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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Food. Sci. Technol.</journal-id>
<journal-title>Frontiers in Food Science and Technology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Food. Sci. Technol.</abbrev-journal-title>
<issn pub-type="epub">2674-1121</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1376415</article-id>
<article-id pub-id-type="doi">10.3389/frfst.2024.1376415</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Food Science and Technology</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Binderless particleboards obtained 100% from winery by-products for the packaging industry</article-title>
<alt-title alt-title-type="left-running-head">Fernandes 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/frfst.2024.1376415">10.3389/frfst.2024.1376415</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Fernandes</surname>
<given-names>Raquel 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="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2256564/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/investigation/"/>
<role content-type="https://credit.niso.org/contributor-roles/methodology/"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Lopes</surname>
<given-names>Sandro</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/methodology/"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Ferreira</surname>
<given-names>Nuno</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/methodology/"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Santos</surname>
<given-names>Jorge</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2257146/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/formal-analysis/"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Martins</surname>
<given-names>Jorge M.</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
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</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Carvalho</surname>
<given-names>Luisa H.</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
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<aff id="aff1">
<sup>1</sup>
<institution>ARCP Colab&#x2014;Rede de Compet&#xea;ncias em Pol&#xed;meros</institution>, <addr-line>Porto</addr-line>, <country>Portugal</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>LEPABE&#x2014;Faculty of Engineering</institution>, <institution>University of Porto</institution>, <addr-line>Porto</addr-line>, <country>Portugal</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>ALiCE&#x2014;Associate Laboratory in Chemical Engineering</institution>, <institution>Faculty of Engineering</institution>, <institution>University of Porto</institution>, <addr-line>Porto</addr-line>, <country>Portugal</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>DEMad&#x2014;Department of Wood Engineering</institution>, <institution>Instituto Polit&#xe9;cnico de Viseu</institution>, <addr-line>Viseu</addr-line>, <country>Portugal</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/1498729/overview">Aris E. Giannakas</ext-link>, University of Patras, Greece</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/1616867/overview">Ricardo G&#xf3;mez Garc&#xed;a</ext-link>, Universidade Cat&#xf3;lica Portuguesa, Portugal</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1123160/overview">Rui M. S. Cruz</ext-link>, Universidade do Algarve, Portugal</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Raquel A. Fernandes, <email>raquel.fernandes@arcp.pt</email>; Luisa H. Carvalho, <email>lhcarvalho@estgv.ipv.pt</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>18</day>
<month>04</month>
<year>2024</year>
</pub-date>
<pub-date pub-type="collection">
<year>2024</year>
</pub-date>
<volume>4</volume>
<elocation-id>1376415</elocation-id>
<history>
<date date-type="received">
<day>25</day>
<month>01</month>
<year>2024</year>
</date>
<date date-type="accepted">
<day>29</day>
<month>03</month>
<year>2024</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2024 Fernandes, Lopes, Ferreira, Santos, Martins and Carvalho.</copyright-statement>
<copyright-year>2024</copyright-year>
<copyright-holder>Fernandes, Lopes, Ferreira, Santos, Martins and Carvalho</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>The valorization of bioeconomy by-products holds immense significance in achieving sustainability goals and fostering resource efficiency, not only to reduce the amount of waste generated but also to significantly decrease the carbon footprint associated with several industrial fields, by promoting circular economy. The wine industry is not only one of the major contributors for world&#x2019;s economy but also a great producer of by-products, with no valorization process associated. Grape stalks are a great source of chemical molecules, as polyphenols, that can be applied in the production of bio-adhesives. In the present work, grape stalk particles were used as raw material to obtain a highly rich extract with bonding properties through solid/liquid extraction. Different extraction agents were tested (water, NaOH, and Na<sub>2</sub>CO<sub>3</sub>) at varied concentrations (0.1%, 0.5%, and 1.0%, respectively). Additionally, extracts were chemically characterized, and the bonding capacity was also evaluated. Using NaOH 1.0%, an extraction efficiency of 8.9% and a total content of polyphenols of 1.4% were achieved. Moreover, all extracts presented an interesting bonding capacity (&#x3e;1.0&#xa0;MPa) by hot-press at 120&#xb0;C for 120&#xa0;s. The composite panel produced using grape stalk adhesive and vine strain particles fulfills the requirements for type P1 particleboards in terms of internal bond strength, reaching 0.66&#xa0;MPa. The mechanical and wettability properties of composite material allow foreseeing a promising application in the food packaging industry.</p>
</abstract>
<kwd-group>
<kwd>grape stalk</kwd>
<kwd>bio-adhesives</kwd>
<kwd>polyphenols</kwd>
<kwd>alkaline extraction</kwd>
<kwd>mechanical properties</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Food Packaging and Preservation</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>The wine industry is one of the major contributors to the world economy of Portugal. According to the International Organization of Vine and Wine (OIV) in 2023, Portugal occupies the 11th place in the world ranking of wine production, with ca. 6.8 million hL (<xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). In the winemaking process, significant quantities of by-products are generated, both liquid, as washing waters, and solid, namely, stalk (5%&#x2013;7%), pomace (20%&#x2013;25%), and lees (2%&#x2013;6%) (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B3">Baptista et al., 2023</xref>). In fact, for producing 100&#xa0;L of wine, ca. 31&#xa0;kg of solid and 50&#x2013;140&#xa0;L of liquid by-products are generated (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B3">Baptista et al., 2023</xref>). One of the biggest issues associated with winemaking residues is the environmental impact of improper disposal. Traditional methods, such as landfilling or open-field burning, contribute to greenhouse gas emissions and soil degradation (<xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B15">Filippi et al., 2021</xref>; <xref ref-type="bibr" rid="B45">Troilo et al., 2021</xref>; <xref ref-type="bibr" rid="B2">Atatoprak et al., 2022</xref>). The organic matter present in these types of by-products can also contribute to the environmental degradation due to the leaching of chemicals into the soil and water, thus posing a threat to ecosystems and human health (<xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B15">Filippi et al., 2021</xref>; <xref ref-type="bibr" rid="B45">Troilo et al., 2021</xref>; <xref ref-type="bibr" rid="B2">Atatoprak et al., 2022</xref>).</p>
