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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem.</journal-id>
<journal-title>Frontiers in Chemistry</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem.</abbrev-journal-title>
<issn pub-type="epub">2296-2646</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1484610</article-id>
<article-id pub-id-type="doi">10.3389/fchem.2024.1484610</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemistry</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Nitrogen-doped reduced graphene oxide for high efficient adsorption of methylene blue</article-title>
<alt-title alt-title-type="left-running-head">Kang et al.</alt-title>
<alt-title alt-title-type="right-running-head">
<ext-link ext-link-type="uri" xlink:href="https://doi.org/10.3389/fchem.2024.1484610">10.3389/fchem.2024.1484610</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Kang</surname>
<given-names>Maoping</given-names>
</name>
<uri xlink:href="https://loop.frontiersin.org/people/2823476/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/conceptualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/data-curation/"/>
<role content-type="https://credit.niso.org/contributor-roles/formal-analysis/"/>
<role content-type="https://credit.niso.org/contributor-roles/investigation/"/>
<role content-type="https://credit.niso.org/contributor-roles/methodology/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Pei</surname>
<given-names>Yongli</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/visualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Zhang</surname>
<given-names>Ying</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/formal-analysis/"/>
<role content-type="https://credit.niso.org/contributor-roles/validation/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Su</surname>
<given-names>Lihong</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/methodology/"/>
<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>Li</surname>
<given-names>Yuxiang</given-names>
</name>
<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" corresp="yes">
<name>
<surname>Wang</surname>
<given-names>Hongyu</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2824398/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
</contrib-group>
<aff>
<institution>Department of Energy Chemistry and Materials Engineering</institution>, <institution>Shanxi Institute of Energy</institution>, <addr-line>Jinzhong</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/589177/overview">Timur Sh. Atabaev</ext-link>, Nazarbayev University, Kazakhstan</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/1931011/overview">K. K. R. Datta</ext-link>, SRM Institute of Science and Technology, India</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2285366/overview">Lakshmi Narayanan Mosur Saravana Murthy</ext-link>, Intel, United States</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2899684/overview">Ling Sun</ext-link>, Beijing University of Technology, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Hongyu Wang, <email>wanghy@sxie.edu.cn</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>06</day>
<month>01</month>
<year>2025</year>
</pub-date>
<pub-date pub-type="collection">
<year>2024</year>
</pub-date>
<volume>12</volume>
<elocation-id>1484610</elocation-id>
<history>
<date date-type="received">
<day>22</day>
<month>08</month>
<year>2024</year>
</date>
<date date-type="accepted">
<day>16</day>
<month>12</month>
<year>2024</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2025 Kang, Pei, Zhang, Su, Li and Wang.</copyright-statement>
<copyright-year>2025</copyright-year>
<copyright-holder>Kang, Pei, Zhang, Su, Li and Wang</copyright-holder>
<license xlink:href="http://creativecommons.org/licenses/by/4.0/">
<p>This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.</p>
</license>
</permissions>
<abstract>
<p>A highly efficient and widely applicable adsorbent for the removal of methylene blue (MB) was created using nitrogen-doped and reduced graphene oxide (NRGO). The effects of NRGO mass, pH, contact time, and the initial MB concentration on the adsorption properties of MB onto NRGO were investigated. The results showed that the adsorption behavior remained stable within the pH range of 2.0&#x2013;10.0, and the adsorption process gradually reached equilibrium after 24&#xa0;h. Additionally, the adsorption kinetics and adsorption isotherms were discussed to propose a theoretical adsorption mechanism. Meanwhile, some characterizations including Scanning Electron Microscopy, Energy Disperse X-ray Spectroscopy, X-ray Photoelectron Spectroscopy, X-ray Powder Diffraction, Fourier Transform Infrared Spectroscopy, etc. were used to explore potential adsorption mechanism, which indicated the physisorption caused by &#x3c0;-&#x3c0; bonds was the main adsorption mechanism. NRGO exhibits efficient MB absorption and holds significant potential application for the wastewater treatment.</p>
</abstract>
<abstract abstract-type="graphical">
<title>Graphical Abstract</title>
<p>
<graphic xlink:href="FCHEM_fchem-2024-1484610_wc_abs.tif"/>
</p>
</abstract>
<kwd-group>
<kwd>nitrogen-doped reduced graphene oxide (NRGO)</kwd>
<kwd>methylene blue (MB)</kwd>
<kwd>adsorption mechanism</kwd>
<kwd>potential application</kwd>
<kwd>wastewater treatment</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Nanoscience</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Methylene blue (MB) is a cationic dye extensively utilized in various industries, including textile, food, pulp mill industries (<xref ref-type="bibr" rid="B3">Ang et al., 2022</xref>), and the medical field. For instance, in oral medicine, MB can act as a photosensitizer in photodynamic therapy (PDT) for the treatment of oral diseases such as dental caries, periodontitis, and oral mucosal disease via photocatalysis. Nevertheless, the residual MB in wastewater has lots of harmful effects on organisms such as mutagenicity, carcinogenicity and teratogenicity, thereby threatening ecological security and human health because of its high toxicity. Additionally, MB is resistant to natural degradation. If untreated sewage containing MB is discharged into natural water bodies, it will result in severe water pollution, adversely affecting on aquatic organisms and human health (<xref ref-type="bibr" rid="B21">Shitu and Ibrahim, 2014</xref>). Consequently, MB has been recognized as one of the major pollutants globally (<xref ref-type="bibr" rid="B9">Fouzia and Nasar, 2020</xref>).</p>
