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dc.contributor.authorYang, Jia
dc.contributor.authorQi, Yanying
dc.contributor.authorZhu, Jun
dc.contributor.authorZhu, Yi-An
dc.contributor.authorChen, De
dc.contributor.authorHolmen, Anders
dc.date.accessioned2018-05-08T11:21:19Z
dc.date.available2018-05-08T11:21:19Z
dc.date.created2013-11-29T09:06:02Z
dc.date.issued2013
dc.identifier.citationJournal of Catalysis. 2013, 308 37-49.nb_NO
dc.identifier.issn0021-9517
dc.identifier.urihttp://hdl.handle.net/11250/2497558
dc.description.abstractA new approach for elucidating reaction mechanism of complex reactions, such as Fischer–Tropsch (F–T) synthesis, is presented. It includes a combination of integrated transient and steady-state kinetic modeling, experimental and DFT investigations of kinetic isotopic effects. The integrated transient and steady-state modeling enable the determination of H2 and CO equilibrium constants and detailed mapping of surface species including surface concentrations and their reactivities. The predictive ability of Langmuir–Hinshelwood type kinetic models has been significantly improved by taking into account the effect of interaction between adsorbed CO on the CO adsorption. Together with DFT investigations of the kinetic isotopic effect, the dominating CO activation pathway through hydrogen-assisted CO dissociation has been confirmed. It led also to a clarification of two carbon pools namely CH2O* (Cα) and CHx* (Cβ) and two corresponding reaction pathways for methane formation. The prevailing reaction pathway for methane formation depends on the operating conditions. Hydrogen surface concentration is the key parameter determining the reactivity of adsorbed CO and the reaction pathways for methane formation.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.titleReaction mechanism of CO activation and methane formation on Co Fischer-Tropsch catalyst: A combined DFT, transient, and steady-state kinetic modelingnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber37-49nb_NO
dc.source.volume308nb_NO
dc.source.journalJournal of Catalysisnb_NO
dc.identifier.doi10.1016/j.jcat.2013.05.018
dc.identifier.cristin1070714
dc.relation.projectNorges forskningsråd: 209337nb_NO
dc.relation.projectNotur/NorStore: NN4685Knb_NO
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2013 by Elseviernb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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