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dc.contributor.authorEnaasen, Nina
dc.contributor.authorTobiesen, Finn Andrew
dc.contributor.authorKvamsdal, Hanne Marie
dc.contributor.authorHillestad, Magne
dc.date.accessioned2018-02-27T12:13:45Z
dc.date.available2018-02-27T12:13:45Z
dc.date.created2014-11-27T10:37:11Z
dc.date.issued2013
dc.identifier.citationEnergy Procedia. 2013, 37 (0), 2058-2065.nb_NO
dc.identifier.issn1876-6102
dc.identifier.urihttp://hdl.handle.net/11250/2487360
dc.description.abstractIn this work, a system of unit operations is modeled and implemented in MATLAB for dynamic simulation of the regeneration part of the CO2 capture process. The system consists of a stripper, a reboiler and a condenser, and it is solved by a simultaneous equation based method. The method proves to be suitable for solving the regeneration part of the CO2 capture process and it shows numerically stable behavior in general. Further, two dynamic simulation cases are carried out and compared to steady state simulation results from CO2SIM. The dynamic simulation results show reasonably good agreement with steady state simulations, even though a very simplified flash tank model is used for simulation of reboiler and condenser and a simplified thermodynamic model is applied compared to the more robust CO2SIM model. Due to lack of dynamic pilot data, validation of the dynamic regeneration model has been difficult at this point. However, this is necessary for a thorough validation of the model for transient conditions.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleDynamic modeling of the solvent regeneration part of a CO2 capture plantnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber2058-2065nb_NO
dc.source.volume37nb_NO
dc.source.journalEnergy Procedianb_NO
dc.source.issue0nb_NO
dc.identifier.doi10.1016/j.egypro.2013.06.084
dc.identifier.cristin1177664
dc.relation.projectNorges forskningsråd: 193816nb_NO
dc.description.localcodeCopyright © 2013 The Authors. Published by Elsevier Ltd. Published under a CC BY-NC-ND 3.0 license.nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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