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dc.contributor.authorPark, Kwangsu
dc.contributor.authorØi, Lars Erik
dc.date.accessioned2017-11-17T12:29:24Z
dc.date.available2017-11-17T12:29:24Z
dc.date.created2017-11-13T12:19:39Z
dc.date.issued2017
dc.identifier.citationLinköping Electronic Conference Proceedings. 2017, 292-297.nb_NO
dc.identifier.issn1650-3686
dc.identifier.urihttp://hdl.handle.net/11250/2466976
dc.description.abstractFor a traditional amine-based CO2 capture system, the absorber column accounts for a significant part of the overall capital- and operating cost. One important design factor of absorber columns is the gas velocity through the absorber packing. Higher gas velocity leads to higher energy cost due to increased pressure drop, but at the same time lower packing cost due to increased effective interfacial area. By utilizing available correlations in the new version 9.0 of the simulation program Aspen HYSYS, the cost optimum gas velocity can be determined. This work evaluated six types of structured packings: Mellapak 250X, 250Y, 2X, 2Y, Mellapak Plus 252Y and Flexipac 2Y. The simulation results show that for all the packings, the cost-optimum gas velocity is in the range of 2.0 to 2.5 m/s giving a pressure drop through the absorber in the range of 10 to 15 mbar.nb_NO
dc.language.isoengnb_NO
dc.rightsNavngivelse-Ikkekommersiell 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc/4.0/deed.no*
dc.titleOptimization of gas velocity and pressure drop in CO2 absorption columnnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber292-297nb_NO
dc.source.journalLinköping Electronic Conference Proceedingsnb_NO
dc.identifier.doi10.3384/ecp17138292
dc.identifier.cristin1513437
cristin.unitcode222,58,3,0
cristin.unitnameInstitutt for prosess-, energi- og miljøteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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Navngivelse-Ikkekommersiell 4.0 Internasjonal
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