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dc.contributor.authorFytianos, Georgios
dc.contributor.authorGrimstvedt, Andreas Magnar
dc.contributor.authorKnuutila, Hanna
dc.contributor.authorSvendsen, Hallvard Fjøsne
dc.date.accessioned2017-10-24T07:21:21Z
dc.date.available2017-10-24T07:21:21Z
dc.date.created2015-01-09T10:20:17Z
dc.date.issued2014
dc.identifier.citationEnergy Procedia. 2014, 63 1869-1875.nb_NO
dc.identifier.issn1876-6102
dc.identifier.urihttp://hdl.handle.net/11250/2461571
dc.description.abstractAmine degradation and corrosion can be a severe operational problem in the CO2 absorption process. In this paper the effect of MEA's degradation products on corrosion is studied. Different solutions of MEA 30wt% containing also 1wt% of a specific degradation product were placed in 316 stainless steel cylinders and stored in a thermostat chamber at 135oC. Samples are analysed for Fe, Cr, Ni and Mo by ICP-MS as an indication of corrosivity. The results showed that after 5 weeks loaded MEA 30wt% with 1wt% oxalic acid was the most corrosive solution.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.titleEffect of MEA's degradation products on corrosion at CO2 capture plantsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber1869-1875nb_NO
dc.source.volume63nb_NO
dc.source.journalEnergy Procedianb_NO
dc.identifier.doi10.1016/j.egypro.2014.11.195
dc.identifier.cristin1193672
dc.relation.projectNorges forskningsråd: 189998nb_NO
dc.description.localcode© 2014 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND licensenb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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