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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">1393609</article-id>
<article-id pub-id-type="doi">10.3389/fenvs.2024.1393609</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>Synergy of carboxymethyl cellulose stabilized nanoscale zero-valent iron and <italic>Penicillium oxalicum</italic> SL2 to remediate Cr(VI) contaminated site soil</article-title>
<alt-title alt-title-type="left-running-head">Pan 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.2024.1393609">10.3389/fenvs.2024.1393609</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Pan</surname>
<given-names>Siyi</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Tong</surname>
<given-names>Jianhao</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Luo</surname>
<given-names>Yating</given-names>
</name>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Pang</surname>
<given-names>Jingli</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
<role content-type="https://credit.niso.org/contributor-roles/supervision/"/>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Zhang</surname>
<given-names>Haonan</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
<role content-type="https://credit.niso.org/contributor-roles/visualization/"/>
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<contrib contrib-type="author">
<name>
<surname>Wang</surname>
<given-names>Jing</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
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</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Shi</surname>
<given-names>Jiyan</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2668911/overview"/>
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<aff>
<institution>Department of Environmental Engineering</institution>, <institution>College of Environmental and Resource Science</institution>, <institution>Zhejiang University</institution>, <addr-line>Hangzhou</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/2346884/overview">Weichun Yang</ext-link>, Central South 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/2119202/overview">Ying-heng Fei</ext-link>, Guangzhou University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2005271/overview">Qi Wang</ext-link>, Zhejiang Gongshang University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Jiyan Shi, <email>shijiyan@zju.edu.cn</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>17</day>
<month>06</month>
<year>2024</year>
</pub-date>
<pub-date pub-type="collection">
<year>2024</year>
</pub-date>
<volume>12</volume>
<elocation-id>1393609</elocation-id>
<history>
<date date-type="received">
<day>29</day>
<month>02</month>
<year>2024</year>
</date>
<date date-type="accepted">
<day>09</day>
<month>05</month>
<year>2024</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2024 Pan, Tong, Luo, Pang, Zhang, Wang and Shi.</copyright-statement>
<copyright-year>2024</copyright-year>
<copyright-holder>Pan, Tong, Luo, Pang, Zhang, Wang and Shi</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>Nano zero-valent iron (nZVI) acting as a high-cost disposable material in soil Cr(VI) remediation faces significant challenges due to its easily oxidizable nature and biological toxicity. In addressing this issue, the present study undertook the synthesis of a series of modified nZVI and combined the selected material with Cr(VI)-resistant filamentous fungus <italic>Penicillium oxalicum</italic> SL2 for real-site chromium pollution remediation. Adsorption experiments demonstrated that the inclusion of carboxymethyl cellulose (CMC) significantly enhanced the adsorption capacity of nZVI for Cr(VI) by 19.3% (from 73.25 to 87.4&#xa0;mg/L), surpassing both biochar (37.42&#xa0;mg/L) and bentonite modified nZVI (48.03&#xa0;mg/L). Characterization results validated the successful synthesis of the nano composite material. Besides, oxidative stress analysis explained the unique detoxification effects of CMC on SL2, acting as a free radical scavenger and isolating layer. In real-sites soil remediation experiments, a low dosage (0.4% w/w) of nZVI/CMC@SL2 (CMC modified nZVI combined with SL2) exhibited an impressive reduction of over 99.5% in TCLP-Cr(VI) and completely transformed 18% of unstable Cr to stable forms. Notably, nZVI/CMC demonstrated its capability to facilitate SL2 colonization in highly contaminated soil and modulate the microbial community structure, enriching chromium-removing microorganisms. In summary, the synergistic system of nZVI/CMC@SL2 merges as a cost-effective and efficient approach for Cr(VI) reduction, providing meaningful insights for its application in the remediating contaminated site soils.</p>
</abstract>
<kwd-group>
<kwd>nZVI stabilization</kwd>
<kwd>carboxymethyl cellulose</kwd>
<kwd>Cr(VI) reduction</kwd>
<kwd>soil microcommunity</kwd>
<kwd>
<italic>Penicillium oxalicum</italic> SL2</kwd>
</kwd-group>
<contract-sponsor id="cn001">National Key Research and Development Program of China<named-content content-type="fundref-id">10.13039/501100012166</named-content>
</contract-sponsor>
<contract-sponsor id="cn002">National Natural Science Foundation of China<named-content content-type="fundref-id">10.13039/501100001809</named-content>
</contract-sponsor>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Soil Processes</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>The extensive use of chromium in industrial processes, such as electroplating, chromate production, and leather tanning (<xref ref-type="bibr" rid="B45">Ma et al., 2024</xref>), due to its excellent corrosion resistance and metallic luster, has resulted in its widespread release into the soil. China&#x2019;s 2014 nationwide soil pollution survey revealed a 1.1% excess of Cr pollution beyond national standards, with particularly severe cases in industrial zones. Recognized as a class &#x201c;A&#x201d; carcinogen by the United States Environmental Protection Agency (EPA) (<xref ref-type="bibr" rid="B8">Chen et al., 2020</xref>) hexavalent chromium poses severe health risks through long-term exposure and food chain transmission which will cause great harm to human health and cause various diseases (<xref ref-type="bibr" rid="B20">Fu et al., 2023</xref>). Therefore, the urgent remediation of Cr(VI) contaminated site soil is imperative.</p>
<p>The main remediation method involves reducing Cr(VI) to Cr(III) (<xref ref-type="bibr" rid="B16">Du et al., 2023</xref>; <xref ref-type="bibr" rid="B71">Wang et al., 2024</xref>). Recently, because of its high reactivity and reduction capability, nano zero-valent iron (nZVI) has gained widespread use in research focusing on the remediation of Cr(VI) contaminated soil (<xref ref-type="bibr" rid="B82">Yang et al., 2021</xref>). However, its application potential is greatly hindered by challenges such as aggregation (<xref ref-type="bibr" rid="B54">Phenrat et al., 2007</xref>) and biotoxicity (<xref ref-type="bibr" rid="B2">Auffan et al., 2008</xref>; <xref ref-type="bibr" rid="B84">Ye et al., 2021</xref>). To address these issues, numerous studies have been conducted based on the surface modification of nZVI such as biochar (<xref ref-type="bibr" rid="B62">Su et al., 2016</xref>), chitosan (<xref ref-type="bibr" rid="B39">Liu et al., 2010</xref>), hydrophobic stabilizers such as carboxymethyl cellulose (CMC) (<xref ref-type="bibr" rid="B59">Raychoudhury et al., 2012</xref>), poly acrylic acid (<xref ref-type="bibr" rid="B32">Laumann et al., 2014</xref>) or starch (<xref ref-type="bibr" rid="B72">Wang et al., 2014</xref>). These materials can impede the gathering and oxidation of nZVI (<xref ref-type="bibr" rid="B1">Ambika et al., 2016</xref>), mitigate its biotoxicity (<xref ref-type="bibr" rid="B7">Chen et al., 2012</xref>) and enhance particle mobility in the soil (<xref ref-type="bibr" rid="B6">Chekli et al., 2016</xref>). However, the application dosages of these materials were often relatively high (<xref ref-type="sec" rid="s10">Supplementary Table S1</xref>), leading to elevated remediation costs and potential alterations to the original physicochemical properties of the soil. Therefore, the identification of a low-dosage, efficient, and environmentally friendly remediation strategy is of paramount importance.</p>