<p>To address this issue, various conventional methods such as coagulation, ion exchange, chemical precipitation, electrolysis, reverse osmosis, and electrodialysis have been adopted to remove MB from wastewater. However, these technologies are complicated operation, time-consuming and inadequate to address modern wastewater treatment issues (<xref ref-type="bibr" rid="B8">Dutt et al., 2020</xref>). Therefore, there is an urgent requirement for an effective and eco-friendly approach to remove MB to mitigate its harmful impacts. The adsorption-based method has garnered significant attention by researchers due to its high efficiency, rapid action, simple operation, and environmental compatibility. Meanwhile, some adsorbents have been studied as shown in <xref ref-type="table" rid="T1">Table 1</xref>. Among these adsorbents, graphene-based materials demonstrated a definite advantage because of its large surface area, abundant functional groups (hydroxyl, carboxyl, and epoxide) (<xref ref-type="bibr" rid="B6">Bhat et al., 2022</xref>; <xref ref-type="bibr" rid="B11">Gordon-Nuez et al., 2019</xref>), low cost, simple preparation and easy modification, etc. However, GO is easy to aggregate to reduce the active site, which will affect its adsorption properties. Also, the separation of nanosized GO from the sewage after adsorption is challenging leading to the waste of adsorbent (<xref ref-type="bibr" rid="B17">Li et al., 2013</xref>). Last but not least, adsorbents applicable over a wide pH range are very necessary due to the different pH levels of different water bodies. Therefore, developing the adsorbent with not easily agglomerate, reduced secondary pollution and wide applicability is extremely crucial for the removal of MB.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Adsorption behavior of MB with different reported absorbents.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Adsorbents</th>
<th align="center">Dye concentration (mg/L)</th>
<th align="center">pH</th>
<th align="center">Adsorption efficiency (%)</th>
<th align="center">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">A/C-GO</td>
<td align="center">100</td>
<td align="center">9</td>
<td align="center">94.70</td>
<td align="center">
<xref ref-type="bibr" rid="B15">Hridoy Roy and Md Mahmud Kamal Bhuiyan (2024)</xref>
</td>
</tr>
<tr>
<td align="center">ZnFe<sub>2</sub>O<sub>4</sub>/GO (1:5)</td>
<td align="center">10</td>
<td align="center">8</td>
<td align="center">97.37</td>
<td align="center">
<xref ref-type="bibr" rid="B5">Aya et al. (2024)</xref>
</td>
</tr>
<tr>
<td align="center">GO</td>
<td align="center">20</td>
<td align="center">6</td>
<td align="center">60.2</td>
<td align="center">
<xref ref-type="bibr" rid="B2">Al et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="center">Perlite@GO</td>
<td align="center">500</td>
<td align="center">8</td>
<td align="center">99.7</td>
<td align="center">
<xref ref-type="bibr" rid="B16">Iuliano et al. (2024)</xref>
</td>
</tr>
<tr>
<td align="center">&#x3b3;-AlOOH/3D-rGO</td>
<td align="center">10</td>
<td align="center">7</td>
<td align="center">N/A</td>
<td align="center">
<xref ref-type="bibr" rid="B12">Han et al. (2024)</xref>
</td>
</tr>
<tr>
<td align="center">GNS</td>
<td align="center">500</td>
<td align="center">&#x2265;8</td>
<td align="center">99</td>
<td align="center">
<xref ref-type="bibr" rid="B24">Wang et al. (2024)</xref>
</td>
</tr>
<tr>
<td align="center">Se-ZnFe<sub>2</sub>O<sub>4</sub>/rGO nanohybrids</td>
<td align="center">50</td>
<td align="center">N/A</td>
<td align="center">92.4</td>
<td align="center">
<xref ref-type="bibr" rid="B1">Krishnan et al. (2021)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Nitrogen-doped reduced graphene oxide (NRGO) is a new type of carbon nanomaterial synthesized from GO with nitrogen as a doping element, which has the advantage of a large specific surface area due to lamellar overlap (<xref ref-type="bibr" rid="B27">Wu et al., 2020</xref>). Meanwhile, the water solubility of NRGO is significantly reduced compared to GO due to the decrease of oxygen-containing functional groups, which indicates that NRGO can hardly dissolve in water resulting in simple removal. In addition, NRGO exhibits non-cytotoxicity up to 100&#xa0;&#x3bc;g/mL (<xref ref-type="bibr" rid="B19">Liu et al., 2016</xref>), which is less cytotoxic than GO (<xref ref-type="bibr" rid="B10">Fu et al., 2016</xref>). With the research progress on the unique performance and advantages of NRGO, its application value has been gradually developed. The incorporation of nitrogenous functional groups narrows the band gap of NRGO, reducing the aggregation of GO and enhancing charge transport, conductivity, and charge separation (<xref ref-type="bibr" rid="B7">Bhirud et al., 2015</xref>). Thus, NRGO has been used as base material to obtain some photocatalytic composites (<xref ref-type="bibr" rid="B4">Appavu et al., 2016</xref>; <xref ref-type="bibr" rid="B20">Meng et al., 2013</xref>). The nitrogen doping and ample functional groups improved the photocatalytic activity, enabling NRGO to act as a catalyst to promote the removal of organic pollutants in water (<xref ref-type="bibr" rid="B26">Wei et al., 2021</xref>; <xref ref-type="bibr" rid="B30">Zeng et al., 2016</xref>). Furthermore, NRGO&#x2019;s robust &#x3c0;-&#x3c0; and hydrophobic interactions allow it to adsorb phenol and p-nitrophenol, and be reused, indicating its potential as an effective and recyclable adsorbent for removing phenolic chemicals from wastewater (<xref ref-type="bibr" rid="B31">Zhao et al., 2020</xref>). Therefore, NRGO is likely to be an alternative adsorbent.</p>
