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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Nanotechnol.</journal-id>
<journal-title>Frontiers in Nanotechnology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Nanotechnol.</abbrev-journal-title>
<issn pub-type="epub">2673-3013</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1599272</article-id>
<article-id pub-id-type="doi">10.3389/fnano.2025.1599272</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Nanotechnology</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Enhanced anti-infective activities of sinapic acid through nebulization of lyophilized protransferosomes</article-title>
<alt-title alt-title-type="left-running-head">Alhadrami 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/fnano.2025.1599272">10.3389/fnano.2025.1599272</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" equal-contrib="yes">
<name>
<surname>Alhadrami</surname>
<given-names>Hani A.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="author-notes" rid="fn001">
<sup>&#x2020;</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/374302/overview"/>
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<contrib contrib-type="author" equal-contrib="yes">
<name>
<surname>Gamal</surname>
<given-names>Amr</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="author-notes" rid="fn001">
<sup>&#x2020;</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/3123496/overview"/>
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<contrib contrib-type="author">
<name>
<surname>Amaeze</surname>
<given-names>Ngozi</given-names>
</name>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Sayed</surname>
<given-names>Ahmed M.</given-names>
</name>
<xref ref-type="aff" rid="aff5">
<sup>5</sup>
</xref>
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<contrib contrib-type="author" corresp="yes">
<name>
<surname>Rateb</surname>
<given-names>Mostafa E.</given-names>
</name>
<xref ref-type="aff" rid="aff6">
<sup>6</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/336209/overview"/>
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<contrib contrib-type="author">
<name>
<surname>Naguib</surname>
<given-names>Demiana M.</given-names>
</name>
<xref ref-type="aff" rid="aff7">
<sup>7</sup>
</xref>
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<aff id="aff1">
<sup>1</sup>
<institution>Department of Medical Laboratory Sciences</institution>, <institution>Faculty of Applied Medical Sciences</institution>, <institution>King Abdulaziz University</institution>, <addr-line>Jeddah</addr-line>, <country>Saudi Arabia</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>King Fahd Medical Research Centre</institution>, <institution>King Abdulaziz University</institution>, <addr-line>Jeddah</addr-line>, <country>Saudi Arabia</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Department of Pharmaceutics and Industrial Pharmacy</institution>, <institution>Faculty of Pharmacy</institution>, <institution>Beni-Suef University</institution>, <addr-line>Beni-Suef</addr-line>, <country>Egypt</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>School of Health and Life Sciences</institution>, <institution>University of the West of Scotland</institution>, <addr-line>Blantyre</addr-line>, <country>United Kingdom</country>
</aff>
<aff id="aff5">
<sup>5</sup>
<institution>Department of Pharmacognosy</institution>, <institution>Faculty of Pharmacy</institution>, <institution>Nahda University</institution>, <addr-line>Beni-Suef</addr-line>, <country>Egypt</country>
</aff>
<aff id="aff6">
<sup>6</sup>
<institution>School of Computing, Engineering and Physical Sciences</institution>, <institution>University of the West of Scotland</institution>, <addr-line>Paisley</addr-line>, <country>United Kingdom</country>
</aff>
<aff id="aff7">
<sup>7</sup>
<institution>Department of Pharmaceutics</institution>, <institution>Faculty of Pharmacy</institution>, <institution>Nahda University (NUB)</institution>, <addr-line>Beni-Suef</addr-line>, <country>Egypt</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/582653/overview">Rajeev K. Tyagi</ext-link>, Institute of Microbial Technology (CSIR), India</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/364134/overview">Hongwu Sun</ext-link>, Third Military Medical University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1672419/overview">Himanshu Paliwal</ext-link>, Prince of Songkla University, Thailand</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Mostafa E. Rateb, <email>mostafa.rateb@uws.ac.uk</email>
</corresp>
<fn fn-type="equal" id="fn001">
<label>
<sup>&#x2020;</sup>
</label>
<p>These authors have contributed equally to this work</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>11</day>
<month>08</month>
<year>2025</year>
</pub-date>
<pub-date pub-type="collection">
<year>2025</year>
</pub-date>
<volume>7</volume>
<elocation-id>1599272</elocation-id>
<history>
<date date-type="received">
<day>24</day>
<month>03</month>
<year>2025</year>
</date>
<date date-type="accepted">
<day>08</day>
<month>07</month>
<year>2025</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2025 Alhadrami, Gamal, Amaeze, Sayed, Rateb and Naguib.</copyright-statement>
<copyright-year>2025</copyright-year>
<copyright-holder>Alhadrami, Gamal, Amaeze, Sayed, Rateb and Naguib</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>
<sec>
<title>Indroduction</title>
<p>COVID-19 is a contagious illness caused by the virus SARS-CoV-2, a major cause of death globally, even with effective vaccinations. Additionally, multidrug resistant bacterial and fungal pathogens are a real threat to many healthcare settings. Sinapic acid (SA), isolated from different plants or marine algae, has been reported to have antioxidant, antibacterial, and antiviral properties. Although there is evidence that SA has anti-SARS-CoV-2 activity, it is poorly absorbed when taken orally due to its intestinal metabolism. The current study aimed to improve SA&#x0027;s activity against SARS-CoV-2, different bacterial and fungal pathogens, bioavailability, and targeting using a nebulized, freeze-dried, transferosomal formulation.</p>
</sec>
<sec>
<title>Methods</title>
<p>A response-surface experimental study using phospholipid, cholesterol, and surfactants was employed to develop transferosomes. Various formulations were prepared and characterized for entrapment efficiency (EE), release, and size to select the optimized formulation. It was then lyophilized into a powder to be evaluated in vivo for its pharmacokinetic properties.</p>
</sec>
<sec>
<title>Results and discussion</title>
<p>SA exhibited antibacterial and antifungal activity, with SA-protransferosomes showing enhanced effectiveness compared to that of pure SA and approaching the efficacy of positive controls. Notably, SA protransferosomes demonstrated activity comparable to that of ciprofloxacin against E. faecalis and S. mutans and were effective against Candida albicans and Aspergillus niger, similar to nystatin. The optimized formula significantly enhanced the SARS-CoV-2 activity (IC<sub>50</sub> &#x003D; 0.016 &#x00B1; 0.008 &#x03BC;g/mL), C<sub>max</sub> by 2.27 times, and AUC (0&#x2013;&#x221E;) by 5.4 times, as compared to pure SA. As a result, the use of nebulized SA-transferosomes can be regarded as a safe and efficient strategy to counter different infections.</p>
</sec>
</abstract>
<kwd-group>
<kwd>sinapic acid</kwd>
<kwd>SARS-CoV-2</kwd>
<kwd>antibacterial</kwd>
<kwd>antifungal</kwd>
<kwd>transferosomes</kwd>
<kwd>nebulizer</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Biomedical Nanotechnology</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>COVID-19, or the novel coronavirus 2019 according to the World Health Organization, is caused by the severe acute respiratory syndrome coronavirus 2 (SARS-CoV-2). Other pandemics caused by different CoVs include severe acute respiratory syndrome (SARS) in 2002&#x2013;2003 and Middle East Respiratory Syndrome (MERS) in 2012 (<xref ref-type="bibr" rid="B30">Jara et al., 2021</xref>). Unfortunately, the COVID-19 pandemic has resulted in more deaths than the previous pandemics combined (<xref ref-type="bibr" rid="B26">Gurwitz, 2020</xref>). Worldwide, research organizations have been studying SARS-CoV-2 pandemic since when it was declared. Several successful vaccinations have been reported, and tests on antiviral medications are currently in progress (<xref ref-type="bibr" rid="B3">Adamson et al., 2021</xref>).</p>
<p>Antimicrobial resistance (AMR) is a major global health and development threat, responsible for 1.27 million deaths directly and contributing to 4.95 million deaths worldwide in 2019 (<xref ref-type="bibr" rid="B9">Antimicrobial Resistance Collaborators et al., 2022</xref>). It affects countries across all regions and income levels, thus posing a significant challenge in the 21st century. The WHO highlighted, among other organisms, the following bacteria on its priority list: <italic>Enterococcus faecalis</italic>, <italic>Streptococcus mutans</italic>, <italic>Escherichia coli</italic>, <italic>Pseudomonas aeruginosa</italic>, <italic>Mycobacterium tuberculosis</italic>, and <italic>Staphylococcus aureus</italic>, all of which pose significant challenges in healthcare settings (<xref ref-type="bibr" rid="B57">WHO, 2024</xref>). The rising resistance levels highlight the insufficient development progress and the urgent need for development of new drugs.</p>
