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dc.contributor.authorWestman, Snorre Foss
dc.contributor.authorStang, Hans Georg Jacob
dc.contributor.authorLøvseth, Sigurd Weidemann
dc.contributor.authorAustegard, Anders
dc.contributor.authorSnustad, Ingrid
dc.contributor.authorStørset, Sigmund Østtveit
dc.contributor.authorErtesvåg, Ivar Ståle
dc.date.accessioned2015-12-22T10:35:46Z
dc.date.accessioned2016-02-08T13:57:14Z
dc.date.available2015-12-22T10:35:46Z
dc.date.available2016-02-08T13:57:14Z
dc.date.issued2015
dc.identifier.citationFluid Phase Equilibria 2015, 409:207-241nb_NO
dc.identifier.issn0378-3812
dc.identifier.urihttp://hdl.handle.net/11250/2377395
dc.description.abstractA new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for carbon capture and storage (CCS) transport conditions is presented. An isothermal analytical method with a variable volume cell is used. The apparatus is capable of highly accurate measurements in terms of pressure, temperature and composition, also in the critical region. Vapor-liquid equilibrium (VLE) measurements for the binary system CO2+N2 are reported at 223, 270, 298 and 303 K, with estimated standard uncertainties of maximum 0.006 K in the temperature, maximum 0.003 MPa in the pressure, and maximum 0.0004 in the mole fractions of the phases. These measurements are verified against existing data. Although some data exists, there is little trustworthy data around critical conditions, and our data indicate a need to revise the parameters of existing models. A fit made against our data of the vapor-liquid equilibrium prediction of GERG-2008/EOS-CG for CO2+N2 is presented. At 223 and 298 K, the critical region of the isotherm are fitted using a scaling law, and high accuracy estimates for the critical composition and pressure are found.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.titleVapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPanb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewed
dc.date.updated2015-12-22T10:35:46Z
dc.description.versionacceptedVersion
dc.source.volume409nb_NO
dc.source.journalFluid Phase Equilibrianb_NO
dc.identifier.doi10.1016/j.fluid.2015.09.034
dc.identifier.cristin1278561
dc.description.localcode© 2015 Elsevier B.V. All rights reserved. This is the authors' accepted and refereed manuscript to the article. Locked until 2017-09-25.nb_NO


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