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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Mater.</journal-id>
<journal-title>Frontiers in Materials</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Mater.</abbrev-journal-title>
<issn pub-type="epub">2296-8016</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1602816</article-id>
<article-id pub-id-type="doi">10.3389/fmats.2025.1602816</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Materials</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Harnessing the power of novel ruthenium-MOF for efficient wastewater treatment</article-title>
<alt-title alt-title-type="left-running-head">Altharawi 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/fmats.2025.1602816">10.3389/fmats.2025.1602816</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Altharawi</surname>
<given-names>Ali</given-names>
</name>
<uri xlink:href="https://loop.frontiersin.org/people/2353355/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Aldakhil</surname>
<given-names>Taibah</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Alossaimi</surname>
<given-names>Manal A.</given-names>
</name>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Afzal</surname>
<given-names>Obaid</given-names>
</name>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/3020737/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
</contrib-group>
<aff>
<institution>Department of Pharmaceutical Chemistry</institution>, <institution>College of Pharmacy</institution>, <institution>Prince Sattam Bin Abdulaziz University</institution>, <addr-line>Al-Kharj</addr-line>, <country>Saudi Arabia</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/114599/overview">Saviour A. Umoren</ext-link>, King Fahd University of Petroleum and Minerals, Saudi Arabia</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/3048581/overview">Hifsa Khurshid</ext-link>, King Fahd University of Petroleum and Minerals, Saudi Arabia</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/3048847/overview">Ubong Etim</ext-link>, The University of Nottingham Ningbo, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Obaid Afzal, <email>o.akram@psau.edu.sa</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>17</day>
<month>06</month>
<year>2025</year>
</pub-date>
<pub-date pub-type="collection">
<year>2025</year>
</pub-date>
<volume>12</volume>
<elocation-id>1602816</elocation-id>
<history>
<date date-type="received">
<day>30</day>
<month>03</month>
<year>2025</year>
</date>
<date date-type="accepted">
<day>02</day>
<month>06</month>
<year>2025</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2025 Altharawi, Aldakhil, Alossaimi and Afzal.</copyright-statement>
<copyright-year>2025</copyright-year>
<copyright-holder>Altharawi, Aldakhil, Alossaimi and Afzal</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 novel metal-organic framework (MOF) was synthesized using 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid and ruthenium (III) chloride via microwave-assisted synthesis. The resulting ruthenium-MOF exhibited a high specific surface area (1856 m<sup>2</sup>/g), and the inclusion of ruthenium, known for its biological activity, endowed the structure with potent antimicrobial properties against key wastewater bacterial strains. Furthermore, its abundant hydrogen bonding sites enhanced its adsorption capacity for phenol red, a major waterborne pollutant. The synthesized MOF demonstrated superior antimicrobial activity compared to certain commercial antibiotics. In adsorption experiments, 0.06 g/L of the MOF successfully removed 92% of 0.6 mg/L phenol red at pH 7 within 75 min, highlighting its rapid and efficient pollutant removal capability. These dual functions, antimicrobial and adsorptive, emphasize the potential of this ruthenium-MOF for practical environmental remediation and wastewater treatment applications.</p>
</abstract>
<kwd-group>
<kwd>ruthenium-based MOF</kwd>
<kwd>absorbent</kwd>
<kwd>bacterial inhibitor</kwd>
<kwd>biological polluta nts</kwd>
<kwd>chemical pollutants</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Polymeric and Composite Materials</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Phenol red is a widely used water-soluble dye that functions primarily as a pH indicator. It exhibits a color transition from yellow to red within the pH range of 6.6&#x2013;8.0 and turns bright pink at pH values above 8.1 (<xref ref-type="bibr" rid="B59">Steinegger et al., 2020</xref>). Due to its sensitivity to pH changes, phenol red finds extensive applications in biomedical research, histology (<xref ref-type="bibr" rid="B11">Benson et al., 2022</xref>), environmental monitoring (<xref ref-type="bibr" rid="B25">Idris et al., 2024</xref>), culture media (<xref ref-type="bibr" rid="B49">Raffay et al., 2022</xref>), pool testing kits (<xref ref-type="bibr" rid="B47">Qin et al., 2023</xref>), and cell culture systems (<xref ref-type="bibr" rid="B64">Weiskirchen et al., 2023</xref>). Although it is not classified as carcinogenic, concerns regarding its toxicological effects have been raised. Contact with skin may lead to sensitization and irritation (<xref ref-type="bibr" rid="B40">Olusegun and Martincigh, 2021</xref>), while eye exposure can result in damage (<xref ref-type="bibr" rid="B27">Kecskem&#xe9;ti et al., 2022</xref>). Ingestion is also considered hazardous (<xref ref-type="bibr" rid="B14">DeLoid et al., 2024</xref>; <xref ref-type="bibr" rid="B7">An et al., 2025</xref>). Given its widespread usage and environmental persistence, phenol red is commonly detected in wastewater and is regarded as a potentially harmful pollutant.</p>
<p>In addition to chemical contaminants such as phenol red, wastewater is frequently burdened with biological pollutants, particularly pathogenic microorganisms. Bacteria <italic>including Salmonella enterica</italic>, <italic>C. jejuni</italic>, <italic>E. coli</italic>, <italic>L. pneumophila</italic>, and <italic>Shigella dysenteriae</italic> are commonly identified in untreated or poorly treated wastewater (<xref ref-type="bibr" rid="B10">Bej et al., 2023</xref>; <xref ref-type="bibr" rid="B55">Singh et al., 2024</xref>). These pathogens pose serious health threats: <italic>S. enterica</italic> is responsible for typhoid fever (<xref ref-type="bibr" rid="B1">Abro et al., 2024</xref>); <italic>Campylobacter jejuni</italic> causes fever and watery diarrhea (<xref ref-type="bibr" rid="B71">Zouganeli et al., 2024</xref>); <italic>Escherichia coli</italic> is associated with gastroenteritis (<xref ref-type="bibr" rid="B51">Roy et al., 2024</xref>); <italic>Legionella pneumophila</italic> may lead to Pontiac fever (<xref ref-type="bibr" rid="B43">Perez Ortiz et al., 2021</xref>); and <italic>S. dysenteriae</italic> results in severe dysentery and intestinal ulceration (<xref ref-type="bibr" rid="B36">Moxley, 2022</xref>). Effective strategies are therefore required to remove both chemical and biological pollutants from wastewater to safeguard public and environmental health.</p>