<p>Beyond chemical remediation approaches, microbial remediation, regarded as an environmentally sustainable and economically feasible method for soil contamination control is extensively researched. Certain bacteria, including QY-1, extremely thermophilic bacterium <italic>(Caldicellulosiruptor saccharolyticus)</italic>, <italic>Shewanella oneidensis</italic> MR-1 as well as sulfate-reducing bacteria (SRB) and iron reducing bacteria (IRB) (<xref ref-type="bibr" rid="B53">Peng et al., 2015</xref>; <xref ref-type="bibr" rid="B3">Bai et al., 2018</xref>; <xref ref-type="bibr" rid="B24">Hou et al., 2020</xref>; <xref ref-type="bibr" rid="B44">Ma et al., 2021</xref>; <xref ref-type="bibr" rid="B35">Lin et al., 2022</xref>) exhibited ability of Cr(VI) reduction. Bacteria can mitigate the toxicity of heavy metals through various mechanisms such as enzymatic detoxification and intracellular isolation (<xref ref-type="bibr" rid="B5">Bruins et al., 2000</xref>), <italic>etc.</italic> There are also studies that amalgamate bacteria with nZVI to address chromium contamination (<xref ref-type="bibr" rid="B64">Tan et al., 2020</xref>). Nevertheless, their tolerance to Cr(VI) are relatively lower, such as <italic>Arthrobacter</italic> sp., <italic>Bacillus</italic> sp. and <italic>Streptomyces</italic> sp. (<xref ref-type="bibr" rid="B48">Megharaj et al., 2003</xref>; <xref ref-type="bibr" rid="B18">Elangovan et al., 2006</xref>; <xref ref-type="bibr" rid="B49">Morales et al., 2007</xref>) (Minimum Inhibitory Concentration range, MIC, range from 80 to 500&#xa0;mg/L), the survival and remediation capabilities in actual highly contaminated site soil remain ambiguous. Contaminated site soil, characterized by diverse and elevated heavy metal concentrations (<xref ref-type="bibr" rid="B75">Wu et al., 2018</xref>; <xref ref-type="bibr" rid="B63">Sun et al., 2022</xref>) and limited organic matter, imposes constraints on microbial growth, underscoring the critical importance of identifying suitable microorganisms.</p>
<p>Fungi, despite demonstrating high tolerance to heavy metals and thriving in low-nutrient environments (<xref ref-type="bibr" rid="B8">Chen et al., 2020</xref>), have received comparatively less attention in remediation studies. <italic>Penicillium oxalicum</italic> SL2, a filamentous fungus with high resistance to Cr(VI) (MIC greater than 1,000&#xa0;mg/L Cr(VI)), was isolated in our antecedent study (<xref ref-type="bibr" rid="B41">Long et al., 2018</xref>), it could grow rapidly and completely remove 96.1&#xa0;mg/L Cr(VI) in electroplating wastewater after inoculation for 96&#xa0;h. Strain SL2 produced acidic metabolites such as LMWOAs playing important role in the mobilization of chromium and improving bioleaching (<xref ref-type="bibr" rid="B40">Long et al., 2023</xref>). Its mechanisms for heavy metal pollution abatement encompass the production of small organic acids, extracellular absorption, bioprecipitation, and transmembrane transport (<xref ref-type="bibr" rid="B67">Tong et al., 2023</xref>). Moreover, SL2 exhibited marked iron precipitate and Fe(II) regeneration capabilities, rendering its amalgamation with nZVI a promising avenue for remediation.</p>
<p>To the best of our knowledge, there is currently no study on the combination of nZVI/CMC and anti-chromium fungus SL2 for the remediation of high Cr(VI) polluted sites soil (Cr(VI) ranging from 348 to 1,305&#xa0;mg/kg) (<xref ref-type="bibr" rid="B34">Li et al., 2023</xref>). Moreover, previous studies often simulated pollution with lower Cr(VI) concentrations (<xref ref-type="sec" rid="s10">Supplementary Table S1</xref>), significantly differing from the complex conditions found in real contaminated soils. Hence, the overall objective of this study was to demonstrate the effect and practicability of the integrate remediation of Cr(VI) polluted site soil by using the stabilized nZVI with SL2. Consequently, this study is specifically structured as follows: (1) synthesize various stabilized nZVI composites and determine their efficacy in removing Cr(VI) in liquid; (2) investigate the biocompatibility of stabilized nZVI with SL2 for Cr(VI) removal from aqueous solutions and determinate the optimal combination; (3) explore the detoxification effect and immobilization of Cr(VI) in soil by the developed composite system consisting of nZVI/CMC and microorganism and elucidating their potential mechanisms; (4) evaluate the impact of these materials on soil microecology. This study aims to provide a scientific basis and technological support for the practical application of nZVI/CMC@SL2 in the remediation of Cr(VI) contaminated site soil.</p>
</sec>
<sec id="s2" sec-type="materials|methods">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Preparation of stabilized nZVI</title>
<p>The sample was prepared by sieving pine powder through a 100-mesh, washed with deionized water to remove impurities, and subsequently dried. Under the protection of nitrogen gas, it underwent thermal decomposition at a heating rate of 10&#xb0;C/min until reaching 600&#xb0;C for a duration of 2&#xa0;h, resulting in the sample referred to as C. A solution containing 5.40&#xa0;g FeCl<sub>3</sub>&#xb7;H<sub>2</sub>O dissolved in 100&#xa0;mL oxygen-free water with 30% anhydrous ethanol was prepared. Different loading materials and concentrations of nano zero-valent iron (nZVI) were synthesized by adding 1% carboxymethyl cellulose (CMC), varying quantities of biochar or bentonite. The solute mixture was thoroughly mixed by shaking at room temperature and at a speed of 150 r/min for 24&#xa0;h. Subsequently, under a nitrogen atmosphere, sodium borohydride (NaBH<sub>4</sub>) weighing 3.04&#xa0;g was slowly added dropwise into the above mixture to form nZVI stabilized by CMC, biochar or bentonite (<xref ref-type="sec" rid="s10">Supplementary Text S1</xref> and <xref ref-type="sec" rid="s10">Figure S1</xref>), named as nZVI/CMC, nZVI/C, nZVI/B, respectively.</p>
</sec>
<sec id="s2-2">
<title>2.2 Adsorption experiments and material characterization</title>
<p>To assess the removal efficiency of stabilized nZVI for Cr(VI) in aqueous solution, a concentration of 2&#xa0;g/L of the aforementioned material was added to a solution containing Cr(VI) with an initial concentration of 200&#xa0;mg/L. The reaction was conducted in a reactor operating at a rotation speed of 150&#xa0;rpm and a temperature of 25&#xb0;C for a duration of 72&#xa0;h. Supernatant was regularly collected and filtered through a 0.22&#xa0;&#xb5;m filter. The concentration of Cr(VI) in the filtrate was determined by employing the diphenyl-carbohydrazide spectrophotometric method. Subsequently, several stable materials with the best effect were selected to establish isothermal adsorption experiments with initial concentration gradients of 10, 20, 50, 100, 200, 400, and 800&#xa0;mg/L for Cr(VI). Various kinetic models, including the pseudo-first-order model, pseudo-second-order model, Avrami model and intraparticle diffusion model were employed to fit the adsorption process of Cr(VI), along with adsorption isotherm models such as Langmuir, Freundlich and Sips models.</p>
<p>The microstructure of synthesized materials above was imaged by scanning electron microscopy (SEM, Zeiss Sigma500). Also, the products were analyzed by X-ray diffraction (XRD, D8 Advance, Bruker, U.S.A) and data were collected the 2&#x3b8; range from 10 to 90&#xb0;. The functional groups on the surface of the materials were characterized by Fourier Transform Infrared Spectroscopy (FTIR, Thermo Scientific Nicolet iS20). In addition, the species of Cr and Fe on the surface of reaction products were analyzed by X-ray photoelectron spectroscopy (XPS, Escalab 250Xi, UK).</p>
