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<dc:title>Isoflavone-rich extracts from okara using supercritical fluid extraction: Kinetic modeling and characterization</dc:title>
<dc:creator>Díaz de Cerio Alonso de Mezquía, Elixabet</dc:creator>
<dc:creator>Barea Gómez, Pedro</dc:creator>
<dc:creator>Melgosa Gómez, Rodrigo</dc:creator>
<dc:creator>Illera Gigante, Alba Ester</dc:creator>
<dc:creator>Sanz, María Teresa</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:subject>Okara</dc:subject>
<dc:subject>Soybean by-product</dc:subject>
<dc:subject>Supercritical fluid extraction</dc:subject>
<dc:subject>Isoflavones</dc:subject>
<dc:subject>Tocopherols</dc:subject>
<dc:description>The lipid fraction and bioactive compounds from okara, a by-product of soybean processing, have been extracted&#xd;
by supercritical fluid extraction. The effect of operating parameters, pressure (20–40 MPa), temperature (40–80&#xd;
ºC), and cosolvent usage (0–10 %wt. ethanol), on the extraction kinetics has been investigated, satisfactorily&#xd;
correlating the experimental data to the Sovov´&#xd;
a’s model. Extraction yield by SFE ranged from 0.1014 g extract/g&#xd;
insoluble solid (IS) at 20 MPa and 80 ºC to 0.1081 g extract/g IS at 30 MPa and 60 ºC (from 9.2 to 9.8 g extract/100 g okara, respectively), similar to Soxhlet extraction with n-hexane (9.2 ± 0.2 g extract/100 g). Pressure&#xd;
positively affected the initial extraction rate, which also increased with temperature except for the lowest&#xd;
pressure of 20 MPa, exhibiting a typical cross-over behavior. The use of ethanol as cosolvent promoted the extraction of phenolic compounds and isoflavones, and was less important in the extraction of tocopherols. Extraction yield using ethanol increased up to 0.1100 g extract/g IS at 40 MPa and 40 ºC. As expected, the higher content of bioactive compounds in the sc-CO2 + ethanol extracts positively affected the antioxidant capacity, with the maximum found at 20 MPa, 40 ºC and 10 %wt. ethanol.</dc:description>
<dc:date>2025-02-11T11:56:08Z</dc:date>
<dc:date>2025-02-11T11:56:08Z</dc:date>
<dc:date>2024-12</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>0960-3085</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/10205</dc:identifier>
<dc:identifier>10.1016/j.fbp.2024.09.019</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Food and Bioproducts Processing. 2024, V. 148, p. 321-329</dc:relation>
<dc:relation>https://doi.org/10.1016/j.fbp.2024.09.019</dc:relation>
<dc:rights>http://creativecommons.org/licenses/by/4.0/</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>Atribución 4.0 Internacional</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
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