<p>A variety of methods have been investigated for phenol red removal, including chemical treatments (<xref ref-type="bibr" rid="B2">Abu-Nada et al., 2021</xref>) and adsorption techniques employing nanomaterials (<xref ref-type="bibr" rid="B20">Ho, 2022</xref>; <xref ref-type="bibr" rid="B35">Mousavi et al., 2023</xref>). Among advanced adsorbents, metal-organic frameworks (MOFs) have gained considerable attention due to their tunable porosity, high surface area, and diverse chemical functionalities (<xref ref-type="bibr" rid="B57">Song and Qin, 2022</xref>).</p>
<p>Some MOFs have demonstrated promising industrial and biomedical applications, including catalysis (<xref ref-type="bibr" rid="B62">Wang et al., 2025</xref>) and antibacterial activity (<xref ref-type="bibr" rid="B30">Li et al., 2025</xref>). Their antimicrobial properties are often attributed to the presence of metal centers, which disrupt microbial membranes, and to structural features such as porosity and surface area that promote physical entrapment or interaction with pathogens (<xref ref-type="bibr" rid="B12">Borsagli et al., 2019</xref>; <xref ref-type="bibr" rid="B31">Li et al., 2021</xref>; <xref ref-type="bibr" rid="B9">Arunkumar et al., 2024</xref>; <xref ref-type="bibr" rid="B16">Ding et al., 2024</xref>; <xref ref-type="bibr" rid="B52">Sharafudheen et al., 2024</xref>). High specific surface area in particular enhances contact between the MOF surface and target pollutants, thereby improving both adsorption efficiency and antimicrobial activity (<xref ref-type="bibr" rid="B17">Farasati Far, 2024</xref>; <xref ref-type="bibr" rid="B24">Hu et al., 2024</xref>; <xref ref-type="bibr" rid="B66">Yao et al., 2024</xref>; <xref ref-type="bibr" rid="B69">Zhang et al., 2024</xref>).</p>
<p>Ruthenium is a transition metal known for its biological activity and has been incorporated into various MOFs with demonstrated potential for therapeutic and environmental applications (<xref ref-type="bibr" rid="B37">Nakhjiri et al., 2022</xref>; <xref ref-type="bibr" rid="B56">Skoczynska et al., 2023</xref>). Ruthenium-based compounds have shown anti-inflammatory and antimicrobial properties (<xref ref-type="bibr" rid="B58">Southam et al., 2017</xref>; <xref ref-type="bibr" rid="B54">Singh and Barman, 2021</xref>; <xref ref-type="bibr" rid="B32">Liu et al., 2022</xref>), and their integration into MOF structures can enhance resistance to degradation while preserving or even improving functional performance (<xref ref-type="bibr" rid="B38">Naseer et al., 2022</xref>; <xref ref-type="bibr" rid="B50">Rajendran et al., 2024</xref>).</p>
<p>In this study, a novel ruthenium-based MOF was synthesized using ruthenium (III) chloride and 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid. Owing to its large specific surface area and presence of biologically active sites, the material was evaluated for its capacity to adsorb phenol red and inhibit bacterial pathogens commonly found in wastewater. The results demonstrated that the synthesized ruthenium-MOF exhibited high efficacy in removing both chemical and biological contaminants. The antimicrobial activity of ruthenium, coupled with the MOF&#x2019;s porosity and extensive surface area, contributes to its strong potential for dual-function wastewater treatment. This underscores the novelty and practical relevance of our findings in addressing complex pollution challenges.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Material and devises</title>
<p>Ruthenium (III) chloride (99.95%, Otto Chemie Pvt. Ltd.) and 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid (95%, Ambeed) were used as precursors for the synthesis of the ruthenium-MOF. Mueller Hinton Agar and Mueller Hinton Broth (HiMedia) were utilized for antimicrobial studies, and bacterial strains were obtained from the American Type Culture Collection (ATCC). Phenol red (analytical grade), sodium hydroxide (99.95%, Merck), and hydrochloric acid (37%, Merck) were used in the phenol red adsorption studies.</p>
<p>A BP211 laboratory-grade microwave reactor was employed for MOF synthesis, while an LMSP-UV1000B UV-Visible spectrophotometer was used to assess pollutant adsorption and antimicrobial efficacy.</p>
</sec>
<sec id="s2-2">
<title>2.2 Synthesis of ruthenium-MOF</title>
<p>To synthesize the ruthenium-MOF, 1 mmol of ruthenium (III) chloride and 2 mmol of 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid were dissolved in 25 mL of deionized water and stirred at 500 rpm at room temperature until a homogeneous solution was obtained. The mixture was then exposed to microwave irradiation. The temperature was gradually increased from 25&#xb0;C to 180&#xb0;C at a rate of 10&#xb0;C/min and maintained at 180&#xb0;C for 20 min under continuous irradiation at 320 W. After cooling for 30 min, the resulting precipitate was separated via nanofiltration, washed three times with a 1:1 mixture of deionized water and ethanol, and dried under vacuum at 100&#xb0;C for 4 h (<xref ref-type="bibr" rid="B5">Al-dolaimy et al., 2023</xref>; <xref ref-type="bibr" rid="B3">Ahmad et al., 2024</xref>)</p>
</sec>
<sec id="s2-3">
<title>2.3 Characterization</title>
<p>To confirm the structure and properties of the synthesized ruthenium-MOF, the following characterization techniques were used:</p>
<p>Nitrogen adsorption/desorption analysis: Conducted at 77 K with relative pressures from 0.01 to 0.99 using the ASAP 2020 instrument to determine BET surface area and pore size distribution via BJH or DFT models.</p>
<p>X-ray diffraction (XRD): Performed using Cu K&#x3b1; radiation at 40 kV/30 mA over a 2&#x3b8; range of 10&#xb0;&#x2013;70&#xb0;, with a step size of 0.02&#xb0; and scan speed of 1 s/step (Drawell DW-XRD-27Mini Desktop).</p>
<p>Scanning electron microscopy (SEM) and energy-dispersive X-ray spectroscopy (EDAX): Conducted using a TESCAN VEGA 3 at 15 kV with a working distance of 10 mm in high vacuum mode.</p>
<p>Elemental analysis (CHNO): Carried out using a FlashSmart Elemental Analyzer by combustion in excess oxygen at 1100&#xb0;C.</p>
<p>Fourier-transform infrared spectroscopy (FT-IR): Acquired using the KBr pellet method on a DW-FTIR-530A Drawell spectrometer.</p>
<p>Thermogravimetric analysis (TGA): Conducted from 25&#xb0;C to 600&#xb0;C at a heating rate of 10&#xb0;C/min using a GA BXT-TGA-1250.</p>
</sec>
<sec id="s2-4">
<title>2.4 Wastewater treatment</title>
<sec id="s2-4-1">
<title>2.4.1 Inhibition of biological agents</title>