</sec>
<sec id="s2-3">
<title>2.3 Metabolic activity of SL2 suffering from nZVIs and Cr(VI)</title>
<p>To assess the oxidative stress response of SL2 to stable nZVI, 1% spore SL2 suspension (10<sup>7</sup>&#xa0;CFU/mL) and 1&#xa0;g/L different materials (nZVI/B was not measured because of the poor growth of SL2) were introduced into Cr(VI) solution. The mixture was incubated in a shaker at 30&#xb0;C and 150&#xa0;rpm for 2&#xa0;days. After centrifugation, the collected bacterial slurry was analyzed for intracellular ATP, reactive oxygen species (ROS), and glutathione (GSH) levels (<xref ref-type="sec" rid="s10">Supplementary Text S2</xref>) as indicators of the oxidative stress reaction.</p>
</sec>
<sec id="s2-4">
<title>2.4 Remediation of site soil by nZVI/CMC@SL2</title>
<sec id="s2-4-1">
<title>2.4.1 Soil preparation and experimental design</title>
<p>Cr(VI) polluted soil samples were collected from a chromium slag dump site in Inner Mongolia (NM), and an electroplating contamination site in Zhangjiakou, Hebei Province (soil sample with higher and lower Cr(VI) pollution was named ZH and ZL respectively), China. After removing larger impurities, the soil was sieved through a 10-mesh screen, thoroughly mixed, and air-dried, referred to as NM, ZH and ZL, respectively. Soil heavy metal concentration and physicochemical characteristics were shown in <xref ref-type="sec" rid="s10">Supplementary Tables S2, S3</xref>. Candidate nZVI/CMC, exhibiting optimal performance, was chosen for soil remediation. 20&#xa0;g contaminated soil was treated with a 0.4% (w/w) nZVI/CMC addition, 10<sup>7</sup>&#xa0;CFU/g soil of SL2, and deionized water to maintain a 25% moisture level, 25&#xb0;C. Five treatments were set for each soil sample, carried out in triplicate: (1) Control Check; (2) sterile potato dextrose liquid medium (1:4; PDL:H<sub>2</sub>O; v/v); (3) PDL &#x002B; SL2; (4) nZVI/CMC; (5) PDL &#x002B; nZVI/CMC@SL2. The soil and additives were thoroughly mixed. Samples were collected on days 0, 3, 7, 15, and 30 (<xref ref-type="sec" rid="s10">Supplementary Figure S2</xref>).</p>
</sec>
<sec id="s2-4-2">
<title>2.4.2 Chemical stability of Cr in the soil after remediation</title>
<p>Analysis of five different chromium species in soil was performed using the Tessier sequential extraction method. The extraction solution was filtered through a 0.45&#xa0;&#xb5;m membrane and analyzed using an atomic absorption spectrometer. Additionally, total Cr(VI) in the soil was measured using an alkaline extraction method, leachable Cr(VI) using the TCLP extraction method and Fe(II) concentrations was determined using colorimetric method with 1,10-o-phenanthroline. Detailed extraction and measurement methods can be found in the <xref ref-type="sec" rid="s10">Supplementary Text S3</xref>.</p>
</sec>
<sec id="s2-4-3">
<title>2.4.3 Soil microecology analysis</title>
<p>Fresh soil samples were collected from each pot to evaluate the soil microecology&#x2014;SL2 microbial counts (<xref ref-type="sec" rid="s10">Supplementary Text S4</xref>) and microbial community.</p>
<p>Soil genomic DNA was extracted using E.Z.N.A. Soil DNA Kit (Omega Bio-tek, Inc., United States) following the manual. Concentration and quality of the genomic DNA were checked by NanoDrop 2000 spectrophotometer (Thermo Scientific Inc., United States). The fungal ITS region and the bacterial 16S rRNA genes were amplified using the primer sets ITS1F/ITS2R and 338F/806R (<xref ref-type="bibr" rid="B83">Yao et al., 2017</xref>; <xref ref-type="bibr" rid="B66">Tang et al., 2018</xref>) respectively by PCR system (Applied Biosystems, Inc., United States). The amplicons were sequenced through the Illumina&#x2019;s Miseq PE300 platform (Illumina, Inc., United States). Qualified sequences were clustered into operational taxonomic units (OTUs) at a similarity threshold of 97% use Uparse (<xref ref-type="bibr" rid="B17">Edgar, 2013</xref>) algorithm of Vsearch (v2.7.1) software. Refer to <xref ref-type="sec" rid="s10">Supplementary Text S5</xref> for detailed analytical methods.</p>
</sec>
</sec>
</sec>
<sec id="s3" sec-type="results|discussion">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Adsorption performance of different stabilized nZVI</title>
<sec id="s3-1-1">
<title>3.1.1 Adsorption kinetics</title>
<p>In order to examine the correlation between contact time and the rate of reduction of Cr(VI) by different materials, kinetics investigations were performed with results presented in <xref ref-type="fig" rid="F1">Figure 1</xref>. It could be noticed that Cr(VI) uptake increased within the initial 240&#xa0;min, which might be attribute to the plentiful adsorption sites provided by the loading material and the reduction reaction of nZVI to Cr(VI). Nonetheless, with the gradual occupation of adsorption sites by Cr(VI), the rate of pollutant adsorption increased at a slower pace, reaching equilibrium after 500&#xa0;min.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Kinetic fitting results of pseudo first-order, second-order and Avrami fractional models for Cr(VI) uptake onto stabilized nZVI (inset: intraparticle diffusion model).<bold>(A)</bold> nZVI; <bold>(B&#x2013;D)</bold> nZVI/B with ratio of 1:2, 1:1, 2:1; <bold>(E, F)</bold> nZVI/C with ratio of 1:1, 1:2; <bold>(G)</bold> nZVI/CMC, T &#x003D; 25&#xb0;C, [Cr(VI)] &#x003D; 200&#xa0;mg/L, [Material dosage] &#x003D; 2&#xa0;g/L.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g001.tif"/>
</fig>
<p>To quantitatively evaluate the kinetic process on Cr(VI) uptake by stabilized nZVI, four acknowledged models involving pseudo-first/second-order, Avrami fractional-order as well as intra-particle diffusion models were chosen to analyze the data (<xref ref-type="bibr" rid="B10">Dai et al., 2019</xref>; <xref ref-type="bibr" rid="B56">Qu et al., 2021</xref>; <xref ref-type="bibr" rid="B57">Qu et al., 2022</xref>), the formulas were shown below (Eqs <xref ref-type="disp-formula" rid="e1">1</xref>-<xref ref-type="disp-formula" rid="e4">4</xref>):<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:msup>
<mml:mi mathvariant="bold-italic">e</mml:mi>
<mml:mrow>
<mml:mo>&#x2212;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">k</mml:mi>
<mml:mn mathvariant="bold">1</mml:mn>
</mml:msub>
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</mml:msup>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:mrow>
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<label>(1)</label>
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<mml:mrow>
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<mml:mi mathvariant="bold-italic">t</mml:mi>
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<mml:mo>&#x003D;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msubsup>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
<mml:mn mathvariant="bold">2</mml:mn>
</mml:msubsup>
<mml:msub>
<mml:mi mathvariant="bold-italic">k</mml:mi>
<mml:mn mathvariant="bold">2</mml:mn>
</mml:msub>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>&#x002B;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">k</mml:mi>
<mml:mn mathvariant="bold">2</mml:mn>
</mml:msub>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>
<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:mrow>
<mml:mfenced close="]" open="[" separators="&#x7c;">
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:msup>
<mml:msup>
<mml:mi mathvariant="bold-italic">e</mml:mi>
<mml:mrow>
<mml:mo>&#x2212;</mml:mo>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">k</mml:mi>
<mml:mn mathvariant="bold">3</mml:mn>
</mml:msub>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:msup>
