<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.2 20190208//EN" "http://jats.nlm.nih.gov/publishing/1.2/JATS-journalpublishing1.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" article-type="review-article" dtd-version="1.2" xml:lang="en">
    <front>
        <journal-meta>
            <journal-id journal-id-type="pmc">F1000Research</journal-id>
            <journal-title-group>
                <journal-title>F1000Research</journal-title>
            </journal-title-group>
            <issn pub-type="epub">2046-1402</issn>
            <publisher>
                <publisher-name>F1000 Research Limited</publisher-name>
                <publisher-loc>London, UK</publisher-loc>
            </publisher>
        </journal-meta>
        <article-meta>
            <article-id pub-id-type="doi">10.12688/f1000research.140748.1</article-id>
            <article-categories>
                <subj-group subj-group-type="heading">
                    <subject>Review</subject>
                </subj-group>
                <subj-group>
                    <subject>Articles</subject>
                </subj-group>
            </article-categories>
            <title-group>
                <article-title>Effect of extrusion cooking on the chemical and nutritional properties of instant flours: a review</article-title>
                <fn-group content-type="pub-status">
                    <fn>
                        <p>[version 1; peer review: 1 approved, 1 approved with reservations]</p>
                    </fn>
                </fn-group>
            </title-group>
            <contrib-group>
                <contrib contrib-type="author" corresp="yes">
                    <name>
                        <surname>Pismag</surname>
                        <given-names>Remigio Yamid</given-names>
                    </name>
                    <role content-type="http://credit.niso.org/">Conceptualization</role>
                    <role content-type="http://credit.niso.org/">Formal Analysis</role>
                    <role content-type="http://credit.niso.org/">Investigation</role>
                    <role content-type="http://credit.niso.org/">Methodology</role>
                    <role content-type="http://credit.niso.org/">Writing &#x2013; Original Draft Preparation</role>
                    <role content-type="http://credit.niso.org/">Writing &#x2013; Review &amp; Editing</role>
                    <uri content-type="orcid">https://orcid.org/0000-0002-7878-3733</uri>
                    <xref ref-type="corresp" rid="c1">a</xref>
                    <xref ref-type="aff" rid="a1">1</xref>
                </contrib>
                <contrib contrib-type="author" corresp="no">
                    <name>
                        <surname>Polo</surname>
                        <given-names>Mar&#x00ed;a Paula</given-names>
                    </name>
                    <role content-type="http://credit.niso.org/">Investigation</role>
                    <role content-type="http://credit.niso.org/">Writing &#x2013; Original Draft Preparation</role>
                    <xref ref-type="aff" rid="a1">1</xref>
                </contrib>
                <contrib contrib-type="author" corresp="no">
                    <name>
                        <surname>Hoyos</surname>
                        <given-names>Jos&#x00e9; Luis</given-names>
                    </name>
                    <role content-type="http://credit.niso.org/">Conceptualization</role>
                    <role content-type="http://credit.niso.org/">Formal Analysis</role>
                    <role content-type="http://credit.niso.org/">Methodology</role>
                    <role content-type="http://credit.niso.org/">Validation</role>
                    <xref ref-type="aff" rid="a1">1</xref>
                </contrib>
                <contrib contrib-type="author" corresp="no">
                    <name>
                        <surname>Bravo</surname>
                        <given-names>Jes&#x00fa;s Eduardo</given-names>
                    </name>
                    <role content-type="http://credit.niso.org/">Funding Acquisition</role>
                    <role content-type="http://credit.niso.org/">Resources</role>
                    <uri content-type="orcid">https://orcid.org/0000-0001-6462-3512</uri>
                    <xref ref-type="aff" rid="a1">1</xref>
                </contrib>
                <contrib contrib-type="author" corresp="no">
                    <name>
                        <surname>Roa</surname>
                        <given-names>Diego Fernando</given-names>
                    </name>
                    <role content-type="http://credit.niso.org/">Formal Analysis</role>
                    <role content-type="http://credit.niso.org/">Methodology</role>
                    <role content-type="http://credit.niso.org/">Project Administration</role>
                    <role content-type="http://credit.niso.org/">Resources</role>
                    <role content-type="http://credit.niso.org/">Writing &#x2013; Review &amp; Editing</role>
                    <uri content-type="orcid">https://orcid.org/0000-0002-7198-9827</uri>
                    <xref ref-type="aff" rid="a1">1</xref>
                </contrib>
                <aff id="a1">
                    <label>1</label>Faculty of Agricultural Science, Universidad del Cauca, Comuna 1, Cauca, Colombia</aff>
            </contrib-group>
            <author-notes>
                <corresp id="c1">
                    <label>a</label>
                    <email xlink:href="mailto:yamid@unicauca.edu.co">yamid@unicauca.edu.co</email>
                </corresp>
                <fn fn-type="conflict">
                    <p>
                        <bold>Competing interests: </bold>SEGALCO S.A.S was part of the project as a validation center for the research results, however the authors declare that SEGALCO S.A.S does not have any commercial interest in this paper and there are no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper. No other competing interests were disclosed.</p>
                </fn>
            </author-notes>
            <pub-date pub-type="epub">
                <day>18</day>
                <month>10</month>
                <year>2023</year>
            </pub-date>
            <pub-date pub-type="collection">
                <year>2023</year>
            </pub-date>
            <volume>12</volume>
            <elocation-id>1356</elocation-id>
            <history>
                <date date-type="accepted">
                    <day>4</day>
                    <month>10</month>
                    <year>2023</year>
                </date>
            </history>
            <permissions>
                <copyright-statement>Copyright: &#x00a9; 2023 Pismag RY et al.</copyright-statement>
                <copyright-year>2023</copyright-year>
                <license xlink:href="https://creativecommons.org/licenses/by/4.0/">
                    <license-p>This is an open access article distributed under the terms of the Creative Commons Attribution Licence, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.</license-p>
                </license>
            </permissions>
            <self-uri content-type="pdf" xlink:href="https://f1000research.com/articles/12-1356/pdf"/>
            <abstract>
                <p>Satisfying the nutritional requirements of consumers has made food industries focus on the development of safe, innocuous, easy-to-prepare products with high nutritional quality through efficient processing technologies. Extrusion cooking has emerged as a prominent technology associated with the nutritional and functional attributes of food products. This review aims to establish a theoretical framework concerning the influence of extrusion parameters on the functional and nutritional properties of precooked or instant flours, both as end-products and ingredients. It highlights the pivotal role of process parameters within the extruder, including temperature, screw speed, and raw materials moisture content, among others, and elucidates their correlation with the modifications observed in the structural composition of these materials. Such modifications subsequently induce notable changes in the ultimate characteristics of the food product. Detailed insights into these transformations are provided within the subsequent sections, emphasizing their associations with critical phenomena such as nutrient availability, starch gelatinization, protein denaturation, enhanced 
                    <italic toggle="yes">in vitro</italic> digestibility, reduction in the content of antinutritional factors (ANFs), and the occurrence of Maillard reactions during specific processing stages. Drawing upon insights from available literature, it is concluded that these effects represent key attributes intertwined with the nutritional properties of the end-product during the production of instant flours.</p>
            </abstract>
            <kwd-group kwd-group-type="author">
                <kwd>precooking</kwd>
                <kwd>instant powders</kwd>
                <kwd>instant preparation</kwd>
                <kwd>instant consumption</kwd>
            </kwd-group>
            <funding-group>
                <award-group id="fund-1">
                    <funding-source>SGR BPIN</funding-source>
                    <award-id>2020000100052</award-id>
                </award-group>
                <funding-statement>This work has been fully financed by the Colombian General Reimbursement System. Executed in the Universidad del Cauca as center of technological development, and SEGALCO as a technological validation center, within the framework of the SGR BPIN 2020000100052 project.</funding-statement>
                <funding-statement>
                    <italic>The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.</italic>
                </funding-statement>
            </funding-group>
        </article-meta>
    </front>
    <body>
        <sec id="sec1" sec-type="intro">
            <title>Introduction</title>
            <p>The market for precooked flours has witnessed significant growth both in developed and developing countries, providing opportunities for industries engaged in offering these products (
                <xref ref-type="bibr" rid="ref5">Allied, 2020</xref>). Developing nations, particularly, seek viable alternatives that facilitate the processing of region-specific raw materials using cost-effective and highly efficient techniques. The aim is to enable the development of instant preparation foods that effectively cater to the nutritional needs of the population (
                <xref ref-type="bibr" rid="ref4">Ali, Singh, &amp; Sharma, 2016</xref>; 
                <xref ref-type="bibr" rid="ref39">Mouquet, Salvignol, Van Hoan, Monvois, &amp; Tr&#x00e8;che, 2003</xref>; 
                <xref ref-type="bibr" rid="ref47">Onyeoziri, Torres, Hamaker, Taylor, &amp; Kock, 2021</xref>; 
                <xref ref-type="bibr" rid="ref65">Sebio &amp; Chang, 2000</xref>). Currently, consumers are increasingly aware of their food consumption, and the ingredients employed in their formulation. The response of the food industry has been offering secure and nutritionally superior products while employing processing technologies that ensure efficiency and productivity (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.,</italic> 2017</xref>; 
                <xref ref-type="bibr" rid="ref62">Sandrin 
                    <italic toggle="yes">et al.,</italic> 2018</xref>). In this context, instant flours have gained prominence as indispensable products or ingredients that contribute to the development of foods with versatile nutritional, functional, and textural properties. Instant flours, often referred to as pregelatinized flours, undergo hydro-thermal modification processes to attain starch gelatinization in the raw materials (
                <xref ref-type="bibr" rid="ref65">Sebio &amp; Chang, 2000</xref>). Pregelatinized flours primarily are made of starch-rich raw materials, such as cereals, tubers, and selected fruits. However, it is vital to acknowledge that plant-based flours encompass additional constituents besides starch, including proteins, fibers, lipids, and bioactive compounds (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.,</italic> 2017</xref>; 
                <xref ref-type="bibr" rid="ref21">Espinosa 
                    <italic toggle="yes">et al.</italic>, 2021</xref>). Hence, the presence of these constituents must be considered during their processing, due to their influence on the physical, chemical, nutritional, and functional properties of the processed flours (
                <xref ref-type="bibr" rid="ref75">Transparency, 2019</xref>).</p>
        </sec>
        <sec id="sec2">
            <title>Extrusion parameters to produce instant flours</title>
            <p>Extrusion is a widely used technique in the creation of instant preparation foods such as beverages, porridges, infant foods, and desserts. Additionally, the raw materials employed in this process encompass a wide range, including cereal flours, legumes, fruits, tubers, and customized blends (see 
