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<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:identifier>doi:10.1016/j.jct.2016.03.026</dc:identifier><dc:language>eng</dc:language><dc:creator>Rivas, C.</dc:creator><dc:creator>Gimeno, B.</dc:creator><dc:creator>Bravo, R.</dc:creator><dc:creator>Artal, M.</dc:creator><dc:creator>Fernández, J.</dc:creator><dc:creator>Blanco, S. T.</dc:creator><dc:creator>Velasco, M. I.</dc:creator><dc:title>Thermodynamic properties of a CO2 - Rich mixture (CO2 + CH3OH) in conditions of interest for carbon dioxide capture and storage technology and other applications</dc:title><dc:identifier>ART-2016-94730</dc:identifier><dc:description>Methanol can be an impurity in transported and stored anthropogenic CO2 in carbon dioxide capture and storage technology; likewise, methanol is one of the most useful CO2 modifiers for supercritical processes. Therefore reliable values of thermodynamic properties of CO2 - rich mixtures CO2 + CH3OH are needed. We measured the following properties of a (CO2 + CH3OH) mixture with xx CO2=0.9700 in dense phase at six temperatures from 263.15 K to 313.15 K:The speed of sound, c, up to 194.49 MPa, using a double-path pulse-echo method at 5 MHz, for which a repeatability study gave an overall standard uncertainty of c, u(c) = 5.9 × 10-4c.The density, ¿, at pressures =20.00 MPa using a vibrating-tube densimeter with a standard uncertainty, u(¿) = 0.4 kg/m-3.Combining our c and ¿ experimental values and the isobaric specific heat capacity, cp, from the GERG equation of state (EoS), we calculated ¿, cp, the volume-dependent solubility parameter, dV, and the Joule-Thomson coefficient, µJT, at pressures =195.0 MPa. We are the first to report the adaptation for compressed gases of a calculation method based on numerical integration previously used only for liquids. The experimental and calculated values were compared with those from the PC-SAFT and GERG EoSs, allowing us to validate both EoSs to represent the experimental properties of the system under most conditions studied and the calculation method up to 195.0 MPa.</dc:description><dc:date>2016</dc:date><dc:source>http://zaguan.unizar.es/record/118227</dc:source><dc:doi>10.1016/j.jct.2016.03.026</dc:doi><dc:identifier>http://zaguan.unizar.es/record/118227</dc:identifier><dc:identifier>oai:zaguan.unizar.es:118227</dc:identifier><dc:identifier.citation>JOURNAL OF CHEMICAL THERMODYNAMICS 98 (2016), 272-281</dc:identifier.citation><dc:rights>by-nc-nd</dc:rights><dc:rights>http://creativecommons.org/licenses/by-nc-nd/3.0/es/</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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