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dc.contributor.authorAursand, Peder
dc.contributor.authorGjennestad, Magnus Aashammer
dc.contributor.authorAursand, Eskil
dc.contributor.authorHammer, Morten
dc.contributor.authorWilhelmsen, Øivind
dc.date.accessioned2017-02-07T14:54:44Z
dc.date.available2017-02-07T14:54:44Z
dc.date.created2016-12-20T13:39:09Z
dc.date.issued2016
dc.identifier.citationFluid Phase Equilibria. 2016, 436 98-112.nb_NO
dc.identifier.issn0378-3812
dc.identifier.urihttp://hdl.handle.net/11250/2429849
dc.description.abstractThe spinodal represents the limit of thermodynamic stability of a homogeneous fluid. In this work, we present a robust methodology to obtain the spinodal of multicomponent fluids described even with the most sophisticated equations of state (EoS) available. We elaborate how information about the spinodal and its uncertainty can contribute both in the development of modern EoS and to estimate their uncertainty in the metastable regions. Inequality constraints are presented that can be exploited in the fitting of modern EoS of single-component fluids to avoid inadmissible pseudo-stable states between the vapor and liquid spinodals. We find that even cubic EoS violate some of these constraints. Using a selection of EoS representative of modern applications, we compare vapor and liquid spinodal curves, superheat and supersaturation limits from classic nucleation theory (CNT), and available experimental data for the superheat limit. Computations are performed with pure species found in natural gas, binary mixtures herein, as well as a multi-component natural gas mixture in order to demonstrate the scalability of the approach. We demonstrate that there are large inconsistencies in predicted spinodals from a wide range of EoS such as cubic EoS, extended corresponding state EoS, SAFT and multiparameter EoS. The overall standard deviation in the prediction of the spinodal temperatures were 1.4 K and 2.7 K for single- and multi-component liquid-spinodals and 6.3 K and 26.9 K for single- and multi-component vapor spinodals. The relationship between the measurable limit of superheat, or supersaturation, and the theoretical concept of the spinodal is discussed. While nucleation rates from CNT can deviate orders of magnitude from experiments, we find that limit of superheat experiments agree within 1.0 K and 2.4 K with predictions from CNT for single- and multi-component fluids respectively. We demonstrate that a large part of the metastable domain of the phase diagram is currently unavailable to experiments, in particular for metastable vapor. Novel techniques, experimental or with computational simulations should be developed to characterize the thermodynamic properties in these regions, and to identify the thermodynamic states that define the spinodal.nb_NO
dc.language.isoengnb_NO
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleThe spinodal of single- and multi-component fluids and its role in the development of modern equations of statenb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.rights.holderForfatterenb_NO
dc.source.pagenumber98-112nb_NO
dc.source.volume436nb_NO
dc.source.journalFluid Phase Equilibrianb_NO
dc.identifier.doi10.1016/j.fluid.2016.12.018
dc.identifier.cristin1415675
cristin.unitcode7548,60,0,0
cristin.unitnameGassteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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