<p>In this study, NRGO was synthesized and utilized as an adsorbent for MB. The effects of different adsorption conditions including NRGO mass, pH, contact time, and initial MB concentration on MB adsorption were comprehensively investigated. Additionally, the adsorption kinetics and isotherms were also explored to elucidate the potential adsorption mechanism. Furthermore, essential characterizations were performed on both NRGO samples before and after MB adsorption to validate the proposed adsorption mechanism. Collectively, this study may provide a highly efficient and widely applicable adsorbent with potential applications in wastewater treatment.</p>
</sec>
<sec sec-type="results|discussion" id="s2">
<title>2 Results and discussion</title>
<sec id="s2-1">
<title>2.1 Characterizations of NRGO</title>
<p>NRGO was synthesized through a simple two-step reaction, including the doping of nitrogen and the reduction of graphene oxide (GO). The morphologies of NRGO and GO were observed by Scanning Electron Microscopy (SEM). The results showed that the microstructure of NRGO (<xref ref-type="fig" rid="F1">Figure 1B</xref>) exhibited a loose, multifold, three-dimensional stacked layer with wrinkles and pores while that of GO (<xref ref-type="fig" rid="F1">Figure 1A</xref>) was a relatively flat layer with some wrinkles, which is consistent with the previous study (<xref ref-type="bibr" rid="B11">Gordon-Nuez et al., 2019</xref>). Meanwhile, the Energy Disperse X-ray spectroscopy (EDX) spectrum ((<xref ref-type="fig" rid="F1">Figure 1C</xref> and elemental mapping images (<xref ref-type="fig" rid="F1">Figures 1D&#x2013;F</xref>) confirmed that nitrogen was clearly observed and uniformly distributed in the synthesized NRGO, distinguishing it from GO, which is composed solely of carbon and oxygen. This observation confirms that NRGO was successfully synthesized by through nitrogen doping.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>SEM images of GO <bold>(A)</bold> and NRGO <bold>(B)</bold>; The EDX spectrum and elemental mapping images of NRGO <bold>(C&#x2013;F)</bold>.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g001.tif"/>
</fig>
<p>Surface charge and Raman were used to further verify the reduction and functionalization of GO. As shown in <xref ref-type="fig" rid="F2">Figure 2A</xref>, GO showed the negative potential (&#x2212;38.25&#xa0;mV), while NRGO showed the positive potential (25.07&#xa0;mV), which possibly indicated graphene oxide was aminated. Meanwhile, the change of carbon frame structure was characterized by Raman spectrum. As shown in <xref ref-type="fig" rid="F2">Figure 2B</xref>, the D and G band were clearly observed for GO and NRGO at 1,349&#xa0;cm<sup>&#x2212;1</sup>, 1587&#xa0;cm<sup>&#x2212;1</sup>, and 1349&#xa0;cm<sup>&#x2212;1</sup>, 1601&#xa0;cm<sup>&#x2212;1</sup>, respectively. The G band of NRGO was slightly split and had a slight peak shift, which indicated GO was reduced and functionalized (<xref ref-type="bibr" rid="B22">Song et al., 2012</xref>). Also, the <italic>I</italic>
<sub>
<italic>D</italic>
</sub>
<italic>/I</italic>
<sub>
<italic>G</italic>
</sub> of NRGO was higher than that of GO, which indicated the amino groups were modified to the edge or surface of the graphene.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Zeta potential <bold>(A)</bold> and Raman spectra <bold>(B)</bold>.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g002.tif"/>
</fig>
<p>Moreover, X-ray powder diffraction (XRD) and Fourier transform infrared spectroscopy (FTIR) were used to characterize the changes in structure and functional groups before and after the modification of GO. As shown in <xref ref-type="fig" rid="F3">Figure 3A</xref>, the XRD patterns exhibited an intense characteristic diffraction peak at 2&#x3b8; &#x3d; 10.10&#xb0; for GO and a weak characteristic peak at 2&#x3b8; &#x3d; 19.95&#xb0; for NRGO, attributed to the reduction of oxygen-containing functional groups of GO, leading to a significant decrease in interlayer spacing (<xref ref-type="bibr" rid="B32">Zheng et al., 2013</xref>; <xref ref-type="bibr" rid="B14">He et al., 2013</xref>). Furthermore, FTIR was used to characterize the changes in functional groups of GO and NRGO. As shown in <xref ref-type="fig" rid="F3">Figure 3B</xref>, the FTIR spectrum of GO displayed a broad and intense peak at 3,420&#xa0;cm<sup>&#x2212;1</sup>, corresponding to -OH stretching vibration peak. Additionally, the other four adsorption peaks of GO are displayed at 1720&#xa0;cm<sup>&#x2212;1</sup>, 1,630&#xa0;cm<sup>&#x2212;1</sup>, 1,380&#xa0;cm<sup>&#x2212;1</sup> and1050&#xa0;cm<sup>&#x2212;1</sup>, indicative of the stretching vibration absorption peak of C&#x3d;O in aryl carboxylic acids, the stretching vibration absorption peak of the C&#x3d;C form six-membered ring skeleton, the deformation vibration absorption peak of O-H in C-OH group, and the stretching vibration absorption peak of C-O, respectively (<xref ref-type="bibr" rid="B18">Liu et al., 2014</xref>; <xref ref-type="bibr" rid="B28">Yang et al., 2020</xref>).In contrast, the characteristic absorption peaks of oxygen-containing functional groups in NRGO at 3,420&#xa0;cm<sup>&#x2212;1</sup>, 1720&#xa0;cm<sup>&#x2212;1</sup>, 1,630&#xa0;cm<sup>&#x2212;1</sup>, and 1,380&#xa0;cm<sup>&#x2212;1</sup> O were significantly weakened or absent as expected, confirming the reduction of GO. Instead, a new adsorption peak representing a carbon-nitrogen heterocyclic ring appears at 1,070&#xa0;cm<sup>&#x2212;1</sup> (<xref ref-type="bibr" rid="B29">Yuan et al., 2017</xref>), and 1,560&#xa0;cm<sup>&#x2212;1</sup> for bending vibration peak of N-H, indicating the successful introduction of N in the graphene lattice. These results suggested that the oxygen-containing groups in GO were decreased, and the N were doped during the synthesis process.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>XRD <bold>(A)</bold> patterns and FTIR spectra <bold>(B)</bold> of GO and NRGO.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g003.tif"/>