<p>Sinapic acid (SA) is a phenolic, acid-containing, natural metabolite found in grapefruits, cranberries, oranges, broccoli, and herbs, such as canola and mustard seed, and seaweed such as <italic>Ulva</italic> sp., <italic>Caulerpa</italic> sp., and <italic>Grateloupia</italic> sp. (<xref ref-type="bibr" rid="B59">Zhong et al., 2020</xref>). It is a cinnamic-acid derivative with the chemical structure (3,5&#x2010;dimethoxy&#x2010;4&#x2010;hydroxycinnamic acid) (<xref ref-type="bibr" rid="B41">Pandi and Manickam, 2021</xref>). SA was reported to have antioxidant, reno-protective, neuroprotective, anti-inflammatory, hepatoprotective, cardioprotective, antibacterial, anti-cancer, and antiviral properties (<xref ref-type="bibr" rid="B8">Angourani et al., 2023</xref>; <xref ref-type="bibr" rid="B28">Hameed et al., 2016</xref>). Recently, we reported SA had anti-SARS-CoV-2 activity with an IC<sub>50</sub> value of 2.69&#xa0;&#xb5;g/mL and a minimal cytotoxicity value of 189.3&#xa0;&#xb5;g/mL (<xref ref-type="bibr" rid="B40">Orfali et al., 2021</xref>). These findings suggested that SA is a good anti-SARS-CoV-2 drug.</p>
<p>Despite SA&#x2019;s comprehensive therapeutic action, its application still needs to be improved because it is slightly soluble in water. In addition, it is metabolized in the intestine, resulting in low oral bioavailability (<xref ref-type="bibr" rid="B41">Pandi and Manickam, 2021</xref>; <xref ref-type="bibr" rid="B32">Kern et al., 2003</xref>; <xref ref-type="bibr" rid="B53">Shakeel et al., 2016a</xref>). To mitigate these limitations, a suitable drug delivery system is required. A few beneficial formulation techniques have been developed in a highly promising, novel sector for SA delivery, including chitosan nanoparticles (<xref ref-type="bibr" rid="B10">Balagangadharan et al., 2019</xref>) and a self-nanoemulsifying formulation (<xref ref-type="bibr" rid="B54">Shakeel et al., 2016b</xref>).</p>
<p>The pulmonary route provided a wide surface area of approximately 100&#xa0;m<sup>2</sup> and a non-invasive method of drug administration (<xref ref-type="bibr" rid="B22">Guimar&#xe3;es et al., 2021</xref>). Current nanotechnology progress has significantly enhanced drug delivery via inhalation (<xref ref-type="bibr" rid="B38">Nesamony et al., 2014</xref>; <xref ref-type="bibr" rid="B45">Pooladanda et al., 2021</xref>; <xref ref-type="bibr" rid="B35">Li et al., 2021</xref>). As compared to the corresponding traditional therapies, drug nanocarriers have typically offered distinct advantages, such as increased lung permeability, improved dissolution profiles, and superior biopharmaceutical properties (<xref ref-type="bibr" rid="B21">Gontijo et al., 2014</xref>).</p>
<p>In 1992, Cevc and Blume first described transferosomes as ultra-deformable, highly flexible vesicles consisting primarily of a permeation enhancer, in addition to the phospholipids (<xref ref-type="bibr" rid="B13">Cevc and Blume, 1992</xref>). Compared with traditional SLNPs, niosome and liposome transfersomes showed high elasticity, allowing them to squeeze themselves through different biological membranes. The deformability of transferosomes over liposomes was accredited to the permeation enhancer as it softened the lipid bilayers; they could squeeze between cells due to their elasticity, which improved the permeability (<xref ref-type="bibr" rid="B49">Salem et al., 2019a</xref>). In pulmonary therapy, transferosomal aerosols had the added benefit of facilitating uniform deposition of the locally active drugs into the lungs (<xref ref-type="bibr" rid="B33">Khan et al., 2020</xref>; <xref ref-type="bibr" rid="B12">Burton et al., 2015</xref>). Nebulizers provided the additional benefit of delivering transferosomes as aqueous dispersions without further processing as compared to the numerous available aerosol delivery systems (<xref ref-type="bibr" rid="B16">Elhissi et al., 2013</xref>). The stability of the aqueous dispersion of the transferosomes was then improved by using the lyophilization method and rehydrating the powder prior to nebulization (<xref ref-type="bibr" rid="B22">Guimar&#xe3;es et al., 2021</xref>).</p>
<p>The current study aimed to improve SA bioavailability and achieve direct lung targeting using a nebulized freeze-dried transferosomal formulation. The thin-film hydration method was used to prepare the SA-loaded transferosomes in a response-surface experimental study. First, the transferosome formulation was characterized for the encapsulation efficiency %, <italic>in vitro</italic> release, and size analysis, and then Design-Expert<sup>&#xae;</sup> was employed for the optimization. Finally, an optimized SA-transferosome was lyophilized into powder and adequately characterized. The optimized SA-transferosome was also examined for its SARS-CoV-2 antiviral activity before being tested for its <italic>in vivo</italic> pharmacokinetics. Moreover, to discover its broad anti-infective effect, SA and its optimized SA-transferosome were also screened against a panel of multidrug-resistant bacterial (<italic>E. coli</italic>, <italic>P. aeruginosa</italic>, <italic>Salmonella typhimurium</italic>, <italic>Enterobacter</italic> sp., <italic>S. aureus</italic>, <italic>E. faecalis</italic>, <italic>S. mutans</italic>) and fungal (<italic>Aspergillus niger</italic> and <italic>Candida albicans)</italic> pathogens.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Materials</title>
<p>Sinapic acid, cholesterol, L-a phosphatidylcholine (soya lecithin), and lactose monohydrate were supplied by Sigma-Aldrich (St. Louis, MO). Tween 80 (polyoxyethylene sorbitan monooleate) of HLB &#x3d; 15 and sodium deoxycholate (HLB &#x3d; 16); cellophane membrane with a (12,000&#xa0;kDa) molecular weight cut-off; methanol; HPLC-grade acetonitrile; and absolute ethanol were purchased from Fisher Scientific United Kingdom Ltd. (Loughborough Leicestershire, United Kingdom).</p>
</sec>
<sec id="s2-2">
<title>2.2 Formulation of SA-loaded transferosomes</title>
<p>Thin-film hydration was used to create SA-loaded transferosomes, with slight modifications identified by preliminary studies (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>). Briefly, absolute ethanol was used to dissolve SA (10&#xa0;mg), surfactant, cholesterol, lactose monohydrate (1,250&#xa0;mg), and phosphatidylcholine. After that, the mixture was sonicated for 10&#xa0;min and then moved into a round flask (100&#xa0;mL). The absolute ethanol was evaporated in a vacuum employing a rotary evaporator (Stuart, United Kingdom) for 1&#xa0;h at 40&#xb0;C. Consequently, the obtained dried film was hydrated via 10&#xa0;mL of an isotonic phosphate buffer (pH 7.4) for 1&#xa0;h at 60&#xb0;C. To transform the large vesicles into smaller ones, they were subjected to sonication for 20&#xa0;min. After that, the developed protransferosomes were separated at 20,000&#xa0;rpm for 3&#xa0;h at 4&#xb0;C in a cooling centrifuge (Hettich Zentrifugen, Germany), and then they were washed using isotonic phosphate buffer. The produced transferosomes were kept in tightly closed amber tubes at 4&#xb0;C for further research.</p>
</sec>
<sec id="s2-3">
<title>2.3 Experimental design of SA-loaded protransferosomes</title>
<p>User-defined response-surface design was employed using Design-Expert software (version 10.0.0.3, United States) for the optimization procedure (<xref ref-type="table" rid="T1">Table 1</xref>). Twelve transferosomal formulations were developed (<xref ref-type="table" rid="T2">Table 2</xref>) using a ratio (w/w) of cholesterol to phospholipid (X1), surfactant type (X2), and the ratio of phospholipid to surfactants (X3) as independent variables. Consequently, the tested dependent variables were particle size (Y1), entrapment efficiency (Y2), and release percentage (Y3). Dependent and independent variables were selected according to literature review and preliminary studies.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Factors and levels of user-defined response-surface design.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="center">Factors</th>
<th colspan="3" align="center">Levels</th>
</tr>
<tr>
<th align="center">1</th>
<th align="center">2</th>
<th align="center">3</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">X<sub>1</sub>: Ratio of cholesterol to phospholipid (w/w)</td>
<td align="center">0:1</td>
<td align="center">1:2</td>
<td align="center">1:1</td>
</tr>
<tr>
<td align="left">X<sub>2</sub>: Surfactant type</td>
<td align="center">Tween 80</td>
<td align="center">Na-deoxy cholate</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">X<sub>3</sub>: Ratio of phospholipid to surfactants (w/w)</td>
<td align="center">75:25</td>
<td align="center">85:15</td>
<td align="center">&#x2014;</td>
</tr>
</tbody>
</table>
</table-wrap>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Composition and observed responses of different SA-loaded transferosome formulations.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Formulation code</th>
<th align="center">X<sub>1</sub>
</th>
<th align="center">X<sub>2</sub>
</th>
<th align="center">X<sub>3</sub>
</th>
<th align="center">Y<sub>1</sub> (nm)<break/>(mean &#xb1; SD)</th>
<th align="center">Y2 (%)<break/>(mean &#xb1; SD)</th>
<th align="center">Y3 (%)<break/>(mean &#xb1; SD)</th>
<th align="center">Zeta<break/>potential (mV)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">F1</td>
<td align="center">1:1</td>
<td align="left">Tween 80</td>