<mml:mi mathvariant="bold-italic">n</mml:mi>
</mml:msup>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>
<disp-formula id="e4">
<mml:math id="m4">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">t</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">k</mml:mi>
<mml:mn mathvariant="bold">4</mml:mn>
</mml:msub>
<mml:msup>
<mml:mi mathvariant="bold-italic">t</mml:mi>
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>/</mml:mo>
<mml:mn mathvariant="bold">2</mml:mn>
</mml:mrow>
</mml:msup>
<mml:mo>&#x002B;</mml:mo>
<mml:mi mathvariant="bold-italic">n</mml:mi>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>in which, <inline-formula id="inf1">
<mml:math id="m5">
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>t</mml:mi>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:mtext>mg</mml:mtext>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">g</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
</inline-formula> express the quantity of Cr(VI) taken up at time t; <inline-formula id="inf2">
<mml:math id="m6">
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:mtext>mg</mml:mtext>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">g</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
</inline-formula> represents the uptake of Cr(VI) adsorbed at equilibrium; kinetic constants associating with different models are <inline-formula id="inf3">
<mml:math id="m7">
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>1</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula>, <inline-formula id="inf4">
<mml:math id="m8">
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula>, <inline-formula id="inf5">
<mml:math id="m9">
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>3</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula> and <inline-formula id="inf6">
<mml:math id="m10">
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>4</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula>. The n (mg/g) is the intercept of intraparticle diffusion model. Values of n give information about the thickness of the boundary layer, the larger intercept the greater is the boundary layer effect (<xref ref-type="bibr" rid="B89">Zhu et al., 2010</xref>).</p>
<p>Standard deviation (SD) and coefficient (<italic>R</italic>
<sup>2</sup>) were used to evaluate the suitability of each model, that was, data with lower SD and higher <italic>R</italic>
<sup>2</sup> indicated superior applicability of the kinetic model. Detail fitting parameters were provided in <xref ref-type="table" rid="T1">Table 1</xref>. As shown, Avrami fractional-order model showed the highest <italic>R</italic>
<sup>2</sup> value (0.9981) among these models, demonstrated to present the best appropriateness for depicting the uptake performance for Cr(VI), revealing that there were multiple kinetics during the binding processes of Cr(VI) onto nZVI/CMC (<xref ref-type="bibr" rid="B57">Qu et al., 2022</xref>). In addition, the <italic>R</italic>
<sup>2</sup> (0.9615) of the pseudo-second-order is also higher than that of the pseudo-first-order model (0.8949), indicating that the rate-limiting step during the reaction was chemical adsorption involving electron exchange between adsorbent and adsorbate, rather than physical diffusion (<xref ref-type="bibr" rid="B43">Lyu et al., 2017</xref>). According to the intra-particle diffusion model consequences (insets of <xref ref-type="fig" rid="F1">Figure 1G</xref>), two stages were involved in Cr(VI) uptake nZVI/CMC, intraparticle diffusion and external surface binding. Besides, both of the fitting curves deviated from the base point (<italic>n</italic> &#x003D; 26.16), which suggested that the intraparticle diffusion was not the rate-controlling step in Cr(VI) uptake process, but the boundary layer diffusion controlled the adsorption to some degree.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Kinetic model parameters for the uptake of Cr(VI) onto stabilized nZVI.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center" rowspan="2">Material</th>
<th align="center" colspan="5">Pseudo-first-order model</th>
<th align="center" colspan="2">Pseudo-second-order model</th>
<th align="center" colspan="6">Avrami fractional-order model</th>
</tr>
<tr>
<th align="center">q<sub>e</sub> (mg/g)</th>
<th align="center">k<sub>1</sub> (min<sup>-1</sup>)</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
<th align="center">SD</th>
<th align="center">q<sub>e</sub> (mg/g)</th>
<th align="center">k<sub>2</sub> (g mg<sup>&#x2212;1</sup> min<sup>&#x2212;1</sup>)</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
<th align="center">SD</th>
<th align="center">q<sub>e</sub> (mg/g)</th>
<th align="center">k<sub>3</sub> (min<sup>-1</sup>)</th>
<th align="center">n</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
<th align="center">SD</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">
<bold>nZVI</bold>
</td>
<td align="center">52.65</td>
<td align="center">0.0146</td>
<td align="center">0.8822</td>
<td align="center">3.50</td>
<td align="center">58.07</td>
<td align="center">0.0003</td>
<td align="center">0.9297</td>
<td align="center">3.47</td>
<td align="center">73.25</td>
<td align="center">0.0025</td>
<td align="center">0.3771</td>
<td align="center">0.9452</td>
<td align="center">21.29</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/C(1:1)</bold>
</td>
<td align="center">45.65</td>
<td align="center">0.0192</td>
<td align="center">0.9755</td>
<td align="center">1.25</td>
<td align="center">46.75</td>
<td align="center">0.0008</td>
<td align="center">0.9290</td>
<td align="center">0.05</td>
<td align="center">46.81</td>
<td align="center">0.0166</td>
<td align="center">0.7340</td>
<td align="center">0.9842</td>
<td align="center">1.27</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/C(2:1)</bold>
</td>
<td align="center">37.36</td>
<td align="center">0.0182</td>
<td align="center">0.9599</td>
<td align="center">1.98</td>
<td align="center">38.77</td>
<td align="center">0.0006</td>
<td align="center">0.9622</td>
<td align="center">2.12</td>
<td align="center">37.42</td>
<td align="center">0.0175</td>
<td align="center">0.9116</td>
<td align="center">0.9605</td>
<td align="center">2.20</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/B(1:1)</bold>
</td>
<td align="center">55.72</td>
<td align="center">0.0249</td>
<td align="center">0.9432</td>
<td align="center">2.20</td>
<td align="center">59.51</td>
<td align="center">0.0005</td>
<td align="center">0.9596</td>
<td align="center">2.24</td>
<td align="center">56.99</td>
<td align="center">0.0220</td>
<td align="center">0.7242</td>
<td align="center">0.9505</td>
<td align="center">2.57</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/B(1:2)</bold>
</td>
<td align="center">46.51</td>
<td align="center">0.0358</td>
<td align="center">0.9730</td>
<td align="center">1.14</td>
<td align="center">49.13</td>
<td align="center">0.0011</td>
<td align="center">0.9904</td>
<td align="center">0.80</td>
<td align="center">48.03</td>
<td align="center">0.0318</td>
<td align="center">0.5992</td>
<td align="center">0.9826</td>
<td align="center">1.24</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/B(2:1)</bold>
</td>
<td align="center">38.60</td>
<td align="center">0.0162</td>
<td align="center">0.8281</td>
<td align="center">2.81</td>
<td align="center">41.67</td>
<td align="center">0.0005</td>
<td align="center">0.9033</td>
<td align="center">2.59</td>
<td align="center">61.38</td>
<td align="center">0.0012</td>
<td align="center">0.2865</td>
<td align="center">0.9733</td>
<td align="center">25.70</td>
</tr>
<tr>
<td align="center">
<bold>nZVI/CMC</bold>
</td>
<td align="center">70.28</td>
<td align="center">0.0244</td>
<td align="center">0.8949</td>
<td align="center">3.66</td>
<td align="center">75.30</td>
<td align="center">0.0004</td>
<td align="center">0.9615</td>