</fig>
<p>Additionally, X-ray photoelectron spectroscopy (XPS) was utilized to verify the elemental composition, and the valence bond form of NRGO. As shown in <xref ref-type="fig" rid="F4">Figure 4A</xref>, the N element was clearly observed after N-doping on GO, whereas GO only contained O and C, indicating successfully doped of N element. Additionally, the C:O ratio in NRGO increased significantly compared to GO, which indicated GO was also reduced in obtaining N-doped reduced graphene oxide. Also, C1s (<xref ref-type="fig" rid="F4">Figure 4B</xref>), N1s (<xref ref-type="fig" rid="F4">Figure 4C</xref>), and O1s (<xref ref-type="fig" rid="F4">Figure 4D</xref>) spectra were studied to analyze the possible valence bond. As shown in C 1s spectrum (<xref ref-type="fig" rid="F4">Figure 4B</xref>), the four characteristic peaks were observed, including C-C (284.6&#xa0;eV), C-N/C-O (285.7&#xa0;eV), C&#x3d;O (286.8&#xa0;eV), and &#x3c0;-&#x3c0;<sup>&#x2a;</sup> (288.9&#xa0;eV). The higher peak area of C-C indicated the reduction of GO. The appearance of C-N indicates that the amino group in oleoamine may be linked to GO. In <xref ref-type="fig" rid="F4">Figure 4C</xref>, the split peaks of N 1s were observed as C-N (401.3&#xa0;eV) and N-H (399.5&#xa0;eV), which indicated the GO was aminated. These results indicated GO was reduced and functionalized by oleylamine through the formation of C-N and N-H, which was also verified by the FTIR results.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>XPS survey spectra of GO and NRGO <bold>(A)</bold>. <bold>(B)</bold> C 1s <bold>(B)</bold>, N 1s <bold>(C)</bold>, and O 1s <bold>(D)</bold> spectra of NRGO.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g004.tif"/>
</fig>
</sec>
<sec id="s2-2">
<title>2.2 Adsorption performance</title>
<sec id="s2-2-1">
<title>2.2.1 The adsorption behavior of NRGO and RGO</title>
<p>The obtained RGO was chosen because it was the reduced GO and a non-water-soluble solid, similar to NRGO. 0.03&#xa0;g of NRGO and RGO was employed to adsorb MB at different pH values. As shown in <xref ref-type="fig" rid="F5">Figure 5</xref>, the adsorption efficiency of GO reached maximum of 92.31% at pH 8, 9 and 10. Nevertheless, the adsorption efficiency was as low as less than 88% under acidic conditions, which indicated that the adsorption behavior of RGO was dependent on the pH values. As for NRGO, the adsorption efficiency for MB remained almost as high as 97% over a wide pH range, which indicated that the adsorption behavior was independent on the pH value of the water body. In summary, NRGO exhibited higher adsorption efficiency for MB than RGO at any pH value, which will be applied in various fields. Therefore, NRGO was chosen as the adsorbent for the further study.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>The adsorption efficiency of NRGO and RGO at different pH values.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g005.tif"/>
</fig>
</sec>
<sec id="s2-2-2">
<title>2.2.2 Effect of adsorbent dose</title>
<p>To explore the effect of the adsorbent dose, varying amounts of NRGO powder (0.005&#xa0;g, 0.01&#xa0;g, 0.02&#xa0;g and 0.06&#xa0;g) was introduced into 1&#xa0;mL of 100&#xa0;mg/L&#xa0;MB solution and shaked for 24&#xa0;h at room temperature. <xref ref-type="fig" rid="F6">Figure 6A</xref> illustrated the correlation between the initial mass of NRGO and the resulting adsorption performance. The results indicated that the adsorption efficiency increased with the mass of NRGO. Meanwhile, the adsorption efficiency was approximately balanced when the adsorbent dosage reached 0.02&#xa0;g, suggesting that this amount provides an optimal number of adsorption sites for 1&#xa0;mL of a 100&#xa0;mg/L&#xa0;MB solution. Consequently, a dosage of 0.02&#xa0;g was selected as the optimal adsorbent dosage for following experiments.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Effect of adsorbent dose <bold>(A)</bold>, initial pH <bold>(B)</bold> and contact time <bold>(C)</bold> on MB adsorbed by NRGO; adsorption kinetics of MB absorbed by NRGO <bold>(D)</bold>.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g006.tif"/>
</fig>
</sec>
<sec id="s2-2-3">
<title>2.2.3 Effect of pH for adsorption MB</title>
<p>The pH of the solution significantly influences the adsorption of MB. In this study, MB solutions (30&#xa0;mg/L) with varying pH values (2.00&#x2013;10.00) were prepared by adjusting the pH values with NaOH solution (0.1&#xa0;M) and HCl solution (0.1&#xa0;M). 0.002&#xa0;g NRGO powder was added to 300&#xa0;&#xb5;L of the above MB solution with different initial pH values, respectively. As shown in <xref ref-type="fig" rid="F6">Figure 6B</xref>, the initial pH of MB solution had a negligible effect on the adsorption efficiency across the acidic to alkaline range. The adsorption efficiency remained consistently around 98% when pH was adjusted to between 2 and 10, indicating that NRGO was a stable and efficient adsorbent in the removal of MB, independent of pH variations. This characteristic positioned NRGO as a potential adsorbent for the actual sample with a wide range of pH. Additionally, the pH of the original MB solution was measured as 6.30. Given the minimal impact of initial pH on the adsorption efficiency, the natural pH of MB solution was utilized for subsequent experiments.</p>
</sec>
<sec id="s2-2-4">
<title>2.2.4 Effect of adsorption time and adsorption kinetics</title>
