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dc.contributor.authorMonteiro, Juliana Garcia Moretz-Sohn
dc.contributor.authorPinto, Diego Di Domenico
dc.contributor.authorZaidy, Syed Amjad Hussain
dc.contributor.authorHartono, Ardi
dc.contributor.authorSvendsen, Hallvard Fjøsne
dc.date.accessioned2014-09-26T12:02:46Z
dc.date.accessioned2016-06-17T11:55:56Z
dc.date.available2014-09-26T12:02:46Z
dc.date.available2016-06-17T11:55:56Z
dc.date.issued2013-11
dc.identifier.citationInternational Journal of Greenhouse Gas Control 2013, 19(Nov):432-440nb_NO
dc.identifier.issn1750-5836
dc.identifier.urihttp://hdl.handle.net/11250/2393066
dc.description.abstractThis work focuses on N,N-diethylethanolamine (DEEA), a tertiary amine relevant in the phase-change solvents context. Vapour liquid equilibrium data for CO2 loaded aqueous solutions of DEEA are presented. These, along with data for pure DEEA and the binary system H2O-DEEA available in literature, are represented by a model correlating the activity coefficients with the electrolyte non-random two-liquid (eNRTL) model. The model is shown to represent the experimental data well. The equilibrium model allows for simulating the regeneration of the solvent, thereby providing a measurement for the energy demand of the process. Experimental heat of absorption data presented by Kim (2009) are used to validate the predictions of the model.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.titleVLE data and modelling of aqueous N,N-diethylethanolamine (DEEA) solutionsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.date.updated2014-09-26T12:02:46Z
dc.source.pagenumber432–440nb_NO
dc.source.volume19nb_NO
dc.source.journalInternational Journal of Greenhouse Gas Controlnb_NO
dc.identifier.doi10.1016/j.ijggc.2013.10.001
dc.identifier.cristin1121864
dc.relation.projectEU/241393nb_NO
dc.description.localcode© 2016 Elsevier B.V. or its licensors or contributors. This is the authors’ accepted and refereed manuscript to the article.nb_NO


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