<p>The antimicrobial efficacy of the synthesized ruthenium-MOF was assessed using a range of concentrations (1&#x2013;1024 &#x3bc;g/mL) against bacterial suspensions (1 &#xd7; 10<sup>5</sup> CFU/mL) of selected wastewater pathogens. The methods and standards established by the Clinical and Laboratory Standards Institute (CLSI) were followed in accordance with previous studies (<xref ref-type="bibr" rid="B34">Moghaddam-Manesh et al., 2020</xref>; <xref ref-type="bibr" rid="B22">Hsu et al., 2024</xref>). The tests performed included:</p>
<p>Minimum Inhibitory Concentration (MIC): A mixture of 100 &#x3bc;L of ruthenium-MOF solution (various concentrations), 100 &#x3bc;L of Mueller Hinton Broth, and 10 &#x3bc;L of bacterial suspension was incubated at 37&#xb0;C for 48 h. The MIC was defined as the lowest concentration that completely inhibited visible bacterial growth (<xref ref-type="bibr" rid="B34">Moghaddam-Manesh et al., 2020</xref>; <xref ref-type="bibr" rid="B22">Hsu et al., 2024</xref>).</p>
<p>Minimum Bactericidal Concentration (MBC): Aliquots from the MIC test and subsequent dilutions were plated on Mueller Hinton Agar and incubated at 37&#xb0;C for 72 h. The MBC was recorded as the lowest concentration at which no bacterial colonies were observed (<xref ref-type="bibr" rid="B34">Moghaddam-Manesh et al., 2020</xref>; <xref ref-type="bibr" rid="B22">Hsu et al., 2024</xref>).</p>
<p>Inhibition Zone Diameter (IZD): The disk diffusion method was employed using sterile paper disks impregnated with 10 &#x3bc;L of ruthenium-MOF at MIC concentrations. The disks were placed on inoculated agar plates and incubated at 37&#xb0;C for 48 h. The diameter of the inhibition zone was measured using calipers (<xref ref-type="bibr" rid="B34">Moghaddam-Manesh et al., 2020</xref>; <xref ref-type="bibr" rid="B22">Hsu et al., 2024</xref>).</p>
</sec>
<sec id="s2-4-2">
<title>2.4.2 Adsorption of chemical agents</title>
<p>Phenol red adsorption experiments were conducted using different initial dye concentrations, MOF dosages, pH levels (4-10), temperatures (25&#xb0;C&#x2013;60&#xb0;C), and contact times (25&#x2013;200 min). In each test, ruthenium-MOF was added to 25 mL of phenol red solution, and the mixture was agitated at 140 rpm. After the desired reaction time, the suspension was centrifuged at 6000 rpm for 10 min, and the absorbance of the supernatant was measured at 430 nm using a UV-Vis spectrophotometer. The removal efficiency (Re, %) was calculated using the <xref ref-type="disp-formula" rid="e1">Equation 1</xref> (<xref ref-type="bibr" rid="B6">Aljubiri et al., 2024</xref>; <xref ref-type="bibr" rid="B33">Moghaddam-Manesh et al., 2024</xref>):<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:mi>R</mml:mi>
<mml:mi>e</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mo>%</mml:mo>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mfrac>
<mml:mrow>
<mml:mi>C</mml:mi>
<mml:mn>0</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>C</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mi>C</mml:mi>
<mml:mn>0</mml:mn>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#xd7;</mml:mo>
<mml:mn>100</mml:mn>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
</p>
<p>The initial concentration of phenol red (mg/L) &#x3d; C<sub>0</sub>
</p>
<p>The equilibrium concentration of phenol red (mg/L) &#x3d; C<sub>e</sub>
</p>
<p>
<xref ref-type="disp-formula" rid="e1">Equation 1</xref>. Phenol red adsorption percentage using ruthenium-MOF.</p>
</sec>
</sec>
</sec>
<sec id="s3">
<title>3 Result and discussion</title>
<sec id="s3-1">
<title>3.1 Synthesis and characterization</title>
<p>Microwave-assisted synthesis has emerged as a rapid and efficient method for producing metal-organic frameworks (MOFs) with desirable physicochemical properties. This technique has been reported to yield MOFs with high crystallinity, nanoscale particle size, and large specific surface area (<xref ref-type="bibr" rid="B19">G&#x142;owniak et al., 2021</xref>; <xref ref-type="bibr" rid="B8">Annamalai et al., 2022</xref>). In this study, a ruthenium-based MOF was successfully synthesized using ruthenium (III) chloride and 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid under controlled microwave conditions, following previously optimized protocols (<xref ref-type="bibr" rid="B5">Al-dolaimy et al., 2023</xref>; <xref ref-type="bibr" rid="B3">Ahmad et al., 2024</xref>).</p>
<p>Nitrogen adsorption/desorption analysis revealed that the synthesized MOF exhibits a remarkably high specific surface area of 1856 m<sup>2</sup>/g, as illustrated in <xref ref-type="fig" rid="F1">Figure 1</xref>. The isotherms corresponded to a type IV profile, characteristic of mesoporous materials (<xref ref-type="bibr" rid="B13">Calzaferri et al., 2022</xref>; <xref ref-type="bibr" rid="B23">Hu et al., 2023</xref>; <xref ref-type="bibr" rid="B42">Peng et al., 2024</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Nitrogen adsorption and desorption curve of synthesized ruthenium-MOF [(I): BET, b (II): BJH].</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g001.tif">
<alt-text content-type="machine-generated">Two graphs are shown. Graph I on the left depicts isotherm data with adsorption and desorption curves plotted as relative pressure versus volume adsorbed. Graph II on the right shows pore size distribution, with a peak around 0.5 nanometers indicating the majority of pore sizes.</alt-text>
</graphic>
</fig>
<p>The surface area and pore characteristics, including BET surface area, Barrett&#x2013;Joyner&#x2013;Halenda (BJH) pore volume, and mean pore diameter (MPD), are summarized in <xref ref-type="table" rid="T1">Table 1</xref>.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>N<sub>2</sub> adsorption-desorption of ruthenium-MOF.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Brunauer&#x2013;Emmett&#x2013;Teller (m<sup>3</sup>/g)</th>
<th align="center">Barett-Joyner-Halenda (cm<sup>3</sup>/g)</th>
<th align="center">Mean pore diameter (nm)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">1856</td>
<td align="center">0.46</td>
<td align="center">1.37</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>X-ray diffraction (XRD) analysis confirmed the crystalline nature of the synthesized MOF (<xref ref-type="fig" rid="F2">Figure 2</xref>). Distinct diffraction peaks were observed at 2&#x3b8; values of 39.9&#xb0;, 42.1&#xb0;, 44.8&#xb0;, and 58.3&#xb0;, corresponding to the (101), (102), (110), and (112) planes, respectively, as referenced by JCPDS card No. 06-0663 (<xref ref-type="bibr" rid="B61">Tee et al., 2015</xref>; <xref ref-type="bibr" rid="B41">Pang et al., 2021</xref>; <xref ref-type="bibr" rid="B63">Wang et al., 2023</xref>). The average crystallite size, calculated using the Scherrer equation, was approximately 92 nm (<xref ref-type="bibr" rid="B21">Holzwarth and Gibson, 2011</xref>; <xref ref-type="bibr" rid="B39">Nasiri et al., 2023</xref>).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>XRD of synthesized ruthenium-MOF (I): Reported JCPDS No 06-0663 for ruthenium; (II): Synthesized ruthenium-MOF).</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g002.tif">