<p>To address these concerns, the valorization of winery residues offers a sustainable solution with great potential. In the last years, efforts have been made by academic and industrial researchers to develop and improve technologies to valorize winery by-products for food, health, energy, and, also, particleboard (PB) manufacturing (<xref ref-type="bibr" rid="B6">Botelho et al., 2018</xref>; <xref ref-type="bibr" rid="B17">Gao et al., 2021</xref>; <xref ref-type="bibr" rid="B10">Contreras M del et al., 2022</xref>; <xref ref-type="bibr" rid="B21">Ju et al., 2022</xref>; <xref ref-type="bibr" rid="B34">Rodrigues et al., 2022</xref>; <xref ref-type="bibr" rid="B22">Li et al., 2023</xref>). In the case of PB manufacturing, wine residues were used as raw material with traditional resin as binders (<xref ref-type="bibr" rid="B26">Ntalos and Grigoriou, 2002</xref>; <xref ref-type="bibr" rid="B50">Yeniocak et al., 2014</xref>; <xref ref-type="bibr" rid="B49">Wronka and Kowaluk, 2019</xref>). However, recent work reported by this research group showed the viability of using wine residues to obtain extracts with applicability in bio-adhesive formulation, which can be an interesting alternative to the use of synthetic binders (<xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). On the other hand, by incorporating winery residues into the composition of particleboards, manufacturers can enhance the material&#x2019;s properties, such as strength and durability, while simultaneously reducing the reliance on conventional wood fibers (<xref ref-type="bibr" rid="B26">Ntalos and Grigoriou, 2002</xref>; <xref ref-type="bibr" rid="B50">Yeniocak et al., 2014</xref>).</p>
<p>One of the emergent applications of wood-based materials is the packaging industry, once the conventional materials adopted, such as plastics, metals, and glass, have created tremendous environmental concerns (<xref ref-type="bibr" rid="B24">Mujtaba et al., 2022</xref>; <xref ref-type="bibr" rid="B47">Wang et al., 2022</xref>). These materials, derived from finite fossil fuel resources, not only contribute significantly to carbon emissions during production but also pose persistent challenges in end-of-life management (<xref ref-type="bibr" rid="B24">Mujtaba et al., 2022</xref>; <xref ref-type="bibr" rid="B47">Wang et al., 2022</xref>). The proliferation of non-biodegradable plastics has resulted in extensive pollution of terrestrial and aquatic ecosystems, with long-lasting environmental consequences. Additionally, the energy-intensive processes involved in manufacturing traditional packaging materials further exacerbate the industry&#x2019;s carbon footprint (<xref ref-type="bibr" rid="B24">Mujtaba et al., 2022</xref>; <xref ref-type="bibr" rid="B47">Wang et al., 2022</xref>). Considering these challenges, a paradigm shift toward sustainable packaging materials is imperative to mitigate the ecological impact of the packaging industry. Wood has been used for packaging purposes for centuries not only to pack but also to transport, handle, preserve, present, and add value to many food products and sectors (<xref ref-type="bibr" rid="B12">Debeaufort, 2021</xref>). In fact, 9%&#x2013;12% of overall production of packaging material is occupied by wood-based products due to the lower price, sustainability, and recyclability of this raw material (<xref ref-type="bibr" rid="B12">Debeaufort, 2021</xref>). However, the existing solutions are based on the use of virgin wood, with high potential to apply in other value-added industries. Therefore, the use of lignocellulosic by-products as raw material for the development of food packaging solutions seems to be a promising route to efficient and eco-friendly products (<xref ref-type="bibr" rid="B36">S&#xe1;nchez-Safont et al., 2018</xref>; <xref ref-type="bibr" rid="B32">Qasim et al., 2021</xref>; <xref ref-type="bibr" rid="B40">Santos et al., 2021</xref>; <xref ref-type="bibr" rid="B4">Basc&#xf3;n-Villegas et al., 2022</xref>; <xref ref-type="bibr" rid="B38">Santos et al., 2024</xref>). Some works have been performed on the development of composite materials using lignocellulosic particles with other polymers, such as PHB and polyethylene glycol (<xref ref-type="bibr" rid="B36">S&#xe1;nchez-Safont et al., 2018</xref>; <xref ref-type="bibr" rid="B4">Basc&#xf3;n-Villegas et al., 2022</xref>). Nevertheless, the development of solutions that are composed by lignocellulosic residues has been slightly explored, with only two reports, by our research group, on the use of poplar peeling and cardoon stalk to the production of composite materials (<xref ref-type="bibr" rid="B40">Santos et al., 2021</xref>; <xref ref-type="bibr" rid="B38">Santos et al., 2024</xref>). However, the bio-adhesives produced in both cases were obtained by mixing the polyphenolic extracts with citric acid, a cross-linking agent that enhances bonding performance.</p>
<p>In this way, the present work proves the use of a 100% bio-adhesive, obtained only from grape stalks, without the addition of cross-linkers or hardeners, to produce composite materials, using winery by-products (grape stalk and vine strains) as raw material. The impact of the extraction agent and its concentration on the efficiency of the process was studied. The chemical characterization of all extracts was also performed, as well as the evaluation of their bonding properties. Lastly, particleboards using the best performing bio-adhesive and grape stalk/vine strains particles were produced, and the physical&#x2013;mechanical evaluation was accessed according to the standard methods for PB (density - EN 323, moisture content - EN 322, internal bond strength (IB) - EN 319, bending strength, BS - EN 310, and thickness swelling, TS - EN317). Additionally, the wettability properties were also studied. To the best of our knowledge, it was the first time that a particleboard 100% based on winery by-products was produced, with the requirements of EN 312 being fulfilled in terms of internal bond strength to be characterized as type P1 (general purpose boards for use in dry conditions).</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Raw materials</title>
<p>Grape stalk and vine strains (<italic>Vitis vinifera</italic> L.) were collected from Quinta da Alameda in the center region of Portugal (Nelas, Viseu) and dried at 40&#xa0;&#xb0;C in an oven until reaching equilibrium moisture for further processing. Raw materials were grounded at 1,500&#xa0;rpm using a 10-mm square grid in a cutting mill (Retsch SN 300) and then sieved using a vibrating sieve shaker (Retsch AS 200 control) with an amplitude of 2&#xa0;mm for 2&#xa0;min to select the fraction of particles with a size between 500&#xa0;&#x3bc;m and 2&#xa0;mm. Sodium hydroxide (97%), sodium carbonate (97%), gallic acid (anhydrous), sodium nitrite (anhydrous), and aluminum chloride (anhydrous) were supplied by Sigma-Aldrich and used as received. Folin&#x2013;Ciocalteu reagent (VWR chemicals) was purchased from VWR and used as received. (&#x2b;)-Catechin hydrate (&#x3e;97.0%) and 2,2-diphenyl-1-picrylhydrazyl free radical (DPPH, &#x3e;97.0%) were provided by TCI and used as received.</p>
</sec>
<sec id="s2-2">
<title>2.2 Extraction of polyphenols</title>
