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dc.contributor.authorFan, Chen
dc.contributor.authorZhu, Yi-An
dc.contributor.authorYang, Ming-Lei
dc.contributor.authorSui, Zhi-Jun
dc.contributor.authorZhou, Xing-Gui
dc.contributor.authorChen, De
dc.date.accessioned2018-05-08T11:59:30Z
dc.date.available2018-05-08T11:59:30Z
dc.date.created2015-08-19T12:54:34Z
dc.date.issued2015
dc.identifier.citationIndustrial & Engineering Chemistry Research. 2015, 54 (22), 5901-5913.nb_NO
dc.identifier.issn0888-5885
dc.identifier.urihttp://hdl.handle.net/11250/2497590
dc.description.abstractA comprehensive microkinetic model based on density functional theory (DFT) calculations is constructed to explore the reaction mechanism for dry methane reforming on Ni catalyst. Three low-index facets, namely, Ni(111), Ni(100), and Ni(211), are utilized to represent the contributions from the flat, open, and stepped surfaces. Adsorption energies of all the possible reaction intermediates as well as activation energies for the elementary reactions involved in dry reforming of methane on the three Ni surfaces are calculated through DFT. These results are further employed to estimate the rate constants for the elementary reactions under realistic temperatures and pressures within the framework of transition state theory and statistical mechanics treatments. The dominant reaction pathway is identified as CH4 successive dissociation followed by carbon oxidation by atomic oxygen. The dependence of the rate-determining step on operating conditions is examined. At low CH4 and CO2 partial pressures, both CH4 dissociative adsorption and carbon oxidation would jointly dominate the overall reaction rate, while at high pressures carbon oxidation is suggested as the rate-determining step for the DRM reaction. Our findings provide a rational interpretation of contradictory experimental observations.nb_NO
dc.language.isoengnb_NO
dc.publisherAmerican Chemical Societynb_NO
dc.titleDensity Functional Theory-Assisted Microkinetic Analysis of Methane Dry Reforming on Ni Catalystnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber5901-5913nb_NO
dc.source.volume54nb_NO
dc.source.journalIndustrial & Engineering Chemistry Researchnb_NO
dc.source.issue22nb_NO
dc.identifier.doi10.1021/acs.iecr.5b00563
dc.identifier.cristin1258831
dc.relation.projectNotur/NorStore: NN4685Knb_NO
dc.relation.projectNorges forskningsråd: 233869nb_NO
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2015 by American Chemical Societynb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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