<?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>2026-04-22T21:30:35Z</responseDate><request verb="GetRecord" identifier="oai:uvadoc.uva.es:10324/65631" metadataPrefix="mods">https://uvadoc.uva.es/oai/request</request><GetRecord><record><header><identifier>oai:uvadoc.uva.es:10324/65631</identifier><datestamp>2026-03-25T09:44:29Z</datestamp><setSpec>com_10324_1185</setSpec><setSpec>com_10324_931</setSpec><setSpec>com_10324_894</setSpec><setSpec>col_10324_1346</setSpec></header><metadata><mods:mods xmlns:mods="http://www.loc.gov/mods/v3" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.loc.gov/mods/v3 http://www.loc.gov/standards/mods/v3/mods-3-1.xsd">
<mods:name>
<mods:namePart>Fernández Requejo, Patricia</mods:namePart>
</mods:name>
<mods:name>
<mods:namePart>Gómez, Elena</mods:namePart>
</mods:name>
<mods:name>
<mods:namePart>Calvar, Noelia</mods:namePart>
</mods:name>
<mods:name>
<mods:namePart>Domínguez, Ángeles</mods:namePart>
</mods:name>
<mods:extension>
<mods:dateAvailable encoding="iso8601">2024-02-03T11:27:35Z</mods:dateAvailable>
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<mods:extension>
<mods:dateAccessioned encoding="iso8601">2024-02-03T11:27:35Z</mods:dateAccessioned>
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<mods:originInfo>
<mods:dateIssued encoding="iso8601">2015</mods:dateIssued>
</mods:originInfo>
<mods:identifier type="citation">Industrial &amp; Engineering Chemistry Research 54 (2015) 1342-1349</mods:identifier>
<mods:identifier type="issn">0888-5885</mods:identifier>
<mods:identifier type="uri">https://uvadoc.uva.es/handle/10324/65631</mods:identifier>
<mods:identifier type="doi">10.1021/ie5040489</mods:identifier>
<mods:identifier type="publicationfirstpage">1342</mods:identifier>
<mods:identifier type="publicationissue">4</mods:identifier>
<mods:identifier type="publicationlastpage">1349</mods:identifier>
<mods:identifier type="publicationtitle">Industrial &amp; Engineering Chemistry Research</mods:identifier>
<mods:identifier type="publicationvolume">54</mods:identifier>
<mods:identifier type="essn">1520-5045</mods:identifier>
<mods:abstract>The ionic liquids 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate, [BMpyr][TfO], 1-butyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, [BMpyr][NTf2], and 1-butyl-1-methylpyrrolidinium dicyanamide, [BMpyr]- [DCA], have been studied as solvents for the extraction of benzene from its  mixtures with several aliphatic hydrocarbons. The liquid−liquid equilibrium (LLE) of the ternary systems {octane (1) + benzene (2) + [BMpyr][TfO] (3)}, {decane (1) + benzene (2) + [BMpyr][TfO] (3)}, {dodecane (1) + benzene (2) + [BMpyr][TfO] (3)}, {dodecane (1) + benzene (2) + [BMpyr][NTf2] (3)}, and {dodecane (1) + benzene (2) + [BMpyr][DCA] (3)} at T = 298.15 K and atmospheric pressure was carried out. The solute distribution ratio and selectivity values derived from the tie-lines were used to evaluate if the studied ionic liquids can be used as extraction solvents, and the obtained values were compared with those found in the literature for the traditional organic solvents. Finally, experimental LLE data for the ternary mixtures were correlated by means of the non-random two-liquid (NRTL) thermodynamic model.</mods:abstract>
<mods:language>
<mods:languageTerm>eng</mods:languageTerm>
</mods:language>
<mods:accessCondition type="useAndReproduction">info:eu-repo/semantics/restrictedAccess</mods:accessCondition>
<mods:accessCondition type="useAndReproduction">http://creativecommons.org/licenses/by-nc-nd/4.0/</mods:accessCondition>
<mods:accessCondition type="useAndReproduction">ACS Publications</mods:accessCondition>
<mods:accessCondition type="useAndReproduction">Attribution-NonCommercial-NoDerivatives 4.0 Internacional</mods:accessCondition>
<mods:titleInfo>
<mods:title>Application of Pyrrolidinium-Based Ionic Liquid as Solvent for the Liquid Extraction of Benzene from Its Mixtures with Aliphatic Hydrocarbons</mods:title>
</mods:titleInfo>
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