                <xref ref-type="table" rid="T1">Table 1</xref>). The common raw materials used for producing precooked flours are rice, wheat, and maize. They have priority due to their wide availability and ease of being processed on an industrial scale. (
                <xref ref-type="bibr" rid="ref75">Transparency, 2019</xref>). Extrusion induces starch modification through the process of gelatinization (
                <xref ref-type="bibr" rid="ref24">Heredia 
                    <italic toggle="yes">et al.,</italic> 2019</xref>). However, it&#x2019;s common to employ additional processes such as germination and enzymatic hydrolysis for starch modifications (
                <xref ref-type="bibr" rid="ref74">Tovar 
                    <italic toggle="yes">et al.,</italic> 2017</xref>; 
                <xref ref-type="bibr" rid="ref55">Pismag 
                    <italic toggle="yes">et al.,</italic> 2023</xref>). These supplementary procedures contribute to the creation of distinct functional properties in instant preparation products, with the objective of achieving effortless solubility and optimal water retention (
                <xref ref-type="bibr" rid="ref62">Sandrin 
                    <italic toggle="yes">et al.,</italic> 2018</xref>; 
                <xref ref-type="bibr" rid="ref21">Espinosa 
                    <italic toggle="yes">et al.,</italic> 2021</xref>). However, ensuring solubility and suspension formation may not be enough, it is essential to consider the target audience when developing instant foods. In the pursuit of nutritional adequacy, the inclusion of legume-derived proteins or defatted raw materials is put forward by certain researchers (
                <xref ref-type="bibr" rid="ref21">Espinosa 
                    <italic toggle="yes">et al.,</italic> 2021</xref>). In some cases, animal-based proteins, such as dairy proteins, have also been explored to achieve balanced nutritional profiles (
                <xref ref-type="bibr" rid="ref24">Heredia 
                    <italic toggle="yes">et al.,</italic> 2019</xref>).</p>
            <table-wrap id="T1" orientation="portrait" position="float">
                <label>Table 1. </label>
                <caption>
                    <title>Operating conditions for obtaining instant preparation flours.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="2" valign="top">Product</th>
                            <th align="left" colspan="1" rowspan="2" valign="top">Ingredient</th>
                            <th align="left" colspan="4" rowspan="1" valign="top">Extrusion conditions</th>
                            <th align="left" colspan="1" rowspan="2" valign="top">Reference</th>
                        </tr>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Temperature (&#x00b0;C)</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture (%)</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Speed screw (rpm)</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Die (mm)</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="7" rowspan="1" valign="middle">
                                <italic toggle="yes">Single screw extruder</italic>
                            </td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Extruded flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Whole quinoa flour and sprouted quinoa flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(96-115-111 &#x2013; 100)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">20-30</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref74">Tovar, 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant porridge flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Chia seed and cassava flour blend</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(50-150-250)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">10-15-20</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">100</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">10</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref49">Otondi 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant beverage extruded flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Green banana flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(20-30-40-50)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">15</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">600, 800, 1000</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">4.5</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref23">Giraldo 
                                    <italic toggle="yes">et al.</italic>, 2019</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant porridge flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Millet flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">120</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">30-32</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">700</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">6</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref47">Onyeoziri 
                                    <italic toggle="yes">et al.</italic>, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant beverage flour, porridge and desserts</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Defatted sesame seeds</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">50-170</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">50-240</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref61">Ruiz 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">QPM corn flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(50-60-70) &#x2013; (80-90-100)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">28</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">30-80</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref59">Reyes 
                                    <italic toggle="yes">et al.</italic>, 2003</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="7" rowspan="1" valign="middle">
                                <italic toggle="yes">Twin screw extruder</italic>
                            </td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Extruded flours</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Quinoa flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(80-120-80) &#x2013; (80-140-80) &#x2013; (80-160-80) &#x2013; (80 &#x2013; 180-80)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">25</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">480</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref72">Song 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Infant food</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Quinoa flour, millet flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(190)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">18</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">260</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref17">Dong 
                                    <italic toggle="yes">et al.</italic>, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Infant foods</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Quinoa flour, amaranth flour and Andean potato flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(45 &#x2013; 175 &#x2013; 180)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">1500</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref28">Jim&#x00e9;nez 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Whey protein concentrate and rice flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">120-180</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">17-23</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">225-375</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">4</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref24">Heredia 
                                    <italic toggle="yes">et al.</italic>, 2019</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant porridge flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth, bean, and corn flours</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(60-130-130) - (60-130-170)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">14-20</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref2">Akande 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant infant-food flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Corn and mung bean flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(40-70-100-108) &#x2013; (40-70-100-192)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">12,6 &#x2013; 19,4</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">349-601</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">1,5</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref4">Ali 
                                    <italic toggle="yes">et al.</italic>, 2016</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant porridge flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Broken rice and cowpea flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">100-140</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">15-25</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref41">Nahemiah 
                                    <italic toggle="yes">et al.</italic>, 2016</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth grain</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(90-110-120) &#x2013; (130-150-160)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">12-16</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">240 &#x2013; 300</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">4</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref6">Atukuri 
                                    <italic toggle="yes">et al.</italic>, 2019</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant beverage flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Chickpea flour modified with &#x03b1;-amylase and alcalase</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">150</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">22,5</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">580</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref68">Silvestre 
                                    <italic toggle="yes">et al.</italic>, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Instant infant-food flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Soy-rice mixed flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">35-45-55-125-140-150-135-120</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">14</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">3,5</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref38">Mayachiew 
                                    <italic toggle="yes">et al.</italic>, 2015</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Cold-hot beverage instant flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Chickpea, corn and sorghum flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">50-80-100-120-150</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">20-24</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">317</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref80">Wang 
                                    <italic toggle="yes">et al.</italic>, 2019</xref>)</td>
                        </tr>
                    </tbody>
                </table>
            </table-wrap>
            <p>
                <xref ref-type="table" rid="T1">Table 1</xref> provides an overview of instant preparation food types obtained through extrusion. It outlines key process conditions that significantly influence product characteristics. Parameters less frequently discussed in the literature encompass extrusion temperature, material moisture content, and screw speed. Additionally, less extensively studied factors, including die opening, feed rate, and the composition ratios of raw material mixtures, warrant further investigation. Notably, both single-screw and twin-screw extruders are employed in processing these raw materials, showcasing the versatility, and expanded horizons of extrusion-based techniques for innovative food development.</p>
        </sec>
        <sec id="sec3">
            <title>Chemical and nutritional properties</title>
            <p>Extrusion cooking is a sequential and staged process that allows for progressive modification of the materials fed into the extruder. The raw materials used in the production of precooked or instant flours has a significant amount of starch (from cereal processing), high protein content (from legume processing) or it is also possible fiber content (mixed with cereal bran) (
                <xref ref-type="bibr" rid="ref4">Ali 
                    <italic toggle="yes">et al.,</italic> 2016</xref>; 
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al</italic>., 2017</xref>; 
                <xref ref-type="bibr" rid="ref29">Kaur 
                    <italic toggle="yes">et al</italic>., 2019</xref>; 
                <xref ref-type="bibr" rid="ref49">Otondi 
                    <italic toggle="yes">et al.,</italic> 2020</xref>). Moreover, these raw materials exhibit a potential complementary component such as lipids, vitamins, minerals and micronutrients (
                <xref ref-type="bibr" rid="ref4">Ali 
                    <italic toggle="yes">et al</italic>., 2016</xref>).</p>
