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<dc:title>Modification of brewer’s spent grain after sc-CO2 extraction: improvement of sugar and phenolic compounds release</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>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 the solid by-product generated in breweries after the&#xd;
mashing and wort filtration process. It comprises about 85 % of the total by-products,&#xd;
generating approximately 20 kg per 100 L [1]. BSG presents a valuable chemical&#xd;
composition with a high content of protein and carbohydrates, 5 % of lipids and an&#xd;
important source of phenolic compounds. Among the different techniques proposed to&#xd;
valorize BSG, supercritical CO2 (sc-CO2) has become a promising technology to process&#xd;
biomass. The main aim of this work was to assess the effect of sc-CO2, after BSG oil&#xd;
extraction, on the subsequent enzymatic hydrolysis to hydrolyze the polysaccharide&#xd;
fraction into monomeric sugars by comparing the sugar yields of sc-CO2 and non-scCO2&#xd;
treated BSG.&#xd;
After sc-CO2 treatment at 40 MPa and 80 oC, the raffinate obtained was subjected to&#xd;
enzymatic hydrolysis by cellulase at different enzyme dose. At the sc-CO2 extraction the&#xd;
carbohydrate fraction remained in the raffinate phase after extraction. Glucose yield&#xd;
increased with enzyme concentration for non-treated and sc-CO2 treated BSG. Higher&#xd;
yields of glucose were obtained for sc-CO2 treated compared to non-treated sc-CO2 for all&#xd;
the enzymes concentrations. The percentage increase in glucose yield for sc-CO2 treated&#xd;
and non-treated BSG was 8, 14 and 18 % for the three cellulase concentrations essayed&#xd;
in this work, 0.25, 0.5 and 1 %, respectively. The hydrolysis kinetics for xylose and&#xd;
arabinose have been also determined for non-treated and sc-CO2 treated BSG at 1 % of&#xd;
cellulase dose. Although not big differences were observed in the final sugar yield in the&#xd;
hydrolysates, the initial hydrolysis rate were significant higher for the sc-CO2 treated BSG&#xd;
than for the untreated samples. The higher enzymatic hydrolysis rate and yield obtained in the raffinate-BSG after sc-&#xd;
CO2 treatment compared with non-treated BSG could be attributed partially to the removal&#xd;
&#xd;
of the lipid fraction. As it has been described in literature [2], fats and oils could influence&#xd;
the susceptibility of carbohydrates to enzymes. This improvement was also due to surface&#xd;
morphology modification. The structural and chemical changes of untreated and sc-CO2&#xd;
treated BSG was assessed by scanning electron microscopy and X-ray powder diffraction&#xd;
(XRD). Although the XRD pattern after sc-CO2 treatment indicated that the pre-treatment&#xd;
was not strong enough to modify the BSG crystallinity, the raffinate exhibited an irregular&#xd;
porosity and lamellar structure. sc-CO2 broke partially some structural barriers allowing&#xd;
a better enzyme access.&#xd;
Furthermore, some phenolic compounds were determined in the enzymatic hydrolysates&#xd;
at the end of the hydrolysis by using 1 % of cellulase (Table 1). It was observed that for&#xd;
p-coumaric acid and ferulic acid, a concentration 31 and 24 % higher, respectively, was&#xd;
obtained in the BSG hydrolysates after sc-CO2 treatment, while for vanillin similar&#xd;
concentration was obtained in both hydrolysates. The concentration of p-coumaric acid&#xd;
and vanillin after cellulase hydrolysis was lower than the values previously reported for&#xd;
the same BSG by alkaline, xylanase (1%) and subcritical water hydrolysis [3], [4].&#xd;
Nevertheless, for ferulic acid, only a higher value was reached for alkaline hydrolysis.</dc:description>
<dc:description>JCyL and ERDF for financial support of project BU050P20&#xd;
Agencia Estatal de Investigación for financial support of project PID2019-104950RB-I00 / AEI / 10.13039/501100011033&#xd;
JCyL and ESF for E. Trigueros (ORDEN EDU/574/2018) and P. Alonso-Riaño predoctoral (EDU/556/2019) contracts&#xd;
R. Melgosa is supported by a Beatriz Galindo Research Fellowship [BG20/00182]</dc:description>
<dc:date>2022-05-16T09:15:00Z</dc:date>
<dc:date>2022-05-16T09:15:00Z</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/10259/6658</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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