<p>The extraction of polyphenols was carried out at 70&#xa0;&#xb0;C in a 3-L jacketed borosilicate reactor. The extractive agent (aqueous NaOH and aqueous Na<sub>2</sub>CO<sub>3</sub>) with a certain concentration (0.1%, 0.5%, and 1.0% w/v) was pumped into the reactor with a flow rate of 20&#xa0;mL&#xa0;min<sup>&#x2212;1</sup> under recirculating mode, and a solid/liquid ratio of 1/5 (w/w) was kept in all cases. Distilled water was also used as an extractive agent for comparison purposes. After 1&#xa0;h of extraction, the suspension was filtered through a nylon membrane (125&#xa0;&#xb5;m), and the liquid extract was chemically characterized (pH, solid content, FTIR, ABES, and extraction yield). In order to improve the stability, the liquid extract was dried through the spray drying process at 180&#xa0;&#xb0;C, using a spray drying system (SD-06, LabPlant, United Kingdom). The liquid was fed at a flow rate of 50&#xa0;mL&#xa0;min<sup>&#x2212;1</sup>, and compressed air (a flow rate of 35&#xa0;m<sup>3</sup>&#xa0;h<sup>&#x2212;1</sup>) was used for dispersion. <xref ref-type="table" rid="T1">Table 1</xref> presents the codification attributed to all experiments, according to extraction conditions.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Codification of the obtained extracts according to the extraction conditions.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Extraction agent</th>
<th align="left">Concentration (w/v %)</th>
<th align="left">Codification</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Water</td>
<td align="left">n.a.</td>
<td align="left">EXT0</td>
</tr>
<tr>
<td align="left"/>
<td align="left">0.1</td>
<td align="left">EXT1</td>
</tr>
<tr>
<td align="left">NaOH</td>
<td align="left">0.5</td>
<td align="left">EXT2</td>
</tr>
<tr>
<td align="left"/>
<td align="left">1.0</td>
<td align="left">EXT3</td>
</tr>
<tr>
<td align="left"/>
<td align="left">0.1</td>
<td align="left">EXT4</td>
</tr>
<tr>
<td align="left">Na<sub>2</sub>CO<sub>3</sub>
</td>
<td align="left">0.5</td>
<td align="left">EXT5</td>
</tr>
<tr>
<td align="left"/>
<td align="left">1.0</td>
<td align="left">EXT6</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>n.a.&#x2014;not applicable.</p>
</fn>
</table-wrap-foot>
</table-wrap>
<p>All the experiments were evaluated in terms of extraction efficiency (EE) according to Eq. <xref ref-type="disp-formula" rid="e1">1</xref>:<disp-formula id="e1">
<mml:math id="m1">
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<mml:mrow>
<mml:mo>%</mml:mo>
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<mml:mi mathvariant="bold-italic">a</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi mathvariant="bold-italic">o</mml:mi>
<mml:mi mathvariant="bold-italic">f</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi mathvariant="bold-italic">r</mml:mi>
<mml:mi mathvariant="bold-italic">a</mml:mi>
<mml:mi mathvariant="bold-italic">w</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi mathvariant="bold-italic">m</mml:mi>
<mml:mi mathvariant="bold-italic">a</mml:mi>
<mml:mi mathvariant="bold-italic">t</mml:mi>
<mml:mi mathvariant="bold-italic">e</mml:mi>
<mml:mi mathvariant="bold-italic">r</mml:mi>
<mml:mi mathvariant="bold-italic">i</mml:mi>
<mml:mi mathvariant="bold-italic">a</mml:mi>
<mml:mi mathvariant="bold-italic">l</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="bold-italic">g</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn mathvariant="bold">100</mml:mn>
<mml:mo>.</mml:mo>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
</p>
</sec>
<sec id="s2-3">
<title>2.3 Chemical characterization of extracts</title>
<sec id="s2-3-1">
<title>2.3.1 Total phenolic content</title>
<p>The determination of the total phenolic content of liquid extracts (obtained immediately after the extraction and without any post-processing) was performed using the Folin&#x2013;Ciocalteu method, as described elsewhere (<xref ref-type="bibr" rid="B35">Rodrigues et al., 2023</xref>). For this, 0.25&#xa0;mL of the liquid extract was diluted in 15&#xa0;mL of distilled water and then mixed with 1.25&#xa0;mL of the Folin&#x2013;Ciocalteu reagent (previously diluted in water 1:10 v:v). The mixture was homogenized and left in the dark for 8&#xa0;min. After this period, 3.75&#xa0;mL of the sodium carbonate solution (75&#xa0;g&#xa0;L<sup>&#x2212;1</sup>) and 4.75&#xa0;mL of distilled water were added. The mixture was homogenized and left in the dark for 2&#xa0;h. A blank sample was also prepared using distilled water. The absorbance of all samples was measured at 760&#xa0;nm using a UV-vis Peak Instruments T-9100 spectrophotometer. Gallic acid was used as standard, and the phenolic content was expressed as gallic acid equivalent (GAE) per 100&#xa0;g of raw material (on dried basis). The analyses were done in triplicate, and the mean value was calculated.</p>
</sec>
<sec id="s2-3-2">
<title>2.3.2 Total flavonoid content</title>
<p>The total flavonoid content was performed through aluminum chloride colorimetric assay (<xref ref-type="bibr" rid="B35">Rodrigues et al., 2023</xref>). For this, 100&#xa0;&#xb5;L of the liquid extract was added to 4&#xa0;mL of distilled water. Then, 0.30&#xa0;mL of sodium nitrite (5% w/v) was mixed, and the solution was homogenized. After 5&#xa0;min, 0.30&#xa0;mL of aluminum chlorite (10% w/v) was added, and the mixture was left at room temperature for over 6&#xa0;min. Upon this period, 2&#xa0;mL of aqueous NaOH (1&#xa0;M) and 3.30&#xa0;mL of distilled water were added. After homogenization, the absorbance was measured at 510&#xa0;nm in a UV-vis Peak Instruments T-9100 spectrophotometer. Catechin was used as the standard, and the total flavonoid content was expressed in terms of catechin equivalents (EC) per 100&#xa0;g of raw material (on a dry basis). The analyses were done in triplicate, and the mean value was calculated.</p>
</sec>
<sec id="s2-3-3">
<title>2.3.3 DPPH radical scavenging activity</title>
<p>The antioxidant activity of liquid extracts was quantified through the free radical scavenging activity of 1,1-diphenyl-2-picrylhydrazyl (DPPH&#x2022;) (<xref ref-type="bibr" rid="B35">Rodrigues et al., 2023</xref>). In this measurement, 3&#xa0;mL of the DPPH&#x2022; methanolic solution (0.60&#xa0;mM) was mixed with 100&#xa0;&#xb5;L of the liquid extract and left in dark at room temperature for 1&#xa0;h. After the reaction, the absorbance was measured at 517&#xa0;nm using a UV-vis Peak Instruments T-9100 spectrophotometer. The antioxidant activity (AA) was calculated according to Eq. <xref ref-type="disp-formula" rid="e1">1</xref>:<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:mi mathvariant="bold-italic">A</mml:mi>
<mml:mi mathvariant="bold-italic">A</mml:mi>
<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:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">A</mml:mi>
<mml:mi mathvariant="bold-italic">b</mml:mi>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="bold-italic">A</mml:mi>
<mml:mi mathvariant="bold-italic">s</mml:mi>
</mml:msub>
</mml:mrow>
<mml:msub>
<mml:mi mathvariant="bold-italic">A</mml:mi>
<mml:mi mathvariant="bold-italic">b</mml:mi>
</mml:msub>
</mml:mfrac>
<mml:mo>&#xd7;</mml:mo>
<mml:mn mathvariant="bold">100</mml:mn>
<mml:mo>,</mml:mo>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>where A<sub>b</sub> is the absorbance of blank (distilled water) and A<sub>s</sub> is the absorbance of the sample. The analyses were done in triplicate, and the mean value was calculated</p>
</sec>
<sec id="s2-3-4">
<title>2.3.4 Fourier-transform infrared (FTIR) spectroscopy</title>