            <p>Understanding the behavior of main components during extrusion cooking is essential to predict the characteristics of the final products. The extent of modification or structural changes in these components depends on the thermo-mechanical conditions regulated or adjusted through process parameters in the extrusion equipment (
                <xref ref-type="bibr" rid="ref4">Ali 
                    <italic toggle="yes">et al</italic>., 2016</xref>; 
                <xref ref-type="bibr" rid="ref42">Nahemiah 
                    <italic toggle="yes">et al</italic>., 2018</xref>). Consequently, the resulting characteristics of the products can vary significantly, leading to desirable attributes such as starch gelatinization, protein denaturation, increasing the 
                <italic toggle="yes">in vitro</italic> digestion, enhanced nutrient availability (including sugars, polypeptides, phenolic compounds, and vitamins), increasing the soluble dietary fiber and reducing the level of antinutritional factors (
                <xref ref-type="bibr" rid="ref10">Chulaluck 
                    <italic toggle="yes">et al.</italic>, 2008</xref>; 
                <xref ref-type="bibr" rid="ref49">Otondi 
                    <italic toggle="yes">et al.,</italic> 2020</xref>). Conversely, some papers describe the occurrence of Maillard reactions promoting a reduction in the protein digestibility as same as decreasing the content of thermolabile compounds like vitamins and phenolic compounds (
                <xref ref-type="bibr" rid="ref3">Alam &amp; Aslam, 2020</xref>; 
                <xref ref-type="bibr" rid="ref45">Offiah, Kontogiorgos, &amp; Falade, 2019</xref>; 
                <xref ref-type="bibr" rid="ref70">Singh, Gamlath, &amp; Wakeling, 2007</xref>). This section specifically focuses on elucidating the influence of process parameter modifications on the chemical and nutritional properties of instant preparation flours.</p>
        </sec>
        <sec id="sec4">
            <title>Free sugars</title>
            <p>Extrusion cooking promotes the formation of low molecules weight from the starches. The main phenomena is called gelatinization, which is a particular process in extrusion that occurs at low moisture contents (12&#x2013;45%), and involves the starch granule swelling, the leaching of amylose fractions and low molecular weight polysaccharides is also promoted. However, as thermo-mechanical conditions become more aggressive, fusion, depolymerization, and dextrinization of starches are induced (
                <xref ref-type="bibr" rid="ref16">Dalbhagat, Mahato, &amp; Mishra, 2019</xref>; 
                <xref ref-type="bibr" rid="ref82">Yadav, Dalbhagat, &amp; Mishra, 2022</xref>). Both amylose and amylopectin are fully exposed to the mechanical effect of the screws, leading to the production of low molecular weight structures, including the generation of sugars (
                <xref ref-type="bibr" rid="ref70">Singh, Gamlath, &amp; Wakeling, 2007</xref>).</p>
            <p>
                <xref ref-type="table" rid="T2">Table 2</xref> demonstrates that the production of free sugars can occur during the extrusion process. High-temperature conditions, elevated moisture contents, and increased screw speeds contribute to significant levels of free sugar production in flours. Mild or low extrusion conditions, characterized by low temperature profiles, low moisture content, and high screw speeds, do not induce structural changes in starches, as reported by (
                <xref ref-type="bibr" rid="ref36">Mart&#x00ed;nez, Calvi&#x00f1;o, Rosell, &amp; G&#x00f3;mez, 2014b</xref>; 
                <xref ref-type="bibr" rid="ref37">Mart&#x00ed;nez, Rosell, &amp; G&#x00f3;mez, 2014a</xref>). Conversely, reversing these conditions during extrusion facilitates structural modifications in starches, leading to increased availability of free sugars in the extruded products (
                <xref ref-type="bibr" rid="ref12">Cheftel, 1986</xref>). This is relevant in legume extrusion, where the structural modification of oligosaccharides, such as raffinose, results in the increased production of reducing and non-reducing sugars (
                <xref ref-type="bibr" rid="ref11">Chauhan &amp; Bains, 1988</xref>; 
                <xref ref-type="bibr" rid="ref52">Pham &amp; Del Rosario, 1984</xref>). Controlling sugar levels during the extrusion process is crucial for ensuring the nutritional and sensory quality of extruded products (
                <xref ref-type="bibr" rid="ref82">Yadav 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). The production of sugars must be regulated to prevent adverse effects on protein digestibility during extrusion processes, unless fermentation is desired (
                <xref ref-type="bibr" rid="ref70">Singh 
                    <italic toggle="yes">et al.</italic>, 2007</xref>).</p>
            <table-wrap id="T2" orientation="portrait" position="float">
                <label>Table 2. </label>
                <caption>
                    <title>Effect of extrusion parameters on free sugars.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Extrusion conditions</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Wheat flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 3,6-21,8%</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref37">Mart&#x00ed;nez 
                                    <italic toggle="yes">et al.</italic>, 2014a</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Rice flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 17&#x2013;30%
                                <break/>Temperature 110&#x2013;140&#x00b0;C</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref37">Mart&#x00ed;nez 
                                    <italic toggle="yes">et al.</italic>, 2014a</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Rice and legume flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Temperature 60&#x2013;95&#x00b0;C</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref11">Chauhan &amp; Bains, 1988</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">White bean and green bean flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 30-45%
                                <break/>Temperature 93-132&#x00b0;C
                                <break/>Screw speed 100-200 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref52">Pham &amp; Del Rosario, 1984</xref>)</td>
                        </tr>
                    </tbody>
                </table>
                <table-wrap-foot>
                    <p>(+) Positive effect of process parameter on product parameter, (-) Negative effect of process parameter on product parameter.</p>
                </table-wrap-foot>
            </table-wrap>
        </sec>
        <sec id="sec5">
            <title>Protein solubility</title>
            <p>Protein is a representative fraction of cereal or legume flours, which suffer modification depending on the extrusion process conditions. During extrusion the hydrothermal and mechanical conditions cause denaturation and aggregation of proteins, leading to reduced solubility (
                <xref ref-type="bibr" rid="ref67">Silvestre, Espinosa, Heredia, &amp; P&#x00e9;rez, 2020</xref>). The treatment of proteins at high temperatures and high moisture contents, unfold their quaternary structures and become part of the melted material. Subsequently, these modified proteins polymerize, cross-link, and reorient themselves, forming longer and fibrous structures. This mechanism is particularly noteworthy in obtaining textured proteins. Most of the extrusion processes reported in 
                <xref ref-type="table" rid="T3">Table 3</xref> demonstrate that protein solubility tends to decrease with increasing temperature. This is likely due to the thermal effect inside the extruder, which promotes cross-linking of shorter protein units (
                <xref ref-type="bibr" rid="ref50">Pelembe, Erasmus, &amp; Taylor, 2002</xref>).</p>
            <table-wrap id="T3" orientation="portrait" position="float">
                <label>Table 3. </label>
                <caption>
                    <title>Effect of extrusion parameters on soluble protein content.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Extrusion conditions</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Soybean meal</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 15 to 27%
                                <break/>Temperature 110 to 150&#x00b0;C
                                <break/>Screw speed 300 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref69">Singh, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Chickpea flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 15 to 22%
                                <break/>Temperature 143 to 150&#x00b0;C
                                <break/>Screw speed 450 to 700 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref67">Silvestre 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Canola flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 24, 30, 36%</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref83">Zhang 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Sorghum and cowpea flour blend</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 200 g/Kg
                                <break/>Temperature 130 to 165&#x00b0;C
                                <break/>Screw speed 200 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref50">Pelembe 
                                    <italic toggle="yes">et al.</italic>, 2002</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Lentil flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 18%
                                <break/>Temperature 135 to 175&#x00b0;C
                                <break/>Screw speed 500 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref34">Li &amp; Lee, 2000</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Wheat flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Moisture 30%
                                <break/>Temperature 60 to 160&#x00b0;C
                                <break/>Screw speed 200 rpm</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref35">Li &amp; Lee, 1997</xref>)</td>
                        </tr>
                    </tbody>
                </table>
            </table-wrap>
            <p>However, some authors report an increase in protein solubility associated with higher barrel temperatures (
                <xref ref-type="bibr" rid="ref67">Silvestre 
                    <italic toggle="yes">et al.</italic>, 2020</xref>; 
                <xref ref-type="bibr" rid="ref83">Zhang 
                    <italic toggle="yes">et al.</italic>, 2017</xref>). This may be attributed to the breakdown of protein aggregates at high temperatures (
                <xref ref-type="bibr" rid="ref69">Singh, 2021</xref>). Comparing the reports of 
                <xref ref-type="bibr" rid="ref69">Singh (2021)</xref> and 
                <xref ref-type="bibr" rid="ref67">Silvestre 
                    <italic toggle="yes">et al.</italic>, (2020)</xref> where the maximum temperature and moisture content are similar, the screw speed is the determining factor for increased nitrogen solubility. The mechanical effect of this parameter is rarely reported, but it may contribute to the breakdown of protein aggregates, thereby increasing protein solubility. According to 
                <xref ref-type="table" rid="T3">Table 3</xref>, solubility losses are evident with increasing moisture content (
                <xref ref-type="bibr" rid="ref83">Zhang 
                    <italic toggle="yes">et al.</italic>, 2017</xref>).</p>
            <p>According to 
                <xref ref-type="bibr" rid="ref83">Zhang 
                    <italic toggle="yes">et al.</italic> (2017)</xref>, the molecular weight distribution of canola proteins undergoes redistribution after the extrusion process, resulting in a decrease of higher molecular weights and increased concentration in intermediate molecular weights due to the formation of protein conglomerates, similar findings were described by 
                <xref ref-type="bibr" rid="ref50">Pelembe 
                    <italic toggle="yes">et al.</italic>, (2002)</xref>. Although a reduction in protein solubility is widely reported, 
                <xref ref-type="bibr" rid="ref34">Li and Lee (2000)</xref> describe the associations or conglomerates formed under high extrusion conditions (temperature, and moisture content) are weak molecular bindings composed of non-covalent or fragile bonds easily breakable. Protein solubility is an outstanding characteristic in the formulation of instant foods. Nonetheless, this techno-functional attribute can be influenced during the extrusion process (
                <xref ref-type="table" rid="T3">Table 3</xref>). Hence, the regulation of processing temperature and moisture content is in the interest of regulating the solubility of these processed flours.</p>
        </sec>
        <sec id="sec6">
            <title>Browning index</title>
            <p>Browning index is the quantification of non-enzymatic browning reaction. This chemical reaction is developed when a reducing sugar interacts with amino groups in protein fractions, resulting in brown pigmentation in products exposed to high-temperature cooking processes such as extrusion (
