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dc.contributor.authorMa, Yuanyuan
dc.contributor.authorGan, Jie
dc.contributor.authorPan, Minjian
dc.contributor.authorZhang, Yanfang
dc.contributor.authorFu, Wenzhao
dc.contributor.authorDuan, Xuezhi
dc.contributor.authorChen, Wenyao
dc.contributor.authorChen, De
dc.contributor.authorQian, Gang
dc.contributor.authorZhou, Xinggui
dc.date.accessioned2020-02-07T10:26:49Z
dc.date.available2020-02-07T10:26:49Z
dc.date.created2019-11-21T15:14:19Z
dc.date.issued2019
dc.identifier.citationChemical Engineering Science. 2019, 203 228-236.nb_NO
dc.identifier.issn0009-2509
dc.identifier.urihttp://hdl.handle.net/11250/2640309
dc.description.abstractFundamental understanding of heterogeneously catalyzed aerobic, base-free oxidation of glycerol is highly desirable for sustainable and highly efficient chemical synthesis. In this work, Pt/CNTs catalyzed base-free oxidation of glycerol is investigated by combining experiments, DFT calculations and kinetics analysis. The solvent effects and kinetic isotope effects measurements as well as DFT calculations reveal that water-assisted O2 activation to form active OH∗ intermediates is not in rate-determining step (RDS) but in equilibrium. Then, Langmuir-Hinshelwood kinetic models are developed and fitted with the experimental data. The OH∗-assisted CH bond cleavage of glycerol is discriminated as the RDS for the two parallel oxidation pathways of glycerol via primary or secondary hydroxyl groups, where the former case exhibits lower activation energy. The insights revealed here could guide the design and optimization of this catalytic process to generate the targeted products.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.titleReaction mechanism and kinetics for Pt/CNTs catalyzed base-free oxidation of glycerolnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber228-236nb_NO
dc.source.volume203nb_NO
dc.source.journalChemical Engineering Sciencenb_NO
dc.identifier.doi10.1016/j.ces.2019.03.068
dc.identifier.cristin1750607
dc.description.localcode© 2019. This is the authors’ accepted and refereed manuscript to the article. Locked until 29.3.2021 due to copyright restrictions. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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