<p>FTIR spectra were recorded on a VERTEX 70 FTIR spectrometer (BRUKER, Biller-ica, MA, United States) in the transmittance mode and equipped with a high-sensitivity DLaTGS detector at room temperature. Dried samples (raw materials and polyphenolic extracts) were measured in the ATR mode with no pre-treatment, using an A225/Q PLATINUM ATR diamond crystal with a single-reflection accessory. The spectra were recorded from 4000 to 400&#xa0;cm<sup>&#x2212;1</sup> with a resolution of 4&#xa0;cm<sup>&#x2212;1</sup>. All spectra were recorded and processed with OPUS 7.0 software.</p>
</sec>
<sec id="s2-3-5">
<title>2.3.5 Automated bonding evaluation system</title>
<p>The bonding capacity of adhesives was evaluated using an automated bonding evaluation system (ABES) (Adhesive Evaluation Systems, United States) at 120&#xa0;&#xb0;C and different pressing times (10, 30, 60, 120, and 180&#xa0;s), as described elsewhere (<xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). Before testing, wood veneer samples (<italic>Fagus sylvatica</italic> L., with 0.7&#xa0;mm of thickness) were conditioned for 1&#xa0;week at 20&#xa0;&#xb0;C and 53% of relative humidity. After this period, probes were cut into 117&#xa0;mm &#xd7; 20-mm&#xa0;strips using a pneumatically driven sample cutting device specific for this type of preparation.</p>
<p>For the test, two probes were along the fiber direction glued using 10&#xa0;mg of adhesive with a 100&#xa0;m<sup>2</sup> overlap. After the chosen pressing time, probes were pulled, and the maximum shear strength was determined. Measurements were done in triplicate for each pressing time, and the results were averaged.</p>
</sec>
</sec>
<sec id="s2-4">
<title>2.4 Particleboard production</title>
<p>A bio-adhesive was produced by concentrating the polyphenolic extract up to 20% of solid content, using a rotary evaporator. The bio-adhesive was used in the manufacturing of particleboards (PBs), using grape stalk and vine strain particles (2&#xa0;mm&#x2013;500&#xa0;&#xb5;m) as raw material. Therefore, PBs with 250 &#xd7; 250&#xa0;mm<sup>2</sup> (8&#xa0;mm of thickness) were produced through hot-pressing with 10&#xa0;wt% of bio-adhesive and a target density of 850&#xa0;kg&#xa0;m<sup>&#x2212;3</sup>. The mixture was hot pressed at 160&#xa0;&#xb0;C during 10&#xa0;min at a fixed thickness of 8&#xa0;mm. The panels were denoted GS or VS, taking into account the raw material used for the production of PBs (grape stalk&#x2013;GS or vine strains&#x2013;VS).</p>
</sec>
<sec id="s2-5">
<title>2.5 Physical&#x2013;mechanical evaluation</title>
<p>The physical&#x2013;mechanical properties of obtained composite panels were evaluated according to the European standards in terms of density (EN 323:2010), moisture content (EN 322:2010), internal bond strength (IB; EN 319:2010), bending strength (BS; EN 310:2010), and thickness swelling (TS; EN 317:2010). Composite panels were classified according to the standard EN 312:2010.</p>
<p>The wetting behavior of composite panels was determined with the Mobile Surface Analyzer (MSA) One-Click SFE (Kruss, GmbH, Germany) equipped with a video measuring system, high-resolution camera, and a high-performance digitizing adapter that enables instantaneous and frequent registration. Advance software (Kruss, GmbH, Germany) was used for data collection. Water (polar) and diiodomethane (non-polar) were used as probe liquids. A measure of 2.0&#xa0;&#x3bc;L drop of each liquid was placed on the sample surface for each measurement. Three test drops of each sample were performed for all liquids. The right and left contact angles between each droplet and the sample surface were collected at intervals of 1&#xa0;s during the first 10&#xa0;s and intervals of 10&#xa0;s for a total duration of 60 s, and then, the average of the contact angles was automatically calculated to determine the surface free energy, according to the Owens, Wendt, Rabel, and Kaelble (OWRK) method.</p>
</sec>
<sec id="s2-6">
<title>2.6 Statistical analysis</title>
<p>All determinations were conducted in triplicate, and the data are presented as the means &#xb1; standard deviations. The impact of extractive agents (NaOH and Na<sub>2</sub>CO<sub>3</sub>) and their concentrations (0.1, 0.5% and 1.0% w/v) on the extraction efficiency and chemical properties of the obtained extracts (TPC, TFC, and AA) were statistically evaluated (<italic>p</italic> &#x3c; 0.05) by two-way analysis of variance (ANOVA) using OriginPro 8.5.2 software and Tukey test for differences of means. Similarly, the variation in wetting properties (contact angle) was also statistically evaluated through two-way ANOVA and the Tukey test. Regarding the comparison of physical&#x2013;mechanical properties and surface free energy of particleboards, statistical analysis was performed by one-way analysis of variance (ANOVA) at <italic>p</italic> &#x3c; 0.05 using OriginPro 8.5.2 software.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Characterization of raw materials</title>
<p>Grape stalk (GS) and vine strain (VS) particles were characterized using FTIR analysis, and the obtained spectra are presented in <xref ref-type="fig" rid="F1">Figure 1</xref>. Due to the lignocellulosic nature of GS and VS, cellulose, hemicellulose, and lignin are the main components (c.a. 70%&#x2013;90%), and for that reason, the normalization of the intensity values of both FTIR spectra was done using the band of the C&#x2212;O, C&#x2212;C, and C&#x2212;C&#x2212;O stretch vibration at 1028 &#xb1; 5&#xa0;cm<sup>&#x2212;1</sup>.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>FTIR spectra of grape stalks (GS) and vine strains (VS). Highlighted zones refer to relevant bands of both materials.</p>
</caption>
<graphic xlink:href="frfst-04-1376415-g001.tif"/>
</fig>
<p>As observed, GS and VS exhibit similar absorption spectra (<xref ref-type="fig" rid="F1">Figure 1</xref>). The broad band at c.a. 3,400&#xa0;cm<sup>&#x2212;1</sup> is attributed to &#x2212;OH stretching (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B30">Prozil et al., 2014</xref>; <xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). At c.a. 2,935&#xa0;cm<sup>&#x2212;1</sup> and 2,873&#xa0;cm<sup>&#x2212;1</sup> is identified two sharp peaks associated with the asymmetric and symmetric stretch of &#x2212;CH<sub>2</sub>, respectively (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B30">Prozil et al., 2014</xref>; <xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). An increase in the intensity of both peaks in the case of GS particles was observed, which indicates a high content of waxes and oils (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B30">Prozil et al., 2014</xref>; <xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>). Additionally, the region attributed to the presence of polyphenols (from 1300&#xa0;cm<sup>&#x2212;1</sup> to 1800&#xa0;cm<sup>&#x2212;1</sup>) is also enhanced in the case of GS particles (<xref ref-type="fig" rid="F1">Figure 1</xref>), corroborating its high potential for the recovery of phenolic compounds (<xref ref-type="bibr" rid="B45">Troilo et al., 2021</xref>; <xref ref-type="bibr" rid="B20">Jesus et al., 2022</xref>; <xref ref-type="bibr" rid="B35">Rodrigues et al., 2023</xref>).</p>
</sec>
<sec id="s3-2">
<title>3.2 Characterization of extracts</title>
