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dc.contributor.authorFeng, Xiang
dc.contributor.authorDuan, Xuezhi
dc.contributor.authorYang, Jia
dc.contributor.authorQian, Gang
dc.contributor.authorZhou, Xinggui
dc.contributor.authorChen, De
dc.contributor.authorYuan, Weikang
dc.date.accessioned2019-04-26T08:07:47Z
dc.date.available2019-04-26T08:07:47Z
dc.date.created2018-11-22T14:38:16Z
dc.date.issued2015
dc.identifier.citationChemical Engineering Journal. 2015, 278 234-239.nb_NO
dc.identifier.issn1385-8947
dc.identifier.urihttp://hdl.handle.net/11250/2595612
dc.description.abstractFor direct propene epoxidation with H2/O2, TS-1 with blocked micropores (TS-1-B) is recognized as an attractive support for Au catalysts with enhanced stability and activity by suppressing the deactivation caused by micropore blocking. In this work, as a consecutive effort, effect of Si/Ti molar ratio of TS-1-B on catalytic performance is investigated. It is shown that the optimum Si/Ti molar ratio is 40. In other words, both lower and higher ratios are unfavorable for the formation of propylene oxide, which are possibly attributed to the presence of extra-framework Ti species and the difficult transmission of hydroperoxide species from Au surface to nearby Ti sites, respectively. Based on this, effect of Au loading on catalytic performance is further examined. When the Au loading is 0.13 wt%, the catalyst shows not only high PO formation rate of 158 gPO h−1 kgCat−1 comparable to the reported best activity without adding promoters, but also significantly enhanced stability at 200 °C over 30 h.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.titleAu/uncalcined TS-1 catalysts for direct propene epoxidation with H2 and O2: Effects of Si/Ti molar ratio and Au loadingnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber234-239nb_NO
dc.source.volume278nb_NO
dc.source.journalChemical Engineering Journalnb_NO
dc.identifier.doihttps://doi.org/10.1016/j.cej.2014.09.108
dc.identifier.cristin1633833
dc.description.localcode© 2014. This is the authors’ accepted and refereed manuscript to the article. Locked until 13 October 2016 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.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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