<alt-text content-type="machine-generated">X-ray diffraction pattern showing intensity versus 2 theta degrees. The blue line represents experimental data with peaks labeled (101), (102), (110), and (112). The red bars below correspond to JCPDS card number 06-0663 for reference.</alt-text>
</graphic>
</fig>
<p>Scanning electron microscopy (SEM) revealed uniform morphology with particle sizes averaging 85 nm and no observable agglomeration (<xref ref-type="fig" rid="F3">Figure 3</xref>).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>SEM image of synthesized ruthenium-MOF.</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g003.tif">
<alt-text content-type="machine-generated">Scanning electron microscope image showing a granular, rough surface texture with irregularly shaped particles clustered together. The scale bar indicates a size of five hundred nanometers.</alt-text>
</graphic>
</fig>
<p>These findings confirm that the adopted synthesis method is effective for producing a highly crystalline and nanoscale MOF with significant surface area and porosity.</p>
<p>Elemental analysis and energy-dispersive X-ray spectroscopy (EDAX) were employed to confirm the presence of ruthenium and other constituent elements. The results are presented in <xref ref-type="table" rid="T2">Table 2</xref>; <xref ref-type="fig" rid="F4">Figure 4</xref>.</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>EA result of ruthenium-MOF.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">C (%)</th>
<th align="center">H (%)</th>
<th align="center">N (%)</th>
<th align="center">O (%)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">52.83</td>
<td align="center">3.46</td>
<td align="center">8.21</td>
<td align="center">19.08</td>
</tr>
</tbody>
</table>
</table-wrap>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>EDAX of synthesized ruthenium-MOF.</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g004.tif">
<alt-text content-type="machine-generated">Energy-dispersive X-ray spectroscopy (EDS) graph showing peaks for elements. Peaks are labeled for oxygen (O), carbon (C), nitrogen (N), and ruthenium (Ru), with carbon having the highest intensity. The x-axis represents energy in kiloelectronvolts (keV), ranging from zero to five.</alt-text>
</graphic>
</fig>
<p>The proposed molecular structure of the ruthenium-MOF, shown in <xref ref-type="fig" rid="F5">Figure 5</xref>, is consistent with the XRD and elemental analysis data.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Structure of synthesized ruthenium-MOF.</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g005.tif">
<alt-text content-type="machine-generated">Chemical structure diagram of a complex organic compound featuring cyclic aromatic rings and various functional groups, connected by single and double bonds. The compound includes repeat units and appears to be part of a polymer network.</alt-text>
</graphic>
</fig>
<p>Fourier-transform infrared (FT-IR) spectroscopy further verified the structural integrity of the MOF. The spectrum of the synthesized product (<xref ref-type="fig" rid="F6">Figures 6&#x2013;II</xref>) demonstrated characteristic absorption bands: Ru&#x2013;N and Ru&#x2013;O bonds in the 400&#x2013;600 cm<sup>&#x2212;1</sup> region (<xref ref-type="bibr" rid="B18">Feng et al., 2022</xref>; <xref ref-type="bibr" rid="B26">Jin et al., 2022</xref>; <xref ref-type="bibr" rid="B4">Akl et al., 2023</xref>), C-H at 3025 cm<sup>&#x2212;1</sup>, C&#x3d;O at 1680 cm<sup>&#x2212;1</sup>, N&#x3d;N at 1565 cm<sup>&#x2212;1</sup>, C&#x3d;C at 1460 cm<sup>&#x2212;1</sup>, N-C at 1100 cm<sup>&#x2212;1</sup>, and C-O at 1025 cm<sup>&#x2212;1</sup>. The broad O&#x2013;H peak at 3250 cm<sup>&#x2212;1</sup>, present in the free ligand, was absent in the MOF spectrum, suggesting successful coordination of the ligand through its oxygen atoms.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>FT-IR spectrum of 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid (I) and synthesized ruthenium-MOF (II).</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g006.tif">
<alt-text content-type="machine-generated">Two infrared spectra labeled (I) and (II) are shown with transmittance percentage on the vertical axis and wavenumber in centimeters inverse on the horizontal axis. Peaks are marked for functional groups, including O-H and C-H in (I), and C-H, C=C, C=O, N=N, C-N, C-O, Ru-O, Ru-N in (II).</alt-text>
</graphic>
</fig>
<p>The FT-IR spectrum of the ruthenium-MOF, as shown in <xref ref-type="fig" rid="F6">Figures 6&#x2013;II</xref>, confirms the presence of the ligand in the structure, as all ligand peaks are observed. Additionally, the broad oxygen-hydrogen peak (3250 cm<sup>&#x2212;1</sup>), which is absent in the FTIR spectrum of the ruthenium-MOF, indicates the binding of the 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid to the ruthenium through the oxygen side. Therefore, oxygen-ruthenium and nitrogen-ruthenium bonds, observed in previous studies in the 400 cm<sup>-1</sup> - 600 cm<sup>&#x2212;1</sup> (<xref ref-type="bibr" rid="B18">Feng et al., 2022</xref>; <xref ref-type="bibr" rid="B26">Jin et al., 2022</xref>; <xref ref-type="bibr" rid="B4">Akl et al., 2023</xref>), and two peaks have been observed in this area, so Ru-N and Ru-O are sites of ruthenium complexation with the 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid, as seen in the FTIR spectrum of the ruthenium-MOF.</p>
<p>Thermogravimetric analysis (TGA) demonstrated the thermal stability of the ruthenium-MOF. The material remained stable up to approximately 350&#xb0;C, with two major weight loss events observed around 350&#xb0;C and 520&#xb0;C. These correspond to the decomposition of the organic ligand and subsequent breakdown of the MOF network.</p>
</sec>
<sec id="s3-2">
<title>3.2 Wastewater treatment results</title>
<p>Given the characterization of the newly synthesized ruthenium-MOF, which had a high specific surface area and high porosity, and the antimicrobial nature of ruthenium, the antimicrobial properties and phenol adsorption were investigated and discussed below.</p>
<sec id="s3-2-1">
<title>3.2.1 Results of inhibition of biological agents</title>
<p>As mentioned in the introduction, <italic>Salmonella enterica (ATCC 35664), Campylobacter jejuni (ATCC 700819), Escherichia coli (ATCC 25922), Legionella pneumophila (ATCC 33152), and Shigella dysenteriae (ATCC 13313)</italic> can be identified as the most important pathogenic agents present in wastewater. The investigation of the inhibition properties of these biological agents by the ruthenium-MOF was conducted using MIC and MBC, as well as measuring the IZD. The findings of these studies are presented in <xref ref-type="table" rid="T3">Table 3</xref>.</p>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Antimicrobial results.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="center">Compounds</th>
