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<dc:title>Subcritical water as hydrolytic medium to recover and fractionate the protein fraction and phenolic compounds from craft brewer’s spent grain</dc:title>
<dc:creator>Alonso Riaño, Patricia</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:creator>Benito Román, Oscar</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Trigueros Andrés, Ester</dc:creator>
<dc:subject>Subcritical water extraction</dc:subject>
<dc:subject>Biorefinery</dc:subject>
<dc:subject>Breweŕs spent grain</dc:subject>
<dc:subject>Protein</dc:subject>
<dc:subject>Amino acids</dc:subject>
<dc:subject>Individual phenolic compounds</dc:subject>
<dc:subject>Antioxidant capacity</dc:subject>
<dc:description>The valorization of the brewer’s spent grain (BSG) generated in a craft beer industry was studied by subcritical water hydrolysis in a semi-continuous fixed-bed reactor. Temperature was varied from 125 to 185 °C at a constant flow rate of 4 mL/min. Biomass hydrolysis yielded a maximum of 78% of solubilized protein at 185 °C. Free amino acids presented a maximum level at 160 °C with a value of 55 mg free amino acids/gprotein-BSG. Polar amino acid presented a maximum at lower temperatures than non-polar amino acids. The maximum in total phenolic compounds was reached at 185 °C. This maximum is the same for aldehyde phenolic compounds such as vanillin, syringic and protocatechuic aldehyde; however, for hydroxycinnamic acids, such as ferulic acid and p-coumaric, the maximum was obtained at 160 °C. This allows a fractionation of the bioactive compounds. Subcritical water addresses opportunities for small breweries to be incorporated within the biorefinery concept.</dc:description>
<dc:date>2021-03-25T12:20:02Z</dc:date>
<dc:date>2021-03-25T12:20:02Z</dc:date>
<dc:date>2021-07</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>0308-8146</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/5672</dc:identifier>
<dc:identifier>10.1016/j.foodchem.2021.129264</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Food Chemistry. 2021, V. 351, 129264</dc:relation>
<dc:relation>https://doi.org/10.1016/j.foodchem.2021.129264</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/Junta de Castilla y León//BU301P18//Valorización integral de subproductos de la industria agroalimentaria mediante tecnologías emergentes (ALVALOR)</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/Junta de Castilla y León//BU050P20//Valorización de la fracción proteica de subproductos de la industria agroalimentaria de Castilla y León mediante tecnologías de fluidos presurizados</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020/PID2019-104950RB-I00/ES/VALORIZACION DE SUBPRODUCTOS MARINOS MEDIANTE TECNOLOGIAS DE FLUIDOS SUB- Y SUPERCRITICOS PARA LA OBTENCION DE BIOCOMPUESTOS VALIOSOS</dc:relation>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 Internacional</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
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