2018
DOI: 10.1039/c8cy00439k
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Direct epoxidation of propene on silylated Au–Ti catalysts: a study on silylation procedures and the effect on propane formation

Abstract: Silylation was employed on an active Au/Ti–SiO2 catalyst, in order to enhance catalyst performance for the direct epoxidation of propene to propene oxide (PO) using H2 and O2.

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Cited by 17 publications
(11 citation statements)
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“…Moreover, it has been proposed that the formation of byproducts is mainly caused by the ring-opening and isomerization of PO catalyzed by the acidic sites on the catalyst surface. ,, To weaken the PO adsorption and thus suppress its side reaction, surface modification would be a promising strategy to enhance the catalytic performance. Previous studies hasve demonstrated that increasing the hydrophobicity of the catalyst surface could improve the catalytic activity and selectivity. , However, these studies are not in the scope of this work, which would be investigated in our future study.…”
Section: Resultsmentioning
confidence: 97%
“…Moreover, it has been proposed that the formation of byproducts is mainly caused by the ring-opening and isomerization of PO catalyzed by the acidic sites on the catalyst surface. ,, To weaken the PO adsorption and thus suppress its side reaction, surface modification would be a promising strategy to enhance the catalytic performance. Previous studies hasve demonstrated that increasing the hydrophobicity of the catalyst surface could improve the catalytic activity and selectivity. , However, these studies are not in the scope of this work, which would be investigated in our future study.…”
Section: Resultsmentioning
confidence: 97%
“…As is the case for mesoporous titanosilicates, hydrophobicity of the catalyst is important for enhancing the catalytic activity and silylation of acidic Ti–OH sites (together with Si–OH sites) by alkoxysilane improved catalytic activity, because acidic Ti–OH sites are responsible for propane formation and/or propionaldehyde formation. , Nijhuis et al performed kinetic studies and reported that PO was formed at Au sites near the Ti 4+ site, while unfavorable H 2 oxidation occurred at both isolated Au sites and Au sites near the Ti 4+ . In both cases, the OOH species is an active intermediate.…”
Section: Catalysis By Gold In Gas-phase Reactionsmentioning
confidence: 99%
“…Moreover, as described in the Introduction section, the strategy that silylation to consume hydroxyl groups with silane coupling agent could be effective over the Au catalyst to improve the catalytic performance by weakening PO adsorption on the catalysts surface. 11, 17–19 To further increase the PO activity, bubbling HMDSO through the catalysts bed for 40 min followed by flushing with reactants was carried out over the Au 20 Pt 1 /TS‐1‐B catalyst after its performance had been relatively stable. Surprisingly, simultaneously enhanced PO formation rate to 356 g PO /h/kg cat , PO selectivity to 88% and H 2 efficiency to 41%, corresponding to the propylene conversion of 11%, were observed in Figure 2D over the silylated catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…In this regard, as a facile and effective method, surface silylation could consume partial hydroxyl groups and graft hydrophobic groups onto the catalyst surface. 11, 17–19 It is noted that in principle, the grafted electron‐rich alkyl groups have a possible impact on the electronic properties of active sites. Therefore, an attempt is made to probe the effects of surface silylation on the geometric and electronic properties and then to guide the rational design of silylated Au/TS‐1 catalyst for the reaction.…”
Section: Introductionmentioning
confidence: 99%