<th rowspan="2" colspan="2" align="center">Parameters</th>
<th colspan="5" align="center">Strains</th>
</tr>
<tr>
<th align="center">
<italic>Salmonella enterica</italic>
</th>
<th align="center">
<italic>Campylobacter</italic> jejuni</th>
<th align="center">
<italic>Escherichia coli</italic>
</th>
<th align="center">
<italic>Legionella pneumophila</italic>
</th>
<th align="center">
<italic>Shigella dysenteriae</italic>
</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td rowspan="6" align="center">Ruthenium-MOF</td>
<td rowspan="2" align="center">MIC (mg/mL)</td>
<td align="left">Amount</td>
<td align="center">32</td>
<td align="center">16</td>
<td align="center">1</td>
<td align="center">32</td>
<td align="center">128</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.01</td>
<td align="center">0.03</td>
<td align="center">0.03</td>
<td align="center">0.00</td>
<td align="center">0.002</td>
</tr>
<tr>
<td rowspan="2" align="center">MBC (mg/mL)</td>
<td align="left">Amount</td>
<td align="center">64</td>
<td align="center">32</td>
<td align="center">2</td>
<td align="center">64</td>
<td align="center">256</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.00</td>
<td align="center">0.01</td>
<td align="center">0.04</td>
<td align="center">0.00</td>
<td align="center">0.02</td>
</tr>
<tr>
<td rowspan="2" align="center">IZD (mm)</td>
<td align="left">Amount</td>
<td align="center">12.67 &#xb1; 0.9</td>
<td align="center">15.29 &#xb1; 1.2</td>
<td align="center">20.77 &#xb1; 0.9</td>
<td align="center">13.46 &#xb1; 0.9</td>
<td align="center">12.92 &#xb1; 0.9</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.01</td>
<td align="center">0.01</td>
<td align="center">0.02</td>
<td align="center">0.00</td>
<td align="center">0.03</td>
</tr>
<tr>
<td rowspan="6" align="center">Cefazolin</td>
<td rowspan="2" align="center">MIC (mg/mL)</td>
<td align="left">Amount</td>
<td align="center">32</td>
<td align="center">Ineffectiveness</td>
<td align="center">2</td>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.04</td>
<td align="center">Ineffectiveness</td>
<td align="center">0.00</td>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td rowspan="2" align="center">MBC (mg/mL)</td>
<td align="left">Amount</td>
<td align="center">64</td>
<td align="center">Ineffectiveness</td>
<td align="center">4</td>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.01</td>
<td align="center">Ineffectiveness</td>
<td align="center">0.02</td>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td rowspan="2" align="center">IZD (mm)</td>
<td align="left">Amount</td>
<td align="center">15.31</td>
<td align="center">Ineffectiveness</td>
<td align="center">21.67</td>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.03</td>
<td align="center">Ineffectiveness</td>
<td align="left"/>
<td align="center">Ineffectiveness</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td rowspan="6" align="center">Azithromycin</td>
<td rowspan="2" align="center">MIC (&#x3bc;g/mL)</td>
<td align="left">Amount</td>
<td align="center">8</td>
<td align="center">8</td>
<td align="center">1</td>
<td align="center">16</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.00</td>
<td align="center">0.04</td>
<td align="center">0.01</td>
<td align="center">0.00</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td rowspan="2" align="center">MBC (mg/mL)</td>
<td align="left">Amount</td>
<td align="center">16</td>
<td align="center">8</td>
<td align="center">2</td>
<td align="center">32</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.02</td>
<td align="center">0.03</td>
<td align="center">0.01</td>
<td align="center">0.04</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td rowspan="2" align="center">IZD (mm)</td>
<td align="left">Amount</td>
<td align="center">19.08</td>
<td align="center">18.69</td>
<td align="center">22.81</td>
<td align="center">17.54</td>
<td align="center">Ineffectiveness</td>
</tr>
<tr>
<td align="center">p-value</td>
<td align="center">0.01</td>
<td align="center">0.00</td>
<td align="center">0.00</td>
<td align="center">0.03</td>
<td align="center">Ineffectiveness</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The results from the table indicate that the ruthenium-MOF was able to inhibit all the studied strains, with MIC values of 32 &#x3bc;g/mL <italic>Salmonella enterica</italic>, 16 &#x3bc;g/mL <italic>Campylobacter jejuni</italic>, 1 &#x3bc;g/mL against <italic>Escherichia coli</italic>, 32 &#x3bc;g/mL against <italic>Legionella pneumophila</italic>, and 128 &#x3bc;g/mL against <italic>Shigella dysenteriae</italic>.</p>
<p>As mentioned, high specific surface area of synthesized ruthenium-MOF and more excellent contact with the studied bacterial agents, along with the presence of a ruthenium compound with strong antibacterial properties and a ligand known to possess several antibacterial properties (<xref ref-type="bibr" rid="B58">Southam et al., 2017</xref>; <xref ref-type="bibr" rid="B54">Singh and Barman, 2021</xref>; <xref ref-type="bibr" rid="B46">Pourmadadi et al., 2023</xref>; <xref ref-type="bibr" rid="B60">Tan et al., 2023</xref>), can be considered factors contributing to the effective inhibition of the studied strains. Additionally, <italic>C. jejuni</italic>, <italic>L. pneumophila</italic>, and <italic>S. dysenteriae</italic> were resistant to cefazolin, and <italic>S. dysenteriae</italic> were resistant to azithromycin, a well-known antibiotic on the market, indicating that the compound synthesized in this study has superior antibacterial properties compared to cefazolin.</p>
<p>Each experiment was independently conducted three times to ensure reproducibility. The MIC and MBC values remained stable across replicates, while the inhibition zone diameters (IZD) are summarized as mean values with corresponding standard deviations (SD). Statistical significance was assessed using p-values to examine the influence of compound concentration on antibacterial activity. The findings suggest a strong concentration-dependent effect on MIC, MBC, and IZD parameters, particularly for the tested Ruthenium-MOF and Azithromycin compounds.</p>
</sec>
<sec id="s3-2-2">
<title>3.2.2 Results of adsorption of chemical agents</title>
<p>The ruthenium-MOF demonstrated excellent adsorption performance for phenol red, attributable to its high surface area, porosity, and abundance of hydrogen bonding sites (<xref ref-type="bibr" rid="B65">Wu et al., 2020</xref>; <xref ref-type="bibr" rid="B29">Lau et al., 2022</xref>; <xref ref-type="bibr" rid="B70">Zhou et al., 2024</xref>). Phenol red exists in two tautomeric forms depending on pH: one in acidic conditions (7-I) and another in alkaline conditions (7-II). The synthesized MOF was able to adsorb phenol red in both environments through hydrogen bonding and electrostatic interactions, as depicted in <xref ref-type="fig" rid="F7">Figures 7&#x2013;III</xref>.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Structure of phenol red in acidic (I) and alkaline (II) environments and its adsorption by synthesized ruthenium-MOF (III).</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g007.tif">