<p>Investigating the effect of time on adsorption is essential for achieving rapid and efficient adsorption. 0.002&#xa0;g NRGO was added to MB solution (300&#xa0;&#x3bc;L, 30&#xa0;&#x3bc;g/mL), and the mixtures were centrifuged after varying interaction time from 1&#xa0;h to 48&#xa0;h. According to <xref ref-type="fig" rid="F6">Figure 6C</xref> both the adsorption efficiency and capacity increased rapidly within 1&#xa0;h, after which the adsorption rate slowed down with the time increased, indicating that the adsorption sites on NRGO were gradually occupied by MB and approached saturated. Meanwhile, the adsorption efficiency almost stabilized after 24&#xa0;h, indicating that the adsorption efficiency and capacity kept constant and reached the adsorption equilibrium. Therefore, an adsorption time of 24&#xa0;h was determined to be optimal for the following experiments.</p>
<p>To explore the adsorption mechanism of the adsorption behavior, the common adsorption kinetic models were investigated using the pseudo-first-order (PFO) and pseudo-second-order (PSO) kinetic models according to the following <xref ref-type="disp-formula" rid="e1">Equations 1</xref>, <xref ref-type="disp-formula" rid="e2">2</xref>. Therein, the PFO model described a physisorption process where the adsorption process is related to the number of reaction sites and the diffusion rate of the adsorbate, and is expressed in <xref ref-type="disp-formula" rid="e1">Equation 1</xref> (<xref ref-type="bibr" rid="B13">Haque et al., 2020</xref>):<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>ln</mml:mi>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>t</mml:mi>
</mml:msub>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>1</mml:mn>
</mml:msub>
<mml:mi>t</mml:mi>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
</p>
<p>The PSO model reflects the chemisorption process, involving the formation of chemical bonding between adsorbate and adsorbent through electron sharing or exchange, and is expressed in <xref ref-type="disp-formula" rid="e2">Equation 2</xref> (<xref ref-type="bibr" rid="B13">Haque et al., 2020</xref>):<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:mfrac>
<mml:mrow>
<mml:mi>t</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>t</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mn>1</mml:mn>
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mn>2</mml:mn>
</mml:msub>
<mml:msubsup>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
<mml:mn>2</mml:mn>
</mml:msubsup>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x2b;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mi>t</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>Where <italic>q</italic>
<sub>
<italic>t</italic>
</sub> is the adsorption capacity at time <italic>t</italic> (mg/g), <italic>t</italic> is adsorption time (h), <italic>q</italic>
<sub>e</sub> is equilibrium adsorption capacity of MB (mg/g), <italic>k</italic>
<sub>1</sub> (h<sup>&#x2212;1</sup>) is the Lagergren rate constant of PFO, <italic>k</italic>
<sub>2</sub> g/(mg&#xb7;h) is the rate constant of PSO. As shown in <xref ref-type="fig" rid="F6">Figure 6D</xref>, the PSO model, with a correlation coefficient (<italic>R</italic>
<sup>2</sup>) of 0.9978, provided a better fit to the data than the PFO model, with a <italic>R</italic>
<sup>2</sup> of 0.8233. Moreover, as shown in <xref ref-type="table" rid="T2">Table 2</xref>, the adsorption capacity <italic>q</italic>
<sub>cal</sub> calculated by the PSO model closely approximated the experimental adsorption equilibrium capacity <italic>q</italic>
<sub>exp</sub>. This further proved the applicability of PSO model to the adsorption process, indicating the adsorption rate was controlled by chemisorption mechanism, which involves the electronic sharing and exchange between NRGO and MB.</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Kinetics models for the adsorption of CHX on NRGO.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center"/>
<th align="center">Pseudo-first-orderln (1&#x2212;q<sub>t</sub>/q<sub>e</sub>) &#x3d; &#x2212;k<sub>1</sub>t</th>
<th colspan="3" align="center">Pseudo-second-order t/q<sub>t</sub> &#x3d; 1/(k<sub>2</sub> q<sub>e</sub>
<sup>2</sup>)&#x2b;t/q<sub>e</sub>
</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Model equations</td>
<td align="center">y &#x3d; 0.9817x&#x2b;0.1487</td>
<td colspan="3" align="center">y &#x3d; 0.2715x&#x2b;0.2678</td>
</tr>
<tr>
<td rowspan="2" align="center">Correlation</td>
<td align="center">
<italic>R</italic>
<sup>
<italic>2</italic>
</sup>
</td>
<td align="center">
<italic>q</italic>
<sub>cal</sub> (mg g<sup>&#x2212;1</sup>)</td>
<td align="center">
<italic>q</italic>
<sub>exp</sub> (mg g<sup>&#x2212;1</sup>)</td>
<td align="center">
<italic>R</italic>
<sup>
<italic>2</italic>
</sup>
</td>
</tr>
<tr>
<td align="center">0.8233</td>
<td align="center">4.61</td>
<td align="center">4.45</td>
<td align="center">0.9978</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s2-2-5">
<title>2.2.5 Effect of the initial concentration of MB and adsorption isotherms</title>
<p>To assess the effect of initial MB concentration on the adsorption performance, 0.002&#xa0;g NRGO powder was added to 1&#xa0;mL&#xa0;MB solution with varying concentrations ranging from 5 to 600&#xa0;mg/L. As shown in <xref ref-type="fig" rid="F7">Figure 7A</xref>, the adsorption efficiency decreased while the adsorption capacity increased as the MB concentration increased, which was attributed to the finite number of reactive sites available on NRGO. Notably, as the initial MB concentration increased from 5&#xa0;mg/L to 100&#xa0;mg/L, there was a marked decrease in adsorption efficiency and a significant increase in adsorption capacity. Upon further increasing the MB concentration from 100&#xa0;mg/L to 400&#xa0;mg/L, the decline in adsorption efficiency and the rise in adsorption capacity continued, but at a decelerating rate. Ultimately, at an initial MB concentration of reached 600&#xa0;mg/L, the adsorption capacity remained consistent at &#x223c;78&#xa0;mg/g, indicating that the adsorption sites on NRGO were nearing saturation.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Effect of the initial concentration of MB solution <bold>(A)</bold> and Langmuir and Freundlich adsorption isotherms <bold>(B)</bold> for the adsorption of MB onto NRGO.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g007.tif"/>