<td align="center">85:15</td>
<td align="center">380.43 &#xb1; 13.39</td>
<td align="center">89.80 &#xb1; 2.65</td>
<td align="center">19.74 &#xb1; 2.26</td>
<td align="center">&#x2212;28.1</td>
</tr>
<tr>
<td align="center">F2</td>
<td align="center">1:2</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">85:15</td>
<td align="center">221.87 &#xb1; 8.16</td>
<td align="center">87.77 &#xb1; 1.70</td>
<td align="center">25.65 &#xb1; 2.08</td>
<td align="center">&#x2212;29.3</td>
</tr>
<tr>
<td align="center">F3</td>
<td align="center">1:1</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">75:25</td>
<td align="center">298.57 &#xb1; 15.57</td>
<td align="center">83.13 &#xb1; 3.55</td>
<td align="center">29.36 &#xb1; 2.11</td>
<td align="center">&#x2212;42.1</td>
</tr>
<tr>
<td align="center">F4</td>
<td align="center">0:1</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">85:15</td>
<td align="center">198.33 &#xb1; 16.05</td>
<td align="center">84.33 &#xb1; 2.97</td>
<td align="center">34.91 &#xb1; 2.12</td>
<td align="center">&#x2212;31.2</td>
</tr>
<tr>
<td align="center">F5</td>
<td align="center">1:1</td>
<td align="left">Tween 80</td>
<td align="center">75:25</td>
<td align="center">310.60 &#xb1; 11.59</td>
<td align="center">76.28 &#xb1; 2.94</td>
<td align="center">25.80 &#xb1; 2.07</td>
<td align="center">&#x2212;30.9</td>
</tr>
<tr>
<td align="center">F6</td>
<td align="center">1:1</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">85:15</td>
<td align="center">500.90 &#xb1; 9.27</td>
<td align="center">89.53 &#xb1; 3.61</td>
<td align="center">23.62 &#xb1; 2.22</td>
<td align="center">&#x2212;34.2</td>
</tr>
<tr>
<td align="center">F7</td>
<td align="center">0:1</td>
<td align="left">Tween 80</td>
<td align="center">75:25</td>
<td align="center">195.67 &#xb1; 13.47</td>
<td align="center">82.6 &#xb1; 3.25</td>
<td align="center">47.47 &#xb1; 1.19</td>
<td align="center">&#x2212;29.1</td>
</tr>
<tr>
<td align="center">F8</td>
<td align="center">1:2</td>
<td align="left">Tween 80</td>
<td align="center">85:15</td>
<td align="center">367.93 &#xb1; 12</td>
<td align="center">89.23 &#xb1; 3.90</td>
<td align="center">29.89 &#xb1; 2.03</td>
<td align="center">&#x2212;26.9</td>
</tr>
<tr>
<td align="center">F9</td>
<td align="center">1:2</td>
<td align="left">Tween 80</td>
<td align="center">75:25</td>
<td align="center">255.63 &#xb1; 7.48</td>
<td align="center">83.13 &#xb1; 2.24</td>
<td align="center">37.87 &#xb1; 0.96</td>
<td align="center">&#x2212;28.3</td>
</tr>
<tr>
<td align="center">F10</td>
<td align="center">0:1</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">75:25</td>
<td align="center">141.7 &#xb1; 9.95</td>
<td align="center">80.3 &#xb1; 2.69</td>
<td align="center">42.84 &#xb1; 2.07</td>
<td align="center">&#x2212;30.9</td>
</tr>
<tr>
<td align="center">F11</td>
<td align="center">1:2</td>
<td align="left">Na-deoxy cholate</td>
<td align="center">75:25</td>
<td align="center">204.20 &#xb1; 11.78</td>
<td align="center">82.20 &#xb1; 1.90</td>
<td align="center">31.35 &#xb1; 1.78</td>
<td align="center">&#x2212;32.7</td>
</tr>
<tr>
<td align="center">F12</td>
<td align="center">0:1</td>
<td align="left">Tween 80</td>
<td align="center">85:15</td>
<td align="center">326.07 &#xb1; 9.98</td>
<td align="center">87.87 &#xb1; 1.168</td>
<td align="center">41.53 &#xb1; 2.11</td>
<td align="center">&#x2212;31.4</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>X1: ratio of cholesterol to phospholipid; X2: surfactant type; X3: ratio of phospholipid to surfactants; (Y1) particle size; (Y2) entrapment efficiency; (Y3) percentage of release; SD , standard deviation.</p>
</fn>
</table-wrap-foot>
</table-wrap>
</sec>
<sec id="s2-4">
<title>2.4 Characterization of SA-loaded transferosomes</title>
<sec id="s2-4-1">
<title>2.4.1 Size and zeta-potential study</title>
<p>A Malvern Zetasizer (Ver.7.11) determined the average transferosomal diameter via dynamic light scattering, Zeta potential, and size distribution curve. The formulated protransferosomes (1&#xa0;mL) were diluted with isotonic buffer (up to 100&#xa0;mL), and the analysis was replicated three times. The obtained findings are displayed in <xref ref-type="table" rid="T2">Table 2</xref>.</p>
</sec>
<sec id="s2-4-2">
<title>2.4.2 Characterization of SA entrapment efficiency percent</title>
<p>The entrapment percent of SA in transferosomes was assessed following the separation of the unentrapped SA in the supernatant obtained by several cooling centrifugation cycles at 4&#xb0;C and 20,000&#xa0;rpm for 3&#xa0;h. First, the obtained vesicles were washed off the transferosomal vesicles. The isolated vesicles were then lysed by Triton X-100 in isotonic buffer (1% w/v), and the lysis was aided by consecutive heating cycles, up to 55&#xb0;C before cooling to 25&#xb0;C. After that, the obtained liquid was centrifuged for 20&#xa0;min at 8,000&#xa0;rpm to separate any debris (<xref ref-type="bibr" rid="B50">Salem et al., 2019b</xref>; <xref ref-type="bibr" rid="B58">Yusuf et al., 2017</xref>). Finally, the SA entrapment percentage was analyzed by UV-spectrophotometry at 322&#xa0;nm, using isotonic phosphate buffer as the dilution media (<xref ref-type="bibr" rid="B42">Parmar et al., 2011</xref>).</p>
</sec>
<sec id="s2-4-3">
<title>2.4.3 <italic>In vitro</italic> SA release percent</title>
<p>The dialysis membrane method was utilized to determine the percentage of SA released from the developed transferosomes, using the USP-II dissolution apparatus (<xref ref-type="bibr" rid="B31">Jose et al., 2014</xref>; <xref ref-type="bibr" rid="B52">Salem et al., 2018</xref>). As the donor component, SA-loaded transferosomes entrapping 10&#xa0;mg SA were added into an open-sided tube. One side of the tube was tightly enclosed via a 12,000&#xa0;kDa-cellophane membrane, while the other was fixed to a paddle. The paddle stirring rate was 100&#xa0;rpm at 37&#xb0;C &#xb1; 0.50&#xb0;C. The isotonic phosphate buffer was used as the receptor liquid (100&#xa0;mL), and 10% propylene glycol was applied to maintain a sink environment (<xref ref-type="bibr" rid="B2">Aboud et al., 2016</xref>). Samples were withdrawn at various intervals (0.25, 0.5, 1, 2, 3, 4, 5, and 12&#xa0;h) and substituted with similar volumes of isotonic phosphate buffer. The obtained samples were examined at 322&#xa0;nm using a UV-spectrophotometer; the test was repeated thrice. The <italic>in vitro</italic> release percentage of SA was estimated by dividing the SA-entrapped quantity by the SA-released quantity and then multiplied by 100 (<xref ref-type="bibr" rid="B48">Salem et al., 2016</xref>). The percentage of SA released from the protransferosomes was estimated against the SA percentage released from the free SA suspension (10&#xa0;mg). The optimized transferosomal formula was chosen according to the results of the characterization studies of the prepared SA transferosomes (<xref ref-type="bibr" rid="B19">Fatima et al., 2022</xref>).</p>
</sec>
</sec>
<sec id="s2-5">
<title>2.5 Optimization of protransferosomes</title>
<p>The statistical significance obtained from the investigated data of each response was estimated using the ANOVA test at <italic>p</italic>-value &#x3c; 0.05. The predicted and adjusted coefficients of determination (R2) were used to determine if the chosen model was suitable for the investigated data. The signal-to-noise ratio was determined using adequate precision to confirm that the applied model may well navigate the model&#x2019;s design spaces (<xref ref-type="bibr" rid="B14">Das et al., 2015</xref>). The optimization process also depended on using the highest desirability index (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>). The relationship between different factors and each response was explained according to the polynomial equations (<xref ref-type="disp-formula" rid="e1">Equations 1</xref>&#x2013;<xref ref-type="disp-formula" rid="e3">3</xref>; <xref ref-type="table" rid="T3">Table 3</xref>).</p>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Data of all dependent variables from regression analysis and analysis of variance.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Dependent variables</th>
<th align="center">Model</th>
<th align="center">F-value</th>
<th align="center">
<italic>p</italic>-value</th>
<th align="center">Adjusted R<sup>2</sup>
</th>
<th align="center">Predicted R<sup>2</sup>
</th>
<th align="center">Adequate precision</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Particle size</td>
<td align="center">Quadratic</td>
<td align="center">43.52</td>
<td align="center">&#x3c;0.0001</td>
<td align="center">0.9285</td>
<td align="center">0.9069</td>
<td align="center">26.370</td>
</tr>
<tr>
<td align="left">Entrapment efficiency</td>
<td align="center">Quadratic</td>
<td align="center">10.15</td>
<td align="center">&#x3c;0.0001</td>
<td align="center">0.6467</td>
<td align="center">0.5250</td>
<td align="center">9.312</td>
</tr>
<tr>
<td align="left">Percentage of release</td>
<td align="center">Quadratic</td>
<td align="center">18.96</td>
<td align="center">&#x3c;0.0001</td>
<td align="center">0.9304</td>
<td align="center">0.9085</td>
<td align="center">27.085</td>
</tr>
</tbody>
</table>
</table-wrap>
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<mml:mi mathvariant="normal">X</mml:mi>
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<mml:mi mathvariant="normal">X</mml:mi>