                <xref ref-type="bibr" rid="ref70">Singh 
                    <italic toggle="yes">et al.</italic>, 2007</xref>). The quantification of non-enzymatic Maillard browning holds significant importance not only due to its desirable attributes in food manufacturing, resulting in appealing colors and aromas that attract consumer preferences (
                <xref ref-type="bibr" rid="ref60">Ruiz 
                    <italic toggle="yes">et al.</italic>, 2008</xref>). However, it becomes crucial to control this reaction as it negatively impacts protein digestibility and causes amino acid depletion from a nutritional perspective (
                <xref ref-type="bibr" rid="ref48">Osen, Toelstede, Eisner, &amp; Schweiggert, 2015</xref>). The development of brown color during the extrusion process is partly associated with lysine depletion caused by interactions with simple sugars. Lysine is an essential amino acid in protein synthesis (
                <xref ref-type="bibr" rid="ref26">Iwe, Van Zuilichem, Stolp, &amp; Ngoddy, 2004</xref>). While the evaluation of non-enzymatic browning relies on color parameters determined through the CIElab protocol, the predictions derived from this index demonstrate remarkable precision in assessing the behavior of Maillard reactions production (
                <xref ref-type="bibr" rid="ref60">Ruiz 
                    <italic toggle="yes">et al.</italic>, 2008</xref>).</p>
            <p>Most of the cereal, legume, or tuber flours encompass readily available free sugars within their matrix, which increase during the extrusion process due to gelatinization and the mechanical impact of the screws within the extruder equipment. Among the sugars documented as susceptible to Maillard reactions, glucose &gt; d-mannose &gt; d-fructose are considered more reactive as fundamental units compared to their dimers. A similar pattern of reactivity is observed for proteins, which exhibit enhanced responsiveness in Maillard reactions when present as basic constituents, namely amino acids (
                <xref ref-type="bibr" rid="ref70">Singh 
                    <italic toggle="yes">et al.</italic>, 2007</xref>; 
                <xref ref-type="bibr" rid="ref82">Yadav 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). Maillard reactions are intensified when the available protein content in the raw material is higher, this is particularly noticeable in legume flours that are ready for such reactions (
                <xref ref-type="bibr" rid="ref82">Yadav 
                    <italic toggle="yes">et al.</italic>, 2022</xref>).</p>
            <p>
                <xref ref-type="table" rid="T4">Table 4</xref> shows the effect of extrusion conditions on the generation of Maillard reactions. It is apparent that during the extrusion of flours to produce instant foods, intensified Maillard reactions occur with higher process temperatures and screw speeds. This can be attributed to the thermal and mechanical effects, which break down both starches and proteins, resulting in simpler components that promote Maillard reactions. As a result, there is an increase in brown color, quantified by the browning index, correlated with a decrease in luminosity (L*) and increasing the red (a*) and yellow (b*) colors (
                <xref ref-type="bibr" rid="ref81">Waramboi, Gidley, &amp; Sopade, 2013</xref>; 
                <xref ref-type="bibr" rid="ref82">Yadav 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). High screw speed promotes a mechanical shearing force on the melted material as it crosses the barrel in the extruder, developing the damage of polysaccharides (starch), which can contribute production of the Maillard reaction (
                <xref ref-type="bibr" rid="ref26">Iwe 
                    <italic toggle="yes">et al.</italic>, 2004</xref>; 
                <xref ref-type="bibr" rid="ref82">Yadav 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). On the other hand, it becomes apparent that the browning index decreases as the moisture content increases during the extrusion process. Although moisture content starts the Maillard reaction, a higher level of moisture increases the flow of the melted material, thereby diminishing its residence time and controlling the formation of this reaction. Water acts as a plasticizer in the process reducing the viscosity of the melted material (
                <xref ref-type="bibr" rid="ref9">Camire, 1991</xref>).</p>
            <table-wrap id="T4" orientation="portrait" position="float">
                <label>Table 4. </label>
                <caption>
                    <title>Effect of extrusion parameters on the browning index.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Sorghum and barley blend</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref30">Koa 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Barley varieties</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref66">Sharma 
                                    <italic toggle="yes">et al.</italic>, 2012</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Soybean and sweet potato</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref26">Iwe 
                                    <italic toggle="yes">et al.</italic>, 2004</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Sweet potato flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref81">Waramboi 
                                    <italic toggle="yes">et al.</italic>, 2013</xref>)</td>
                        </tr>
                    </tbody>
                </table>
            </table-wrap>
        </sec>
        <sec id="sec7">
            <title>
                <italic toggle="yes">In vitro</italic> starch digestion</title>
            <p>
                <xref ref-type="bibr" rid="ref20">Englyst, Kingman, and Cummings (1992)</xref> developed a colorimetric method to describe the three starches fractions in food matrices. Rapidly Digestible Starch (RDS), indicating starch that undergoes digestion within 20 minutes based on hydrolysis rates; Slowly Digestible Starch (SDS), denoting starch that is digested between 20 and 120 minutes; and Resistant Starch (RS), which can be analyzed in three fractions and corresponds to the starch fraction that remains undigested after 120 minutes. This method relies on controlled enzymatic assessment using pancreatin and amyloglucosidase. The evaluation of these starch fractions provides information into the 
                <italic toggle="yes">in vivo</italic> starch digestion rate (
                <xref ref-type="bibr" rid="ref71">Smrckova 
                    <italic toggle="yes">et al.</italic>, 2014</xref>; 
                <xref ref-type="bibr" rid="ref85">Zhang 
                    <italic toggle="yes">et al.</italic>, 2019</xref>).</p>
            <p>The evaluation of 
                <italic toggle="yes">in vitro</italic> starch digestibility is one of the extensively studied process parameters in extruded foods. this method is capable to reveal the changes that occur in the starch fraction of raw and processed materials, as same as their potential nutritional effects. Moreover, the rate at which modified starches can be digested, the proportion of starches available for digestion, and indirectly their relationship with glycemic index (GI) associated to the blood sugar content. This can be critical when RDS levels are elevated as they could negatively affect consumer health (
                <xref ref-type="bibr" rid="ref57">Qi 
                    <italic toggle="yes">et al.</italic>, 2021</xref>; 
                <xref ref-type="bibr" rid="ref71">Smrckova 
                    <italic toggle="yes">et al.</italic>, 2014</xref>). The available information regarding 
                <italic toggle="yes">in vitro</italic> starch digestion in extruded instant flours is limited. Based on 
                <xref ref-type="table" rid="T5">Table 5</xref>, it is possible to assess the impact of modifying the parameter process during extrusion on the starch fractions in the raw materials. In a general, it can be established that the modification of process parameters such as temperature, moisture, and screw speed exhibit an inverse correlation with the quantification of the Rapidly Digestible Starch (RDS) fraction, in comparison to the Slowly Digestible Starch (SDS) and Resistant Starch (RS) fractions. Within the extrusion process, alterations take place in each starch fraction because of gelatinization and shear forces. Consequently, RDS starches tend to convert into dextrin and/or simple sugars, while the SDS and RS fractions exhibit a decline content and may be quantified as RDS due to those modifications.</p>
            <table-wrap id="T5" orientation="portrait" position="float">
                <label>Table 5. </label>
                <caption>
                    <title>Effect of extrusion parameters on 
                        <italic toggle="yes">in vitro</italic> starch digestion.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="2" valign="top">Raw material</th>
                            <th align="left" colspan="3" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="3" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="3" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="2" valign="top">Reference</th>
                        </tr>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">RDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">SDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">RS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">RDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">SDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">RS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">RDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">SDS</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">RS</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Buckwheat flour (Tartary)</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref86">Zhang 
                                    <italic toggle="yes">et al.</italic>, 2023</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Pea flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref57">Qi 
                                    <italic toggle="yes">et al.</italic>, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Rice flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref33">Lai 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Bean varieties</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref1">Ai 
                                    <italic toggle="yes">et al.</italic>, 2016</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">High amylose corn flour</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref84">Zhang 
                                    <italic toggle="yes">et al.</italic>, 2016</xref>)</td>
                        </tr>
                    </tbody>
                </table>
                <table-wrap-foot>
                    <p>RDS = Rapidly Digestible Starch, SDS = Slowly Digestible Starch, RS = Resistant Starch.</p>
                </table-wrap-foot>
            </table-wrap>
            <p>The variability in the 
                <italic toggle="yes">in vitro</italic> starch digestion depends on the severity of the applied extrusion conditions to the raw material. Increasing the extrusion temperature leads to a high RDS content, attributable to modifications in the SDS and RS fractions (
                <xref ref-type="bibr" rid="ref86">Zhang 
                    <italic toggle="yes">et al.</italic>, 2023</xref>). The extrusion temperature constitutes one of the principal factors responsible for the gelatinization of available starches, causing the loss of their crystalline structure and the fragmentation of amylose and amylopectin chains due to the thermo-mechanical impact of the screw. This facilitates amylase accessibility during digestion (
                <xref ref-type="bibr" rid="ref33">Lai 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). Conversely, increasing moisture content during the extrusion process reduces the mean residence time of the material inside extruder, resulting in higher quantifications of SDS and RS than RDS content. These results agree with the reduction in the 
                <italic toggle="yes">in vitro</italic> starch digestion (
                <xref ref-type="bibr" rid="ref86">Zhang 
                    <italic toggle="yes">et al.</italic>, 2023</xref>). Water acts as a plasticizer capable to modify the gelatinization temperature of starches (
                <xref ref-type="bibr" rid="ref30">Koa 
                    <italic toggle="yes">et al.</italic>, 2017</xref>). Screw speed represents the factor with higher influence on the mechanical and shear forces during the extrusion process. Heightened screw speed enhances the starch structure modification through mechanical and shear-induced depolymerization, which impact the 
                <italic toggle="yes">in vitro</italic> starch digestibility (
                <xref ref-type="bibr" rid="ref30">Koa 
                    <italic toggle="yes">et al.</italic>, 2017</xref>). 
