<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-04-29T04:29:41Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/4322" metadataPrefix="oai_dc">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/4322</identifier><datestamp>2022-04-29T12:02:46Z</datestamp><setSpec>com_10259_4244</setSpec><setSpec>com_10259_5086</setSpec><setSpec>com_10259_2604</setSpec><setSpec>col_10259_4245</setSpec></header><metadata><oai_dc:dc xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dc="http://purl.org/dc/elements/1.1/" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd">
<dc:title>Kinetic study and kinetic parameters of lipase‐catalyzed glycerolysis of sardine oil in a homogeneous medium</dc:title>
<dc:creator>García Solaesa, Ángela</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Melgosa Gómez, Rodrigo</dc:creator>
<dc:subject>Lipase</dc:subject>
<dc:subject>Glycerolysis</dc:subject>
<dc:subject>Tert-butanol</dc:subject>
<dc:subject>Mass transfer</dc:subject>
<dc:subject>Kinetic model</dc:subject>
<dc:subject>Chemical engineering</dc:subject>
<dc:subject>Ingeniería química</dc:subject>
<dc:description>The production of polyunsaturated fatty acids (PUFAs) concentrates by enzymatic catalysis has&#xd;
gained interest due to their stereospecificity and the milder conditions employed compared to the&#xd;
use of inorganic catalysts. The enzymatic glycerolysis of sardine oil by Lipozyme 435 to get PUFA&#xd;
concentrates in the forms of di‐ and monoacylglycerols (DAGs, MAGs) in an optimized amount of&#xd;
tert‐butanol as the organic solvent was studied. First, mass transfer limitation of the reaction system&#xd;
was analyzed. The effects of different operating variables such as lipase loading, temperature&#xd;
and feed composition were investigated. A semi‐empirical kinetic model based on the reversible&#xd;
elementary reactions of glycerolysis and hydrolysis of the glycerides was employed to correlate the&#xd;
experimental kinetic data. A molar ratio glycerol:oil of 3:1 was the optimum, which produced more&#xd;
than 84 wt% of MAG at 323 K. A comparison with other glycerolysis systems was performed using&#xd;
MAG yield, reaction rate and significance of kinetic parameters.</dc:description>
<dc:description>Spanish Government through MINECO&#xd;
(CTQ2012‐39131‐C02‐01)</dc:description>
<dc:date>2017-02-02T11:31:31Z</dc:date>
<dc:date>2018-04-01T02:45:06Z</dc:date>
<dc:date>2016-04</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:type>info:eu-repo/semantics/acceptedVersion</dc:type>
<dc:identifier>0253-9837</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/4322</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Chinese Journal of Catalysis. 2016,  V. 37, n. 4, p. 596–606</dc:relation>
<dc:relation>http://dx.doi.org/10.1016/S1872-2067(15)61040-3</dc:relation>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 International</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:format>application/pdf</dc:format>
<dc:publisher>Elsevier</dc:publisher>
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