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dc.contributor.authorTrigueros Andrés, Ester 
dc.contributor.authorSanz Díez, Mª Teresa 
dc.contributor.authorBeltrán Calvo, Sagrario 
dc.contributor.authorRuiz Pérez, María Olga 
dc.date.accessioned2023-02-14T08:41:32Z
dc.date.available2023-02-14T08:41:32Z
dc.date.issued2022-10
dc.identifier.issn0376-7388
dc.identifier.urihttp://hdl.handle.net/10259/7453
dc.description.abstractAn ultrafiltration-based process for oligosaccharide and peptide fractionation from a macroalgae subcritical water hydrolysate was studied. A wide range of separation results was obtained depending on the membrane pore. 100 kDa cut-off size was enough for hydrolysate clarification with total retention of colloidal materials. Oligosaccharides present in the hydrolysate showed the highest retention with all membranes, glucans mostly, followed by galactans, and finally arabinans. Peptides obtained after subcritical water treatment were some of the lowest rejected compounds, even using a 5 kDa membrane. The increase in temperature from 20 to 50 ◦C and feed flow rate from 6.6 to 11.2 L/h enhanced permeate flux for 5 kDa membrane, without perturbing the membrane retention. The Hermia’s models identified the cake layer resistance as the major fouling resistance in hydrolysate filtrations at 20 ◦C, but standard pore blockage was the principal fouling mechanism at 50 ◦C. A fractionation process with sequential filtration stages at 20 ◦C and TMP = 1.1 bar was examined. Oligosaccharides were fractionated in the retentates of the sequential filtrations with 100, 5 and 1 kDa membranes. The final permeate collected from the 1 kDa membrane was freeze-dried to obtain a peptide-rich solid (71 wt%) that could be used in different applications.en
dc.description.sponsorshipThe authors gratefully acknowledge the financial support provided by the Agencia Estatal de Investigación [grant number PID2019–104950RB-I00/AEI/10.13039/501100011033] and by the Junta de Castilla y León (JCyL) and the European Regional Development Fund (ERF) [grant number BU050P20]. E. Trigueros predoctoral contract was funded by the JCyL and the European Social Fund (ESF) by ORDEN EDU/574/2018.en
dc.format.mimetypeapplication/pdf
dc.language.isoenges
dc.publisherElsevieren
dc.relation.ispartofJournal of Membrane Science. 2022, V. 660, 120822en
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectPeptide purificationen
dc.subjectOligosaccharide recoveryen
dc.subjectMembrane foulingen
dc.subjectMacroalga byproductsen
dc.subjectBiorefineryen
dc.subject.otherQuímica orgánicaes
dc.subject.otherChemistry, Organicen
dc.subject.otherIngeniería químicaes
dc.subject.otherChemical engineeringen
dc.titleFiltration of subcritical water hydrolysates from red macroalgae byproducts with ultraporous ceramic membranes for oligosaccharide and peptide fractionationen
dc.typeinfo:eu-repo/semantics/articlees
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses
dc.relation.publisherversionhttps://doi.org/10.1016/j.memsci.2022.120822es
dc.identifier.doi10.1016/j.memsci.2022.120822
dc.relation.projectIDinfo:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020/PID2019-104950RB-I00/ES/VALORIZACION DE SUBPRODUCTOS MARINOS MEDIANTE TECNOLOGIAS DE FLUIDOS SUB- Y SUPERCRITICOS PARA LA OBTENCION DE BIOCOMPUESTOS VALIOSOS/es
dc.relation.projectIDinfo:eu-repo/grantAgreement/Junta de Castilla y León//BU050P20//Valorización de la fracción proteica de subproductos de la industria agroalimentaria de Castilla y León mediante tecnologías de fluidos presurizados/es
dc.journal.titleJournal of Membrane Scienceen
dc.volume.number660es
dc.type.hasVersioninfo:eu-repo/semantics/publishedVersiones


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