<alt-text content-type="machine-generated">Chemical structures labeled (I), (II), and (III). Structures (I) and (II) are simpler, consisting of red and black molecular diagrams. Structure (III) is more complex, with interconnected rings and chains, incorporating both red and black elements.</alt-text>
</graphic>
</fig>
<p>To evaluate the adsorption performance, several experimental parameters were optimized, including initial dye concentration, adsorbent dose, pH, temperature, and contact time.</p>
<sec id="s3-2-2-1">
<title>3.2.2.1 Phenol red concentration effect</title>
<p>Phenol red concentrations ranging from 100 to 1000 mg/L were tested using 0.01 g of ruthenium-MOF under fixed conditions (pH 7, 25&#xb0;C, 50 min). As shown in <xref ref-type="fig" rid="F8">Figures 8&#x2013;I</xref>, the adsorption efficiency decreased with increasing dye concentration. This inverse relationship is attributed to the limited number of active hydrogen bonding sites, which become saturated at higher dye concentrations (<xref ref-type="bibr" rid="B68">Zhang et al., 2021</xref>).</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>Phenol red adsorption study results using synthesized ruthenium-MOF (I: Phenol red concentrations, II: Ruthenium-MOF concentrations, III: pH, IV: Temperature, V: Time).</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g008.tif">
<alt-text content-type="machine-generated">Five line graphs displaying adsorption percentages: 1. Phenol red concentrations: Adsorption decreases from about 95% to 20% as concentration increases from 100 to 1000 mg/L. 2. Ruthenium-MOF concentrations: Adsorption remains stable around 90% across concentrations from 0.02 to 0.1 g/L. 3. pH: Adsorption peaks near 8 pH, reaching nearly 90%. 4. Temperature: Adsorption slightly increases from 90% at 25&#xb0;C to 95% at 60&#xb0;C. 5. Time: Adsorption rises rapidly to about 90% at 75 minutes, then stabilizes.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-2-2-2">
<title>3.2.2.2 Amount of adsorbent effect</title>
<p>To identify the optimal adsorbent dosage, various concentrations of ruthenium-MOF (0.01&#x2013;0.10 g/L) were tested. The results (<xref ref-type="fig" rid="F8">Figures 8&#x2013;II</xref>) indicate that adsorption increased with increasing adsorbent amount, reaching a plateau at 0.06 g/L. Beyond this point, additional adsorbent did not significantly improve removal efficiency, likely due to particle agglomeration and site carbonization (<xref ref-type="bibr" rid="B45">Poon et al., 2022</xref>). Therefore, 0.06 g/L was used in subsequent experiments.</p>
</sec>
<sec id="s3-2-2-3">
<title>3.2.2.3 pH effect</title>
<p>Phenol red adsorption was evaluated across a pH range of 4&#x2013;10, maintaining constant adsorbent dose, temperature, and contact time. Maximum adsorption occurred at pH 8 (<xref ref-type="fig" rid="F8">Figures 8&#x2013;III</xref>). At this pH, the anionic form of phenol red interacts more effectively with electron-rich oxygen and nitrogen atoms in the MOF structure. Conversely, extreme acidic and alkaline conditions were detrimental to adsorption, likely due to hydrolysis or protonation effects (<xref ref-type="bibr" rid="B53">Siddique et al., 2024</xref>; <xref ref-type="bibr" rid="B44">Pessoa and Correia, 2021</xref>; <xref ref-type="bibr" rid="B67">Yesil et al., 2021</xref>). Nevertheless, since the difference between pH 7 and pH 8 was minimal, further tests were conducted at neutral pH.</p>
</sec>
<sec id="s3-2-2-4">
<title>3.2.2.4 Temperature effect</title>
<p>Temperature variation (25&#xb0;C&#x2013;60&#xb0;C) showed a positive correlation with adsorption performance (<xref ref-type="fig" rid="F8">Figures 8&#x2013;IV</xref>). Higher temperatures enhanced molecular motion and diffusion rates, resulting in increased adsorption of phenol red (<xref ref-type="bibr" rid="B48">Qiu et al., 2022</xref>).</p>
</sec>
<sec id="s3-2-2-5">
<title>3.2.2.5 Time effect</title>
<p>Adsorption were evaluated over contact times ranging from 30 to 120 min. Maximum adsorption occurred at 75 min, after which equilibrium was reached (<xref ref-type="fig" rid="F8">Figures 8&#x2013;V</xref>). The saturation of active adsorption sites explains the observed plateau beyond this time point.</p>
<p>The excellent adsorption performance is largely attributed to the high surface area and mesoporosity of the MOF structure, which provide abundant access to active binding sites (<xref ref-type="bibr" rid="B15">Dendy et al., 2025</xref>). Under optimal conditions (0.06 g/L MOF, 0.6 mg/L phenol red, pH 7, 25&#xb0;C, 75 min), the ruthenium-MOF achieved 92% removal efficiency (23 mg/g), outperforming several previously reported MOFs (<xref ref-type="table" rid="T4">Table 4</xref>).</p>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Comparison dye adsorption of ruthenium-MOF with other MOFs.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">MOF type</th>
<th align="center">Target dye</th>
<th align="center">Optimal conditions</th>
<th align="center">Adsorption capacity</th>
<th align="center">Reference</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Ruthenium-MOF (This work)</td>
<td align="center">Phenol red</td>
<td align="center">pH 7, 0.06 g/L, 75 min, 25&#xb0;C</td>
<td align="center">&#x223c;23 mg/g (92% of 0.6 mg/L)</td>
<td align="left">Current document</td>
</tr>
<tr>
<td align="center">Uranyl-Curcumin-MOF</td>
<td align="center">Phenol red</td>
<td align="center">pH 8</td>
<td align="center">0.11 mg/L</td>
<td align="left">
<xref ref-type="bibr" rid="B28">Khandan et al. (2018)</xref>
</td>
</tr>
<tr>
<td align="center">MIL-101(Fe)</td>
<td align="center">Congo red</td>
<td align="center">pH 6, 60 min</td>
<td align="center">&#x223c;180 mg/g</td>
<td align="left">
<xref ref-type="bibr" rid="B53">Siddique et al. (2024)</xref>
</td>
</tr>
<tr>
<td align="center">ZIF-8</td>
<td align="center">Methyl orange</td>
<td align="center">pH 4, 120 min</td>
<td align="center">&#x223c;90 mg/g</td>
<td align="left">
<xref ref-type="bibr" rid="B20">Ho (2022)</xref>
</td>
</tr>
<tr>
<td align="center">Cu-BTC</td>
<td align="center">Rhodamine B</td>
<td align="center">pH 7, 60 min</td>
<td align="center">&#x223c;250 mg/g</td>
<td align="left">
<xref ref-type="bibr" rid="B35">Mousavi et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="center">MOF@Chitosan Composite</td>
<td align="center">Phenol red</td>
<td align="center">pH 7, 40 min</td>
