Vis enkel innførsel

dc.contributor.authorSheng, Nan
dc.contributor.authorLiu, Zhikun
dc.contributor.authorSong, Zhaoning
dc.contributor.authorLin, Dong
dc.contributor.authorFeng, Xiang
dc.contributor.authorLiu, Yibin
dc.contributor.authorChen, Xiaobo
dc.contributor.authorChen, De
dc.contributor.authorZhou, Xinggui
dc.contributor.authorYang, Chaohe
dc.date.accessioned2019-04-02T09:13:43Z
dc.date.available2019-04-02T09:13:43Z
dc.date.created2018-11-22T14:08:38Z
dc.date.issued2018
dc.identifier.citationChemical Engineering Journal. 2018, 1-9.nb_NO
dc.identifier.issn1385-8947
dc.identifier.urihttp://hdl.handle.net/11250/2592869
dc.description.abstractDesigning highly efficient Au/Ti-containing catalysts for propene epoxidation with H2 and O2 harbors tremendous scientific and industrial importance. In this work, novel hydrophobic hierarchical TS-1 (HTS-1) with wormhole-like mesopores (ca. 45 nm) and small crystal size (100 nm) is firstly synthesized by a two-step crystallization method using CTAB as template. Gratifyingly, the Au/HTS-1 catalyst shows simultaneously high PO formation rate of 150 gpoh−1kgCat−1 without any promoter additive, PO selectivity of 90% and impressive stability of 100 h, which are much better than traditional Au/TS-1 catalyst. Furthermore, the intrinsic reason for the enhanced performance is elucidated by multi-techniques such as N2 physisorption, HRTEM, TGA, FT-IR and 29Si NMR. Interestingly, it is found that the coke in 0.10 wt% Au/HTS-1 catalyst partly reside in mesopores, alleviating the deactivation of micropore blocking. Moreover, the enhanced mass transfer ability and higher hydrophobicity of Au/HTS-1 catalyst also lead to reduced coke weight and absence of aromatic coke.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.titleEnhanced stability for propene epoxidation with H2 and O2 over wormhole-like hierarchical TS-1 supported Au nanocatalystnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber1-9nb_NO
dc.source.journalChemical Engineering Journalnb_NO
dc.identifier.doi10.1016/j.cej.2018.09.115
dc.identifier.cristin1633805
dc.description.localcode© 2018. This is the authors’ accepted and refereed manuscript to the article. Locked until 17.9.2020 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


Tilhørende fil(er)

Thumbnail

Denne innførselen finnes i følgende samling(er)

Vis enkel innførsel

Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
Med mindre annet er angitt, så er denne innførselen lisensiert som Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal