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<dc:title>Filtration of subcritical water hydrolysates from red macroalgae byproducts with ultraporous ceramic membranes for oligosaccharide and peptide fractionation</dc:title>
<dc:creator>Trigueros Andrés, Ester</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Ruiz Pérez, María Olga</dc:creator>
<dc:subject>Peptide purification</dc:subject>
<dc:subject>Oligosaccharide recovery</dc:subject>
<dc:subject>Membrane fouling</dc:subject>
<dc:subject>Macroalga byproducts</dc:subject>
<dc:subject>Biorefinery</dc:subject>
<dcterms:abstract>An ultrafiltration-based process for oligosaccharide and peptide fractionation from a macroalgae subcritical&#xd;
water hydrolysate was studied. A wide range of separation results was obtained depending on the membrane&#xd;
pore. 100 kDa cut-off size was enough for hydrolysate clarification with total retention of colloidal materials.&#xd;
Oligosaccharides present in the hydrolysate showed the highest retention with all membranes, glucans mostly,&#xd;
followed by galactans, and finally arabinans. Peptides obtained after subcritical water treatment were some of&#xd;
the lowest rejected compounds, even using a 5 kDa membrane. The increase in temperature from 20 to 50 ◦C and&#xd;
feed flow rate from 6.6 to 11.2 L/h enhanced permeate flux for 5 kDa membrane, without perturbing the&#xd;
membrane retention. The Hermia’s models identified the cake layer resistance as the major fouling resistance in&#xd;
hydrolysate filtrations at 20 ◦C, but standard pore blockage was the principal fouling mechanism at 50 ◦C. A&#xd;
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&#xd;
final permeate collected from the 1 kDa membrane was freeze-dried to obtain a peptide-rich solid (71 wt%) that&#xd;
could be used in different applications.</dcterms:abstract>
<dcterms:dateAccepted>2023-02-14T08:41:32Z</dcterms:dateAccepted>
<dcterms:available>2023-02-14T08:41:32Z</dcterms:available>
<dcterms:created>2023-02-14T08:41:32Z</dcterms:created>
<dcterms:issued>2022-10</dcterms:issued>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>0376-7388</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/7453</dc:identifier>
<dc:identifier>10.1016/j.memsci.2022.120822</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Journal of Membrane Science. 2022, V. 660, 120822</dc:relation>
<dc:relation>https://doi.org/10.1016/j.memsci.2022.120822</dc:relation>
<dc:relation>info: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/</dc:relation>
<dc:relation>info: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/</dc:relation>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 Internacional</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
</qdc:qualifieddc></metadata></record></GetRecord></OAI-PMH>