<td align="center">&#x223c;45 mg/g</td>
<td align="left">
<xref ref-type="bibr" rid="B29">Lau et al. (2022)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Compared to the uranyl-curcumin-MOF (<xref ref-type="bibr" rid="B28">Khandan et al., 2018</xref>), which only removed 0.11 mg/L, the ruthenium-MOF performed significantly better. While some other MOFs (e.g., Cu-BTC) showed higher absolute adsorption capacities, they were tested against different dyes, often at higher concentrations and under different conditions. The advantage of ruthenium-MOF lies in its fast kinetics, high surface area, and ability to work efficiently at neutral pH, making it highly practical for real wastewater treatment.</p>
</sec>
</sec>
<sec id="s3-2-3">
<title>3.2.3 Reusability</title>
<p>After the adsorption process, the synthesized ruthenium-MOF was washed three times with water and ethanol and it was placed in an oven at 100&#xb0;C for 4 h under vacuum conditions. It&#x2019;s TGA (<xref ref-type="fig" rid="F9">Figures 9&#x2013;I</xref>), FT-IR (<xref ref-type="fig" rid="F9">Figures 9&#x2013;II</xref>), and XRD (<xref ref-type="fig" rid="F9">Figures 9&#x2013;II</xref>) was prepared and no significant change was observed compared to before use. Only in the TGA curve was a weight loss observed near 100&#xb0;C, which can be attributed to the evaporation of water absorbed on the surface or pores of the MOF, which occurred during the absorption or washing process. Then, the adsorption process was re-evaluated under obtained optimal conditions. The results showed that under obtained optimal conditions, including phenol red concentrations (0.6 mg/L), ruthenium-MOF concentrations (0.06 g/L), pH (7), temperature (25&#xb0;C), and time (75 min), the percentage adsorption did not change significantly up to three times (<xref ref-type="fig" rid="F9">Figures 9&#x2013;IV</xref>).</p>
<fig id="F9" position="float">
<label>FIGURE 9</label>
<caption>
<p>XRD (I), FT-IR (II) and TGA (III) of ruthenium-MOF after the adsorption process, and its reusability in phenol red adsorption (IV).</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g009.tif">
<alt-text content-type="machine-generated">Chart (I) displays X-ray diffraction patterns before and after the adsorption process, with peaks at different angles. Chart (II) shows FTIR spectra before and after adsorption, indicating changes in functional groups. Chart (III) presents thermogravimetric analysis, comparing weight loss over temperature before and after adsorption. Chart (IV) depicts a bar graph illustrating adsorption efficiency, showing a decrease in effectiveness from initial use to third reuse.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-2-4">
<title>3.2.4 Kinetic modeling in phenol red adsorption using ruthenium-MOF</title>
<p>To investigate the adsorption mechanism and rate-controlling steps, kinetic studies were conducted using pseudo-first-order and pseudo-second-order models. These models provide insight into the nature of the interaction between phenol red molecules and the active sites of the ruthenium-MOF.</p>
<sec id="s3-2-4-1">
<title>3.2.4.1 Pseudo-first-order</title>
<p>The pseudo-first-order equation is as follows (<xref ref-type="disp-formula" rid="e2">Equation 2</xref>):<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:mi>ln</mml:mi>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mtext>qe</mml:mtext>
<mml:mo>&#x2212;</mml:mo>
<mml:mtext>qt</mml:mtext>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:mi>ln</mml:mi>
<mml:mo>&#x2061;</mml:mo>
<mml:mtext>qt</mml:mtext>
<mml:mo>&#x2013;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">k</mml:mi>
<mml:mn>1</mml:mn>
</mml:msub>
</mml:mrow>
<mml:mi mathvariant="normal">t</mml:mi>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>
<italic>k</italic>
<sub>1</sub> &#x3d; 0.0457 min<sup>&#x2212;1</sup>
</p>
<p>
<italic>q</italic>
<sub>e</sub> &#x3d; 9.32 mg/g.</p>
<p>
<xref ref-type="disp-formula" rid="e2">Equation 2</xref>. Pseudo-first-order in phenol red adsorption using ruthenium-MOF.</p>
<p>Suitable when the adsorption rate depends on available vacant sites.</p>
</sec>
<sec id="s3-2-4-2">
<title>3.2.4.2 Pseudo-second-order</title>
<p>The pseudo-second-order is as follows (<xref ref-type="disp-formula" rid="e3">Equation 3</xref>):<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:mfrac>
<mml:mi>t</mml:mi>
<mml:mrow>
<mml:mi>q</mml:mi>
<mml:mi>t</mml:mi>
</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:mi>q</mml:mi>
<mml:msup>
<mml:mi>e</mml:mi>
<mml:mn>2</mml:mn>
</mml:msup>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x2b;</mml:mo>
<mml:mfrac>
<mml:mi>t</mml:mi>
<mml:mrow>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>k<sub>2</sub> &#x3d; 0.00655 g/mg.min.</p>
<p>q<sub>e</sub> &#x3d; 10.59 mg/g.</p>
<p>
<xref ref-type="disp-formula" rid="e3">Equation 3</xref>. Pseudo-second-order in phenol red adsorption using ruthenium-MOF.</p>
<p>Assumes chemisorption as the rate-limiting step.</p>
<p>Based on the results in <xref ref-type="fig" rid="F10">Figure 10</xref>; <xref ref-type="table" rid="T5">Table 5</xref>, the pseudo-second-order model fits the data better and predicts a higher adsorption capacity, which is consistent with the assumption of chem-adsorption. Also, the saturation of the adsorbent surface at &#x223c;75 min is also consistent with the behavior of the second model.</p>
<fig id="F10" position="float">
<label>FIGURE 10</label>
<caption>
<p>Kinetic modeling of phenol red adsorption using ruthenium-MOF.</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g010.tif">
<alt-text content-type="machine-generated">A graph showing the relationship between time in minutes on the x-axis and qt in milligrams per gram on the y-axis. Data points (black crosses), Pseudo-first order (red dashed line), and Pseudo-second order (blue solid line) are plotted. The curves demonstrate adsorption kinetics over time, with the Pseudo-second order model closely fitting the data points.</alt-text>
</graphic>
</fig>
<table-wrap id="T5" position="float">
<label>TABLE 5</label>
<caption>
<p>Kinetic model parameters phenol red adsorption using ruthenium-MOF.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Kinetic model</th>
<th align="center">Parameter</th>
<th align="center">Value</th>
<th align="center">Description</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Pseudo-first-order</td>
<td align="center">k<sub>1</sub> (min<sup>&#x2212;1</sup>)</td>
<td align="center">0.0457</td>
<td align="center">Rate constant</td>
</tr>
<tr>
<td align="center">Pseudo-first-order</td>
<td align="center">q<sub>e</sub> (mg/g)</td>
<td align="center">9.32</td>
<td align="center">Equilibrium adsorption capacity</td>
</tr>
<tr>
<td align="center">Pseudo-second-order</td>
<td align="center">k<sub>2</sub> (g&#xb7;mg<sup>&#x2212;1</sup>&#xb7;min<sup>&#x2212;1</sup>)</td>
