dc.contributor.author | Ibrahim, Mohamed | |
dc.contributor.author | Skaugen, Geir | |
dc.contributor.author | Ertesvåg, Ivar Ståle | |
dc.date.accessioned | 2017-12-21T08:17:42Z | |
dc.date.available | 2017-12-21T08:17:42Z | |
dc.date.created | 2015-07-07T14:00:04Z | |
dc.date.issued | 2015 | |
dc.identifier.citation | Chemical Engineering Science. 2015, 137 572-582. | nb_NO |
dc.identifier.issn | 0009-2509 | |
dc.identifier.uri | http://hdl.handle.net/11250/2473380 | |
dc.description.abstract | For a good design of all the processes in Carbon Capture and Storage, the thermodynamics of the CO2 and CO2 mixtures should be accurately predicted. Among these mixtures are CO2-water systems that are very difficult to deal with due to the polar nature. In this work we suggest a new extended corresponding states equation of state (EoS) that can handle polar mixtures. The new EoS uses the Bender Modified Benedict-Webb-Rubin EoS as a reference equation. NH3, R23 and R503 are used as reference fluids with parameters from Polt. The EoS presented uses the Soave-Redlich-Kwong EoS with Huron Vidal mixing rules based approach to compute the scale factors. The evaluation of the new EoS is done over a large set of experimental data. The results show very high accuracy in predicting both phase equilibrium and densities | nb_NO |
dc.language.iso | eng | nb_NO |
dc.publisher | Elsevier | nb_NO |
dc.title | An Extended Corresponding States Equation of State (EoS) for CCS Industry | nb_NO |
dc.type | Journal article | nb_NO |
dc.type | Peer reviewed | nb_NO |
dc.description.version | submittedVersion | nb_NO |
dc.source.pagenumber | 572-582 | nb_NO |
dc.source.volume | 137 | nb_NO |
dc.source.journal | Chemical Engineering Science | nb_NO |
dc.identifier.doi | 10.1016/j.ces.2015.06.013 | |
dc.identifier.cristin | 1252818 | |
dc.relation.project | Norges forskningsråd: 189978 | nb_NO |
dc.description.localcode | Preprint submitted to Chemical Engineering Science. | nb_NO |
cristin.unitcode | 194,64,25,0 | |
cristin.unitname | Institutt for energi- og prosessteknikk | |
cristin.ispublished | true | |
cristin.fulltext | preprint | |
cristin.qualitycode | 2 | |