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<mml:mi mathvariant="normal">X</mml:mi>
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<mml:msub>
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</sec>
<sec id="s2-6">
<title>2.6 Formulation and characterization of the optimal SA protransferosomes</title>
<p>The optimized SA-loaded transferosomes were chosen based on the following criteria: maximizing the <italic>in vitro</italic> released SA, maximizing the EE%, and minimizing the mean particle size. Consequently, the selected optimized formula was developed using thin-film hydration, as previously described, and subjected to further characterization studies. As a result, the optimized transferosomes were prepared and analyzed for vesicle size, PDI, EE%, and % of SA released, as previously mentioned.</p>
</sec>
<sec id="s2-7">
<title>2.7 Preparation and characterization of the lyophilized, optimal SA protransferosomes</title>
<p>The optimal SA-protransferosomes were dried via freeze-dryer EF03 (Edwards High Vacuum, Ltd.) to develop protransferosomes powder. Then, the lyophilized optimal SA protransferosomes were applied to the following characterization studies.</p>
<sec id="s2-7-1">
<title>2.7.1 Size analysis, drug content, and release study</title>
<p>The lyophilized powder of SA-protranferosomes was suspended in 100&#xa0;mL isotonic phosphate buffer and then characterized for different parameters, including vesicular mean size, PDI, drug content, and % of SA released, as previously described.</p>
</sec>
<sec id="s2-7-2">
<title>2.7.2 Differential scanning calorimetry study (DSC)</title>
<p>The DSC study was carried out to clarify the thermal analysis of SA and the different components used in the developed transferosomes. The tested samples were placed on a standard crimped aluminum pan using an increased heating rate of 10&#xb0;C per minute while the temperature was elevated from 25&#xb0;C to 200&#xb0;C (<xref ref-type="bibr" rid="B11">Bhattacharjee et al., 2017</xref>).</p>
</sec>
<sec id="s2-7-3">
<title>2.7.3 Morphology analysis</title>
<p>The optimized SA-loaded transferosome morphology was characterized via TEM-JEOL JEM-1400 transmission electron microscopy (Tokyo, Japan) through an 80&#xa0;kV accelerating voltage. A grid of carbon copper was wrapped with a dried film of freshly developed protransferosomes. The protransferosomes were stained with a dye of phospho-tungstic acid, and the stained vesicles were dried; prior to this, the protransferosome morphologies were characterized via TEM (<xref ref-type="bibr" rid="B19">Fatima et al., 2022</xref>).</p>
</sec>
<sec id="s2-7-4">
<title>2.7.4 Stability study</title>
<p>After storing the optimized formula (equivalent to 5&#xa0;mg SA) in firmly sealed amber glass tubes at 4&#xb0;C and 25&#xb0;C for 3&#xa0;months, the optimized, lyophilized protransferosomes were tested for stability. Throughout the storage time, samples were taken and characterized for EE% and the protransferosome mean diameter, and stability testing was performed three times (<xref ref-type="bibr" rid="B25">Gupta and Trivedi, 2012</xref>).</p>
</sec>
<sec id="s2-7-5">
<title>2.7.5 Aerodynamic behavior of the optimized SA protransferosomes</title>
<p>The study was conducted according to the standard approach for aerodynamic testing outlined in Appendix XII F of the British Pharmacopoeia (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>). Briefly, samples of pure SA and the optimized SA protransferosomes (each equivalent to 200&#xa0;mg) were individually packed into five size-3 hard gelatin capsules for aerodynamic testing. Before analysis, all components of the Andersen MKII Cascade Impactor were rinsed with methanol. The impactor was set up with a modified plate configuration&#x2014;adjusted to a flow rate of 60&#xa0;L/min using a vacuum pump&#x2014;which required removing two stages (0 and 7) and adding two new plates at the top (stages 1 and 0). To prevent particle adhesion, all plates were pre-coated with silicone spray (Releasil B, Glamorgan, United Kingdom), and a GF 50 filter was placed at the base. Following pharmacopoeial guidelines, the pump was activated for 4&#xa0;s per run, drawing 4&#xa0;L of air through the impactor (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>). Each sample was tested five times using the Foradil&#x2122; Aerolizer inhaler. After drug dispersion, the deposited particles on each stage and filter were collected by soaking them in 10% methanol and sonicating them for 3&#xa0;min. The aerodynamic performance was analyzed using Copley Scientific&#x2019;s CITDAS software (United Kingdom) to determine three key parameters: fine particle fraction (FPF%), fine particle dose (FPD, &#x3bc;g), and mass median aerodynamic diameter (MMAD, &#x3bc;m) (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>). MMAD plays a crucial role in determining where inhaled particles will deposit in the respiratory tract, while FPF was calculated as the percentage of drug particles that exited the mouthpiece relative to the total amount collected in the throat piece and all impactor stages.</p>
</sec>
</sec>
<sec id="s2-8">
<title>2.8 In vitro antibacterial, antifungal, and antiviral activity studies</title>
<sec id="s2-8-1">
<title>2.8.1 Antibacterial activity</title>
<p>To measure the antibacterial activity of the tested compound against Gram-negative (<italic>E. coli</italic> 0157 ATCC700728, <italic>P. aeruginosa</italic> ATCC90902, <italic>S. typhimurium</italic> ATCC14028, <italic>Enterobacter</italic> sp.) and Gram-positive (<italic>S. aureus</italic> ATCC25923, <italic>E. faecalis</italic>, <italic>S. mutans</italic>), and acid-fast bacteria <italic>Mycobacterium</italic> sp., the method described by Alhadrami et al. (2021) was used (<xref ref-type="bibr" rid="B6">Alhadrami et al., 2020</xref>). The test was performed in 96-well flat polystyrene plates. Ten microliters of tested SA or SA-protranferosomes (final concentration of 250&#xa0;&#xb5;g/mL) was added to 80&#xa0;&#xb5;L of lysogeny broth (LB broth). Afterward, each bacterial suspension was adjusted to a final concentration of 100&#xa0;cfu/mL (OD600 nm), and 10&#xa0;&#xb5;L of the bacterial culture suspension was then added to the sample preparation of SA or SA-protranferosomes in LB. The plates were incubated overnight at 37&#xb0;C. After incubation, the positive antibacterial effect of the tested compound was observed as clearance in the wells. For compounds without antibacterial activity, the growth media appeared opaque in the wells. The control consisted of the pathogen without any treatment. The absorbance was measured after approximately 20&#xa0;h at OD600 using a Spectrostar Nano Microplate Reader (BMG LABTECH GmbH, Allmendgrun, Germany).</p>
</sec>
<sec id="s2-8-2">
<title>2.8.2 Antifungal activity</title>
<p>For pathogenic fungi, the activity of the tested SA or SA-protranferosomes was determined against <italic>A. niger</italic> and <italic>C. albicans</italic>, obtained from Microbial chemistry culture collection, National Research Center, Egypt, using a microplate assay (MTP) with Sabouraud Dextrose Broth (SDB), according to <xref ref-type="bibr" rid="B44">Pierce et al. (2010)</xref> with some modification (<xref ref-type="bibr" rid="B44">Pierce et al., 2010</xref>). After 48&#xa0;h of incubation at 30&#xb0;C in potato dextrose broth (PDB), the fungal cells were recovered after centrifugation and washed twice with sterile PBS. The cells were counted using a hemocytometer and adjusted to a final concentration of 1.0 &#xd7; 10<sup>6</sup> cells/mL. PDB (180 &#xb5;L) was added into wells of a microtiter plate, followed by the addition of 10&#xa0;&#xb5;L of the test molecule (final concentration of 250&#xa0;&#xb5;g/mL) and 10&#xa0;&#xb5;L of an overnight fungal seed. After incubation, the positive antifungal effect of the tested compound was observed as clearance in the wells. Compounds without antifungal activity resulted in opaque growth media in the wells. The control consisted of the non-treated fungal pathogen. The absorbance was measured after approximately 20&#xa0;h at OD<sub>600</sub> using a Spectrostar Nano Microplate Reader (BMG LABTECH GmbH, Allmendgrun, Germany).</p>
</sec>
<sec id="s2-8-3">
<title>2.8.3 Minimum inhibitory concentration (MIC)</title>
<p>The minimum inhibitory concentration (MIC) of the evaluated drug against pathogenic strains was determined using a microplate experiment and serial dilution technique. A stock solution of the antimicrobial compound was prepared by dissolving it in a suitable solvent, such as dimethyl sulfoxide (DMSO) or water, to achieve the necessary concentration. The pathogens, comprising both Gram-negative and Gram-positive bacteria, were cultivated in Mueller&#x2013;Hinton Broth (MHB) for each strain. Serial two-fold dilutions of the compound were prepared on a 96-well microtiter plate, starting with a high concentration in the first column and progressively decreasing in subsequent columns. Each well was inoculated with an identical amount of the bacterial suspension, calibrated to a standard inoculum density (typically 10<sup>5</sup>&#xa0;CFU/mL), and the plate was incubated at 37&#xb0;C for 18&#x2013;24&#xa0;h. After incubation, the MIC was determined by visually examining the wells for bacterial growth. The absence of turbidity indicated inhibition of growth. The OD<sub>600</sub> was measured using a microplate reader. The minimum concentration of the compound that prevented observable growth was designated as the MIC. This assay provides an accurate assessment of the antibacterial efficacy of the compound against each evaluated pathogen. In the same way, MIC for fungi was determined using the same technique with potato dextrose broth and incubation at 30&#xb0;C for 48&#xa0;h.</p>
