="left">Reference</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Magnetic biochar (MBC)</td>
<td align="left">Tetracycline</td>
<td align="left">80% in 120&#xa0;min</td>
<td align="left">Four times recycled with 55% removal</td>
<td align="left">O<sub>2</sub>
<sup>&#x2022;-</sup>, &#x2022;OH, SO<sub>4</sub>
<sup>&#x2022;-</sup>, and <sup>1</sup>O<sub>2</sub>
</td>
<td align="left">
<xref ref-type="bibr" rid="B20">Luo et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">D-FeTiO3/C</td>
<td align="left">Tetracycline</td>
<td align="left">90% in 120&#xa0;min</td>
<td align="left">Five times recycled with 70% removal</td>
<td align="left">O<sub>2</sub>
<sup>&#x2022;-</sup>, &#x2022;OH, SO<sub>4</sub>
<sup>&#x2022;-</sup>, and <sup>1</sup>O<sub>2</sub>
</td>
<td align="left">
<xref ref-type="bibr" rid="B21">Luo et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">Goethite/biochar</td>
<td align="left">Tetracycline</td>
<td align="left">66% in 60&#xa0;min</td>
<td align="left">Three times recycled with 55% removal</td>
<td align="left">&#x2022;OH, SO<sub>4</sub>
<sup>&#x2022;-</sup>, and <sup>1</sup>O<sub>2</sub>
</td>
<td align="left">
<xref ref-type="bibr" rid="B11">Guo et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Fe-GMC</td>
<td align="left">Tetracycline</td>
<td align="left">81% in 60&#xa0;min</td>
<td align="left">Five times recycled with 55% removal</td>
<td align="left">&#x2022;OH</td>
<td align="left">This work</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>To gain a more detailed understanding of the reusability properties of Fe-GMC, the TEM, XPS, and XRD patterns of the Fe-GMC material were compared before and after five cycles of the reaction. TEM (<xref ref-type="sec" rid="s10">Supplementary Figures S6A, B</xref>) demonstrated that the composite material retained its structural integrity after five cycles of the reaction, with a substantial number of Fe nanoparticles still encapsulated within the material. XPS (<xref ref-type="sec" rid="s10">Supplementary Figures S6C, D</xref>) revealed that a portion of Fe(II) remained within the material, a finding that was corroborated by XRD (<xref ref-type="sec" rid="s10">Supplementary Figure S6E</xref>). The intensity of the Fe&#x2083;C and Fe&#x2083;O&#x2084; peaks exhibited a slight reduction following the reaction compared to unreacted Fe-GMC. This observation can be attributed to the decline in the removal rate observed after five cycles. The findings of this study illustrate the favorable stability and reusability of the material.</p>
</sec>
</sec>
<sec id="s3-3">
<title>3.3 Catalytic degradation mechanism</title>
<p>To identify the mechanism of TC degradation in the Fe-GMC/PMS system, the contribution of related radicals in the system was differentiated by different quenching experiments (<xref ref-type="bibr" rid="B10">Guangfei et al., 2020</xref>). According to previously reported studies, alcohols with &#x3b1;-H (such as Et-OH) are capable of reacting with both <sup>&#x2022;</sup>OH and SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup>. TBA was employed as a radical <sup>&#x2022;</sup>OH scavenger. L-histidine (L-His) was used to prove the existence of <sup>1</sup>O<sub>2</sub>, and p-benzoquinone (p-BQ) was used to prove the existence of O<sub>2</sub>
<sup>&#x2022;&#x2212;</sup> radicals (<xref ref-type="bibr" rid="B19">Luo et al., 2020</xref>). As shown in <xref ref-type="fig" rid="F7">Figure 7A</xref>, the reaction was significantly inhibited when Et-OH was added to the system. Only 27.7% of TC was removed within 60&#xa0;min. Furthermore, TBA also showed an intense inhibition on TC degradation, and the removal rate was 37.9%. In addition, to consider the possible presence of <sup>1</sup>O<sub>2</sub> and O<sub>2</sub>
<sup>&#x2022;&#x2212;</sup> in the system, p-BQ and L-His were separately added into the solution, both of which showed slight inhibitions on the oxidation process. Furthermore, p-BQ and L-His were added to the solution to verify the presence of <sup>1</sup>O<sub>2</sub> and O<sub>2</sub>
<sup>&#x2022;&#x2212;</sup>, respectively, which did not show any inhibition of TC degradation. These results indicated that SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> and <sup>&#x2022;</sup>OH were involved in the activation of PMS, and <sup>&#x2022;</sup>OH was the main contributor. In general, due to the acidic environment, <sup>&#x2022;</sup>OH should not theoretically dominate in the Fe-GMC/PMS systems.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Identification of active species and possible degradation mechanism. <bold>(A)</bold> Impact of different quenchers on the TC degradation (Et-OH, TBA, L-His, and p-BQ) and <bold>(B)</bold> EPR spectra. Experiment conditions: 0.20&#xa0;g/L catalyst, 10&#xa0;mg/L TC, 1&#xa0;mM PMS, initial pH &#x3d; 3.01, and 30&#xb0;C.</p>
</caption>
<graphic xlink:href="fenvs-12-1467797-g007.tif"/>
</fig>
<p>Fe(IV) has been reported as an emerging and powerful oxidant with higher selectivity compared to SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> and <sup>&#x2022;</sup>OH(<xref ref-type="bibr" rid="B44">Wang et al., 2022</xref>). To further verify the generated radicals in the degradation reaction, an ESR test was coupled with 5,5-dimethylpyrroline (DMPO) and 2,2,6,6-tetramethyl-4-piperidinol (TEMP) as a spin trappers. In <xref ref-type="fig" rid="F7">Figure 7B</xref>, the representative signals of 1:2:2:1 were observed, which represented DMPO-OH adducts. The formation of DMPO-<sup>&#x2022;</sup>OH adducts may also result from the formation of Fe(IV) to transform DMPO. Since the DMPO-SO<sub>4</sub>