</fig>
<p>In addition to kinetics studies, the adsorption isotherms were examined to explore the adsorption performance. The experimental data of the effect of the initial MB concentration were fitted with Langmuir and Freundlich isotherm models according to <xref ref-type="disp-formula" rid="e3">Equations 3</xref>, <xref ref-type="disp-formula" rid="e4">4</xref>.</p>
<p>The Langmuir model, which describes the equilibrium condition of monolayer homogeneous adsorption is expressed as <xref ref-type="disp-formula" rid="e3">Equation 3</xref> (<xref ref-type="bibr" rid="B25">Wang and Guo, 2020</xref>):<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:mfrac>
<mml:mrow>
<mml:mn>1</mml:mn>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mn>1</mml:mn>
<mml:mrow>
<mml:msub>
<mml:mi>k</mml:mi>
<mml:mi>L</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>m</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi>c</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x2b;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mn>1</mml:mn>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>m</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>
</p>
<p>The Freundlich model, which represents the multi-layer adsorption on heterogamous surfaces is expressed as <xref ref-type="disp-formula" rid="e4">Equation 4</xref> (<xref ref-type="bibr" rid="B25">Wang and Guo, 2020</xref>):<disp-formula id="e4">
<mml:math id="m4">
<mml:mrow>
<mml:mi mathvariant="italic">ln</mml:mi>
<mml:mo>&#x2061;</mml:mo>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mi mathvariant="italic">ln</mml:mi>
<mml:mo>&#x2061;</mml:mo>
<mml:msub>
<mml:mi>K</mml:mi>
<mml:mi>F</mml:mi>
</mml:msub>
<mml:mo>&#x2b;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mn>1</mml:mn>
</mml:mrow>
<mml:mrow>
<mml:mi>n</mml:mi>
</mml:mrow>
</mml:mfrac>
<mml:mi>ln</mml:mi>
<mml:mo>&#x2061;</mml:mo>
<mml:msub>
<mml:mi>C</mml:mi>
<mml:mi>e</mml:mi>
</mml:msub>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>Where <italic>C</italic>
<sub>e</sub> (mg/g) is the equilibrium concentration, <italic>q</italic>
<sub>e</sub> (mg/L) is the adsorption capacity at equilibrium. The Langmuir constants <italic>q</italic>
<sub>m</sub> (mg/L) and <italic>K</italic>
<sub>L</sub> (L/mg) are related to the adsorption capacity and energy, respectively, and were calculated from the intercept and slope of the plot of 1/<italic>q</italic>
<sub>e</sub> versus 1/<italic>C</italic>
<sub>e</sub>, respectively. The Freundlich constants <italic>K</italic>
<sub>F</sub> (mg/g) and 1/n are related to the adsorption capacity and intensity, respectively, and were determined from the intercept and slope of the plot of ln <italic>q</italic>
<sub>e</sub> versus ln <italic>C</italic>
<sub>e</sub>, respectively.</p>
<p>The plots of the Langmuir and Freundlich isotherm models, along with the data in detail, were displayed in <xref ref-type="fig" rid="F7">Figure 7B</xref>; <xref ref-type="table" rid="T2">Table 2</xref>, respectively. The results showed that the adsorption performance was both in accordance with Langmuir and Freundlich models, as evidenced by the high correlation coefficients (<italic>R</italic>
<sup>2</sup>) This suggested that both monolayer and heterogeneous adsorption appeared in the adsorption process. According to <xref ref-type="table" rid="T3">Table 3</xref>, the theoretical maximum adsorption capacity (<italic>q</italic>
<sub>m</sub>) was calculated to be 27.90&#xa0;mg/g according to the Langmuir isotherm. As for the Freundlich constants, <italic>K</italic>
<sub>F</sub> gave an adsorption capacity as 2.949&#xa0;mg/g, and the value of n was 2.029 (1 &#x3c; <italic>n</italic> &#x3c; 10), which indicated the adsorption process of NRGO was obviously heterogeneous (<xref ref-type="bibr" rid="B23">Tanzifi et al., 2018</xref>).</p>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Langmuir and Freundlich adsorption isotherm parameters for MB on NRGO.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center"/>
<th colspan="3" align="center">Langmuir</th>
<th colspan="3" align="center">Freundlich</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Material</td>
<td align="center">
<italic>q</italic>
<sub>
<italic>m</italic>
</sub> (mg g<sup>&#x2212;1</sup>)</td>
<td align="center">
<italic>K</italic>
<sub>
<italic>L</italic>
</sub> (L mg<sup>&#x2212;1</sup>)</td>
<td align="center">
<italic>R</italic>
<sup>
<italic>2</italic>
</sup>
</td>
<td align="center">
<italic>K</italic>
<sub>
<italic>F</italic>
</sub> (mg g<sup>&#x2212;1</sup>)</td>
<td align="center">n</td>
<td align="center">
<italic>R</italic>
<sup>
<italic>2</italic>
</sup>
</td>
</tr>
<tr>
<td align="center">NRGO</td>
<td align="center">27.90</td>
<td align="center">0.2026</td>
<td align="center">0.9622</td>
<td align="center">2.949</td>
<td align="center">2.029</td>
<td align="center">0.9857</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
<sec id="s2-3">
<title>2.3 Adsorption mechanism</title>
<p>The possible adsorption mechanism of NRGO for MB can be roughly delineated into three points: 1) The microstructure of NRGO. SEM image in <xref ref-type="fig" rid="F1">Figure 1B</xref> showed that NRGO had more folds and pores, and the three-dimensional lamellar structure of NRGO was conducive to improving the adsorption efficiency of MB. 2) The &#x3c0;-&#x3c0; interaction between NRGO and MB. According to the previous reports, a large number of benzene rings on NRGO have been proved to be effective adsorption of phenols through &#x3c0;-&#x3c0; bonds (<xref ref-type="bibr" rid="B31">Zhao et al., 2020</xref>), potentially facilitating interactions with the aromatic groups of MB molecules. 3) The formation of new chemical bonds. The kinetic study results indicated that the adsorption of MB by NRGO was more in accordance with pseudo-second-order kinetics, suggesting that the chemisorption predominantly governs the adsorption rate. Therefore, some necessary characterizations were conducted to further elucidate the adsorption mechanism.</p>