                <xref ref-type="table" rid="T5">Table 5</xref> demonstrates that higher screw speeds yield a greater amount of RDS while reducing the proportion of SDS and RS.</p>
        </sec>
        <sec id="sec8">
            <title>
                <italic toggle="yes">In vitro</italic> protein digestion</title>
            <p>
                <italic toggle="yes">In vitro</italic> protein digestion is an indirect assessment of protein nutritional quality (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref46">Omosebi 
                    <italic toggle="yes">et al.</italic>, 2018</xref>). Plant proteins generally exhibit lower digestibility compared to the animal-derived proteins due to their amino acid configuration and the presence of antinutritional factors (
                <xref ref-type="bibr" rid="ref6">Atukuri 
                    <italic toggle="yes">et al.</italic>, 2019</xref>). The digestibility of plant proteins can be enhanced through treatments such as extrusion cooking. The fitted process parameters during extrusion and their intensity effect in the extruder influence protein digestibility. These factors impart different characteristics to the protein fractions found in the raw materials. From a nutritional perspective, the protein digestion extent is related to their level of denaturation, wherein their quaternary structures lose order and transition into lower-order structures, promoting the intestinal proteolysis during digestion (
                <xref ref-type="bibr" rid="ref57">Qi 
                    <italic toggle="yes">et al.</italic>, 2021</xref>; 
                <xref ref-type="bibr" rid="ref60">Ruiz 
                    <italic toggle="yes">et al.</italic>, 2008</xref>). Based on the studies in 
                <xref ref-type="table" rid="T6">Table 6</xref>, it can be observed that, in most cases, an increase in temperature correlates with enhanced 
                <italic toggle="yes">in vitro</italic> protein digestibility. However, some reports showed a reduction in the 
                <italic toggle="yes">in vitro</italic> protein digestion when the raw materials were exposed to extremely high temperature conditions during the extrusion process (see 
                <xref ref-type="table" rid="T6">Table 6</xref>).</p>
            <table-wrap id="T6" orientation="portrait" position="float">
                <label>Table 6. </label>
                <caption>
                    <title>Effect of extrusion parameters on 
                        <italic toggle="yes">in vitro</italic> protein digestibility.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Defatted Quinoa and Chia</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref63">S&#x00e1;nchez 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Sesame Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref61">Ruiz 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Pea Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref57">Qi 
                                    <italic toggle="yes">et al.</italic>, 2021</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref6">Atukuri 
                                    <italic toggle="yes">et al.</italic>, 2019</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Corn and Soy Protein</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref46">Omosebi 
                                    <italic toggle="yes">et al.</italic>, 2018</xref>
                            </td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth-Based Mixture</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref2">Akande 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">QPM flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref59">Reyes 
                                    <italic toggle="yes">et al.</italic>, 2003</xref>)</td>
                        </tr>
                    </tbody>
                </table>
                <table-wrap-foot>
                    <p>QPM = Quality Protein Maize.</p>
                </table-wrap-foot>
            </table-wrap>
            <p>Between the most reported reaction involving proteins during the extrusion process encompass Maillard reactions, protein crosslinking, racemization, degradation, and the generation of lysinoalanine (
                <xref ref-type="bibr" rid="ref37">Mart&#x00ed;nez 
                    <italic toggle="yes">et al.</italic>, 2014a</xref>; 
                <xref ref-type="bibr" rid="ref40">Nahemiah 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref46">Omosebi 
                    <italic toggle="yes">et al.</italic>, 2018</xref>; 
                <xref ref-type="bibr" rid="ref61">Ruiz 
                    <italic toggle="yes">et al.</italic>, 2022</xref>; 
                <xref ref-type="bibr" rid="ref68">Silvestre 
                    <italic toggle="yes">et al.</italic>, 2021</xref>). The quantification of these reactions tends to increase when proteins undergo excessive cooking during extrusion with a reduction in the 
                <italic toggle="yes">in vitro</italic> protein digestion (
                <xref ref-type="bibr" rid="ref59">Reyes 
                    <italic toggle="yes">et al.</italic>, 2003</xref>). Furthermore, it can be observed that an increase in moisture content generally leads to a reduction in protein digestibility. This is attributed to the low residence time effect, which hinders structural modifications of the proteins. Conversely, the high screw speed increases protein digestibility due to the mechanical impact exerted by the screws on the raw material. Considering that the extrusion process requires a direct exposure of raw materials to high temperatures and relatively reduced moisture levels, a substantial quantity of complexes resulting from the reaction between reducing sugars and free amino acids is generated, leading to the occurrence of Maillard reactions. Then it becomes an important condition that should be regulated. The Maillard reaction imparts costumer pleasing flavors and colors, but as a uncontrolled reaction imposes limitations on protein availability and digestibility (
                <xref ref-type="bibr" rid="ref3">Alam &amp; Aslam, 2020</xref>; 
                <xref ref-type="bibr" rid="ref6">Atukuri 
                    <italic toggle="yes">et al.</italic>, 2019</xref>). In extreme conditions it&#x2019;s possible the formation of compounds such as acrylamides, which pose health risks and are synthesized when process temperatures overpass the threshold or when exposure time is long, even under low moisture content conditions during the extrusion process (
                <xref ref-type="bibr" rid="ref3">Alam &amp; Aslam, 2020</xref>). Furthermore, higher screw speed during extrusion generates high shear forces, thereby boosting protein denaturation within the raw material and enhancing enzymatic hydrolysis during digestion (
                <xref ref-type="bibr" rid="ref6">Atukuri 
                    <italic toggle="yes">et al.</italic>, 2019</xref>). The excessive thermo-mechanical effect made during the extrusion process can also give rise to protein crosslinking. In addition, the high moisture content during the extrusion process prompts protein swelling and softening, consequently facilitating their denaturation and fractioning due to the thermo-mechanical impact within the extruder (
                <xref ref-type="bibr" rid="ref6">Atukuri 
                    <italic toggle="yes">et al.</italic>, 2019</xref>).</p>
            <p>A few factors affecting 
                <italic toggle="yes">in vitro</italic> protein digestibility during the extrusion process have been discussed thus far. However, it is notable to acknowledge that in plant-based raw materials, there exist other interfering elements that can also influence protein digestibility (
                <xref ref-type="bibr" rid="ref57">Qi 
                    <italic toggle="yes">et al.</italic>, 2021</xref>; 
                <xref ref-type="bibr" rid="ref60">Ruiz 
                    <italic toggle="yes">et al.</italic>, 2008</xref>; 
                <xref ref-type="bibr" rid="ref67">Silvestre 
                    <italic toggle="yes">et al.</italic>, 2020</xref>; 
                <xref ref-type="bibr" rid="ref54">Pico 
                    <italic toggle="yes">et al.</italic>, 2019</xref>). The presence of polyphenols in plant matrices can directly interact with digestive enzymes (such as amylase, trypsin, chymotrypsin, lipases), diminishing protein functionality and, consequently, reducing nutrient digestibility (
                <xref ref-type="bibr" rid="ref46">Omosebi 
                    <italic toggle="yes">et al.</italic>, 2018</xref>). However, the extrusion process can significantly decrease the presence of these interfering compounds in protein digestion and decrease the molecular weight of proteins to facilitate their digestion.</p>
        </sec>
        <sec id="sec9">
            <title>Total phenolic compounds</title>
            <p>The quantification of total phenolic compounds in vegetable matrices include free and bounded fractions and during extrusion process is possible to modify the relationship between the quantity of both fractions. Furthermore, it has been possible to observe a high quantification of total phenolic compounds when the extrusion conditions effectively break down the cell walls of the matrix (
                <xref ref-type="bibr" rid="ref53">Pico, 
                    <italic toggle="yes">et al.</italic>, 2020</xref>; 
                <xref ref-type="bibr" rid="ref54">Pico 
                    <italic toggle="yes">et al.</italic>, 2019</xref>). The increase of the temperature and screw speed during extrusion promotes the thermo-mechanical movement of the melted material inside the extruder, facilitating the release, extraction, and quantification of bound phenolic compounds, which then become part of the free phenolic fraction. Some phenolic species released include hydroxybenzoic acids, flavonols, catechins, and low molecular weight proanthocyanidins. However, it is important to note that certain studies report an increase in total phenolic compounds, while others report a decrease in this parameter, suggesting that the response may depend on the specific characteristics of the raw material and the employed extrusion conditions (see 
                <xref ref-type="table" rid="T7">Table 7</xref>).</p>
            <table-wrap id="T7" orientation="portrait" position="float">
                <label>Table 7. </label>
                <caption>
                    <title>Effect of extrusion parameters on total phenolic compounds.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Sesame Cake flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref61">Ruiz 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Defatted Quinoa and Chia Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref63">S&#x00e1;nchez 
                                    <italic toggle="yes">et al.</italic>, 2022</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Buckwheat</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref13">Cheng 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Red Quinoa</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref72">Song 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth, Bean, and Corn Flours</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref2">Akande 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Green Banana Flour</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref64">Sarawong 
