<?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>2026-04-28T17:55:28Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/4566" metadataPrefix="qdc">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/4566</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><qdc:qualifieddc xmlns:qdc="http://dspace.org/qualifieddc/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dcterms="http://purl.org/dc/terms/" xmlns:dc="http://purl.org/dc/elements/1.1/" xsi:schemaLocation="http://purl.org/dc/elements/1.1/ http://dublincore.org/schemas/xmls/qdc/2006/01/06/dc.xsd http://purl.org/dc/terms/ http://dublincore.org/schemas/xmls/qdc/2006/01/06/dcterms.xsd http://dspace.org/qualifieddc/ http://www.ukoln.ac.uk/metadata/dcmi/xmlschema/qualifieddc.xsd">
<dc:title>Phase behaviour of the pseudo-ternary system carbon dioxide + ethanol + fish oil at high pressures</dc:title>
<dc:creator>Melgosa Gómez, Rodrigo</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:creator>García Solaesa, Ángela</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:subject>Phase equilibrium</dc:subject>
<dc:subject>Supercritical carbon dioxide</dc:subject>
<dc:subject>Ethanol</dc:subject>
<dc:subject>Fish oilThermodynamic modelling</dc:subject>
<dc:subject>Peng-Robinson equation of state</dc:subject>
<dcterms:abstract>This work provides experimental fluid phase equilibrium data of the pseudo-ternary mixture CO2 + ethanol + fish oil, a system of interest in pharmaceutical and food-industry applications such as the production of omega-3-enriched lipid derivatives at mild, non-oxidative conditions. Experimental tie-lines were obtained by means of an analytical isothermal method with recirculation of the vapour phase. Measurements were carried out in the temperature range 323.15 K–343.15 K and at pressures from 10 MPa to 30 MPa. The Peng-Robinson equation of state coupled with the conventional van der Waals mixing rules with two adjustable parameters was used for experimental data correlation.</dcterms:abstract>
<dcterms:issued>2017-12</dcterms:issued>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>0021-9614</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/4566</dc:identifier>
<dc:identifier>10.1016/j.jct.2017.07.032</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>The Journal of Chemical Thermodynamics. 2017,  V. 115,  p. 106-113</dc:relation>
<dc:relation>https://doi.org/10.1016/j.jct.2017.07.032</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 International</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
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