<p>The recovery of polyphenolic compounds from grape stalks is a widely studied topic, due to the significant amount of lignin and tannins in its composition (<xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B30">Prozil et al., 2014</xref>; <xref ref-type="bibr" rid="B34">Rodrigues et al., 2022</xref>). Additionally, alkaline extraction is a well-known method for phenolics and lignin isolation from lignocellulosic biomass, with several operational advantages, such as low toxicity, safety, and interesting yield (<xref ref-type="bibr" rid="B9">Cavali et al., 2020</xref>; <xref ref-type="bibr" rid="B27">Oriez et al., 2020</xref>; <xref ref-type="bibr" rid="B13">Deniz, 2023</xref>). Grape stalk particles were used for alkaline extraction to obtain a phenolic-rich liquid extract showing potential as an adhesive. In order to optimize the process, two extractive agents were studied, namely, sodium hydroxide (NaOH) and sodium carbonate (Na<sub>2</sub>CO<sub>3</sub>). Moreover, the impact of the concentration of both agents was also evaluated, using aqueous solutions with 0.1%, 0.5%, and 1.0% w/v. Distilled water was also used as the extractive agent for comparison purposes. For each experiment that was determined, the extraction efficiency (EE) and the final extracts were chemically characterized in terms of total phenolic content (TPC), total flavonoid content (TFC), and antioxidant activity (AA), and the results are presented in <xref ref-type="table" rid="T2">Table 2</xref>.</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Extraction efficiency (EE), total phenolic content (TPC), total flavonoid content (TFC), and antioxidant activity (AA) of the obtained extracts.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Extraction</th>
<th align="left">Extraction efficiency, EE (%)</th>
<th align="left">Total phenolic content, TPC (mg GAE/100&#xa0;g dry sample)</th>
<th align="left">Total flavonoid content, TFC (mg CE/100&#xa0;g dry sample)</th>
<th align="left">Antioxidant activity, AA (% inhibition)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">EXT0</td>
<td align="left">2.13 &#xb1; 0.04<sup>a</sup>
</td>
<td align="left">1.3 &#xb1; 0.3<sup>a</sup>
</td>
<td align="left">81.2 &#xb1; 1.3<sup>a</sup>
</td>
<td align="left">17.5 &#xb1; 1.2<sup>a</sup>
</td>
</tr>
<tr>
<td align="left">EXT1</td>
<td align="left">2.44 &#xb1; 0.08<sup>b</sup>
</td>
<td align="left">74.3 &#xb1; 0.1<sup>b</sup>
</td>
<td align="left">171.8 &#xb1; 1.4<sup>b</sup>
</td>
<td align="left">40.4 &#xb1; 0.9<sup>b</sup>
</td>
</tr>
<tr>
<td align="left">EXT2</td>
<td align="left">5.76 &#xb1; 0.12<sup>c</sup>
</td>
<td align="left">996.4 &#xb1; 8.2<sup>c</sup>
</td>
<td align="left">624.6 &#xb1; 4.8<sup>c</sup>
</td>
<td align="left">60.3 &#xb1; 0.3<sup>c</sup>
</td>
</tr>
<tr>
<td align="left">EXT3</td>
<td align="left">8.92 &#xb1; 0.19<sup>d</sup>
</td>
<td align="left">1,406.2 &#xb1; 19.1<sup>d</sup>
</td>
<td align="left">1,218.3 &#xb1; 2.5<sup>d</sup>
</td>
<td align="left">99.8 &#xb1; 1.6<sup>d</sup>
</td>
</tr>
<tr>
<td align="left">EXT4</td>
<td align="left">3.02 &#xb1; 0.02<sup>e</sup>
</td>
<td align="left">52.6 &#xb1; 0.5<sup>e</sup>
</td>
<td align="left">96.5 &#xb1; 3.8<sup>e</sup>
</td>
<td align="left">47.4 &#xb1; 0.7<sup>e</sup>
</td>
</tr>
<tr>
<td align="left">EXT5</td>
<td align="left">4.59 &#xb1; 0.09<sup>f</sup>
</td>
<td align="left">227.9 &#xb1; 6.8<sup>f</sup>
</td>
<td align="left">309.4 &#xb1; 2.7<sup>f</sup>
</td>
<td align="left">31.3 &#xb1; 0.4<sup>f</sup>
</td>
</tr>
<tr>
<td align="left">EXT6</td>
<td align="left">6.28 &#xb1; 0.10<sup>g</sup>
</td>
<td align="left">538.8 &#xb1; 9.2<sup>g</sup>
</td>
<td align="left">624.1 &#xb1; 6.3<sup>g</sup>
</td>
<td align="left">27.8 &#xb1; 1.5<sup>g</sup>
</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>Note: Data are presented as mean &#xb1; SD (n &#x3d; 3). Values in the same column superscripted by different letters are significantly different at <italic>p</italic> &#x3c; 0.05. GAE, gallic acid equivalent; CE, catechin equivalent.</p>
</fn>
</table-wrap-foot>
</table-wrap>
<p>As it can be observed, the extractive agent had a significative effect (<italic>p</italic> &#x3c; 0.05) on the EE of the process (<xref ref-type="table" rid="T2">Table 2</xref>). The use of NaOH or Na<sub>2</sub>CO<sub>3</sub> as extraction agents allowed improving the efficiency in comparison with water alone, increasing from 2.13% (EXT0, <xref ref-type="table" rid="T2">Table 2</xref>) to 2.44% and 3.02% of EE, respectively (EXT1 and EXT4, <xref ref-type="table" rid="T2">Table 2</xref>). However, a sharp variation was noticed in the chemical properties of the extracts. The use of NaOH (EXT1, <xref ref-type="table" rid="T2">Table 2</xref>) and Na<sub>2</sub>CO<sub>3</sub> (EXT4, <xref ref-type="table" rid="T2">Table 2</xref>) as extraction agents allowed obtaining extracts with a higher content of phenols and flavonoids than the extract obtained using water (EXT0, <xref ref-type="table" rid="T2">Table 2</xref>). Furthermore, the antioxidant capacity of the extracts was also significantly increased (<italic>p</italic> &#x3c; 0.05) with the change in the extraction agent, from c.a. 18% (EXT0, <xref ref-type="table" rid="T2">Table 2</xref>) to more than 40% (EXT1 and EXT4, <xref ref-type="table" rid="T2">Table 2</xref>). According to the literature, several phenolic compounds present in lignocellulosic biomass, as grape stalks, are highly soluble under alkaline conditions, which allow their isolation and recovery (<xref ref-type="bibr" rid="B9">Cavali et al., 2020</xref>; <xref ref-type="bibr" rid="B27">Oriez et al., 2020</xref>). Therefore, the use of aqueous solutions of weak and strong basis, such as Na<sub>2</sub>CO<sub>3</sub> and NaOH, as a solvent in the extraction process allow to obtain highly rich mixtures of polyphenols, such as tannins, flavan-3-ols, hydroxycinnamic acids, monomeric and oligomeric flavonols, and stilbenes (<xref ref-type="bibr" rid="B9">Cavali et al., 2020</xref>; <xref ref-type="bibr" rid="B27">Oriez et al., 2020</xref>; <xref ref-type="bibr" rid="B45">Troilo et al., 2021</xref>).</p>
<p>By tuning the concentration of extractive agents, it was possible to significantly improve (<italic>p</italic> &#x3c; 0.05) the extraction efficiency. With 0.5% and 1.0% of NaOH, EE was improved to 5.76% (EXT2, <xref ref-type="table" rid="T2">Table 2</xref>) and 8.92% (EXT3, <xref ref-type="table" rid="T2">Table 2</xref>), respectively. In the case of Na<sub>2</sub>CO<sub>3</sub>, efficiency was 1.5 and 2 times higher with 0.5% (EXT5, <xref ref-type="table" rid="T2">Table 2</xref>) and 1.0% (EXT6, <xref ref-type="table" rid="T2">Table 2</xref>), respectively, when compared to the result obtained with Na<sub>2</sub>CO<sub>3</sub> 0.1% (EXT4, <xref ref-type="table" rid="T2">Table 2</xref>). In terms of chemical composition, both phenolic and flavonoid contents follow the same tendency, with a great increase in NaOH or Na<sub>2</sub>CO<sub>3</sub> concentrations (<xref ref-type="table" rid="T2">Table 2</xref>). On the other hand, the variation in the antioxidant capacity of the extracts presents a quite different behavior depending on the extractive agent used. In the case of extractions with NaOH, increasing the concentration improves the extraction of phenolic compounds and flavonoids, which led to an increase in the AA of the extracts (EXT1-EXT3, <xref ref-type="table" rid="T2">Table 2</xref>). However, in the case of Na<sub>2</sub>CO<sub>3</sub>, the antioxidant potential decreased with the increase in the phenol derivatives and flavonoid content (EXT4-6, <xref ref-type="table" rid="T2">Table 2</xref>), which may indicate an antagonist effect between the extracted polyphenols. According to the literature, when two or more antioxidant compounds are present in the extract, an antagonist effect may occur, hindering the total antioxidant activity of the extract (<xref ref-type="bibr" rid="B23">Meyer et al., 1998</xref>; <xref ref-type="bibr" rid="B28">Pinelo et al., 2004</xref>; <xref ref-type="bibr" rid="B19">Hajimehdipoor et al., 2014</xref>; <xref ref-type="bibr" rid="B43">Skroza et al., 2022</xref>; <xref ref-type="bibr" rid="B46">Uduwana et al., 2023</xref>). This effect