                                    <italic toggle="yes">et al.</italic>, 2014</xref>)</td>
                        </tr>
                    </tbody>
                </table>
            </table-wrap>
            <p>On the other hand, it has been observed that increasing the moisture content during the extrusion process tends to reduce the quantification of total phenolic compounds (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref64">Sarawong 
                    <italic toggle="yes">et al.</italic>, 2014</xref>). Water acts as a plasticizer, preventing the structural breakdown of the cell walls in the matrices and making it difficult to quantify the fractions of bound phenolics (
                <xref ref-type="bibr" rid="ref27">Jan 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref64">Sarawong 
                    <italic toggle="yes">et al.</italic>, 2014</xref>; 
                <xref ref-type="bibr" rid="ref79">Wang 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). However, it has also been reported that an increase in moisture content enhance the preservation of released phenolic fractions, as low moisture contents during the extrusion process can cause structural disruption or alteration of phenolic compounds (
                <xref ref-type="bibr" rid="ref13">Cheng 
                    <italic toggle="yes">et al.</italic>, 2020</xref>). Nevertheless, it is imperative to optimize the operational parameters of the extrusion process to prevent excessive temperatures and/or shear conditions. Most of the phenolic compounds are sensitive to temperature, which can induce their structural modifications, leading to the loss of their functionality and potential quantification as functional constituents in foods (
                <xref ref-type="bibr" rid="ref79">Wang 
                    <italic toggle="yes">et al.</italic>, 2022</xref>).</p>
        </sec>
        <sec id="sec10">
            <title>Antinutritional Factors (ANFs)</title>
            <p>Plant-based raw materials used in food production possess small quantities of a distinctive chemical compound, which are synthesized primarily for the plant&#x2019;s survival and multiple physiological functions (
                <xref ref-type="bibr" rid="ref19">Elizalde 
                    <italic toggle="yes">et al.</italic>, 2009</xref>). Among these group of compounds are phytic acid, lectins, protease inhibitors (trypsin and chymotrypsin), saponins, oligosaccharides (raffinose and stachyose), and phenolic compounds (see 
                <xref ref-type="table" rid="T8">Table 8</xref>). Consuming these components in high concentrations can lead to digestive issues, intoxication, allergies, and, in some cases, damage to intestinal epithelial cells, all these compounds have been grouped as antinutritional factors (ANFs) (
                <xref ref-type="bibr" rid="ref19">Elizalde 
                    <italic toggle="yes">et al.</italic>, 2009</xref>). ANFs possess high activity and exhibit the capability of conformation complexes with molecules of nutritional importance. Trypsin inhibitors disrupt the enzymatic activity during protein hydrolysis, thereby impeding its absorption (
                <xref ref-type="bibr" rid="ref73">Thirunathan &amp; Manickavasagan, 2019</xref>). Lectins, as glycoproteins, readily bind to red blood cell and intestinal epithelial cell walls, causing harm and an adverse effect in the intestinal microbiota (
                <xref ref-type="bibr" rid="ref78">Vidal 
                    <italic toggle="yes">et al.,</italic> 2022</xref>). Phytic acid hinders mineral absorption at the intestinal level by forming complexes involving phytate-mineral-protein, which exhibit low solubility (
                <xref ref-type="bibr" rid="ref77">Vega 
                    <italic toggle="yes">et al.</italic>, 2010</xref>). Certain phenolic compounds are regarded as ANFs due to their capacity to bind with proteins, reducing protein solubility and digestibility (
                <xref ref-type="bibr" rid="ref78">Vidal 
                    <italic toggle="yes">et al.,</italic> 2022</xref>). Additionally, they influence consumption and acceptance due to production of bitter tastes and dark coloration (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref46">Omosebi 
                    <italic toggle="yes">et al.</italic>, 2018</xref>; 
                <xref ref-type="bibr" rid="ref78">Vidal 
                    <italic toggle="yes">et al.</italic>, 2022</xref>). Oligosaccharides, such as raffinose and stachyose, are high molecular weight sugars commonly found in most legumes (
                <xref ref-type="bibr" rid="ref73">Thirunathan &amp; Manickavasagan, 2019</xref>). These sugars are indigestible due to their structure and the presence of &#x03b1;-1-6 galactose linkages that resist intestinal hydrolysis. Legume grains generally contain higher proportions of these sugars, which, according to some studies, display reduced sensitivity to temperature effects (
                <xref ref-type="bibr" rid="ref19">Elizalde 
                    <italic toggle="yes">et al.</italic>, 2009</xref>). However, their behavior can be influenced by processing conditions. Saponins, classified as glycosides of steroids or triterpenoids, display distinct characteristics such as imparting a bitter taste to quinoa and soybean seeds and their ability to generate foams, which interfere with mineral absorption in the intestine (
                <xref ref-type="bibr" rid="ref19">Elizalde 
                    <italic toggle="yes">et al.</italic>, 2009</xref>; 
                <xref ref-type="bibr" rid="ref22">Gee 
                    <italic toggle="yes">et al.</italic>, 1993</xref>).</p>
            <table-wrap id="T8" orientation="portrait" position="float">
                <label>Table 8. </label>
                <caption>
                    <title>Effect of extrusion parameters on ANF content.</title>
                </caption>
                <table content-type="article-table" frame="hsides">
                    <thead>
                        <tr>
                            <th align="left" colspan="1" rowspan="1" valign="top">Raw material</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Product parameter/condition</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Barrel temperature</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Moisture</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Screw speed</th>
                            <th align="left" colspan="1" rowspan="1" valign="top">Reference</th>
                        </tr>
                    </thead>
                    <tbody>
                        <tr>
                            <td align="left" colspan="1" rowspan="2" valign="middle">Lentil flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Raffinose</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="2" valign="middle">(
                                <xref ref-type="bibr" rid="ref14">Ciudad 
                                    <italic toggle="yes">et al.</italic>, 2020</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Stachyose</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="2" valign="middle">Bean flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Refinase</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="2" valign="middle">(
                                <xref ref-type="bibr" rid="ref73">Thirunathan &amp; Manickavasagan, 2019</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Stachyose</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Amaranth, Bean, and Corn Flours</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Phytic Acid</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref2">Akande 
                                    <italic toggle="yes">et al.</italic>, 2017</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Quinoa Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Saponins</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref32">Kowalski 
                                    <italic toggle="yes">et al.</italic>, 2016</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="2" valign="middle">Corn, soybean, and African Treculia blend</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Phytic acid</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="2" valign="middle">(
                                <xref ref-type="bibr" rid="ref44">Nwabueze, 2007</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">TI</td>
                            <td colspan="1" rowspan="1"/>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Peanut, Corn, and Soybean Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">TI</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref56">Plahar 
                                    <italic toggle="yes">et al.</italic>, 2003</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Soybean and Sweet Potato Flour Blend</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">TI</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td colspan="1" rowspan="1"/>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref25">Iwe &amp; Ngoddy, 2000</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Lentil Flour</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Tannins</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref76">Ummadi 
                                    <italic toggle="yes">et al.</italic>, 1995</xref>)</td>
                        </tr>
                        <tr>
                            <td align="left" colspan="1" rowspan="1" valign="middle">Soybean</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">TI</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">+</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">-</td>
                            <td align="left" colspan="1" rowspan="1" valign="middle">(
                                <xref ref-type="bibr" rid="ref51">Petres &amp; Czukor, 1989</xref>)</td>
                        </tr>
                    </tbody>
                </table>
                <table-wrap-foot>
                    <p>TI = Trypsin Inhibitors, ANFs = Antinutritional Factors.</p>
                </table-wrap-foot>
            </table-wrap>
            <p>Tannins, categorized as phenolic compounds and recognized as ANFs, are present in the structure of various plant-based raw materials. Their consumption interferes with protein and mineral digestion as tannins form complexes with carbonyl groups in dietary proteins or enzymes (
                <xref ref-type="bibr" rid="ref18">Duguma, Forsido, Belachew, &amp; Hensel, 2021</xref>; 
                <xref ref-type="bibr" rid="ref43">Nikmaram 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref57">Qi 
                    <italic toggle="yes">et al.</italic>, 2021</xref>).</p>
            <p>The ANFs in plant matrices interfere on nutrient absorption. Therefore, thermal treatments like extrusion are employed to mitigate their effects and enhance the overall digestibility of nutrients in pre-cooked cereal and legume flours. 