<p>The intuitive observation of microscopic morphologies could directly reflect the adsorption of MB. Thus, SEM was employed to observe the morphologies change of before and after MB adsorption. As shown in <xref ref-type="fig" rid="F8">Figure 8A</xref>, MB presented a stacked particles form. After the adsorption of MB (<xref ref-type="fig" rid="F8">Figure 8B</xref>), NRGO-MB still kept a stacked lamellar structure, similar to that of NRGO. However, MB was not observed clearly on the surface of NRGO-MB because of the encapsulation of MB by the lamellar structure of NRGO. To further confirm the adsorption of MB by NRGO, EDX analysis was conducted. As shown in <xref ref-type="fig" rid="F8">Figure 8D</xref>, the result showed the presence of carbon, oxygen, nitrogen, chlorine, and sulfur in NRGO-MB, which was consistent with the elements present in MB (<xref ref-type="fig" rid="F8">Figure 8C</xref>). Additionally, the mapping images showed uniformly dispersion of chlorine and sulfur elements on the surface of NRGO-MB (<xref ref-type="fig" rid="F8">Figures 8E, F</xref>). Furthermore, as depicted in the inset image of (<xref ref-type="fig" rid="F8">Figure 8D</xref>), the blue coloration associated with MB appeared lighter or even disappeared after the adsorption by NRGO, indicating successfully adsorption of MB by NRGO.</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>SEM images of MB <bold>(A)</bold> and NRGO-MB <bold>(B)</bold>, and EDX spectra and elemental mapping images of NRGO-MB <bold>(C&#x2013;F)</bold>.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g008.tif"/>
</fig>
<p>In addition, XPS was utilized to further analyze the elements before and after MB adsorption. As shown in <xref ref-type="fig" rid="F9">Figure 9A</xref>, the NRGO surface was predominantly composed of carbon, oxygen and nitrogen. Apart from carbon, oxygen and nitrogen, the MB surface also contained chlorine and sulfur. Compared with NRGO, sulfur was observed on the surface of NRGO-MB, which aligned with the elemental analysis results of MB, suggesting the successful adsorption of MB onto NRGO. The XRD patterns, as shown in <xref ref-type="fig" rid="F9">Figure 9B</xref>, revealed a shift in the characteristic peak from 2&#x3b8; &#x3d; 19.98&#xb0; for NRGO to 2&#x3b8; &#x3d; 19.87&#xb0; for NRGO-MB, indicating an increased interlayer spacing due to the adsorption of MB on NRGO surface. Moreover, three other characteristic peaks at 2&#x3b8; &#x3d; 7.45&#xb0;, 2&#x3b8; &#x3d; 12.33&#xb0; and 2&#x3b8; &#x3d; 29.11&#xb0; were clearly observed in NRGO-MB, which closely matched with XRD pattern of MB, which indicated that MB was successfully loaded onto NRGO to form NRGO-MB. Furthermore, FTIR was used to characterize the functional groups before and after MB adsorption. As shown in <xref ref-type="fig" rid="F9">Figure 9C</xref>, no significant changes or new peaks were observed in the infrared spectra of NRGO after adsorbing MB, which indicated that the adsorption process was attributed to physisorption through &#x3c0;-&#x3c0; interactions between NRGO and MB.</p>
<fig id="F9" position="float">
<label>FIGURE 9</label>
<caption>
<p>XPS spectra <bold>(A)</bold>, XRD patterns <bold>(B)</bold> and FTIR spectra <bold>(C)</bold> of NRGO, MB and NRGO-MB.</p>
</caption>
<graphic xlink:href="fchem-12-1484610-g009.tif"/>
</fig>
<p>Taking into account the adsorption kinetic, isotherms, and aforementioned characterizations, the adsorption mechanism was attributed to physisorption attracted by the &#x3c0;-&#x3c0; bonds between NRGO and MB.</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s3">
<title>3 Conclusion</title>
<p>In this study, NRGO was successfully synthesized via amination of GO and subsequently applied for MB adsorption. The effects of NRGO dosage, pH, contact time, and initial MB concentrations on adsorption were thoroughly examined, alongside the adsorption kinetics and isotherms. The results indicated that NRGO exhibited superior and consistent adsorption capacity towards MB at a wide pH range, with the adsorption process following the PSO kinetic model as well as Langmuir and Freundlich isotherm models. Furthermore, the potential adsorption mechanism, attributed to physisorption through &#x3c0;-&#x3c0; interactions between NRGO and MB, was verified through essential characterizations including SEM, EDX, XRD, XPS, and FTIR. These findings highlight the potential application value of NRGO in environmental treatment.</p>
</sec>
<sec id="s4">
<title>4 Experiment section</title>
<sec id="s4-1">
<title>4.1 Materials</title>
<p>Graphene oxide (GO) was prepared in our previous study. The chemicals used in the experiments, including N, N-Dimethylformamide (DMF), 1-(3-Dimethylaminopropyl)-3-ethylcarbodiimide hydrochloride (EDC), cis-9-Octadecenylamine, trichloromethane, petroleum, ethanol, sodium hydroxide (NaOH), hydrochloric acid (HCl) and methylene blue (MB), were all purchased from Chengdu Kelong Chemical Reagent Company (China), and used without further purification. Deionized water (18.25&#xa0;M&#x3a9;&#xa0;cm) was obtained using ULUPURE Water Purification System (Chengdu, China) and was used to prepare all aqueous solutions.</p>
</sec>
<sec id="s4-2">
<title>4.2 Preparation of NRGO and RGO</title>