may be caused by chemical interactions between phenolic compounds, which can produce weaker antioxidant species, forming complexes and adducts, promote polymerization reactions, and neutralize oxidant radicals (<xref ref-type="bibr" rid="B23">Meyer et al., 1998</xref>; <xref ref-type="bibr" rid="B28">Pinelo et al., 2004</xref>; <xref ref-type="bibr" rid="B19">Hajimehdipoor et al., 2014</xref>; <xref ref-type="bibr" rid="B43">Skroza et al., 2022</xref>; <xref ref-type="bibr" rid="B46">Uduwana et al., 2023</xref>). For example, <xref ref-type="bibr" rid="B23">Meyer et al. (1998)</xref> proved the antagonist effect on antioxidant activity of catechin when combined with quercetin, cyanidin, and caffeic and ellagic acids, due to the chemical interaction between their functional groups and, consequently, to the reduced availability of hydroxyl groups for oxidation (<xref ref-type="bibr" rid="B23">Meyer et al., 1998</xref>). Furthermore, <xref ref-type="bibr" rid="B46">Uduwana et al. (2023)</xref> observed the same effect by combining green tea with bee honey and <italic>Citrus limonum</italic> extracts (<xref ref-type="bibr" rid="B46">Uduwana et al., 2023</xref>). <xref ref-type="bibr" rid="B19">Hajimehdipoor et al. (2014)</xref> concluded that ternary combinations of quercetin, rosmarinic acid, rutin, gallic acid, and caffeic acid also exhibit antagonist effect regarding antioxidant activity (<xref ref-type="bibr" rid="B19">Hajimehdipoor et al., 2014</xref>).</p>
<p>The impact of extraction agents (water, NaOH, and Na<sub>2</sub>CO<sub>3</sub>) on the chemical composition of the extracts (EXT0, EXT3, and EXT6) was evaluated by FTIR-ATR, and the obtained spectra are presented in <xref ref-type="fig" rid="F2">Figure 2A</xref>. The normalization of the intensity values was done using the band of the aromatic skeletal vibration at (1600 &#xb1; 5) cm<sup>&#x2212;1</sup>.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>
<bold>(A)</bold> FTIR spectra of EXT0, EXT3, and EXT6 and <bold>(B)</bold> a magnification of the region from 600 to 1800&#xa0;cm<sup>&#x2212;1</sup>. Highlighted zones refer to bands/peaks characteristic of the produced extracts.</p>
</caption>
<graphic xlink:href="frfst-04-1376415-g002.tif"/>
</fig>
<p>As expected, grape stalk extracts are rich in flavonoids and stilbenes (<xref ref-type="bibr" rid="B1">Anastasiadi et al., 2012</xref>), and regardless of the extraction conditions used, all extracts showed the presence of the pattern bands due to the presence of these polyphenolic compounds (<xref ref-type="fig" rid="F2">Figure 2A</xref>). However, the intensity of these bands is low in the spectrum of the extract obtained using only water as an extraction agent (EXT0). This confirms the results obtained for the characterization of phenolic and flavonoid content (<xref ref-type="table" rid="T2">Table 2</xref>). The low amount of extractable polyphenolic compounds in the extract obtained only with water is due to the fact that most of the water-extractable compounds were previously extracted in the winemaking process.</p>
<p>Regarding the extracts obtained using alkaline extraction agents (NaOH and Na<sub>2</sub>CO<sub>3</sub>), it was interesting to see that the alkaline agent used impacted the compounds present in the extracts. The spectra of the extract obtained with NaOH (EXT3, <xref ref-type="fig" rid="F2">Figure 2B</xref>) show higher amount of stilbenes in the extract due to the intensity on its characteristics bands: a double peak at c.a. 1600&#xa0;cm<sup>&#x2212;1</sup> and c.a. 1568&#xa0;cm<sup>&#x2212;1</sup>, corresponding to C&#x2212;C aromatic double bond stretching and C&#x2212;C oleophilic stretching, peaks at c.a. 1516&#xa0;cm<sup>&#x2212;1</sup> and c.a. 1463&#xa0;cm<sup>&#x2212;1</sup> due to benzene skeleton vibrations, at c.a. 987&#xa0;cm<sup>&#x2212;1</sup> and c.a. 956&#xa0;cm<sup>&#x2212;1</sup> due to the bending vibration of C&#x3d;C&#x2212;H (<xref ref-type="bibr" rid="B33">Ricci et al., 2015</xref>; <xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>; <xref ref-type="bibr" rid="B37">Santos et al., 2022b</xref>).</p>
<p>Furthermore, the spectrum of the extract obtained with Na<sub>2</sub>CO<sub>3</sub> (EXT 6) shows a high proportion of tannins in the extract, based on the intensity of the bands at 1334 cm<sup>&#x2212;1</sup>, 338&#xa0;cm<sup>&#x2212;1</sup>, and 1283&#xa0;cm<sup>&#x2212;1</sup> due to the C&#x2212;O&#x2212;H of primary and tertiary alcohol bending vibrations; 1235&#xa0;cm<sup>&#x2212;1</sup> of cyclic ether C&#x2212;O&#x2212;C stretching vibration; 1028&#xa0;cm<sup>&#x2212;1</sup> of aromatic cycle bending in a plane vibration, characteristic of the presence of condensed tannins, and the bands at 1728&#xa0;cm<sup>&#x2212;1</sup> due to the vibrations of the C&#x3d;O groups (<xref ref-type="bibr" rid="B31">Pujol et al., 2013</xref>; <xref ref-type="bibr" rid="B39">Santos et al., 2022a</xref>; <xref ref-type="bibr" rid="B37">Santos et al., 2022b</xref>; <xref ref-type="bibr" rid="B7">&#x10c;abalov&#xe1; et al., 2023</xref>), at 1240&#xa0;cm<sup>&#x2212;1</sup> due to the stretching vibration of the C&#x2013;O groups; and at 865&#xa0;cm<sup>&#x2212;1</sup>, due to the aromatic C&#x2013;H out-of-plane bending vibrations, characteristic of the presence of hydrolyzable tannins (<xref ref-type="bibr" rid="B18">Grasel et al., 2016</xref>).</p>
<p>The bonding properties of all extracts were evaluated through ABES. Therefore, the extracts were previously concentrated through a rotary evaporator until reached a solid content of 15%. <xref ref-type="fig" rid="F3">Figure 3</xref> presents the shear strength of each extract after hot-pressing at 120&#xb0;C and different press times.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>ABES shear strength of all extracts after hot-pressing at different pressing times (10, 30, 60, 120, and 180&#xa0;s) and 120&#xb0;C.</p>
</caption>
<graphic xlink:href="frfst-04-1376415-g003.tif"/>
</fig>
<p>All extracts proved to have adhesive properties, reaching a shear strength over 1.0&#xa0;MPa after 60&#xa0;s of pressing time at 120&#xa0;&#xb0;C (<xref ref-type="fig" rid="F3">Figure 3</xref>). However, significant differences were noted regarding the maximum of performance (<xref ref-type="fig" rid="F3">Figure 3</xref>). In the case of EXT0, the maximum of shear strength was 1.5&#xa0;MPa and was achieved only after 180&#xa0;s of pressing (<xref ref-type="fig" rid="F3">Figure 3</xref>). Using an extractive agent (NaOH or Na<sub>2</sub>CO<sub>3</sub>), the bonding capacity of extracts was significantly improved (<xref ref-type="fig" rid="F3">Figure 3</xref>). Regarding Na<sub>2</sub>CO<sub>3</sub> (EXT4-6, <xref ref-type="fig" rid="F3">Figure 3</xref>), the best bonding performance was registered after 120&#xa0;s (regardless of concentration), which means 33% less pressing time required to complete cure at 120&#xb0;C. Additionally, higher amounts of Na<sub>2</sub>CO<sub>3</sub> (0.5% and 1.0%) slightly increased the maxima of shear strength to 1.6 MPa and 1.7&#xa0;MPa (EXT5 and EXT6, respectively; <xref ref-type="fig" rid="F3">Figure 3</xref>). On the same way, NaOH extracts&#x2019; (EX1-3) also performed better than EXT0, not only by reducing the pressing time (in the case of EXT1) but also increasing the maximum of shear strength to values over 2.0&#xa0;MPa (EXT2 and EXT3, <xref ref-type="fig" rid="F3">Figure 3</xref>). These findings are closely related to the chemical composition of the extracts, particularly with the phenolic content. As it was previously discussed, hot water extraction has low efficiency to recover phenolics and flavonoids from grape