                <xref ref-type="table" rid="T8">Table 8</xref> shows the behavior of oligosaccharides, such as raffinose and stachyose, and the influence of the processing conditions applied during extrusion. It has been observed that increasing the temperature leads to a decrease in raffinose content while increasing stachyose content (
                <xref ref-type="bibr" rid="ref14">Ciudad 
                    <italic toggle="yes">et al.</italic>, 2020</xref>; 
                <xref ref-type="bibr" rid="ref73">Thirunathan &amp; Manickavasagan, 2019</xref>). The reduction in raffinose can be attributed to structural modifications, including the cleavage of 1-2 furanosidic bonds, which occur due to exposure to high temperatures. On the other hand, the increase in stachyose at higher temperatures and screw speeds is associated with the thermo-mechanical effect on the food matrix, which facilitates the release of bound oligosaccharides from other macromolecules and the disruption of cell walls, allowing their extraction as soluble components (
                <xref ref-type="bibr" rid="ref15">Cotacallapa 
                    <italic toggle="yes">et al.</italic>, 2021</xref>). Similarly, 
                <xref ref-type="table" rid="T8">Table 8</xref> demonstrates that high temperatures inactivate the content of phytic acid due to its thermosensitivity and the formation of insoluble complexes with other components (
                <xref ref-type="bibr" rid="ref46">Omosebi 
                    <italic toggle="yes">et al.</italic>, 2018</xref>; 
                <xref ref-type="bibr" rid="ref8">Batista 
                    <italic toggle="yes">et al.</italic>, 2010</xref>). According to 
                <xref ref-type="bibr" rid="ref58">Rathod and Annapure (2016)</xref>, both temperature and moisture content during the extrusion process contribute to the structural modifications of phytates in the raw materials. These changes may involve the cleavage of covalent bonds between amino groups and the hydrolysis of peptide bonds in aspartic acid residues, leading to the inactivation of phytates.</p>
            <p>Likewise, the content of saponins exhibits a decrease with increasing temperature and moisture content during the extrusion process (see 
                <xref ref-type="table" rid="T8">Table 8</xref>). This behavior is attributed to the shear and mechanical energy during extrusion, which alters the original structure of saponins, resulting in smaller chemical fragments and a reduction in the pungent or astringent taste in quinoa-based products (
                <xref ref-type="bibr" rid="ref32">Kowalski 
                    <italic toggle="yes">et al.</italic>, 2016</xref>). In addition, 
                <xref ref-type="table" rid="T8">Table 8</xref> shows that the trypsin inhibitors tend to decrease under intense thermal and mechanical effects during extrusion, leading to molecular degradation (
                <xref ref-type="bibr" rid="ref8">Batista 
                    <italic toggle="yes">et al.</italic>, 2010</xref>; 
                <xref ref-type="bibr" rid="ref14">Ciudad 
                    <italic toggle="yes">et al.</italic>, 2020</xref>; 
                <xref ref-type="bibr" rid="ref31">Konstance 
                    <italic toggle="yes">et al.</italic>, 1998</xref>). However, the trypsin inhibitors content increases when the extrusion conditions are less aggressive. The only condition that modifies this behavior is an increase in moisture content. While some reports suggest classifying ANFs based on their temperature sensitivity, it has been observed that the most affected by thermal and mechanical effects are protease inhibitors (trypsin and chymotrypsin inhibitors), including phytic acid and lectins (
                <xref ref-type="bibr" rid="ref2">Akande 
                    <italic toggle="yes">et al.</italic>, 2017</xref>; 
                <xref ref-type="bibr" rid="ref7">Balandran 
                    <italic toggle="yes">et al.</italic>, 1998</xref>; 
                <xref ref-type="bibr" rid="ref9">Camire, 1991</xref>; 
                <xref ref-type="bibr" rid="ref19">Elizalde 
                    <italic toggle="yes">et al.</italic>, 2009</xref>). Tannins can develop complexes during the extrusion process under strong processing conditions. High temperatures and high screw speeds induce a thermal and shear effect that modifies the structure of these phenolic compounds. However, when the extrusion conditions are milder, achieved by increasing the moisture content, the preservation of tannins in the final product is higher (
                <xref ref-type="bibr" rid="ref76">Ummadi 
                    <italic toggle="yes">et al.</italic>, 1995</xref>).</p>
        </sec>
        <sec id="sec11" sec-type="conclusions">
            <title>Conclusions</title>
            <p>This review has demonstrated the usefulness of the extrusion cooking process in obtaining instant flours known as pregelatinized flours. The extrusion cooking process conditions such as temperature, moisture content of the material and screw speed, directly affect the behavior of the raw material components during the process. The most used raw materials to obtain pre-cooked flours have in their composition a significant amount of starch, protein, lipids, and others like fiber, micronutrients such as vitamins and minerals, all of them exposed to be modified by the thermo-mechanical conditions. These modifications influence the nutritional and functional characteristics of the final product.</p>
            <p>The final results of the process will be associated with the modification of the operative extruder parameters, finding as results characteristics that become beneficial for the final product such as starch gelatinization, protein denaturation, increased 
                <italic toggle="yes">in vitro</italic> digestibility, nutrient availability, increased soluble dietary fiber and reduction in the content of anti-nutritional factors (ANF), all of these characteristics are linked to the nutritional and functional properties of the instant flours. However, there is a lack of information that must be investigated regarding the already mentioned process conditions and other new ones, in the same way, to study their effect on the processed raw materials. There are even raw materials whose behavior is unknown, and which may be important in obtaining instant flour by extrusion.</p>
            <p>It should be noted that the moisture content and the temperature of the process influence the solubility of the proteins and the gelatinization of the starch, which is fundamental in the development of instant preparation foods; therefore, it is necessary to modulate the moisture content and the process temperature to keep the solubility of these processed flours under control. On the other hand, the increase in temperature increases the digestibility of protein 
                <italic toggle="yes">in vitro</italic> and by extrusion cooking it is possible to improve the digestibility of proteins of vegetable origin. In the same way, the phenolic content is modified by increasing in availability of thermostable bonded species due to cell wall broken of raw materials due to thermo-mechanical conditions during extrusion process.</p>
            <p>As it has been established so far, the presence of ANFs in plant matrices represents an important limitation on the levels of nutrient absorption, it is for this reason that heat treatments such as extrusion reduce their effect and enhance the effective digestibility of available nutrients from precooked cereal and legume flours.</p>
        </sec>
    </body>
    <back>
        <sec id="sec14">
            <title>Data availability</title>
            <p>No data are associated with this article.</p>
        </sec>
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                    <article-title>Effects of extrusion treatment on physicochemical properties and 
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    </back>
    <sub-article article-type="reviewer-report" id="report220796">
        <front-stub>
            <article-id pub-id-type="doi">10.5256/f1000research.154135.r220796</article-id>
            <title-group>
                <article-title>Reviewer response for version 1</article-title>
            </title-group>
            <contrib-group>
                <contrib contrib-type="author">
                    <name>
                        <surname>Sanchez</surname>
                        <given-names>Martha Isabel</given-names>
                    </name>
                    <xref ref-type="aff" rid="r220796a1">1</xref>
                    <role>Referee</role>
                    <uri content-type="orcid">https://orcid.org/0000-0002-8381-9171</uri>
                </contrib>
                <aff id="r220796a1">
                    <label>1</label>Faculty of Agronomic Engineering, University of Tolima, Ibague, Tolima, Colombia</aff>
            </contrib-group>
            <author-notes>
                <fn fn-type="conflict">
                    <p>
                        <bold>Competing interests: </bold>No competing interests were disclosed.</p>
                </fn>
            </author-notes>
            <pub-date pub-type="epub">
                <day>8</day>
                <month>2</month>
                <year>2024</year>
            </pub-date>
            <permissions>
                <copyright-statement>Copyright: &#x00a9; 2024 Sanchez MI</copyright-statement>
                <copyright-year>2024</copyright-year>
                <license xlink:href="https://creativecommons.org/licenses/by/4.0/">
                    <license-p>This is an open access peer review report distributed under the terms of the Creative Commons Attribution Licence, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.</license-p>
                </license>
            </permissions>
            <related-article ext-link-type="doi" id="relatedArticleReport220796" related-article-type="peer-reviewed-article" xlink:href="10.12688/f1000research.140748.1"/>
            <custom-meta-group>
                <custom-meta>
                    <meta-name>recommendation</meta-name>
                    <meta-value>approve</meta-value>
                </custom-meta>
            </custom-meta-group>
        </front-stub>
        <body>
            <p>This review presents in a comprehensive and organized way the theoretical framework concerning the influence of extrusion parameters on the functional and nutritional properties of precooked or instant flours, both as end-products and ingredients. It highlights the pivotal role of process parameters within the extruder, including temperature, screw speed, and raw materials moisture content, among others, and elucidates their correlation with the modifications observed in the structural composition of these materials.</p>
            <p> </p>
            <p> Below are some recommendations from the text:</p>
            <p> </p>
            <p> 1. I recommend including a figure of the extrusion process/equipment where parts and some operating conditions are mentioned, considering that throughout the manuscript, reference is made to process/equipment operating conditions.</p>
            <p> </p>
            <p> 2. It is necessary to include an explanation in the footer of each Table indicating the information and the meaning of the symbols (+) and (-).</p>
            <p> </p>
            <p> 3. In the section on Maillard reactions, it is necessary to mention in more detail the type of raw materials involved, what type of colors are desirable or undesirable in the final product, and their effect on consumer preference.</p>
            <p> </p>
            <p> 4. Conclusion "&#x00a0;
                <italic>However, there is a lack of information that must be investigated regarding the already mentioned process conditions and other new ones, in the same way, to study their effect on the processed raw material"&#x00a0;</italic>does not take into account information previously mentioned in the text, is broad, and has no basis in the text to be included as a conclusion of the manuscript.</p>
            <p>Is the review written in accessible language?</p>
            <p>Yes</p>
            <p>Are all factual statements correct and adequately supported by citations?</p>
            <p>Yes</p>
            <p>Are the conclusions drawn appropriate in the context of the current research literature?</p>
            <p>Partly</p>
            <p>Is the topic of the review discussed comprehensively in the context of the current literature?</p>
            <p>Yes</p>
            <p>Reviewer Expertise:</p>
