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2018
DOI: 10.1016/j.cej.2018.04.085
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Kinetics of the transesterification of methyl palmitate and sucrose using surfactants

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Cited by 15 publications
(21 citation statements)
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“…As shown in Table entries 1, 5, and 6, the total SE yield increased from 76.9% to 88.2% and the conversion of MS was around 93% when the stirring rate increased from 300 to 500 rpm. Combined with related studies (Gutiérrez et al, ), the main limitation of solvent‐free transesterification was shown to be the solid–liquid interfaces among the catalyst, sucrose, and FAME. The above results suggested that reducing the particle sizes of solid substrates by sand milling and intensifying mass transfer could promote the formation of SE and avoid side reactions probably due to the increasing of the interfacial contact of reaction mixtures.…”
Section: Resultsmentioning
confidence: 74%
“…As shown in Table entries 1, 5, and 6, the total SE yield increased from 76.9% to 88.2% and the conversion of MS was around 93% when the stirring rate increased from 300 to 500 rpm. Combined with related studies (Gutiérrez et al, ), the main limitation of solvent‐free transesterification was shown to be the solid–liquid interfaces among the catalyst, sucrose, and FAME. The above results suggested that reducing the particle sizes of solid substrates by sand milling and intensifying mass transfer could promote the formation of SE and avoid side reactions probably due to the increasing of the interfacial contact of reaction mixtures.…”
Section: Resultsmentioning
confidence: 74%
“…Nevertheless, in all cases, color removal in the aqueous phase was also verified during the salting‐out process, which indicates that part of the coloring compounds were also of polar nature. This was expected as sucrose could degrade into caramel‐like compounds under reaction conditions (Balzer and Luders, ; Gutiérrez et al, ; Gutiérrez et al, ).…”
Section: Resultsmentioning
confidence: 99%
“…However, during the solvent‐free method, complete conversion is hardly achieved, and considerable amount of reactants remain in reactor effluents. Despite the low conversion of the solvent‐free route, SE productivity is similar to that obtained in the solvent process (~50 kg SE/h‐kg reactive mixture),(Gutiérrez et al, ) mainly because large solvent loadings are required (i.e., up to 60% w/w) for a complete dissolution of reactants.…”
Section: Introductionmentioning
confidence: 80%
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