<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-10-03T02:56:47Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/12213" metadataPrefix="dim">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/12213</identifier><datestamp>2026-10-03T00:05:23Z</datestamp><setSpec>com_10259_4244</setSpec><setSpec>com_10259_5086</setSpec><setSpec>com_10259_2604</setSpec><setSpec>col_10259_4569</setSpec></header><metadata><dim:dim xmlns:dim="http://www.dspace.org/xmlns/dspace/dim" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.dspace.org/xmlns/dspace/dim http://www.dspace.org/schema/dim.xsd">
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="865" confidence="600" orcid_id="0000-0003-0525-327X">Barea Gómez, Pedro</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="296" confidence="600" orcid_id="0000-0001-8321-5282">Illera Gigante, Alba Ester</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="357" confidence="600" orcid_id="0000-0003-2130-2422">Melgosa Gómez, Rodrigo</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="59" confidence="600" orcid_id="0000-0002-4418-0045">Benito Román, Oscar</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="924" confidence="600" orcid_id="0009-0000-8962-4837">Candela Gil, Helena</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="57" confidence="600" orcid_id="0000-0003-2559-3925">Beltrán Calvo, Sagrario</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="530" confidence="600" orcid_id="0000-0003-1799-3099">Sanz Díez, Mª Teresa</dim:field>
<dim:field mdschema="dc" element="date" qualifier="accessioned">2026-10-02T10:24:32Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="available">2026-10-02T10:24:32Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="issued">2025</dim:field>
<dim:field mdschema="dc" element="identifier" qualifier="uri">https://hdl.handle.net/10259/12213</dim:field>
<dim:field mdschema="dc" element="description" lang="en">Póster presentado en: XVI International Scientific Agriculture Symposium "Agrosym 2025", Jahorina, Bosnia and Herzegovina, October 2-5, 2025</dim:field>
<dim:field mdschema="dc" element="description" qualifier="abstract" lang="en">The use of water under subcritical conditions (subW) for the processing of okara, a by-product of&#xd;
soybean beverage production, has promoted advancements in sustainable resource management.&#xd;
A key advantage of using water as a solvent is the elimination of the need for additional chemicals.&#xd;
Industrial okara (Frías Nutrición S.A.U., Burgos, Spain) exhibits a moisture content of 82% w/w&#xd;
and a protein content of 32% w/w. The subW process is environmentally friendly and eliminates&#xd;
the need for a drying step, thus reducing energy costs. Various stages have been proposed to&#xd;
fractionate the valuable bioactive compounds of this by-product: (1) extraction of isoflavones at&#xd;
120 °C in a batch reactor and (2) extraction and hydrolysis of proteins from the residual solid at&#xd;
higher temperatures in a semi-continuous reactor. More than 1000 μg isoflavones/g dry okara was&#xd;
obtained after 30 min at 120 °C, with the genistein family being the most abundant group. The&#xd;
residual solid was processed in a 2-liter semicontinuous extractor without drying. A total of 625&#xd;
grams of solid were placed in baskets horizontally. Water flowed at 0.82 L/min, with a residence&#xd;
time of 2.7 minutes. Two sequential temperatures were tested, 180ºC and 270ºC. At 270ºC,&#xd;
approximately 80% of the protein was hydrolyzed. Very low concentrations of degradation&#xd;
products were observed, owing to the short residence time. A medium productivity values of 1.2&#xd;
g protein/Lh was achieved in a semi-continuous plant. SubW treatment is a promising green&#xd;
chemistry approach for the sustainable valorization of by-products.</dim:field>
<dim:field mdschema="dc" element="description" qualifier="sponsorship" lang="en">This work was supported by the Spanish Research Agency (AEI) [grant number PID2022-136385OB-I00], Junta de Castilla y León (JCyL), and European Regional Development Fund (ERDF) [grant number BU027P23]. A.E. Illera postdoctoral contract was funded by BU027P23. H Candela pre-doctoral contract was funded by JCyL and the European Social Fund [ORDEN EDU/1009/2024]. P. Barea pre-doctoral contract is funded by JCyL and the European Social Fund (ESF) [ORDEN EDU/1868/2022].</dim:field>
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<dim:field mdschema="dc" element="language" qualifier="iso" lang="es">eng</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Okara</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Subcritical water</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Bio-cascade</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Protein</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Scale-up</dim:field>
<dim:field mdschema="dc" element="title" lang="en">Biocascade approach to valorize okara by using subcritical water to obtain valuable compounds: scaling up proces</dim:field>
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