<td align="center">0.00655</td>
<td align="center">Rate constant</td>
</tr>
<tr>
<td align="center">Pseudo-second-order</td>
<td align="center">q<sub>e</sub> (mg/g)</td>
<td align="center">10.59</td>
<td align="center">Equilibrium adsorption capacity</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
<sec id="s3-2-5">
<title>3.2.5 Isotherm modeling in phenol red adsorption using ruthenium-MOF</title>
<p>To better understand the adsorption behavior and surface interactions, isotherm models were applied. Both Langmuir and Freundlich models were evaluated using experimental equilibrium data.</p>
<sec id="s3-2-5-1">
<title>3.2.5.1 Langmuir isotherm</title>
<p>The Langmuir isotherm equation is as follows (<xref ref-type="disp-formula" rid="e4">Equation 4</xref>):<disp-formula id="e4">
<mml:math id="m4">
<mml:mrow>
<mml:mtext>qe</mml:mtext>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:msub>
<mml:mi>q</mml:mi>
<mml:mrow>
<mml:mi>max</mml:mi>
<mml:mo>&#x2061;</mml:mo>
<mml:msub>
<mml:mi>K</mml:mi>
<mml:mi>L</mml:mi>
</mml:msub>
<mml:mi>C</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>&#x2b;</mml:mo>
<mml:msub>
<mml:mi>K</mml:mi>
<mml:mi>L</mml:mi>
</mml:msub>
<mml:mi>C</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>
<italic>q</italic>
<sub>max</sub> &#x3d; 1000 mg/g.</p>
<p>
<italic>K</italic>
<sub>
<italic>L</italic>
</sub> &#x3d; 0.0314 L/mg.</p>
<p>
<xref ref-type="disp-formula" rid="e4">Equation 4</xref>. Langmuir isotherm in phenol red adsorption using ruthenium-MOF.</p>
</sec>
<sec id="s3-2-5-2">
<title>3.2.5.2 Freundlich isotherm</title>
<p>The Freundlich isotherm equation is as follows (<xref ref-type="disp-formula" rid="e5">Equation 5</xref>):<disp-formula id="e5">
<mml:math id="m5">
<mml:mrow>
<mml:mi>q</mml:mi>
<mml:mi>e</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:msub>
<mml:mi>K</mml:mi>
<mml:mi>F</mml:mi>
</mml:msub>
<mml:msup>
<mml:mrow>
<mml:mi>C</mml:mi>
<mml:mi>e</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>/</mml:mo>
<mml:mi>n</mml:mi>
</mml:mrow>
</mml:msup>
</mml:mrow>
</mml:math>
<label>(5)</label>
</disp-formula>KF &#x3d; 164.79.</p>
<p>
<italic>n</italic> &#x3d; 3.33.</p>
<p>
<xref ref-type="disp-formula" rid="e5">Equation 5</xref>. Freundlich isotherm in phenol red adsorption using ruthenium-MOF.</p>
<p>Based on the results in <xref ref-type="fig" rid="F11">Figure 11</xref>; <xref ref-type="table" rid="T6">Table 6</xref>, the Freundlich model better represents the system and supports a heterogeneous multilayer adsorption process.</p>
<fig id="F11" position="float">
<label>FIGURE 11</label>
<caption>
<p>Isotherm modeling of phenol red adsorption using ruthenium-MOF.</p>
</caption>
<graphic xlink:href="fmats-12-1602816-g011.tif">
<alt-text content-type="machine-generated">Graph showing adsorption models. The x-axis represents Ce (mg/L) and the y-axis represents qe (mg/g). Data points are marked with black crosses. The Langmuir model is a red dashed line, and the Freundlich model is a solid blue line. The blue line closely follows the data trend.</alt-text>
</graphic>
</fig>
<table-wrap id="T6" position="float">
<label>TABLE 6</label>
<caption>
<p>Isotherm model parameters phenol red adsorption using ruthenium-MOF.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Isotherm model</th>
<th align="center">Parameter</th>
<th align="center">Value</th>
<th align="center">Description</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Langmuir</td>
<td align="center">q<sub>max</sub> (mg/g)</td>
<td align="center">1000</td>
<td align="center">Maximum adsorption capacity (approximate)</td>
</tr>
<tr>
<td align="center">Langmuir</td>
<td align="center">K_L (L/mg)</td>
<td align="center">0.0314</td>
<td align="center">Langmuir constant</td>
</tr>
<tr>
<td align="center">Freundlich</td>
<td align="center">K_F [(mg/g)(L/mg)<sup>1&#x2044;n</sup>]</td>
<td align="center">164.79</td>
<td align="center">Adsorption capacity constant</td>
</tr>
<tr>
<td align="center">Freundlich</td>
<td align="center">n</td>
<td align="center">3.33</td>
<td align="center">Adsorption intensity (n &#x3e; 1 indicates favorable adsorption)</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>In light of the human need for clean water and the challenges posed by population growth, climate change, and limited freshwater resources, this study focuses on the synthesis of a new metal-organic framework (ruthenium-MOF) and its application in treating biological pollutants, specifically the inhibition of bacterial strains <italic>Salmonella enterica</italic>, <italic>Campylobacter jejuni</italic>, <italic>Escherichia coli</italic>, <italic>Legionella pneumophila</italic>, and <italic>Shigella dysenteriae</italic>, which are among the most significant pathogens found in wastewater. Additionally, this MOF was designed to remove chemical pollutants such as phenol red, a compound associated with various diseases and skin irritations. The synthesized MOF incorporates ruthenium and 4,4&#x27;-(diazene-1,2-diyl)dibenzoic acid as structural components. The biological properties of these compounds, along with the high specific surface area of the ruthenium-MOF, contribute to its unique ability to eliminate both biological and chemical contaminants from wastewater. In biological tests, the MOF showed higher inhibition rates for certain bacterial strains compared to cefazolin and azithromycin. Regarding chemical pollutant removal, the MOF achieved 92% removal of 0.6 mg/L phenol red using 0.06 g/L of the adsorbent at neutral pH and 75 min. Based on kinetic and isotherm studies, the pseudo-second-order model best described the adsorption process, and the Freundlich model best fit the isotherm data. The synthesized ruthenium-MOF demonstrates great potential as an efficient material for wastewater treatment. Further studies are recommended to evaluate its effectiveness against other biological and chemical pollutants.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The authors confirm that the data supporting the findings of this study are available within the article.</p>
</sec>
<sec sec-type="author-contributions" id="s6">
<title>Author contributions</title>
<p>AA: Writing &#x2013; original draft. TA: Writing &#x2013; original draft. MAA: Writing &#x2013; review and editing. OA: 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 and/or publication of this article. This study is supported via funding from Prince Sattam Bin Abdulaziz University project number (PSAU/2025/R/1446).</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="ai-statement" id="s9">
<title>Generative AI statement</title>
<p>The author(s) declare that no Generative AI was used in the creation of this manuscript.</p>
</sec>
<sec sec-type="disclaimer" id="s10">
<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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