</sec>
<sec id="s2-8-4">
<title>2.8.4 Antiviral analysis</title>
<p>Vero E6 cells (ATCC<sup>&#xae;</sup> number 1568) were maintained and grown in Dulbecco&#x2019;s modified Eagle medium (DMEM) containing 10% fetal bovine serum (FBS) as described before (<xref ref-type="bibr" rid="B5">Al-Amri et al., 2017</xref>). SARS-CoV-2/human/SAU/85791C/2020 (Gene accession number MT630432.1) was isolated from a human nasopharyngeal swab confirmed positive by RT-PCR in August 2020. IRP number H-02-K-076-00520-298 was obtained from the Saudi Ministry of Health to use patient samples. All experiments involving live SARS-CoV-2 were performed following the internationally recommended safety measures and precautions in the Biosafety Level 3 Facility at the Special Infectious Agent Unit, King Fahd Medical Research Center, King Abdulaziz University, Saudi Arabia. The cytotoxicity and antiviral activities were investigated using Vero E6 cells (Sigma Aldrich). Then, serial concentrations of the test compounds incubated with Vero E6 were infected with SARS-CoV-2 (SARS-CoV-2/human/SAU/85791C/2020 isolate) at a multiplicity of infection (MOI) of approximately 0.5. DMSO was used as a solvent control. The detailed procedure of the quantitative real-time PCR antiviral assay can be found in the <xref ref-type="sec" rid="s12">Supplementary Material</xref>.</p>
</sec>
<sec id="s2-8-5">
<title>2.8.5 Cellular proliferation and cytotoxicity assays</title>
<p>A directly automated cell-counting method was utilized to determine the cell proliferation. At first, the counted cells were seeded on CellCarier-96-optical plates (PerkinElmer) before the study, followed by the addition of SA or remdesivir, and finally, they were incubated for 3&#xa0;days. Next, the cells were counted via a PerkinElmer EnSight reader. Finally, the counted number of cells was compared with those obtained in the solvent controls.</p>
</sec>
<sec id="s2-8-6">
<title>2.8.6 Quantification of RNA</title>
<p>The viral content in harvested cellular supernatants (125&#xa0;&#xb5;L) was deactivated via MagNA Pure LC total NA Lysis/binding buffer. Then, the viral RNA isolation was performed via the isolation device of MagNA Pure 24 NA, consistent with Roche&#x2019;s guidelines. The amplification was performed via a Master Probe kit for RNA, consistent with Roche&#x2019;s guidelines. All PCRs and quantifications were performed via Roche&#x2019;s guidelines with the respective cycler software.</p>
</sec>
</sec>
<sec id="s2-9">
<title>2.9 <italic>In vivo</italic> pharmacokinetics study</title>
<p>The <italic>in vivo</italic> performance of the optimal formulation was examined utilizing <italic>in vivo</italic> pharmacokinetic examination. In addition, the bioavailability of SA was studied in a rabbit model following nebulization of the re-dispersed optimal lyophilized SA protransferosomes and oral administration of the SA suspension.</p>
<p>A total of 12 adult albino rabbits weighing 1.35&#x2013;1.60&#xa0;kg were distributed into two groups. Group 1 received 10&#xa0;mg of the SA suspension orally with the help of a gauge needle (<xref ref-type="bibr" rid="B23">G&#xfc;nther et al., 2004</xref>). In comparison, group 2 received a suspension of the optimized lyophilized protransferosomes (10&#xa0;mg of SA) through nebulization after anesthesia using diethyl ether (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>; <xref ref-type="bibr" rid="B43">Pastor et al., 2015</xref>). The protocol developed for this <italic>in vivo</italic> experiment was certified through the Animal Ethics Committee of Nahda University. (Regd. No. NUB-032-022). Blood samples were taken using EDTA tubes at various intervals for 24&#xa0;h; then, they were centrifuged for 10&#xa0;min at 5,000&#xa0;rpm, and then plasma separation and HPLC-UV analysis were performed.</p>
<p>The plasma samples were analyzed using Dionex Ultimate 3000 UHPLC, supplied with an auto-sampler, a diode array detector (Massachusetts, United States), and a quaternary solvent delivery pump. The C18 reverse-phase column ZORBAX Eclipse Plus<sup>&#xae;</sup> (5&#xa0;&#xb5;m, 250 &#xd7; 4.6&#xa0;mm) (California, United States) was used for the development and quantitation. The internal standard was ciprofloxacin, while the mobile phase was water&#x2013;acetonitrile (2:98% v/v) at a 1.0&#xa0;mL/min flow rate. The test temperature was set to 25&#xb0;C, and UV detection was carried out at 320&#xa0;nm. The output signal was checked and processed using Chromeleon software. Different pharmacokinetic parameters, such as MRT, AUC, t<sub>1/2</sub>, T<sub>max</sub>, and C<sub>max</sub>, were computed via the PKSolver program. The statistical data analysis utilized SPSS 16.0 software (Chicago, IL).</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Optimization of protransferosomes and experimental model evaluation</title>
<p>The user-defined design was a proper statistical design-of-experiments (DOE) technique, and it was used to perform the optimization process. DOE was utilized for this study to estimate the model parameters because it lowered the variance of the constraints estimator due to its efficient norm reduction of the covariance matrix. In addition, it was suggested that applying a DOE design would lead to fewer samples being needed, as compared to other designs, while not impacting the estimated error and variance, which was strongly desired (<xref ref-type="bibr" rid="B7">Ali et al., 2021</xref>).</p>
<p>Twelve transferosomes were developed corresponding to the user-defined experimental design, and then they were characterized for numerous responses. In addition, the interactions among the examined independent and dependent variables were demonstrated mathematically using polynomial equations (<xref ref-type="disp-formula" rid="e1">Equations 1</xref>&#x2013;<xref ref-type="disp-formula" rid="e3">3</xref>; <xref ref-type="table" rid="T3">Table 3</xref>).</p>
<p>The quadratic approach was observed as the best-fitting model for the Y1, Y2, and Y3 variables. All the obtained models were significant at a <italic>p</italic>-value of 0.05. The positive coefficient for the impact of each factor on the measured responses was considered synergistic, while the antagonistic influence was determined by a negative coefficient (<xref ref-type="bibr" rid="B49">Salem et al., 2019a</xref>). All the responses indicated good agreement between the predicted R2 of the determination and the adjusted R2.</p>
<p>Given that the applied model&#x2019;s signal-to-noise ratio had a sufficient degree of precision, that is, more significant than 4, it could be used to explore the design space (<xref ref-type="table" rid="T3">Table 3</xref>; <xref ref-type="bibr" rid="B17">El-Menshawe et al., 2018</xref>). A response-surface analysis was performed to explain how certain independent variables had affected the observed responses. It was clear from the resulting equations (<xref ref-type="table" rid="T3">Table 3</xref>) that the intercept had a positive influence on each of the three responses. <xref ref-type="fig" rid="F1">Figure 1</xref> shows how the independent variables affected the measured responses.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>The impact of the independent variables on the responses.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g001.tif">
<alt-text content-type="machine-generated">Four interaction plots from Design-Expert software display the relationship between cholesterol (X1) and type of surfactant (X2: Tween80 and Na-deoxy cholate) on different responses. Top left plot shows desirability, top right shows percent entrapment efficiency, bottom left shows size, and bottom right shows release. The actual factor is phospholipid to surfactant ratio at eighty-five to fifteen. Data points are indicated, with red and green lines differentiating surfactants.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-2">
<title>3.2 Effect of design variables on vesicle size (Y1)</title>
<p>The ANOVA test results showed that each of the tested factors significantly affected the vesicle size at a <italic>p</italic>-value &#x3c; 0.05, except X2. The size of the transferosomes varied from 141.7 &#xb1; 9.95 to 500.90 &#xb1; 9.27&#xa0;nm (<xref ref-type="table" rid="T2">Table 2</xref>). The examined factors (X1 and X3) had an antagonistic influence on the transferosome mean size, excluding X2, which had a synergistic impact. The increase in the concentration of phospholipid or cholesterol resulted in a significant increase in the transferosome size, while the increase in the surfactant concentration significantly decreased the transferosome size (<xref ref-type="bibr" rid="B33">Khan et al., 2020</xref>).</p>