stalks when compared to alkaline extraction agents (<xref ref-type="table" rid="T2">Table 2</xref>). In the literature, it is referred that the liquid extraction of lignocellulosic biomass, as grape stalk, generates a mixture of long- and short-chain polymers that can be successfully used as bio-adhesives in several industries (<xref ref-type="bibr" rid="B25">Muranaka et al., 2017</xref>; <xref ref-type="bibr" rid="B14">Ferreira-Santos et al., 2020</xref>; <xref ref-type="bibr" rid="B44">Sun et al., 2022</xref>; <xref ref-type="bibr" rid="B51">Zhang et al., 2022</xref>; <xref ref-type="bibr" rid="B22">Li et al., 2023</xref>; <xref ref-type="bibr" rid="B42">&#x160;ernek and &#x17d;igon, 2023</xref>). The bonding potential is commonly associated with the presence of phenolic compounds, and a high amount of polyphenols usually results in an enhanced bonding capacity of the extracts (<xref ref-type="bibr" rid="B16">Friedman and J&#xfc;rgens, 2000</xref>; <xref ref-type="bibr" rid="B5">Benito-Gonz&#xe1;lez et al., 2020</xref>; <xref ref-type="bibr" rid="B27">Oriez et al., 2020</xref>; <xref ref-type="bibr" rid="B45">Troilo et al., 2021</xref>; <xref ref-type="bibr" rid="B35">Rodrigues et al., 2023</xref>). Therefore, NaOH extracts (EXT1-3; <xref ref-type="fig" rid="F3">Figure 3</xref>) exhibit improved adhesive properties when compared to Na<sub>2</sub>CO<sub>3</sub> (EXT4-6, <xref ref-type="fig" rid="F3">Figure 3</xref>) and water (EXT0, <xref ref-type="fig" rid="F3">Figure 3</xref>) extracts possibly due to the higher TPC and TFC (<xref ref-type="table" rid="T2">Table 2</xref>).</p>
</sec>
<sec id="s3-3">
<title>3.3 Particleboard performance</title>
<p>The use of grape stalk as raw material for the production of bio-adhesives to apply in the particleboard industry was evaluated. In this way, EXT3, the best performing extract in terms of bonding capacity, was selected as adhesive, and two types of particles were used as lignocellulosic matrix, namely, grape stalk and vine strains. The objective was to evaluate a circular economy concept, with grape stalks being used for both applications (adhesive production and fiber) and also to study the effect of using other types of winery residue (vine strains) to improve physical&#x2013;mechanical properties of the composite panels. Vine strains have a high content of cellulose (<xref ref-type="bibr" rid="B5">Benito-Gonz&#xe1;lez et al., 2020</xref>; <xref ref-type="bibr" rid="B41">Senila et al., 2020</xref>; <xref ref-type="bibr" rid="B20">Jesus et al., 2022</xref>), which provides to this by-product increased resistance against tension forces when compared to grape stalk. In this way, EXT3 was previously concentrated to reach a solid content of 20% before producing the panels. The composite panels were hot-pressed at 160&#xa0;&#xb0;C for 10&#xa0;min at a fixed thickness of 8&#xa0;mm, with 10&#xa0;wt% of adhesive. <xref ref-type="fig" rid="F4">Figure 4</xref> presents the obtained composite panels, using grape stalk (GS_P, <xref ref-type="fig" rid="F4">Figure 4A</xref>) and vine strain (VS_P, <xref ref-type="fig" rid="F4">Figure 4B</xref>) particles.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Samples of the composite panels produced using <bold>(A)</bold> grape stalk particles (GS_P) and <bold>(B)</bold> vine strains particles (VS_P) as the matrix and EXT3 as bio-adhesive.</p>
</caption>
<graphic xlink:href="frfst-04-1376415-g004.tif"/>
</fig>
<p>Physical&#x2013;mechanical performance of both materials was evaluated in terms of density (D), moisture content (MC), internal bond strength (IB), bending strength (IB), and thickness swelling (TS), and the results 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>Density (D), moisture content (MC), internal bond strength (IB), bending strength (BS), and thickness swelling (TS) of the composite panels produced using EXT3 as adhesive and grape stalks (GS) and vine strain (VS) particles.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Material</th>
<th align="left">Thickness (mm)</th>
<th align="left">D (kg m<sup>-3</sup>)</th>
<th align="left">MC (%)</th>
<th align="left">IB (MPa)</th>
<th align="left">BS (MPa)</th>
<th align="left">TS (%)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">GS_P</td>
<td align="left">8.0 &#xb1; 0.1<sup>a</sup>
</td>
<td align="left">875 &#xb1; 77<sup>a</sup>
</td>
<td align="left">4.3 &#xb1; 0.3<sup>a</sup>
</td>
<td align="left">0.25 &#xb1; 0.03<sup>a</sup>
</td>
<td align="left">2.2 &#xb1; 0.6<sup>a</sup>
</td>
<td align="left">45.1 &#xb1; 4.5<sup>a</sup>
</td>
</tr>
<tr>
<td align="left">VS_P</td>
<td align="left">8.0 &#xb1; 0.2<sup>a</sup>
</td>
<td align="left">833 &#xb1; 27<sup>a</sup>
</td>
<td align="left">4.6 &#xb1; 0.7<sup>a</sup>
</td>
<td align="left">0.66 &#xb1; 0.06<sup>b</sup>
</td>
<td align="left">4.0 &#xb1; 0.9<sup>b</sup>
</td>
<td align="left">116.0 &#xb1; 6.5<sup>b</sup>
</td>
</tr>
<tr>
<td align="left">Type P1<xref ref-type="table-fn" rid="Tfn1">
<sup>c</sup>
</xref>
</td>
<td align="left">&#x3e;6 to 13</td>
<td align="left">n.r.</td>
<td align="left">n.r.</td>
<td align="left">0.28</td>
<td align="left">12.5</td>
<td align="left">n.r.</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>Note: Data are presented as mean &#xb1; SD (n &#x3d; 3). Values in the same column superscripted by different letters are significantly different at <italic>p</italic> &#x3c; 0.05.</p>
</fn>
<fn id="Tfn1">
<label>
<sup>c</sup>
</label>
<p>According to standard EN, 312 for particleboards with thickness range of 6&#x2013;13&#xa0;mm; n.r., no requirement.</p>
</fn>
</table-wrap-foot>
</table-wrap>
<p>As expected, both composite materials present similar (<italic>p</italic> &#x3c; 0.05) thickness and density (c.a. 8.5&#xa0;mm and 850&#xa0;kg&#xa0;m<sup>&#x2212;3</sup>, <xref ref-type="table" rid="T3">Table 3</xref>). Moreover, the moisture content was also very close in both cases (<italic>p</italic> &#x3c; 0.05), with values between 4% and 5% (<xref ref-type="table" rid="T3">Table 3</xref>). Nevertheless, mechanical properties are substantially different, depending on the type of particles used. In the case of GS_P, IB was 0.25&#xa0;MPa and BS was 2.2&#xa0;MPa (<xref ref-type="table" rid="T3">Table 3</xref>). Using VS particles, the mechanical properties were significantly improved (<italic>p</italic> &#x3c; 0.05), with an IB of 0.66&#xa0;MPa and BS of 4.0&#xa0;MPa (<xref ref-type="table" rid="T3">Table 3</xref>). As previously mentioned, vine strains have a higher content of cellulose than grape stalk, providing it higher resistance. Additionally, the mixture of grape stalk particles has a lower fraction of material with a size between 1 and 2&#xa0;mm than the vine strain mixture, once that GS particles are less dense, and for that reason, the grinding process generates a higher amount of small particles (between 500&#xa0;&#x3bc;m and 1&#xa0;mm), which may negatively affect mechanical properties. Although BS is significantly lower regarding to the requirements of type P1 particleboards according to EN 312 (<xref ref-type="table" rid="T3">Table 3</xref>), the value of IB was 2.3 times higher (<xref ref-type="table" rid="T3">Table 3</xref>), which proves the potential application of VS_P. Regarding TS, the results showed that GS_P has much higher resistance to swelling than VS_P (<xref ref-type="table" rid="T3">Table 3</xref>), which can be attributed to the higher oleophilic characteristic of GS particles, as already proved by FTIR analyses (<xref ref-type="fig" rid="F1">Figure 1</xref>), providing the composite material a lower tendency to absorb water and, consequently, to swell. Additionally, the lower content of cellulose in grape stalk particles (when compared to vine strains particles) also promotes the hydrophobic characteristic of GS_P, contributing to a lower TS (<xref ref-type="bibr" rid="B29">Prozil et al., 2012</xref>; <xref ref-type="bibr" rid="B5">Benito-Gonz&#xe1;lez et al., 2020</xref>; <xref ref-type="bibr" rid="B41">Senila et al., 2020</xref>).</p>