<td align="center">2.67</td>
<td align="center">87.42</td>
<td align="center">0.0076</td>
<td align="center">0.3284</td>
<td align="center">0.9981</td>
<td align="center">3.02</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s3-1-2">
<title>3.1.2 Adsorption isotherms</title>
<p>In order to investigate the effect of Cr(VI) concentration gradient on the adsorption capacity of stabilized nZVI, the interaction between them was quantitatively described using isothermal adsorption.</p>
<p>Three famous isotherm models including Langmuir, Freundlich and Sips models were then applied for fitting the uptake results (Eqs <xref ref-type="disp-formula" rid="e5">5</xref>-<xref ref-type="disp-formula" rid="e7">7</xref>), which are expressed as:<disp-formula id="e5">
<mml:math id="m11">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">max</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">K</mml:mi>
<mml:mi mathvariant="bold-italic">L</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">C</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>&#x002B;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">K</mml:mi>
<mml:mi mathvariant="bold-italic">L</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">C</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(5)</label>
</disp-formula>
<disp-formula id="e6">
<mml:math id="m12">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">K</mml:mi>
<mml:mi mathvariant="bold-italic">F</mml:mi>
</mml:msub>
<mml:msubsup>
<mml:mi mathvariant="bold-italic">C</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>/</mml:mo>
<mml:msub>
<mml:mi mathvariant="bold-italic">n</mml:mi>
<mml:mi mathvariant="bold-italic">F</mml:mi>
</mml:msub>
</mml:mrow>
</mml:msubsup>
</mml:mrow>
</mml:math>
<label>(6)</label>
</disp-formula>
<disp-formula id="e7">
<mml:math id="m13">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
<mml:mo>&#x003D;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">q</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
<mml:msup>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">K</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">C</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">m</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
</mml:msup>
</mml:mrow>
<mml:mrow>
<mml:mn mathvariant="bold">1</mml:mn>
<mml:mo>&#x002B;</mml:mo>
<mml:msup>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">K</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi mathvariant="bold-italic">C</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">m</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
</mml:msup>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(7)</label>
</disp-formula>in which, the maximum adsorbing quantity of Cr(VI) represented by <inline-formula id="inf7">
<mml:math id="m14">
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi mathvariant="italic">max</mml:mi>
</mml:msub>
<mml:mrow>
<mml:mfenced close=")" open="(" separators="&#x7c;">
<mml:mrow>
<mml:mtext>mg</mml:mtext>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">g</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
</inline-formula>; K<sub>L</sub>, K<sub>F</sub> and n<sub>F</sub> respectively involve the Langmuir coefficient, Freundlich coefficient and Freundlich intensity parameters; K<sub>S</sub> and m<sub>S</sub> are the identical Sips heterogeneity divisors.</p>
<p>In the Langmuir model, adsorption is considered to occur on homogeneous surface. Freundlich is an empirical model for heterogeneous systems. Sips model is a combination of Langmuir and Freundlich (<xref ref-type="bibr" rid="B11">Deng et al., 2020</xref>) capable of modeling both homogeneous and heterogeneous binding surfaces (<xref ref-type="bibr" rid="B85">Zhang et al., 2019</xref>). The results (<xref ref-type="sec" rid="s10">Supplementary Figure S3</xref>; <xref ref-type="sec" rid="s10">Supplementary Table S4</xref>) showed that the Sips model had the best fitting results (<italic>R</italic>
<sup>2</sup> &#x003D; 0.9302), which suggested that adsorption of Cr(VI) was a non-ideal sorption on heterogeneous (<xref ref-type="bibr" rid="B65">Tang et al., 2016</xref>).</p>
<p>In summary, the introduction of CMC significantly enhanced the removal efficiency of Cr(VI) by nZVI, for its maximum adsorption capacity of 87.42&#xa0;mg/g, surpassing the performance of biochar and bentonite. Moreover, the process involved multiple kinetic mechanisms, with boundary layer diffusion identified as the primary rate-limiting step.</p>
</sec>
</sec>
<sec id="s3-2">
<title>3.2 Characterizations of stabilized nZVI</title>
<p>The morphology and size of the newly prepared stabilized nZVI were characterized by scanning electron microscopy (SEM). As depicted in <xref ref-type="fig" rid="F2">Figure 2A</xref>, individual particles of nZVI appeared irregularly spherical and had a diameter of approximately 50&#xa0;nm. After stabilization, the nZVI was uniformly dispersed on the surface of the carriers. The CMC stabilized nZVI exhibited a reticular dendritic structure and smaller particle size, due to the significant influence of high-concentration CMC solution on the nucleation of nZVI. Throughout the nanoscale particle growth process, CMC molecules adhere to the particle surface, impeding further growth through electrostatic repulsion and steric hindrance (<xref ref-type="bibr" rid="B22">He and Zhao, 2007</xref>). This preservation of smaller particle sizes for nZVI results in higher reactivity in reactions. In the EDS maps, each material exhibited elevated levels of Fe element, along with characteristic elements of the loaded material, such as C, Si and Al, indicating successful loading of iron onto the material. It is noteworthy that the iron element content on the surface of nZVI/CMC (89.4%) is significantly higher than that of biochar (53.28%) and bentonite (20.21%). This characteristic enables better preservation of the nZVI properties and facilitates the reactivity towards Cr(VI) reduction. To elucidate the stabilization mechanisms and gain further insight into the various functional groups of the nanoparticles, XRD, FTIR and XPS measurements were carried out on stabilized nanoparticles. From XRD pattern, a distinctive peak corresponding to Fe (0) is observed at 2&#x3b8; &#x003D; 45&#xb0; (<xref ref-type="bibr" rid="B4">Bian et al., 2021</xref>; <xref ref-type="bibr" rid="B87">Zhou et al., 2022</xref>). The broad peak signified the body-centered cubic (bcc) Fe (0) crystal lattice plane (110) (<xref ref-type="bibr" rid="B36">Lin et al., 2010</xref>) with a relatively poor crystallinity (<xref ref-type="bibr" rid="B21">Gong et al., 2017</xref>), providing further evidence of the presence of iron in the material in the form of zero-valent iron. The types of surface functional groups on the nanoparticles were qualitatively analyzed using FTIR spectroscopy, the characteristic broad peaks near 3,400&#xa0;cm<sup>&#x2212;1</sup> related to the stretching vibration of -OH (<xref ref-type="bibr" rid="B80">Xu et al., 2020</xref>; <xref ref-type="bibr" rid="B26">Ji et al., 2022</xref>) were observed in all materials, potentially associated with iron hydroxides (<xref ref-type="bibr" rid="B4">Bian et al., 2021</xref>). Additionally, bands corresponding to C&#x003D;O were identified in the range of 1,610&#x2013;1,660&#xa0;cm&#x207b;<sup>1</sup>, those acidic O-containing functional groups were reported to have a great effect on absorption and reduction of Cr(VI) (<xref ref-type="bibr" rid="B69">Wang K. et al., 2020</xref>). Particularly, nZVI/CMC revealed a carboxyl group (-COO) at 1,420&#xa0;cm&#x207b;<sup>1</sup>, suggesting its role as one of the binding sites for Fe. To identify the carboxylate-metal complexation mechanism, the separation of the symmetric and asymmetric stretches [&#x394;&#x3bd; &#x003D; &#x394;(asym) &#x2212; &#x394;(sym)] of the carboxylate group