<p>Our results agreed with those of <xref ref-type="bibr" rid="B37">Moawad et al. (2017)</xref> as we found that the Tween 80 (HLB &#x3d; 15) samples showed smaller transferosomes, as compared to the sodium deoxycholate samples (HLB &#x3d; 16). Despite the higher HLB of sodium deoxycholate, the samples showed larger vesicular sizes, explained by their anionic character. This resulted in a negative charge and caused a powerful repulsion force to develop among the lamellae of the vesicles. Consequently, the aqueous core size increased, producing larger vesicles, as previously mentioned (<xref ref-type="bibr" rid="B37">Moawad et al., 2017</xref>). The homogeneity of the vesicular dispersions was assessed using the PDI. A system with a PDI of 0 had mono-dispersed vesicles, whereas a system with a PDI of 1 had high poly-dispersed vesicles (<xref ref-type="bibr" rid="B56">Song et al., 2022</xref>). The obtained PDI of the SA-loaded transferosomes ranged from 0.103 &#xb1; 0.06 to 1.00 &#xb1; 0.25, indicating that some transferosomes had a balanced size distribution and homogeneity (<xref ref-type="table" rid="T2">Table 2</xref>).</p>
<p>The zeta potential (ZP) is regarded as an essential measure of the physical stability of nano-formulations. The high repelling forces between the vesicles and the large ZP on the surfaces (positive or negative) minimized the aggregation of the vesicles and provided more sustained vesicular stability. The transferosome stability resulted from the decreased interfacial tension caused by using a high surfactant concentration. In addition, the prepared transferosomes had a negative charge ranging from &#x2212;18.1 to &#x2212;42.1&#xa0;mV (<xref ref-type="table" rid="T2">Table 2</xref>). This high negative charge caused steric stabilization and electrostatic repulsion (<xref ref-type="bibr" rid="B51">Salem et al., 2019c</xref>). Nanoparticles have been demonstrated to have a stronger affinity for biological membranes due to the predominant electrostatic interactions. The uptake of strongly negatively charged nanoparticles was preferred by the cells despite the presence of extensive negative charges in the biological membranes due to the predominance of the non-specific interaction mechanisms, as well as the cluster arrangement of the nanoparticles (<xref ref-type="bibr" rid="B51">Salem et al., 2019c</xref>).</p>
</sec>
<sec id="s3-3">
<title>3.3 Effect of design variables on EE% (Y2)</title>
<p>The ANOVA results indicated that each of the tested factors significantly affected the EE% at a <italic>p</italic>-value &#x3c; 0.05, except X2. As shown in <xref ref-type="table" rid="T2">Table 2</xref>, the entrapment efficiency of the transferosomes varied from 76.28% &#xb1; 2.94% to 89.53% &#xb1; 3.61%. The high SA entrapment tendency may have been caused by the hydrophobicity of SA, which made it insoluble in water (<xref ref-type="bibr" rid="B53">Shakeel et al., 2016a</xref>).</p>
<p>The investigated variables (X1 and X3) revealed synergistic interactions, as compared to variable X2, which displayed a significant negative interaction. It was evident that SA entrapment had been increased by the higher ratio of phospholipids to surfactants. These results could have been related to the liquid membrane rupture caused by the high surfactant concentration, which weakened the membrane entrapping the SA (<xref ref-type="bibr" rid="B36">L&#xf3;pez et al., 1998</xref>). Consequently, the increase in surfactant concentration showed a decline in EE%.</p>
<p>Regardless of the kind of surfactant, the percentage of entrapped SA increased with higher cholesterol-to-phospholipid ratio. The transferosomal membrane became highly rigid, and the spaces between the phospholipid and surfactant molecules were filled with cholesterol. This reduced the drug leakage from the vesicles through the cholesterol interaction with the membrane core during the annealing process. Accordingly, the capacity of the transferosomal bilayer membrane to entrap hydrophobic drugs was increased; this might also have been due to the phospholipid bilayer conversion to the solid-phase bilayer as a result of the inclusion of cholesterol (<xref ref-type="bibr" rid="B27">Gyanewali et al., 2021</xref>; <xref ref-type="bibr" rid="B34">Khan et al., 2021</xref>).</p>
</sec>
<sec id="s3-4">
<title>3.4 Effect of design variables on <italic>in vitro</italic> release (Y3)</title>
<p>The ANOVA results showed that each tested factor significantly affected the SA release at <italic>p</italic>-value &#x3c; 0.05. The examined factors X1, X2, and X3 had a significant antagonistic impact on the release percentage.</p>
<p>As shown in <xref ref-type="fig" rid="F2">Figure 2</xref>, the examined release varied from 19.74% &#xb1; 2.26% to 47.47% &#xb1; 1.19%. The increase in the ratio of phospholipid to cholesterol resulted in a significant decrease in the SA released. In contrast, the increase in surfactant concentration significantly increased SA release, owing to the added rigidity and the hydrophobicity of the prepared transferosomes caused by the cholesterol (<xref ref-type="bibr" rid="B1">Abd-Elbary et al., 2008</xref>). Using Tween 80 as a surfactant significantly increased SA release, as compared to use of sodium deoxycholate. These findings agreed with those of both <xref ref-type="bibr" rid="B37">Moawad et al. (2017)</xref> and <xref ref-type="bibr" rid="B29">Jain et al. (2003)</xref>.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>
<italic>In vitro</italic> release profiles of sinapic acid from the prepared transferosomes: <bold>(A)</bold> F1&#x2013;F7, <bold>(B)</bold> F8&#x2013;F12 and SA suspension.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g002.tif">
<alt-text content-type="machine-generated">Line graphs labeled &#x22;A&#x22; and &#x22;B&#x22; show cumulative percentage of release over time. Graph A displays seven formulations (F1-F7) and Graph B displays five formulations (F8-F12) along with SA-suspension. Each line represents different time-release data over five hours, with error bars indicating variability.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-5">
<title>3.5 Selection of optimized SA protransferosomes</title>
<p>The optimization process for the prepared transferosomes aimed to identify the levels of the independent variables required to develop the transferosomes with optimal characteristics. The numerical optimization of the Design-Expert<sup>&#xae;</sup> program was utilized to select an optimal formulation from 12 prepared transferosomal formulations in compliance with the DOE design. The following optimization criteria were used: (i) achievement of maximum percentage of <italic>in vitro</italic> release; (ii) maximum percentage of entrapment efficiency; (iii) minimal size of transferosomes. Following the numerical optimization, the formulation composed of Tween 80 as a surfactant (85:15% w/w as a ratio of phospholipid to Tween 80) and 1:2 w/w as a ratio of cholesterol to phospholipid was selected as the optimized SA-loaded transferosomes. The developed optimized formulation showed a desirability index of 0.678, an <italic>in vitro</italic> release of 28.03% &#xb1; 2.3%, an EE of 89.47% &#xb1; 3.01%, and a mean vesicle size of 232.13 &#xb1; 3.30. The observed study and predicted model achieved an acceptable level of agreement, proving the validity of the model.</p>
</sec>
<sec id="s3-6">
<title>3.6 Characterization of the lyophilized optimal SA protransferosomes</title>
<p>The re-dispersed lyophilized protransferosomes had a vesicle size of 270.2 &#xb1; 5.1&#xa0;nm and a drug content of 98.11% &#xb1; 3.6%. The <italic>in vitro</italic> percentage of the release of SA from the optimal lyophilized transferosome was 32.8% &#xb1; 2.1%, as displayed in <xref ref-type="fig" rid="F3">Figure 3</xref>.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>
<italic>In vitro</italic> percentage of release of sinapic acid from optimal lyophilized transferosome and sinapic acid-suspension.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g003.tif">
<alt-text content-type="machine-generated">Graph showing the cumulative percentage of release over time (hours) for Sinapic suspension and optimum lyophilized transferosomes. The orange line (transferosomes) shows a higher release rate compared to the blue line (Sinapic suspension), with error bars indicating variability at each time point.</alt-text>
</graphic>
</fig>
<sec id="s3-6-1">
<title>3.6.1 Differential scanning calorimetric analysis (DSC)</title>
<p>The melting parameters and DSC thermograms for the phospholipid, Tween 80, cholesterol, SA, and SA-loaded protransferosomes are shown in <xref ref-type="fig" rid="F4">Figure 4</xref>. The DSC thermograms displayed 2 endothermic peaks that appeared at 188&#xb0;C and 194&#xb0;C, corresponding to the melting temperature of the phospholipids with enthalpy fusion &#x394;H &#x3d; &#x2212; 10.6 and &#x2212;0.8&#xa0;MJ, respectively. In addition, two endothermic peaks appeared at 148&#xb0;C and 167&#xb0;C, corresponding to the melting temperature of the Tween 80 with enthalpy fusion &#x394;H &#x3d; &#x2212; 10.6 and &#x2212;2.8&#xa0;MJ, respectively. Additionally, two endothermic peaks appeared at 150&#xb0;C and 170&#xb0;C, corresponding to the melting temperature of the lactose with enthalpy fusion &#x394;H &#x3d; &#x2212; 318.2 and &#x2212;77.9&#xa0;MJ, respectively. The DSC thermograms displayed an endothermic peak at 149&#xb0;C, indicating the melting temperature of the cholesterol with enthalpy fusion &#x394;H &#x3d; &#x2212;199.8&#xa0;mJ. In comparison, the sharp endothermic peaks of SA were observed at 194&#xb0;C, with enthalpy fusion &#x394;H &#x3d; &#x2212;303.0&#xa0;mJ. The SA-loaded protransferosomes exhibited two endothermic peaks at 145&#xb0;C and 170&#xb0;C, with enthalpy fusion &#x394;H &#x3d; &#x2212; 386.7 and &#x2212;40.2&#xa0;mJ, correspondingly. The crystallinity of the phospholipid, cholesterol, Tween 80, and lactose samples was reduced after mixing as they assembled as a transferosome bilayer. The crystallinity of SA was reduced upon loading the transferosomes as SA was loaded within the vesicles in an amorphous form. Moreover, including surfactants in the formulations may have contributed to the crystal distortion and, in turn, a depression in the melting points (<xref ref-type="bibr" rid="B15">Dolatabadi et al., 2021</xref>).</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>DSC thermograms of sinapic acid (drug), phospholipid, Tween 80, cholesterol, and the optimal transferosomes (mix).</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g004.tif">