            <p>Food Engineering, Food Science and Technology</p>
            <p>I confirm that I have read this submission and believe that I have an appropriate level of expertise to confirm that it is of an acceptable scientific standard.</p>
        </body>
    </sub-article>
    <sub-article article-type="reviewer-report" id="report220802">
        <front-stub>
            <article-id pub-id-type="doi">10.5256/f1000research.154135.r220802</article-id>
            <title-group>
                <article-title>Reviewer response for version 1</article-title>
            </title-group>
            <contrib-group>
                <contrib contrib-type="author">
                    <name>
                        <surname>Pedrosa</surname>
                        <given-names>Mercedes</given-names>
                    </name>
                    <xref ref-type="aff" rid="r220802a1">1</xref>
                    <role>Referee</role>
                </contrib>
                <aff id="r220802a1">
                    <label>1</label>Food Technology Department, INIA-CSIC, Ctra. de La Coru&#x00f1;a, Marbrid, Spain</aff>
            </contrib-group>
            <author-notes>
                <fn fn-type="conflict">
                    <p>
                        <bold>Competing interests: </bold>No competing interests were disclosed.</p>
                </fn>
            </author-notes>
            <pub-date pub-type="epub">
                <day>15</day>
                <month>11</month>
                <year>2023</year>
            </pub-date>
            <permissions>
                <copyright-statement>Copyright: &#x00a9; 2023 Pedrosa M</copyright-statement>
                <copyright-year>2023</copyright-year>
                <license xlink:href="https://creativecommons.org/licenses/by/4.0/">
                    <license-p>This is an open access peer review report distributed under the terms of the Creative Commons Attribution Licence, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.</license-p>
                </license>
            </permissions>
            <related-article ext-link-type="doi" id="relatedArticleReport220802" related-article-type="peer-reviewed-article" xlink:href="10.12688/f1000research.140748.1"/>
            <custom-meta-group>
                <custom-meta>
                    <meta-name>recommendation</meta-name>
                    <meta-value>approve-with-reservations</meta-value>
                </custom-meta>
            </custom-meta-group>
        </front-stub>
        <body>
            <p>I have reviewed the paper entitled effect of extrusion cooking on the chemical and nutritional properties of instant flours: a review.</p>
            <p> </p>
            <p> In general, the paper is of interest and it is well written. However, the discussion according to the literature has to be improved.</p>
            <p> </p>
            <p> I do not agree with the sentence on page 3 that affirms that the parameters of extrusion are less discussed in the literature. There are many papers that compare the effect of temperature, moisture, speed screw, etc. on different compounds. Please revise this fact and add the corresponding references.</p>
            <p> </p>
            <p> The main criticism is about the values of the parameters that the authors discuss. The authors include the different values of the parameters chose in the table 1; however, these values do not appear in the other tables nor in the text.</p>
            <p> </p>
            <p> For example, in table 2. The first line the authors write that barrel temperature, moisture and screw speed affect the free sugars of wheat flour. However, they only write in the table the moisture values.</p>
            <p> </p>
            <p> This problem can be observed in all the tables. Moreover, from table 4 to 8, the values do not appear.</p>
            <p> </p>
            <p> In page 8, the authors write that table 5 demonstrates that higher screw speeds yield a greater amount of RDS&#x2026;.. However, in the 5 and in the text they do not write the values of these parameters.</p>
            <p> </p>
            <p> Something similar can be observed in the text. For example, the authors write about an increase in the temperature or moisture produce an &#x00a0;XXX&#x00a0; effect. However, it is impossible to know which the range of this increase is, or they write about milder extrusion conditions, but they do not say which are the values of the different parameter necessaries to establish these mild conditions.</p>
            <p> </p>
            <p> On page 5, the authors say that extrusion produces free-sugars. Please add an example of these sugars.</p>
            <p> </p>
            <p> In page 9 when they write about ANF, please correct the name oligosaccharides by galacto-oligosaccharides or oligosaccharides of raffinose family...</p>
            <p> </p>
            <p> Table 6. Many of these papers studied more than an ANF, please include them in the table. The raffinose and stachyose resit the intestinal hydrolysis because mammals do not have the enzyme galactosidase. Please correct the sentence.</p>
            <p> </p>
            <p> Phytic acid is not very thermosensitibe compounds.</p>
            <p> </p>
            <p> Page 11, the authors say that extrusion produced an increase of trypsin inhibitors; however there are many papers that establish the opposite trend.</p>
            <p> </p>
            <p> The extrusion reduces some ANF and the smallest amount present in the extruded products can exert a positive health effect. Please add some sentence.</p>
            <p>Is the review written in accessible language?</p>
            <p>Yes</p>
            <p>Are all factual statements correct and adequately supported by citations?</p>
            <p>Yes</p>
            <p>Are the conclusions drawn appropriate in the context of the current research literature?</p>
            <p>Partly</p>
            <p>Is the topic of the review discussed comprehensively in the context of the current literature?</p>
            <p>Partly</p>
            <p>Reviewer Expertise:</p>
            <p>Food Technology,&#x00a0; extrusion, bioactive compounds.</p>
            <p>I confirm that I have read this submission and believe that I have an appropriate level of expertise to confirm that it is of an acceptable scientific standard, however I have significant reservations, as outlined above.</p>
        </body>
        <sub-article article-type="response" id="comment10870-220802">
            <front-stub>
                <contrib-group>
                    <contrib contrib-type="author">
                        <name>
                            <surname>Pismag</surname>
                            <given-names>Remigio</given-names>
                        </name>
                        <aff>Cauca, Universidad del Cauca, Comuna 4, Cauca, Colombia</aff>
                    </contrib>
                </contrib-group>
                <author-notes>
                    <fn fn-type="conflict">
                        <p>
                            <bold>Competing interests: </bold>No competing interests were disclosed.</p>
                    </fn>
                </author-notes>
                <pub-date pub-type="epub">
                    <day>10</day>
                    <month>1</month>
                    <year>2024</year>
                </pub-date>
            </front-stub>
            <body>
                <p>I do not agree with the sentence on page 3 that affirms that the parameters of extrusion are less discussed in the literature. There are many papers that compare the effect of temperature, moisture, speed screw, etc. on different compounds. Please revise this fact and add the corresponding references.</p>
                <p> </p>
                <p> R/ Dear reviewer,</p>
                <p> </p>
                <p> In this paper, we are discussing about the reduced amount of information about the extrusion process in the develop of instant food products specifically. We carry out a searching focused on these topics: instant powders, instant porridge, instant beverages, and other same products all of them obtained by extrusion.</p>
                <p> </p>
                <p> However, we had clarified this issue on page 3 following your recommendation.</p>
                <p> </p>
                <p> The main criticism is about the values of the parameters that the authors discuss. The authors include the different values of the parameters chose in the table 1; however, these values do not appear in the other tables nor in the text.</p>
                <p> </p>
                <p> R/ We have adjusted the table with the information required. In addition, we had extended our discussion around the table 1. &#x00a0;</p>
                <p> </p>
                <p> For example, in table 2. The first line the authors write that barrel temperature, moisture and screw speed affect the free sugars of wheat flour. However, they only write in the table the moisture values.</p>
                <p> </p>
                <p> R/ We have adjusted the table with the information required.</p>
                <p> </p>
                <p> This problem can be observed in all the tables. Moreover, from table 4 to 8, the values do not appear.</p>
                <p> </p>
                <p> </p>
                <p> R/ We have adjusted the tables with the information required.</p>
                <p> </p>
                <p> In page 8, the authors write that table 5 demonstrates that higher screw speeds yield a greater amount of RDS&#x2026;.. However, in the 5 and in the text they do not write the values of these parameters.</p>
                <p> </p>
                <p> </p>
                <p> R/ We have adjusted the tables with the information required.</p>
                <p> </p>
                <p> Something similar can be observed in the text. For example, the authors write about an increase in the temperature or moisture produce an &#x00a0;XXX&#x00a0; effect. However, it is impossible to know which the range of this increase is, or they write about milder extrusion conditions, but they do not say which are the values of the different parameter necessaries to establish these mild conditions.</p>
                <p> R/ We have adjusted all the tables with the information required. We are following your recommendation.</p>
                <p> </p>
                <p> </p>
                <p> On page 5, the authors say that extrusion produces free-sugars. Please add an example of these sugars.</p>
                <p> </p>
                <p> </p>
                <p> R/ We describe the type of sugars generated during extrusion of cereal flours and we added examples of free sugars reported in extrusion of legume flours.</p>
                <p> </p>
                <p> In page 9 when they write about ANF, please correct the name oligosaccharides by galacto-oligosaccharides or oligosaccharides of raffinose family...</p>
                <p> </p>
                <p> </p>
                <p> R/ We are following your recommendations, and this issue was fitted.</p>
                <p> </p>
                <p> Table 6. Many of these papers studied more than an ANF, please include them in the table. The raffinose and stachyose resit the intestinal hydrolysis because mammals do not have the enzyme galactosidase. Please correct the sentence.</p>
                <p> </p>
                <p> </p>
                <p> R/ We added the ANFs available in the papers and all of them were included. On the other hand, we included the sentence adjusted in our discussion.</p>
                <p> </p>
                <p> </p>
                <p> Phytic acid is not very thermosensitibe compounds.</p>
                <p> </p>
                <p> </p>
                <p> R/ We are following your recommendations, and this issue was fitted.</p>
                <p> </p>
                <p> </p>
                <p> Page 11, the authors say that extrusion produced an increase of trypsin inhibitors; however there are many papers that establish the opposite trend.</p>
                <p> </p>
                <p> </p>
                <p> R/ We have fitted this issue, and we have explained the soft extrusion condition promotes the release and preservation of trypsin inhibitors.</p>
                <p> </p>
                <p> The extrusion reduces some ANF and the smallest amount present in the extruded products can exert a positive health effect. Please add some sentence.</p>
                <p> </p>
                <p> R/ We are following your recommendations, and we added a sentence.</p>
            </body>
        </sub-article>
    </sub-article>
</article>