was calculated (<xref ref-type="bibr" rid="B12">Deng et al., 2021</xref>). In the present work, &#x394;&#x3bd; was determined to be 189&#xa0;cm<sup>&#x2212;1</sup> (1,615&#x2013;1,426&#xa0;cm<sup>&#x2212;1</sup>), proved that bidentate bridging was the primary mechanism for binding CMC molecules to Fe nanoparticles, same as the previous research (<xref ref-type="bibr" rid="B23">He et al., 2007</xref>; <xref ref-type="bibr" rid="B36">Lin et al., 2010</xref>). Simultaneously, polydentate ligands were commonly reported to possess stronger chelating affinities compared to monodentate ligands (<xref ref-type="bibr" rid="B61">Su and Puls, 2004</xref>), this structural characteristic enhanced the stability of nZVI/CMC, underlining the increased robustness conferred by the multidentate coordination in this complex. It is noteworthy that oxygen-containing functional groups in the materials, such as C&#x003D;O, -OH and -COO may concurrently contribute electrons, thereby facilitating the reduction of Cr(VI) (<xref ref-type="bibr" rid="B86">Zhao et al., 2022</xref>). The implication is that the O functional groups may play a crucial role as electron transfer stations in the Cr-Fe reaction.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>SEM <bold>(A)</bold>, EDS <bold>(B)</bold>, XRD <bold>(C)</bold>, FTIR <bold>(D)</bold> patterns of stabilized nZVI.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g002.tif"/>
</fig>
<p>Further, XPS was performed for CMC-nZVI before and after Cr(VI) uptake (<xref ref-type="fig" rid="F3">Figure 3</xref>). The XPS spectra before the reaction confirmed the presence of zero-valent iron in the material by a characteristic peak of Fe2p with a binding energy of 706.23&#xa0;eV (<xref ref-type="bibr" rid="B60">Ren et al., 2018</xref>), accounting for 30.21%. Another portion of Fe, likely oxidized upon exposure to air during transportation and storage, formed Fe(II), constituting 69.79% (<xref ref-type="bibr" rid="B81">Yamashita and Hayes, 2008</xref>). After reaction, the peaks corresponding to Fe (0) and Fe(II) disappeared, and a characteristic satellite peak of Fe(III) emerged (<xref ref-type="bibr" rid="B37">Liu et al., 2020</xref>), indicating the complete oxidation of iron in the material to trivalent state. Additionally, the results of the Cr elemental partition spectra revealed that the Cr in the reaction product existed mainly in the valence state of Cr(III), including chromium oxides and hydroxides. Therefore, both Fe (0) and Fe(II) in the material directly serve as electron donors for the reduction of Cr(VI) to Cr(III). Subsequently, these Cr(III) species co-precipitate with Fe<sup>3&#x002B;</sup>, forming Cr<sub>n</sub>Fe<sub>1&#x2212;n</sub> (OH)<sub>3</sub> (<xref ref-type="bibr" rid="B52">Pan et al., 2016</xref>; <xref ref-type="bibr" rid="B84">Ye et al., 2021</xref>). Moreover, upon contact with water, zero-valent iron generated H&#x2a;, which was confirmed to be the predominant reactive species for Cr(VI) reduction (<xref ref-type="bibr" rid="B55">Qian et al., 2014</xref>). Besides, the abundant -OH and -C&#x003D;O groups on CMC play a crucial role as electron donors for the reduction of Cr(VI) (<xref ref-type="bibr" rid="B58">Rajapaksha et al., 2018</xref>; <xref ref-type="bibr" rid="B78">Xu et al., 2019</xref>). In conclusion, the analysis confirmed that the removal of Cr(VI) by nZVI/CMC involved both adsorption and reduction processes, consistent with previous study (<xref ref-type="bibr" rid="B19">Fang et al., 2011</xref>).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>XPS spectra of Fe 2p <bold>(A)</bold> for fresh nZVI/CMC, Fe 2p <bold>(B)</bold> and Cr 2p <bold>(C)</bold> for product after Cr(VI) reduction. [Cr(VI)] &#x003D; 200&#xa0;mg/L, [nZVI/CMC] &#x003D; 2&#xa0;g/L, shanked at 150rpm for 24&#xa0;h at 25&#xb0;C.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g003.tif"/>
</fig>
<p>In summary, the potential electrostatic repulsion and spatial hindrance capabilities of CMC contributed to maintaining the small size of nZVI particles, preventing its easy aggregation. Additionally, the combination of nZVI with CMC was achieved through a more stable bidentate bridging mechanism. Furthermore, it revealed that both Fe (0) and Fe(II) contributed to the reduction of Cr(VI), and the presence of oxygen-containing acidic functional groups suggested the potential for electron donation in the reduction of Cr(VI).</p>
</sec>
<sec id="s3-3">
<title>3.3 Mechanistic implications about CMC detoxifying</title>
<p>Through the assessment of intracellular ATP, GSH, and ROS concentrations, we compared the toxicity of nZVI with different stabilization methods on SL2. ATP, which is known to play a crucial role in cellular metabolism, and its concentration reflects the cellular activity (<xref ref-type="bibr" rid="B68">Tsitonaki et al., 2010</xref>; <xref ref-type="bibr" rid="B74">Wu et al., 2013</xref>). In the experimental group where only SL2 was added, the intracellular ATP content was highest, while the ATP levels significantly decreased in the groups with added materials, indicating a certain toxicity of the materials to SL2, affecting its metabolism. In comparison, the ATP content in the nZVI/CMC experimental group (0.5981&#xa0;&#x3bc;mol/g) was higher than that in the nZVI (0.1655&#xa0;&#x3bc;mol/g) and nZVI/C (0.2532&#xa0;&#x3bc;mol/g) groups, suggesting that the encapsulation of CMC reduced the toxicity of nZVI to SL2.</p>
<p>nZVI exhibits considerable oxidative power in oxygen-containing water (<xref ref-type="bibr" rid="B9">Cheng et al., 2016</xref>). It can be oxidated to generate Fe(II) and H<sub>2</sub>O<sub>2</sub> (<xref ref-type="bibr" rid="B31">Kim et al., 2011</xref>), followed by Fenton reaction to produce highly toxic ROS, such as &#xb7;OH and &#xb7;O<sub>2</sub>
<sup>&#x2212;</sup> (<xref ref-type="bibr" rid="B30">Keenan and Sedlak, 2008</xref>; <xref ref-type="bibr" rid="B79">Xu et al., 2022</xref>). The reaction equations are as follows (Eqs <xref ref-type="disp-formula" rid="e8">8</xref>-<xref ref-type="disp-formula" rid="e11">11</xref>):<disp-formula id="e8">
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<p>Typically, ROS produced at low frequencies are easily neutralized by antioxidant defenses (<xref ref-type="bibr" rid="B51">Nel et al., 2006</xref>). However, excessive ROS can overwhelm cellular antioxidant defenses, causing membrane damage (<xref ref-type="bibr" rid="B77">Xia et al., 2020</xref>), DNA fragmentation (<xref ref-type="bibr" rid="B76">Xia et al., 2019</xref>), and even cellular inactivation (<xref ref-type="bibr" rid="B50">Nel, 2005</xref>). Therefore, cellular oxidative stress responses were further investigated by assessing intracellular levels of ROS and GSH to elucidate the molecular mechanisms. As depicted in the <xref ref-type="fig" rid="F4">Figure 4</xref>, the ROS content in the nZVI-treated group exhibited a dramatic increase (5376 u/s/g), surpassing that of other groups (819, 387 and 361 u/s/g respectively). This elevation suggested a potential dual effect: an increase in endogenous ROS production within the cells and a possible disruption of cell structures (<xref ref-type="bibr" rid="B38">Liu et al., 2011</xref>; <xref ref-type="bibr" rid="B47">Mao et al., 2019</xref>) allowing enhanced penetration of exogenous ROS (<xref ref-type="bibr" rid="B33">Li et al., 2022</xref>), leading to a substantial concentration surge. Simultaneously, the ROS content in the nZVI/CMC and nZVI/C remained comparatively lower, indicating a certain degree of mitigation of cellular oxidative stress reactions. From the perspective of GSH content, CMC-stabilized nZVI generated a significant amount of antioxidant enzymes to shield itself from external oxidation, thereby maintaining lower ROS levels. Although the nZVI-treated group also exhibited elevated GSH levels, it proved insufficient to eliminate the excessive intracellular ROS, resulting in an imbalance in the cellular redox state and compromising the cell&#x2019;s self-protective capacity.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Intracellular levels of <bold>(A)</bold> ATP, <bold>(B)</bold> ROS, <bold>(C)</bold> GSH contents in SL2. Experimental conditions: [SL2] &#x003D; 10<sup>5</sup>&#xa0;CFU/mL, [Cr(VI)] &#x003D; 128&#xa0;mg/L, [stabilized nZVI] &#x003D; 1&#xa0;g/L, 2&#xa0;days.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g004.tif"/>
