2020
DOI: 10.1016/j.ces.2020.115695
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Modelling of a microreactor for the partial oxidation of 1-butanol on a titania supported gold catalyst

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Cited by 12 publications
(8 citation statements)
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“…Besides, the choice of support was also crucial and has been linked to the high catalytic activity of many Aubased catalysts. [30][31][32][33][34] However, in this study, the unsaturated Au sites were the active species. At an 8 h reaction time, attempts to use the support for the oxidative coupling of 1 a to azobenzene resulted in a reduced 2 a yield and selectivity (Table 1, entry 17); however, when the reaction time was increased to 16 h, the conversion and yield improved somewhat (Table 1, entry 18).…”
Section: Catalyst Screeningmentioning
confidence: 56%
See 1 more Smart Citation
“…Besides, the choice of support was also crucial and has been linked to the high catalytic activity of many Aubased catalysts. [30][31][32][33][34] However, in this study, the unsaturated Au sites were the active species. At an 8 h reaction time, attempts to use the support for the oxidative coupling of 1 a to azobenzene resulted in a reduced 2 a yield and selectivity (Table 1, entry 17); however, when the reaction time was increased to 16 h, the conversion and yield improved somewhat (Table 1, entry 18).…”
Section: Catalyst Screeningmentioning
confidence: 56%
“…Likewise, increasing the time up to 24 h did not significantly improve the reaction, but instead, it gave a trace amount of the product (Table 1, entry 11–16). Besides, the choice of support was also crucial and has been linked to the high catalytic activity of many Au‐based catalysts [30–34] . However, in this study, the unsaturated Au sites were the active species.…”
Section: Resultsmentioning
confidence: 84%
“…The usual method of generating droplets (emulsion) consists of uneven droplet size and irregular mixing and dispersion. Moreover, the process needs additional energy input for stabilizing emulsion [ 13 , 14 ]. The slug flow microreactor provides an effective solution with minimal energy input for the dispersion of droplets.…”
Section: Microstructure Reactors Design Principlesmentioning
confidence: 99%
“…In many cases, a centrally mounted orifice is used to create the discrete segmented flow, where the droplet of the immiscible phase will be smaller than that of the orifice opening and the phases are well mixed due to a pressure difference. The orifice opening or any obstacle to the flow will disturb the central fluid stream and this destabilization will be helpful for the formation of segments in the channel [ 14 , 17 , 18 ]. Surfactants present in the continuous phase can be used for the stabilization of droplets in the channel.…”
Section: Microstructure Reactors Design Principlesmentioning
confidence: 99%
“…[ 11,16 ] Nowadays, vanadium‐based catalysts are extensively used in the catalytic oxidation of alcohols with a stoichiometric amount of H 2 O 2 , TBHP, or dioxygen. [ 14a,17,c–d ] Due to the immense importance of alcohol oxidation reactions, a variety of catalytic systems, like homogeneous, [ 17i,18 ] heterogeneous, [ 19 ] biphasic, [ 20 ] or gas phase, [ 21 ] have been developed. A range of catalytic systems based on metals [ 21b,22 ] (especially transition metals) and nonmetals [ 23 ] are also found in the literature for the catalytic conversion of alcohols.…”
Section: Introductionmentioning
confidence: 99%