2011
DOI: 10.1016/j.ces.2011.03.024
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Ideal micromixing performance in packed microchannels

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Cited by 66 publications
(39 citation statements)
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References 33 publications
(31 reference statements)
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“…It is well known that whenever fast reactions occur in reactors, the characteristic micromixing time (t m ) is in competition with the characteristic reaction time (t R ). When t m of reactants is comparable to t R , unequal molar ratios exists locally during the reaction and the reaction conversion is controlled by micromixing [39]. The micromixing time depends on hydrodynamic conditions and it only can be evaluated for each experiment using micromixing models.…”
Section: Effect Of Confluence Angle On Mixing Time (T M )mentioning
confidence: 99%
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“…It is well known that whenever fast reactions occur in reactors, the characteristic micromixing time (t m ) is in competition with the characteristic reaction time (t R ). When t m of reactants is comparable to t R , unequal molar ratios exists locally during the reaction and the reaction conversion is controlled by micromixing [39]. The micromixing time depends on hydrodynamic conditions and it only can be evaluated for each experiment using micromixing models.…”
Section: Effect Of Confluence Angle On Mixing Time (T M )mentioning
confidence: 99%
“…The reaction between iodide and iodate, coupled with a neutralization reaction, is one of the well-known parallel competing reactions namely the Villermaux/Dushman reaction. The reaction formula is described by the following scheme: [36][37][38][39].…”
Section: Micromixing Characterization In Villermaux-dushman Test Reacmentioning
confidence: 99%
“…They extended a method of using iodine/iodide reaction system together with IEM mixing model to study microreactors. The method has become very popular and since then frequently applied to examine all kinds of microreactors, see for example (Guo et al, 2013;Kashid et al, 2011;Su et al, 2011) and (Aubin et al, 2010;Kölbl et al, 2008;Panic et al, 2004) for earlier applications of Villermaux-Dushman reaction. Falk and Commenge (2010) have shown how to identify mixing time, and how to relate it to operating parameters such as Reynolds number of the flow and the specific power (dissipation of mechanical energy per unit mass of fluid).…”
Section: Microreactorsmentioning
confidence: 99%
“…This is a substantial increase, which results improved mass transfer characteristics for multiphase flow compared to a segmented flow regime. [44][45][46] The immiscible fluids flow into confined interstices at high flow rates. This causes an increased shear between the fluids and results in a good dispersion, resulting in higher mixing efficiency and mass transfer rates.…”
Section: Mass Transport Phenomenamentioning
confidence: 99%
“…This causes an increased shear between the fluids and results in a good dispersion, resulting in higher mixing efficiency and mass transfer rates. 47,48 A modified Reynolds number (RePB) can be identified, which is used to identify the boundaries of the different flow regimes in a packed-bed:…”
Section: Mass Transport Phenomenamentioning
confidence: 99%