<alt-text content-type="machine-generated">A differential scanning calorimetry graph shows heat flow versus temperature for five substances: Drug, Lipid, Tween, Cholesterol, and Mix. Each substance&#x27;s curve runs horizontally, displaying different peak patterns at varying temperatures between 0 and 200 degrees Celsius.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-6-2">
<title>3.6.2 Morphology analysis of optimal protransferosomes</title>
<p>The response-surface morphological analysis of the optimal protransferosomes by TEM is displayed in <xref ref-type="fig" rid="F5">Figure 5</xref>. The photomicrograph presented the prepared protransferosomes as well-identified, homogenous, spherical nano-vesicles. In addition, the TEM photomicrograph showed the coating of the carrier particles on the transferosome surface, which was observed as bright spots.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Photomicrograph of optimal lyophilized transferosomes using TEM.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g005.tif">
<alt-text content-type="machine-generated">Electron microscope image showing several spherical particles of the coronavirus. The particles have a distinct spiked surface, resembling a crown. A scale bar indicating 200 nanometers is visible in the lower left corner.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-6-3">
<title>3.6.3 Stability study</title>
<p>The stability study of the optimized SA protransferosomes at 4&#xb0;C and 25&#xb0;C, after 1, 2, and 3 months, was evaluated by studying the EE % and vesicle size. As displayed in <xref ref-type="fig" rid="F6">Figure 6</xref>, the EE % decreased insignificantly during the 3 months of the study. In addition, the vesicle size increased insignificantly at a <italic>p</italic>-value &#x3e; 0.05, after applying the ANOVA test. The vesicle tendency to coalesce due to the weak cohesive and van der Waals forces, which were present all over the transferosomes, had been reported as the cause of the increase in the transferosome size (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>).</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Effect of storage on the vesicle size <bold>(A)</bold> and EE% <bold>(B)</bold> of the optimal lyophilized protransferosomes, at 25&#xb0;C and 4&#xb0;C.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g006.tif">
<alt-text content-type="machine-generated">Graph (A) shows vesicle size in nanometers over three months, with similar results at 4&#xB0;C (red) and 25&#xB0;C (blue). Graph (B) shows entrapment efficiency percentage, also consistent at both temperatures over the same period.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-6-4">
<title>3.6.4 Aerodynamic behavior of the optimized SA protransferosomes</title>
<p>The cascade impactor was used to evaluate and compare the aerodynamic properties of the optimized protransferosome powder and pure SA. Statistical analysis revealed that the protransferosome formulation outperformed that of pure SA in all tested parameters (&#x2a;p&#x2a; &#x3c; 0.05). Fine particle fraction (FPF) obtained for optimized protransferosome powder achieved 29.85% &#xb1; 5.8% FPF, significantly higher (p &#x3c; 0.05) than that of pure SA (17.79% &#xb1; 2.33%). Similarly, fine particle dose (FPD) obtained for optimized protransferosomes exhibited markedly greater FPD values. Particle size emerged as a key reason governing respiratory tract deposition patterns, which directly influence both the deposition site and the delivered drug amount within the lungs (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>; <xref ref-type="bibr" rid="B47">Salem et al., 2011</xref>). The results also showed that the optimized protransferosomes demonstrated significantly smaller MMAD values (2.96 &#xb1; 0.41&#xa0;&#x3bc;m) than pure SA (3.86 &#xb1; 0.10&#xa0;&#x3bc;m) (p &#x3c; 0.05), indicating superior aerosol performance. This enhanced aerodynamic behavior may be due to the improved powder flow characteristics of the protransferosomes, which may explain the more efficient lung targeting compared to the unformulated SA.</p>
</sec>
</sec>
<sec id="s3-7">
<title>3.7 <italic>In vitro</italic> antibacterial and antifungal activity study</title>
<p>Both SA and its protransferosomes demonstrated good inhibition for most of the bacterial and fungal pathogens tested (<xref ref-type="table" rid="T4">Table 4</xref>). MIC for the antibacterial activity demonstrated enhanced activity of SA protransferosomes compared to the pure SA, moving it much closer to the positive control (<xref ref-type="table" rid="T4">Table 4</xref>). Interestingly, in the case of <italic>E. faecalis</italic> and <italic>S. mutans</italic>, although the pure SA did not show good activity, SA protransferosomes demonstrated comparable effects to ciprofloxacin, the positive control. Additionally, SA protransferosomes demonstrated comparable MIC to nystatin, the positive antifungal control drug, against both <italic>C. albicans</italic> and <italic>A. niger</italic> (<xref ref-type="table" rid="T4">Table 4</xref>) and a more enhanced effect compared to pure SA.</p>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Minimum inhibitory concentration (MIC) values (ug/mL).</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="center">Pathogen</th>
<th colspan="4" align="center">MIC (&#xb5;g/mL)</th>
</tr>
<tr>
<th align="center">SA protransferosomes</th>
<th align="center">SA</th>
<th align="center">Ciprofloxacin</th>
<th align="center">Nystatin</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">
<italic>S. aureus</italic> ATCC 25923</td>
<td align="center">2.05 &#xb1; 0.33</td>
<td align="center">3.22 &#xb1; 0.15</td>
<td align="center">0.5 &#xb1; 1.10</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>S. typhimurium</italic> ATCC 14028</td>
<td align="center">1.13 &#xb1; 0.37</td>
<td align="center">3.15 &#xb1; 1.07</td>
<td align="center">0.12 &#xb1; 1.05</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>P. aeruginosa</italic> ATCC 90902</td>
<td align="center">1.22 &#xb1; 0.42</td>
<td align="center">7.23 &#xb1; 0.05</td>
<td align="center">0.25 &#xb1; 0.05</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>E. coli</italic> O157 ATCC 700728</td>
<td align="center">0.40 &#xb1; 0.09</td>
<td align="center">2.23 &#xb1; 0.15</td>
<td align="center">0.06 &#xb1; 1.17</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>E. faecalis</italic>
</td>
<td align="center">1.05 &#xb1; 1.09</td>
<td align="center">&#x2014;</td>
<td align="center">0.5 &#xb1; 1.10</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>S. mutans</italic>
</td>
<td align="center">1.02 &#xb1; 0.85</td>
<td align="center">&#x2014;</td>
<td align="center">0.8 &#xb1; 1.05</td>
<td align="center">&#x2014;</td>
</tr>
<tr>
<td align="left">
<italic>C. albicans</italic>
</td>
<td align="center">3.5.26 &#xb1; 0.14</td>
<td align="center">6.5 &#xb1; 0.12</td>
<td align="center">&#x2014;</td>
<td align="center">3.05 &#xb1; 0.18</td>
</tr>
<tr>
<td align="left">
<italic>A. niger</italic>
</td>
<td align="center">5.25 &#xb1; 0.15</td>
<td align="center">6.23 &#xb1; 0.15</td>
<td align="center">&#x2014;</td>
<td align="center">5.1 &#xb1; 0.25</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Phenolic compounds such as SA can exhibit varying antibacterial activity against different bacterial pathogens due to differences in cell envelope composition, permeability, and resistance mechanisms. For example, Gram-negative bacteria possess an outer membrane that can hinder the penetration of phenolics, reducing their efficacy, while Gram-positive bacteria lack this barrier, making them more susceptible. Additionally, variations in membrane-bound enzymes, efflux pumps, and intracellular targets influence how each strain responds to phenolic stress. The compound&#x2019;s activity may also depend on its ability to disrupt membrane integrity, generate oxidative stress, or denature proteins, mechanisms that can vary in effectiveness depending on the bacterial species and strain.</p>
<p>The higher MIC of SA protransferosomes vs. ciprofloxacin reflects its superior potency, while the lower MIC vs. free SA highlighted the benefits of transfersomes in improving the activity compared to the pure SA, due to its ultra-deformability that enhances penetration through biological membranes due to their elasticity. Transferosomes retain SA longer, so they provide prolonged release, which sustains its activity longer. It also provides a shield for SA from enzymatic degradation through encapsulation. These properties regarding transfersomes may be the explanation for its enhanced activity (<xref ref-type="bibr" rid="B4">Aguilar-Toal&#xe1; et al., 2022</xref>; <xref ref-type="bibr" rid="B39">Opatha et al., 2020</xref>).</p>
