<?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>2026-05-12T02:46:29Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/6657" metadataPrefix="dim">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/6657</identifier><datestamp>2022-05-20T13:22:04Z</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="aad9756c-ad87-4f31-ba02-459668ce3469" confidence="600" orcid_id="">Alonso Riaño, Patricia</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="357" confidence="600" orcid_id="">Melgosa Gómez, Rodrigo</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="557" confidence="600" orcid_id="">Trigueros Andrés, Ester</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="296" confidence="600" orcid_id="">Illera Gigante, Alba Ester</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="57" confidence="600" orcid_id="">Beltrán Calvo, Sagrario</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="530" confidence="600" orcid_id="">Sanz Díez, Mª Teresa</dim:field>
<dim:field mdschema="dc" element="date" qualifier="accessioned">2022-05-16T09:14:39Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="available">2022-05-16T09:14:39Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="issued">2022</dim:field>
<dim:field mdschema="dc" element="identifier" qualifier="uri">http://hdl.handle.net/10259/6657</dim:field>
<dim:field mdschema="dc" element="description" lang="es">Póster presentado en: EIFS2022, the 2nd Iberian Meeting on Supercritical Fluids (2º Encontro Ibérico de Fluidos Supercríticos / 2º Encuentro Ibérico de Fluidos Supercríticos), to be held on 28.February - 2.March 2022 in Coimbra, Portugal.</dim:field>
<dim:field mdschema="dc" element="description" qualifier="abstract" lang="en">Brewer’s spent grain (BSG) is one of the most important by-products in large and small-&#xd;
scale breweries. BSG is the solid residue generated after mashing and wort filtration&#xd;
&#xd;
process, it is generated at an average rate of 20 kg per 100 L of beer and accounts for&#xd;
approximately 85 % of the total residues of the brewing process [4]. Nowadays, it is&#xd;
mainly used for animal feed (70 %), biogas production (10 %), or landfilled [5].&#xd;
However, BSG presents a valuable chemical composition with a high content of protein&#xd;
and carbohydrates, as well as important quantities of phenolic compounds with potential&#xd;
bioactive properties. BSG also contains non-negligible amount of lipids (5 %) with more&#xd;
than 50 % being linoleic acid (C18:2 ω-6) [6].&#xd;
Due to the valuable chemical composition of BSG, different techniques have been&#xd;
proposed to valorize this lignocellulosic biomass, such as enzymatic and chemical&#xd;
hydrolysis, ultrasound assisted extraction or microwave assisted extraction [7]. High&#xd;
pressure processing of biomass has been also proposed since it offers unique opportunities&#xd;
in the extraction and valorization of the bioactive compounds of BSG. Among the different high-pressure processes, the use of supercritical CO2 (sc-CO2)&#xd;
presents a great attractive since it is considered a green solvent and it presents gas-like&#xd;
(high diffusivities) and liquid-like (good solvation power) properties at supercritical&#xd;
conditions (Tc = 31.1 oC pc= 7.39 MPa). Sc-CO2 has been extensively studied as a green&#xd;
extracting agent over traditional organic solvents to valorize the lipophilic fraction of&#xd;
biomass [8].&#xd;
From a biorefinery perspective and aiming at the integral valorization of BSG, sc-CO2&#xd;
extraction and enzymatic hydrolysis processes have been applied to this by-product. First,&#xd;
the extraction of the lipophilic fraction of BSG with sc-CO2 has been systematically&#xd;
studied. The most influential extraction conditions, namely pressure and temperature,&#xd;
were varied from 20 to 40 MPa and from 313 to 353 K, respectively. A maximum yield&#xd;
of 5.70 ± 0.07 g /100 gBSG was obtained at 353 K and 40 MPa (see Graphical abstract, Fig.&#xd;
a)). High pressures and temperatures resulted in higher content of total phenolic and&#xd;
flavonoids compounds, as well as higher antioxidant capacity.&#xd;
Enzymatic hydrolysis was performed on samples after sc-CO2 treatment and non-treated&#xd;
BSG samples. Enzymatic hydrolysis was carried out at 323 K in an acetate buffer at pH=5&#xd;
with a cellulase, 1,4-(1,3:1,4)-β-D-Glucan 4-glucanohydrolase, EC 3.2.1.4, from&#xd;
Aspergillus niger provided by Sigma-Aldrich.&#xd;
&#xd;
The graphical abstract b) represents the glucose yield along enzymatic hydrolysis for sc-&#xd;
CO2 treated and non-treated BSG at different enzyme concentrations. An improvement of&#xd;
&#xd;
the enzymatic hydrolysis yield by cellulase was observed in the sc-CO2 treated BSG&#xd;
compared to the non-treated. This improvement could be partially attributed to the&#xd;
removal of the lipid fraction and to morphological changes of BSG after sc-CO2. Based&#xd;
on this double benefit, sc-CO2 can play an important role on biomass valorization [8].</dim:field>
<dim:field mdschema="dc" element="description" qualifier="sponsorship" lang="en">AEI [PID2019-104950RB-I00 and PID2020-116716RJ-I00] and JCyL and ERDF [BU050P20]. P. AlonsoRiaño and E. Trigueros acknowledge funding from JCyL and ESF [Orden EDU/556/2019 and EDU/574/2018, respectively]. R.&#xd;
Melgosa is supported by a Beatriz Galindo Research Fellowship [BG20/00182]. Ó. Benito-Román post-doctoral contract was funded&#xd;
by AEI [PID2020-116716RJ-I00/AEI/10.13039/501100011033]. A.E. Illera post-doctoral contract was funded by JCyL and ERDF&#xd;
[BU050P20].</dim:field>
<dim:field mdschema="dc" element="format" qualifier="mimetype">application/pdf</dim:field>
<dim:field mdschema="dc" element="language" qualifier="iso" lang="es">eng</dim:field>
<dim:field mdschema="dc" element="subject" qualifier="other" lang="es">Ingeniería química</dim:field>
<dim:field mdschema="dc" element="subject" qualifier="other" lang="en">Chemical engineering</dim:field>
<dim:field mdschema="dc" element="title" lang="en">Supercritical carbon dioxide extraction of brewer´s spent grain (BSG)</dim:field>
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