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<dc:title>Supercritical carbon dioxide extraction of brewer´s spent grain (BSG)</dc:title>
<dc:creator>Alonso Riaño, Patricia</dc:creator>
<dc:creator>Melgosa Gómez, Rodrigo</dc:creator>
<dc:creator>Trigueros Andrés, Ester</dc:creator>
<dc:creator>Benito Román, Oscar</dc:creator>
<dc:creator>Illera Gigante, Alba Ester</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:subject>Ingeniería química</dc:subject>
<dc:subject>Chemical engineering</dc:subject>
<dc:description>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.</dc:description>
<dc:description>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].</dc:description>
<dc:description>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].</dc:description>
<dc:date>2022-05-16T09:14:39Z</dc:date>
<dc:date>2022-05-16T09:14:39Z</dc:date>
<dc:date>2022</dc:date>
<dc:type>info:eu-repo/semantics/conferenceObject</dc:type>
<dc:type>info:eu-repo/semantics/acceptedVersion</dc:type>
<dc:identifier>http://hdl.handle.net/10259/6657</dc:identifier>
<dc:language>eng</dc:language>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:format>application/pdf</dc:format>
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