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<dc:title>Valorization of brewer’s spent grain by furfural recovery/removal from subcritical water hydrolysates by pervaporation</dc:title>
<dc:creator>Alonso Riaño, Patricia</dc:creator>
<dc:creator>Illera Gigante, Alba Ester</dc:creator>
<dc:creator>Amândio, Mariana S.T.</dc:creator>
<dc:creator>Xavier, Ana María Rebelo Barreto</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:subject>Brewer's spent grain</dc:subject>
<dc:subject>Subcritical water hydrolysates</dc:subject>
<dc:subject>Pervaporation</dc:subject>
<dc:subject>PDMS/POMS membranes</dc:subject>
<dc:subject>Furfural</dc:subject>
<dc:description>This work is focused on the development of a sustainable process for the valorisation of the main by-product&#xd;
generated in the brewing industry, the brewer’s spent grain (BSG). A two-step process combining subcritical&#xd;
water treatment and pervaporation (PV) was proposed to hydrolyse the hemicelluloses fraction of this lignocellulosic biomass and further removal/recovery of some of the degradation products of sugars by using two&#xd;
different organophilic membranes, polydimethylsiloxane (PDMS) and polyoctilmethylsiloxane (POMS) membranes. Specifically, furfural is the dehydration product of pentoses and it is one of the top biomass-based&#xd;
chemicals being an important platform chemical. For synthetic binary mixtures, lower total permeation flux&#xd;
but higher enrichment factors for furfural were determined for POMS. When dealing with subW hydrolysates,&#xd;
POMS membranes yielded the highest furfural recovery, 94.1 %, with permeate concentrations as high as 40 g⋅L1&#xd;
. Furthermore, it was assessed that PV is a suitable detoxification method that yielded a retentate nearly free of&#xd;
furfural allowing its use as growth media in the opposite to the subW hydrolysate with inhibitory furfural&#xd;
concentrations for microbial bioprocesses.</dc:description>
<dc:date>2023-02-13T11:41:51Z</dc:date>
<dc:date>2023-02-13T11:41:51Z</dc:date>
<dc:date>2023-03</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>1383-5866</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/7442</dc:identifier>
<dc:identifier>10.1016/j.seppur.2022.123008</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Separation and Purification Technology. 2023, V. 309, 123008</dc:relation>
<dc:relation>https://doi.org/10.1016/j.seppur.2022.123008</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:relation>info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica, Técnica y de Innovación 2021-2023/TED2021-129311B-I00/ES/Tecnologías verdes basadas en el empleo de fluidos presurizados para valorizar biomasa lignocelulósica mediante la producción de furfural/</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica, Técnica y de Innovación 2021-2023/PDC2022-133443-I00/ES/Diseño de un prototipo para la extracción de bioproductos con agua subcrítica/</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/FCT//UIDB%2F50011%2F2020/PT/</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/FCT//UIDP%2F50011%2F2020/PT/</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/FCT//LA%2FP%2F0006%2F2020/PT/</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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