<p>Taking into account the packaging purpose of these composite materials, both panels were characterized in terms of wettability, and the results are presented in <xref ref-type="table" rid="T4">Table 4</xref>.</p>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Contact angle (using water and diiodomethane) and surface free energy of grape stalk (GS_P) and vine strain (VS_P) composite panels.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="left">Material</th>
<th colspan="2" align="left">Contact angle (&#xb0;)</th>
<th rowspan="2" align="left">Surface free energy (mJ m<sup>-2</sup>)</th>
</tr>
<tr>
<th align="left">Water</th>
<th align="left">Diiodomethane</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">GS_P</td>
<td align="left">52.16 &#xb1; 7.94<sup>a</sup>
</td>
<td align="left">70.33 &#xb1; 0.51<sup>a</sup>
</td>
<td align="left">48.80 &#xb1; 5.99<sup>a</sup>
</td>
</tr>
<tr>
<td align="left">VS_P</td>
<td align="left">51.79 &#xb1; 14.31<sup>a</sup>
</td>
<td align="left">56.12 &#xb1; 0.10<sup>b</sup>
</td>
<td align="left">52.16 &#xb1; 9.31<sup>a</sup>
</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>Note: Data are presented as mean &#xb1; SD (n &#x3d; 3). Values in the same column superscripted by different letters are significantly different at <italic>p</italic> &#x3c; 0.05.</p>
</fn>
</table-wrap-foot>
</table-wrap>
<p>The contact angles were very similar (<italic>p</italic> &#x3c; 0.05) when water was used as test liquid (c.a. 50&#xb0;, <xref ref-type="table" rid="T4">Table 4</xref>), revealing an equivalent hydrophilicity of the surface of both composite materials. However, when diiodomethane was used (<xref ref-type="table" rid="T4">Table 4</xref>), GS_P registered a higher contact angle (c.a. 70&#xb0;, <xref ref-type="table" rid="T4">Table 4</xref>) than VS_P (c.a. 56&#xb0;, <xref ref-type="table" rid="T4">Table 4</xref>), which may indicate a lower tendency to the penetration of oils and fats (<xref ref-type="bibr" rid="B8">Candan et al., 2012</xref>; <xref ref-type="bibr" rid="B48">Wang et al., 2017</xref>; <xref ref-type="bibr" rid="B11">Danish et al., 2019</xref>). Although surface free energy seems to corroborate this tendency, with VS_P reaching the highest value (c.a. 52&#xa0;mJ&#xa0;m<sup>&#x2212;2</sup>, <xref ref-type="table" rid="T4">Table 4</xref>), the difference was not statistically significant (<italic>p</italic> &#x3c; 0.05). In this way, GS_P seems to be a valuable alternative to consider in packaging solutions, not only due to the 100% bio-character but also to its mechanical and wettability properties that provide resistance to mechanical stress caused by handling and transportation and also reduce chemical migration of compounds from package to food.</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>Grape stalk extracts were successfully applied as raw material for the production of a bio-adhesive. Two different extractive agents were evaluated, namely, NaOH and Na<sub>2</sub>CO<sub>3</sub>, as well as the effect of its concentration on the extraction efficiency. The extracts were characterized in terms of composition (total phenolic and flavonoid contents, antioxidant activity, and FTIR) and bonding capacity (ABES).</p>
<p>The extraction efficiency was improved using NaOH as the extractive agent, when compared to water and Na<sub>2</sub>CO<sub>3</sub>, with noticeable differences in the chemical composition of the respective extracts. According to FTIR analysis, NaOH was more efficient in the recovery of stilbenes, while the extracts obtained using Na<sub>2</sub>CO<sub>3</sub> exhibit a higher fraction of tannins. Moreover, increasing the concentration of the extractive agents promoted an effective increase in the solubilization of polyphenols, as phenolics and flavonoids, and consequently, improved the efficiency of the process. Regarding adhesive properties, NaOH extracts also exhibit improved capacity by pressing at 120&#xb0;C.</p>
<p>A composite material, 100% derived from waste from the wine industry, was developed by mixing the best performing extract with vine strains/grape stalk particles. The physical&#x2013;mechanical performance of the composite panels was deeply influenced by the type of lignocellulosic particles chosen. Vine strain particles allowed to develop a composite material with enhanced resistance in terms of mechanical properties (internal bon and bending strength) when compared to the composite material produced using grape stalk particles. However, the use of grape stalk particles allowed obtaining a lower thickness swelling, which can be related to its higher content of waxes. Additionally, wettability properties demonstrate a lower tendency of grape stalk panel to be penetrated by oils and fats, which has a great relevance in terms of chemical contamination between food and package.</p>
<p>Considering food packaging applications, composite materials obtained from winery residues may be a valuable alternative to explore in order to increase the sustainable characteristic of this industry, without compromising resistance, functionality, and quality.</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="s10">Supplementary Material</xref>; further inquiries can be directed to the corresponding authors.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>RF: conceptualization, investigation, methodology, and writing&#x2013;original draft. SL: methodology and writing&#x2013;original draft. NF: methodology and writing&#x2013;original draft. JS: conceptualization, formal analysis, and writing&#x2013;review and editing. JM: conceptualization, project administration, and writing&#x2013;review and editing. LC: conceptualization, formal analysis, project administration, and writing&#x2013;review and editing.</p>
</sec>
<sec sec-type="funding-information" id="s7">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research, authorship, and/or publication of this article. The authors gratefully acknowledge the funding by: LEPABE, UIDB/00511/2020 (DOI: 10.54499/UIDB/00511/2020) and UIDP/00511/2020 (DOI: 10.54499/UIDP/00511/2020), ALiCE, LA/P/0045/2020 (DOI: 10.54499/LA/P/0045/2020), supported by national funds through FCT/MCTES (PIDDAC), and Project &#x201c;INOVC&#x2b;: Smart Innovation Ecosystem of Centro Region of Portugal&#x201d; (project number CENTRO-01-0246-FEDER-000044), partially supported by the FEDER (Fundo Europeu de Desenvolvimento Regional), through the Regional Operational Programme of Centre (CENTRO 2020) of the Portugal 2020 Partnership Agreement.</p>
</sec>
<ack>
<p>The authors acknowledge Quinta da Alameda (Nelas, Portugal) and MOVECHO Company (Nelas, Portugal) for providing raw materials and technical support.</p>
</ack>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s9">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors, and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
<sec id="s10">
<title>Supplementary material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/frfst.2024.1376415/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/frfst.2024.1376415/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="Table1.pdf" id="SM1" mimetype="application/pdf" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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