</fig>
<p>Taken together, the results presented herein indicate a significant enhancement in surface reactivity after CMC-coating, accompanied by a concurrent reduction in the nanomaterial&#x2019;s toxicity towards SL2. This aligns with findings from previous studies conducted on <italic>Escherichia coli</italic> (<xref ref-type="bibr" rid="B88">Zhou et al., 2014</xref>). We hypothesize that the detoxifying effect of this CMC-coating can be attributed to three key factors: Firstly, its role as a scavenger of free radicals, leading to the substantial elimination of &#xb7;OH radicals (&#xb7;OH &#x002B; CMC &#x2192; H<sub>2</sub>O&#x002B; CMC<sup>&#x2a;</sup>) (<xref ref-type="bibr" rid="B29">Joo and Zhao, 2008</xref>); Secondly, its ability to prevent direct contact between SL2 and nZVI particles (<xref ref-type="bibr" rid="B15">Dong et al., 2016</xref>), thereby mitigating oxidative stress reactions in cells and ensuring their viability; Thirdly, CMC can provide an organic carbon source for the growth of SL2 (<xref ref-type="bibr" rid="B73">Wang ZY. et al., 2020</xref>).</p>
</sec>
<sec id="s3-4">
<title>3.4 Soil remediation</title>
<p>In order to investigate the application potential of nZVI/CMC@SL2 in reducing Cr(VI) in soil, we conducted remediation experiments using soils from different types of contaminated sites. The TCLP method was employed to assess the leaching risk of Cr, and the changes in the total Cr(VI) content in the soil were also measured. As shown in <xref ref-type="fig" rid="F5">Figure 5</xref>, after a 3-day remediation period, a significant reduction in TCLP-Cr(VI) was observed in soils amended with 0.4% nZVI/CMC. For NM, ZH, and ZL soils, the Cr(VI) concentration decreased from 28.6, 7.05, and 3.21&#xa0;mg/L to less than 0.5&#xa0;mg/L. However, a slight rebound was observed after 15&#xa0;days, potentially attributed to the oxidation of ferrous species (<xref ref-type="bibr" rid="B70">Wang et al., 2023</xref>), leading to a loss of remediation capacity. Notably, the rebound was less pronounced in the presence of nZVI/CMC@SL2, indicating that the addition of SL2 could inhibit the oxidation of Cr(III). Furthermore, after 30-days remediation, the Fe(II) concentration in the nZVI/CMC@SL2 treatment group was significantly higher than in the group that only received nZVI/CMC (<xref ref-type="fig" rid="F6">Figure 6</xref>). This observation indicated that SL2 could effectively facilitate the reduction of Fe(III) to Fe(II), thereby sustaining the reduction of Cr(VI). According to previous studies, oxalic acid was the most abundant LMWOA produced by strain SL2, and the affinity of oxalic acid with Cr(VI) leads to the expansion of Cr(VI) coordination from tetrahedron to hexahedron, which was preferable for hexahedral species of Cr(III). Oxalic acid was used as a substitute electron donor for Cr(VI) reduction through intramolecular electron transfer reaction, which significantly improved the Cr(VI) removal efficiency (<xref ref-type="bibr" rid="B27">Jiang et al., 2017</xref>). Furthermore, nZVI promoted oxalic acid secretion by SL2, and its generated iron ions could accelerate the reduction of Cr(VI) by oxalic acid (<xref ref-type="bibr" rid="B25">Hug et al., 1997</xref>). Studies have detected the formation of compounds containing Fe(II), Cr(V), and oxalate salts (HCrFeC<sub>4</sub>O<sub>9</sub>)(<xref ref-type="bibr" rid="B42">Luo et al., 2023</xref>), providing crucial evidence for the involvement of Fe(II)/Fe(III) cycling in organic acid reduction of Cr(VI). In the case of the reaction group with only SL2 added, the removal efficiency for Cr(VI) increased with prolonged incubation time within the 30-day period, suggesting that SL2 successfully colonized and persisted in the soil, continuously fixing Cr(VI) through biological processes, in accordance with SL2 biomass change (<xref ref-type="sec" rid="s10">Supplementary Figure S4</xref>). For all nZVI/CMC@SL2 composite systems, the treatment groups achieved a removal efficiency of over 99.5% for TCLP-Cr(VI) after 30 days, and the TCLP-Cr(VI) was lower than the level IV standard of groundwater quality criterion in China (0.1&#xa0;mg/L, GB/T 14848&#x2013;2017). In addition, the total Cr(VI) in the NM soil decreased from over 600&#xa0;mg/kg to 16&#xa0;mg/kg, which was below the regulatory limit for Class I construction land specified in GB36600-2018 (30&#xa0;mg/kg). In heavily contaminated soil (ZH, <xref ref-type="fig" rid="F5">Figure 5E</xref>) with elevated concentrations of Cr(VI), the growth of SL2 was suboptimal due to the toxic effects of Cr(VI), therefore basically did not demonstrate any removal effectiveness against Cr(VI). However, with the addition of nZVI/CMC, the pollutant concentration was reduced to a level conducive to growth. This combination successfully decreased the total Cr(VI) content from around 1,200&#xa0;mg/kg to approximately 300&#xa0;mg/kg within a 30-day period.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>The TCLP <bold>(A&#x2013;C)</bold> and total Cr(VI) <bold>(D&#x2013;F)</bold> concentrations in different soils after diverse treatments, NM <bold>(A, D)</bold>, ZH <bold>(B, E)</bold>, ZL <bold>(C, F)</bold>.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g005.tif"/>
</fig>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Fe(II) concentration in soil after 30-days remediation.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g006.tif"/>
</fig>
<p>This study evaluated sequential extraction procedures for identifying the relative availability of soil-bound heavy metal by partitioning the particulate trace metals into five fractions. The five species have been defined as exchangeable (F1), bound to carbonates (F2), Fe-Mn oxides-bound (F3), organic matter-bound (F4) and residual (F5). <xref ref-type="fig" rid="F7">Figure 7</xref> showed the transformation in chromium components in different treatment group which aligned with the earlier leaching results. After a 30-day treatment period, the exchangeable Cr content in all soils significantly decreased, undergoing transformation into Fe-Mn oxide-bound and the organic-bound forms. According to previous investigations, the elevated Fe-Mn oxides-bound fraction might be largely attributed to the precipitation of Cr(OH)<sub>3</sub> or Cr(III)/Fe(III) oxides/hydroxides (Cr<sub>n</sub>Fe<sub>1&#x2212;n</sub>OOH and Cr<sub>n</sub>Fe<sub>1&#x2212;n</sub> (OH)<sub>3</sub>) during the CMC-nZVI remediation (<xref ref-type="bibr" rid="B46">Manning et al., 2007</xref>). Specifically, 17.82% of exchangeable chromium in the NM soil was completely transformed into other more stable forms of Cr. According to <xref ref-type="sec" rid="s10">Supplementary Figure S5</xref>, after 7&#xa0;days of treatment, noticeable changes in pH were observed in the experimental groups. The group with the addition of nZVI/CMC exhibited the highest pH increase, rising from 8.70, 8.55, and 8.45 to 8.93, 8.72, and 8.70, respectively. This phenomenon may be attributed to the alkaline nature of the material and the reduction of Cr(VI) acting in concert. In the experimental group with the addition of SL2, the pH initially showed a decline followed by an upward trend, gradually stabilizing. This suggested that SL2 proliferated extensively in the early stages, producing acidic substances, and later reached a stable state. Due to the natural buffering capacity of the complex soil system, the fluctuation range of pH during the remediation process remained relatively small.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Soil Cr speciation after 30-days remediation with 0.4% nZVI/CMC@SL2. (Cr species: F1: exchangeable (EX); F2: carbonate bound (CB); F3: Fe-Mn oxide bound (OX); F4: organic matter bound (OM); F5: residual (RS); NMK and NM represented the control check and nZVI/CMC@SL2 treatment of NM soil, ZHK and ZH, ZLK and ZL were the same).</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g007.tif"/>