<p>NRGO was prepared according to the previous reports. In brief, 0.30&#xa0;g of GO was weighed and dispersed in 50.0&#xa0;mL DMF under sonication for 30&#xa0;min and stirring for 1&#xa0;h. Then, 0.46&#xa0;g of EDC was dissolved in 20.0&#xa0;mL DMF by sonication. The EDC solution was added to GO dispersion, stirred for 2&#xa0;h and sonicated for 30&#xa0;min. Subsequently, 0.27&#xa0;g of NHS was dissolved to 10.0&#xa0;mL DMF under sonication and then was added to the above reaction system, stirred for 2&#xa0;h and sonicated for 30&#xa0;min to ensure complete reaction. Next, 1.28&#xa0;g of olamine was weighed and added to 10.0&#xa0;mL of chloroform. After the olamine completely dissolved, the solution was added to the above reaction system. Then the mixture was treated by sonicated at 40&#xb0;C for 30&#xa0;min and stirred overnight. The obtained material was filtered through organic membrane (0.22&#xa0;&#x3bc;m), followed by washing with petroleum ether and ethanol. Finally, the modified graphene oxide was obtained by freeze-drying and marked as N doped reduced graphene oxide (NRGO).</p>
<p>Reduced graphene oxide was prepared as follows:the 0.5&#xa0;mg/mL GO solution was transferred to polytetrafluoroethylene autoclave at 120&#xb0;C for 8&#xa0;h, and the reduced material was obtained as RGO.</p>
</sec>
<sec id="s4-3">
<title>4.3 Characterization of the samples</title>
<p>The surface morphologies of GO, NRGO, MB, and the composite after MB adsorption were examined by environmental scanning electron microscope (ESEM, JSM-IT500, JEOL Company, Japan). Materials compositions were analyzed by energy disperse X-ray spectroscopy (EDX, JEOL Company, Japan) and X-ray photoelectron spectroscopy (XPS, Kratos, Britain). Changes in the crystal structure of the materials were measured by X-ray powder diffraction (XRD, X&#x2019;Pert Pro, Philips, Netherlands). The alterations of functional groups of the material were determined using a Fourier transform infrared spectrometer (FTIR, Nicolet IS10, Thermo, America) with KBr pellets in a scanning range of 500&#x2013;4000&#xa0;cm<sup>&#x2212;1</sup>. The change of frame structure was measured by Raman spectrometer (Jobin Yvon S.A.S., HORIBA). The surface charge was detected by zeta potential analyzer (Zetasizer-ZS series, England).</p>
</sec>
<sec id="s4-4">
<title>4.4 Batch adsorption experiment</title>
<p>Batch adsorption tests were performed to assess the impact of various factors on the adsorption property of MB onto NRGO. The prepared NRGO was grinded into powder and the solid MB powder was dissolved in deionized water to prepare a methylene blue solution for subsequent experiments. For the adsorption experiments, different doses of NRGO with 300&#xa0;&#xb5;L of 0.3&#xa0;mg/mL of MB solution were firstly optimized to ensure the adsorption efficiency as high as possible. Subsequently, a certain amount of NRGO was introduced into MB solution of varying initial concentrations (to study the effect of concentration) at various pH values (for pH experiment) for different contact time (forvadsorption kinetic experiment). After adsorption at room temperature (25&#xb0;C), the absorbance of their supernatant was measured by U-2910 UV&#x2013;Vis spectrophotometer. The final concentration of MB after adsorption was calculated to determine the adsorption rate (<italic>E</italic>,%) and adsorption capacity (<italic>q</italic>, mg/g) according to experimental <xref ref-type="disp-formula" rid="e5">Equations 5</xref>, <xref ref-type="disp-formula" rid="e6">6</xref> as follows:<disp-formula id="e5">
<mml:math id="m5">
<mml:mrow>
<mml:mi mathvariant="normal">E</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mn>0</mml:mn>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:mi mathvariant="normal">C</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>/</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mn>0</mml:mn>
</mml:msub>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
<mml:mo>%</mml:mo>
</mml:mrow>
</mml:math>
<label>(5)</label>
</disp-formula>
<disp-formula id="e6">
<mml:math id="m6">
<mml:mrow>
<mml:mi>q</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mi>C</mml:mi>
<mml:mn>0</mml:mn>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>C</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#xd7;</mml:mo>
<mml:mi>V</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi>M</mml:mi>
</mml:mrow>
</mml:math>
<label>(6)</label>
</disp-formula>Where <italic>E</italic> is the adsorption efficiency of MB (%), <italic>q</italic> is the adsorption capacity of MB (mg/g), <italic>C</italic>
<sub>0</sub> and <italic>C</italic> are the initial and final concentration of MB solution (&#xb5;g/mL), respectively, <italic>V</italic> is the volume of MB solution (L), <italic>M</italic> is the mass of the adsorbent (g).</p>
</sec>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The original contributions presented in the study are included in the article/supplementary material, further inquiries can be directed to the corresponding author.</p>
</sec>
<sec sec-type="author-contributions" id="s6">
<title>Author contributions</title>
<p>MK: Writing&#x2013;original draft, Writing&#x2013;review and editing, Conceptualization, Data curation, Formal Analysis, Investigation, Methodology. YP: Visualization, Writing&#x2013;review and editing. YZ: Formal Analysis, Validation, Writing&#x2013;review and editing. LS: Methodology, Formal Analysis, Writing&#x2013;review and editing. YL: Investigation, Writing&#x2013;review and editing. HW: 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. This work was supported by the Fundamental Research Program of Shanxi Province (202303021222296), the Scientific and technological innovation projects of colleges and universities of Shanxi Province (2022L605, 2023L400), and the Foundation of Shanxi Province Key Laboratory of Higee-Oriented Chemical Engineering (No: 2023-HOCE06).</p>
</sec>
<ack>
<p>The authors would like to thank Liying Hao, Qiang Wei (State Key Laboratory of Oral Diseases, West China Hospital of Stomatology, Sichuan University) and Shuguang Yan (Analytical and Testing Center, Sichuan University) for their help in characterizing SEM, and XPS, respectively.</p>
</ack>
<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>
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