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<dc:title>Liquid–Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes</dc:title>
<dc:creator>Alonso Tristán, Cristina</dc:creator>
<dc:creator>González López, Juan Antonio</dc:creator>
<dc:creator>Hevia de los Mozos, Fernando</dc:creator>
<dc:creator>García de la Fuente, Isaías</dc:creator>
<dc:creator>Cobos, José Carlos .</dc:creator>
<dcterms:abstract>Liquid−liquid equilibrium (LLE) phase diagrams&#xd;
have been determined, by means of the critical opalescence method&#xd;
with a laser scattering technique, for the mixtures 4-phenylbutan-2-&#xd;
one + CH3(CH2)nCH3 (n = 10,12,14) and for benzyl ethanoate +&#xd;
CH3(CH2)nCH3 (n = 12,14). The systems are characterized by&#xd;
having an upper critical solution temperature (UCST), which&#xd;
increases with n. The corresponding LLE curves show a rather&#xd;
horizontal top and become skewed toward higher mole fractions of&#xd;
the polar compound when n is increased. Calorimetric and LLE&#xd;
measurements show that, for mixtures with molecules with a given&#xd;
functional group, interactions between aromatic molecules are&#xd;
stronger than those between homomorphic linear molecules&#xd;
(aromaticity effect). This has been ascribed to proximity effects&#xd;
arising from the presence of the polar group and the aromatic ring within the same molecule. Proximity effects become weaker in&#xd;
the sequence 1-phenylpropan-2-one >4-phenylbutan-2-one >1-phenylethanone and are more important in benzyl ethanoate than&#xd;
in ethyl benzoate molecules. Values of the critical compositions and temperatures calculated with the DISQUAC group&#xd;
contribution model are in good agreement with the experimental results. Accordingly, the shape of the LLE curves is also&#xd;
correctly described by DISQUAC.</dcterms:abstract>
<dcterms:dateAccepted>2018-03-09T03:45:06Z</dcterms:dateAccepted>
<dcterms:available>2018-03-09T03:45:06Z</dcterms:available>
<dcterms:created>2018-03-09T03:45:06Z</dcterms:created>
<dcterms:issued>2017-03</dcterms:issued>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>0021-9568</dc:identifier>
<dc:identifier>http://hdl.handle.net/10259/4698</dc:identifier>
<dc:identifier>10.1021/acs.jced.6b00803</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Journal of Chemical and Engineering Data. 2017, V. 62, n. 3, p. 988–994</dc:relation>
<dc:relation>https://doi.org/10.1021/acs.jced.6b00803</dc:relation>
<dc:relation>info:eu-repo/grantAgreement/JCyL/BU034U16</dc:relation>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:publisher>American Chemical Society</dc:publisher>
</qdc:qualifieddc></metadata></record></GetRecord></OAI-PMH>