</sec>
<sec id="s3-8">
<title>3.8 <italic>In vitro</italic> antiviral activity study</title>
<p>An <italic>in vitro</italic> antiviral assay of SA against SARS-CoV-2 showed an IC<sub>50</sub> value of 2.29 &#xb1; 0.065&#xa0;&#x3bc;g/mL. This value was comparable to our previous report, where IC<sub>50</sub> had been found to be 2.69&#xa0;&#x3bc;g/mL (<xref ref-type="bibr" rid="B40">Orfali et al., 2021</xref>). The IC<sub>50</sub> of the reference antiviral drug, remdesivir, was 0.036 &#xb1; 0.002&#xa0;&#x3bc;g/mL. Both SA and remdesivir showed significantly low cytotoxicity to the host cells, with a CC<sub>50</sub> of 188.33 &#xb1; 10.8 and 170.74&#xa0;&#x3bc;g/mL, respectively.</p>
<p>The newly formulated SA protransferosomes showed significantly enhanced antiviral activity: 50% viral growth inhibition at significantly reduced concentrations (IC<sub>50</sub> &#x3d; 0.016 &#xb1; 0.008&#xa0;&#x3bc;g/mL; the IC<sub>50</sub> of the lyophilized SA formulation &#x3d; 0.0179 &#xb1; 0.0089&#xa0;&#x3bc;g/mL). Hence, this new formulation was more potent than remdesivir. Accordingly, the present nano-formulation improved the cellular delivery of SA.</p>
<p>The enhanced antiviral activity of SA-loaded protransferosomes can be attributed to the unique physicochemical properties of transferosomes, particularly their ultra-deformability. This high flexibility allows transferosomes to traverse biological barriers more effectively than conventional liposomes by squeezing through tight intercellular spaces and facilitating fusion with cellular membranes, thereby improving intracellular delivery and bioavailability of SA (<xref ref-type="bibr" rid="B18">Elsayed et al., 2006</xref>; <xref ref-type="bibr" rid="B24">Gupta et al., 2005</xref>). Additionally, transferosomes offer a sustained release profile, prolonging the retention and therapeutic effect of SA (<xref ref-type="bibr" rid="B55">Song et al., 2012</xref>). The encapsulation also protects SA from enzymatic degradation, preserving its structural integrity and antiviral efficacy (<xref ref-type="bibr" rid="B4">Aguilar-Toal&#xe1; et al., 2022</xref>; <xref ref-type="bibr" rid="B39">Opatha et al., 2020</xref>). These combined features likely contribute to the superior antiviral performance observed with SA protransferosomes. Of course, this should be supported by future <italic>in vivo</italic> studies.</p>
</sec>
<sec id="s3-9">
<title>3.9 <italic>In vivo</italic> pharmacokinetic study</title>
<p>Each of the calculated pharmacokinetic parameters was determined by constructing a plasma&#x2013;concentration time curve, as presented in <xref ref-type="fig" rid="F7">Figure 7</xref>. The relative bioavailability of the nebulized SA protransferosomes was 6.1-fold of the oral SA. The AUC for the SA protransferosomes was significantly more than the AUC of the oral SA, by a factor of 6.1 (<italic>p</italic> &#x3d; 0.001). The increased bioavailability of the SA protransferosomes can be attributed to their ability to bypass the first-pass hepatic processing. Whereas the oral SA had a T<sub>max</sub> of 2&#xa0;h and a C<sub>max</sub> of 118.136&#xa0;&#x3bc;g/mL, the SA protransferosomes had a T<sub>max</sub> of 4&#xa0;h and a C<sub>max</sub> of 287.116&#xa0;&#x3bc;g/mL, as shown in <xref ref-type="table" rid="T5">Table 5</xref>. Moreover, the SA protransferosomes had an increased MRT and t1/2 with a considerable (<italic>p</italic> &#x3d; 0.001) increase and effectively maintained their plasma concentration. The longer T<sub>max</sub>, which was correlated with the release date, may have been caused by the prolonged SA release into the alveolar fluid from the protransferosomes before it could be absorbed via the systemic circulation (<xref ref-type="bibr" rid="B20">Gamal et al., 2020</xref>; <xref ref-type="bibr" rid="B46">Saimi et al., 2021</xref>).</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Mean sinapic acid concentrations in rabbit plasma after administration of oral sinapic suspension and nebulized lyophilized protransferosomes.</p>
</caption>
<graphic xlink:href="fnano-07-1599272-g007.tif">
<alt-text content-type="machine-generated">Line graph showing plasma concentration versus time for oral-sinapic suspension and nebulized protransferosomes. The red line for nebulized protransferosomes peaks at over 300 micrograms per milliliter at around 2 hours, then declines. The blue line for oral-sinapic suspension peaks at around 50 micrograms per milliliter at 1 hour and drops steadily. Time is on the x-axis, ranging from 0 to 25 hours, and concentration is on the y-axis, from 0 to 350 micrograms per milliliter.</alt-text>
</graphic>
</fig>
<table-wrap id="T5" position="float">
<label>TABLE 5</label>
<caption>
<p>Pharmacokinetic parameters for sinapic acid in rabbit plasma, following administration of oral sinapic suspension and nebulized protransferosomes.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Parameters</th>
<th align="center">Oral sinapic suspension</th>
<th align="center">Nebulized protransferosomes</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">C<sub>max</sub> (&#xb5;g/mL)</td>
<td align="center">118.136</td>
<td align="center">287.116</td>
</tr>
<tr>
<td align="left">T<sub>max</sub> (h)</td>
<td align="center">2</td>
<td align="center">4</td>
</tr>
<tr>
<td align="left">AUC<sub>0-24</sub> (&#xb5;g.h/mL)</td>
<td align="center">644.590</td>
<td align="center">3930.165</td>
</tr>
<tr>
<td align="left">
<inline-formula id="inf2">
<mml:math id="m5">
<mml:mrow>
<mml:msub>
<mml:mtext>AUC</mml:mtext>
<mml:mrow>
<mml:mn>0</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>&#x221e;</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula> (&#xb5;g.h/mL)</td>
<td align="center">746.686</td>
<td align="center">4870.390</td>
</tr>
<tr>
<td align="left">
<inline-formula id="inf3">
<mml:math id="m6">
<mml:mrow>
<mml:msub>
<mml:mtext>MRT</mml:mtext>
<mml:mrow>
<mml:mn>0</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>&#x221e;</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula> (h)</td>
<td align="center">6.74</td>
<td align="center">9.17</td>
</tr>
<tr>
<td align="left">t<sub>1/2</sub> (h)</td>
<td align="center">8.29</td>
<td align="center">9.45</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>This study focused on developing a nanocarrier that could deliver SA to the lungs. The developed SA protransferosomes displayed dramatically improved bioavailability and <italic>in vitro</italic> antiviral efficacy through pulmonary nebulization, making them a potential SA delivery strategy. Additionally, the developed SA protransferosomes showed enhanced antibacterial and antifungal effects against a panel of tested pathogens. As a result, the produced SA protransferosomes could be considered a safe and efficient pulmonary targeting system via nebulization. Furthermore, there are encouraging prospects for the therapeutic use of medications that target the lungs, which could be crucial therapies for many other pulmonary disorders, SARS-CoV-2 infection, and bacterial and fungal infections. The current study should be verified using a suitable animal model to quantify the lung targeting efficiency and safety.</p>
</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/<xref ref-type="sec" rid="s12">Supplementary Material</xref>; further inquiries can be directed to the corresponding author.</p>
</sec>
<sec sec-type="ethics-statement" id="s6">
<title>Ethics statement</title>
<p>The animal study was approved by the Animal Ethics Committee of Nahda University. The study was conducted in accordance with the local legislation and institutional requirements.</p>
</sec>
<sec sec-type="author-contributions" id="s7">
<title>Author contributions</title>
<p>HA: software, project administration, writing &#x2013; original draft, funding acquisition, methodology, and investigation. AG: investigation, writing &#x2013; original draft, software, methodology, and formal analysis. NA: investigation, writing &#x2013; review and editing, methodology, and formal analysis. AS: writing &#x2013; original draft, methodology, formal analysis, validation, software, and investigation. MR: project administration, supervision, funding acquisition, validation, data curation, conceptualization, resources, and writing &#x2013; review and editing. DN: software, supervision, resources, conceptualization, formal analysis, validation, methodology, and writing &#x2013; original draft.</p>
</sec>
<sec sec-type="funding-information" id="s8">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research and/or publication of this article. This study was funded by the British Council, UK-Saudi Challenge Fund 2023-24 &#x2013; UWS/KAU.</p>
</sec>
<ack>
<p>The authors therefore acknowledge with thanks the British Council for their financial and technical support.</p>
</ack>
<sec sec-type="COI-statement" id="s9">
<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="s10">
<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="s11">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
<sec sec-type="supplementary-material" id="s12">
<title>Supplementary material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/fnano.2025.1599272/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fnano.2025.1599272/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="DataSheet1.pdf" id="SM1" mimetype="application/pdf" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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