</fig>
<p>In short, the results indicated the excellent stabilization and environmental adaptability of the nZVI/CMC@SL2 composite remediation system towards chromium. It promoted the conversion of more easily available Cr (EX and CB) to the less available (OX and OM) and thus reduce the toxic effect of Cr. Furthermore, SL2 possessed the ability to regenerate Fe(II), facilitating the sustained reduction of Cr(VI).</p>
</sec>
<sec id="s3-5">
<title>3.5 Microecology analysis</title>
<p>After 30 days of treatment, the quantity of SL2 in the nZVI/CMC@SL2 treatment group gradually stabilized and maintained at a high level (4.23 &#xd7; 10<sup>4</sup>&#xa0;CFU/mL, <xref ref-type="sec" rid="s10">Supplementary Figure S4</xref>). Microbial community analysis of the ZL soil revealed an average of 81,938 quality sequences and 740 OUTs generated from the ITS1 gene. The fungal community&#x2019;s similarities and differences were analyzed based on OTUs using a Venn diagram (<xref ref-type="fig" rid="F8">Figure 8A</xref>). There were 353 shared OTUs, constituting 47.7% of the total observed OTUs (740), with 296 and 91 unique OUTs in the CK and treatment groups, respectively. This indicates that different treatments cultivated distinct microbial populations. Comparing with the CK, the treatment group exhibited a slight reduction in OUT levels, suggesting that this composite system could influence the fungal abundance in the soil. In terms of alpha diversity, both fungi and bacteria were significantly affected (<xref ref-type="sec" rid="s10">Supplementary Table S6</xref>). In the CK group, the three most abundant fungi were <italic>Ascomycota</italic> (68.66%), <italic>Basidiomycota</italic> (6.65%), and <italic>Mortierellomycota</italic> (4.03%). In the experimental group, the relative abundance of <italic>Ascomycota</italic> surged to 98.09%. As SL2 belongs to <italic>Ascomycota</italic>, its relative abundance increased from 4.75% to 87.18% at genus level, further confirming the successful colonization of SL2 in the soil and its competition with indigenous microorganisms to become the dominant strain (<xref ref-type="fig" rid="F8">Figure 8</xref>). Looking at the bacterial community (<xref ref-type="sec" rid="s10">Supplementary Figure S6</xref>), there was a significant increase in the relative abundance of <italic>Proteobacteria</italic> and <italic>Firmicutes</italic>, rising from 38.70% to 10.68%&#x2013;55.84% and 35.47%, respectively. Meanwhile, <italic>Actinobacteria</italic> decreased substantially (38.66%&#x2013;7.35%). <italic>Proteobacteria</italic> was often found as a dominant species in chromium-contaminated soil (<xref ref-type="bibr" rid="B14">Desai et al., 2009</xref>), with <italic>Bacillus</italic> within this phylum known to possess Cr(VI) reductase activity, capable of resisting and reducing high concentrations of Cr(VI) (<xref ref-type="bibr" rid="B18">Elangovan et al., 2006</xref>; <xref ref-type="bibr" rid="B13">Desai et al., 2008</xref>). <italic>Firmicutes</italic> harbored various heavy metal resistance genes, exhibiting stronger adaptability to heavy metal-polluted environments. Also, they are reported typically to be Fe(III)-reducing bacteria (FeRB)(<xref ref-type="bibr" rid="B28">Jin et al., 2023</xref>), thus regenerating Fe(II) and reduce Cr(VI).</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>Venn diagram <bold>(A)</bold> based on OTU and microbial community structures (fungi) at the phylum <bold>(B)</bold> and genus <bold>(C)</bold> level of different treatments after 30-days.</p>
</caption>
<graphic xlink:href="fenvs-12-1393609-g008.tif"/>
</fig>
<p>In conclusion, the nZVI/CMC@SL2 composite system enabled the successful colonization of SL2 in soils highly contaminated with Cr(VI). It demonstrates the ability to enrich chromium-tolerant and chromium-removing microorganisms, thereby promoting the reduction of Cr(VI).</p>
</sec>
</sec>
<sec id="s4" sec-type="conclusion">
<title>4 Conclusion</title>
<p>In this study, nano zero-valent iron (nZVI) stabilized in different ways were successfully prepared and compared. Specifically, nZVI/CMC not only efficiently removed Cr(VI) but also exhibited a detoxification effect on SL2. The heightened reactivity towards Cr(VI) can be attributed to the smaller size of the nano particles and the abundant oxygen-containing acidic groups in CMC. The detoxification effect may result from its identity as a free radical scavenger and the direct isolation achieved through CMC-coating. Furthermore, this combination of nZVI/CMC and SL2 for the stabilization of Cr(VI) in actual contaminated site soil was successfully applied, and through multiple perspectives such as leaching risk, chemical speciation changes, and soil microecology, we revealed the composite system&#x2019;s application potential in soil remediation. In conclusion, the chemical-fungal composite system of nZVI/CMC@SL2 explored in this study offers a novel approach for the remediation of highly contaminated Cr(VI) site soil. However, the mechanism by which SL2 reduces Fe(III) and the long-term stability of the nZVI/CMC@SL2 composite system remain unclear. It is recommended to delve deeper into the reduction mechanism in future research and conduct studies at field scales and real heavy metal-contaminated sites for a more comprehensive understanding.</p>
</sec>
</body>
<back>
<sec id="s5" sec-type="data-availability">
<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 below: <ext-link ext-link-type="uri" xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="https://www.ncbi.nlm.nih.gov/bioproject/">https://www.ncbi.nlm.nih.gov/bioproject/</ext-link>, accession number PRJNA1117622.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>SP: Writing&#x2013;review and editing, Writing&#x2013;original draft, Visualization, Methodology, Investigation, Formal Analysis, Data curation, Conceptualization. JT: Writing&#x2013;review and editing, Supervision, Methodology, Investigation, Formal Analysis. YL: Writing&#x2013;review and editing, Methodology, Investigation, Formal Analysis. JP: Writing&#x2013;review and editing, Supervision, Software. HZ: Writing&#x2013;review and editing, Visualization, Resources. JW: Writing&#x2013;review and editing, Visualization, Data curation. JS: Writing&#x2013;review and editing, Supervision, Project administration, Funding acquisition.</p>
</sec>
<sec id="s7" sec-type="funding-information">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research, authorship, and/or publication of this article. This research was supported by the National Natural Science Foundation of China (42277004) and the National Key Research and Development Program of China (2022YFC3702104).</p>
</sec>
<ack>
<p>The authors thank the editors and reviewers for their valuable comments to improve this article.</p>
</ack>
<sec id="s8" sec-type="COI-statement">
<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 id="s9" sec-type="disclaimer">
<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.2024.1393609/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fenvs.2024.1393609/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="DataSheet1.docx" id="SM1" mimetype="application/docx" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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