<sup>&#x2022;&#x2212;</sup> adduct can translate to DMPO-OH adduct, the DMPO-SO<sub>4</sub>
<sup>&#x2022;</sup>- adduct signal was not detected (<xref ref-type="bibr" rid="B37">Timmins Graham S et al., 1999</xref>). In addition, no TEMP-<sup>1</sup>O<sub>2</sub> and DMPO-O<sub>2</sub>
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<p>Furthermore, we postulated the reaction mechanism underlying the removal of TC by &#x2022;OH radicals. It is established that the TCs are susceptible to attack by reactive radicals such as &#x2022;OH, O<sub>2</sub>
<sup>&#x2022;-</sup>, and <sup>1</sup>O<sub>2</sub> because they have three high-electron-density functional groups, namely, double bonds, phenolic groups, and amino groups. <xref ref-type="sec" rid="s10">Supplementary Table S4</xref> (<xref ref-type="bibr" rid="B55">Zhang et al., 2023</xref>) After the attack of &#x2022;OH radical, TC will undergo demethylation and dehydration to produce intermediates 1 and 5 (<xref ref-type="sec" rid="s10">Supplementary Figure S7</xref>), while intermediate 1 in the left pathway will continue to dehydration to produce 2, and the central carbon chain of intermediate 2 will break to produce intermediates 3 and 4, which will ultimately be degraded to CO<sub>2</sub> and H<sub>2</sub>O. Meanwhile, in the right pathway, &#x2022;OH will attack the para or ortho position of the phenol ring of 2, and demethylation occurs to yield intermediate 6, which will undergo the reaction of ring-opening and de-hydroxylation to obtain intermediate 7, which ultimately produces CO<sub>2</sub> and H<sub>2</sub>O.</p>
<p>To confirm the charge transfer between the catalysts, we conducted electrochemical tests on both GMC and Fe-GMC materials, as illustrated in <xref ref-type="sec" rid="s10">Supplementary Figure S8</xref>. Upon the addition of PMS at 100&#xa0;s, a notable alteration in current was observed for both GMC and Fe-GMC, indicative of electron transfer between the catalyst and PMS. Concurrently, the addition of TC to the system at 200&#xa0;s resulted in a notable decline in the current of the Fe-GMC material compared to the GMC material. This observation suggests that the Fe-GMC/PMS system facilitated the acceleration of electron transfer.</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>In summary, the biochar carrier Fe-GMC synthesized can efficiently degrade TC in water under PMS catalysis. This study utilized goat manure and FeSO<sub>4</sub>&#xb7;7H<sub>2</sub>O as sustainable feedstocks for composite catalysts and revealed the mechanism of TC degradation. The characterization results indicate that the Fe-GMC surface exhibits a porous structure, and the BET characterization results demonstrate that Fe-GMC possesses a substantial specific surface area of 416&#xa0;m<sup>2</sup>/g. The TEM, XPS, and XRD results demonstrate that Fe was successfully loaded and existed as Fe&#x2083;O&#x2084;. In the Fe-GMC/PMS system, the primary degradation reaction is the &#x2022;OH radical pathway, with charge transfer facilitated between Fe-GMC/PMS and TC. Moreover, the conditional experiments demonstrate that Fe-GMC exhibits excellent practical applicability and recycling potential. This work realizes the resource utilization of sheep manure waste and provides a new idea for removing antibiotics in the water environment, with excellent application prospects.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The datasets presented in this study can be found in online repositories. The names of the repository/repositories and accession number(s) can be found in the article/<xref ref-type="sec" rid="s10">Supplementary Material</xref>.</p>
</sec>
<sec sec-type="author-contributions" id="s6">
<title>Author contributions</title>
<p>LF: writing&#x2013;original draft, writing&#x2013;review and editing, and data curation. QX: conceptualization and writing&#x2013;original draft. YL: data curation and writing&#x2013;review and editing. SZ: formal analysis and writing&#x2013;review and editing. HL: investigation and writing&#x2013;review and editing. SL: data curation and writing&#x2013;review and editing. XL: conceptualization, writing&#x2013;original draft, and writing&#x2013;review and editing.</p>
</sec>
<sec sec-type="funding-information" id="s7">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research, authorship, and/or publication of this article. The authors gratefully acknowledge the financial support provided by the Guangxi Key Research and Development Plan Project of China (grant no. Gui Ke AB21220044) and the Geological Survey Project of the China Geological Survey (grant nos DD20221758 and DD20230081).</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s9">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
<sec id="s10">
<title>Supplementary material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/fenvs.2024.1467797/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fenvs.2024.1467797/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="Supplementaryfile1.docx" id="SM1" mimetype="application/docx" xmlns:xlink="http://www.w3.org/1999/xlink"/>
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