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<dc:title>Membrane fractionation of hydrolysates of the water-soluble protein from tuna fish meal obtained by subcritical water and enzymatic treatments. Comparison of physical and chemical properties</dc:title>
<dc:creator>Barea Gómez, Pedro</dc:creator>
<dc:creator>Illera Gigante, Alba Ester</dc:creator>
<dc:creator>Candela Gil, Helena</dc:creator>
<dc:creator>Melgosa Gómez, Rodrigo</dc:creator>
<dc:creator>Benito Moreno, José Manuel</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:subject>Protein hydrolysis</dc:subject>
<dc:subject>Dead-end fltration (UF and NF)</dc:subject>
<dc:subject>Protein and Free amino acids profle</dc:subject>
<dc:subject>Reducing and chelating capacities</dc:subject>
<dc:subject>Molecular weight distribution</dc:subject>
<dc:description>Two different hydrolysates of the water-soluble protein (WSP) fraction from tuna fish meal were obtained by subcritical water-CO2 (subW-CO2) and Alcalase® treatments. Hydrolysates showed different chemical composition regarding their free amino acid (FAA) profile and molecular weight distribution of the peptides generated. Consequently, different strategies were proposed by using a stirred dead-end filtration system equipped with flat sheet membranes. Two nanofiltration (NF) consecutive steps were proposed for fractionation of subW-CO2 hydrolysates with polyamide membranes (800–600 Da and 300–150 Da) yielding a first retentate where 79% of the protein fraction was retained, while 92% of FAA were retained in the second step with a purity index of 29%. Alcalase® hydrolysates were fractionated by ultrafiltration (UF, 10 kDa) followed by NF (1–1.1 kDa) with polyethersulfone membranes obtaining a first retentate with more than 65% of protein fraction retention with a purity index of 50%. A relatively wide molecular weight distribution was observed in all streams, with high antioxidant and iron-chelating capacities in the retentate fractions.</dc:description>
<dc:date>2025-05-08T10:50:13Z</dc:date>
<dc:date>2025-05-08T10:50:13Z</dc:date>
<dc:date>2025-03</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>2197-4365</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/10443</dc:identifier>
<dc:identifier>10.1186/s40643-025-00850-3</dc:identifier>
<dc:identifier>2197-4365</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Bioresources and Bioprocessing. 2025, V. 12, n. 16</dc:relation>
<dc:relation>https://doi.org/10.1186/s40643-025-00850-3</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>Springer</dc:publisher>
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