2006
DOI: 10.1016/j.ces.2006.01.047
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Design of mixing in microfluidic liquid slugs based on a new dimensionless number for precise reaction and mixing operations

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Cited by 64 publications
(49 citation statements)
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“…The micromixing efficiency in the liquid slug was dependent on the length and the velocity of the liquid slug, and the initial distribution of reactants. These experimental results were similar to the numerical simulation results of Tanthapanichakoon et al 54 They reported the mixing characteristics inside a microfluidic liquid slug of immiscible liquid-liquid two phases using the computational fluid dynamics (CFD) simulations. Their simulation results provided insights into the influences of operating parameters on the rate of slug-based mixing (such as initial arrangement of reactants in liquid slugs, slug velocity and slug diameter), and Peclet number of liquid slugs (Pe ¼ U S d 2 Diff /l S D) for estimating mixing rates and designing liquid slugs was proposed based on the simulation results.…”
Section: Modified Peclet Number For Micromixedness Ratiosupporting
confidence: 79%
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“…The micromixing efficiency in the liquid slug was dependent on the length and the velocity of the liquid slug, and the initial distribution of reactants. These experimental results were similar to the numerical simulation results of Tanthapanichakoon et al 54 They reported the mixing characteristics inside a microfluidic liquid slug of immiscible liquid-liquid two phases using the computational fluid dynamics (CFD) simulations. Their simulation results provided insights into the influences of operating parameters on the rate of slug-based mixing (such as initial arrangement of reactants in liquid slugs, slug velocity and slug diameter), and Peclet number of liquid slugs (Pe ¼ U S d 2 Diff /l S D) for estimating mixing rates and designing liquid slugs was proposed based on the simulation results.…”
Section: Modified Peclet Number For Micromixedness Ratiosupporting
confidence: 79%
“…Furthermore, the separation of the gas-liquid two phases after the outlet of microchannel is much easier than that of the immiscible liquid-liquid two phases because of larger density difference between the gasliquid two phases. Actually, the Peclet number proposed by Tanthapanichakoon et al 54 was the ratio of the diffusive time scale (t Diff ¼ d 2 Diff /D), to the convective transport time scale (t Conv ¼ l S / U S ) in liquid slugs, where d Diff was the diffusion distance and considered to be equal to the hydraulic diameter of the microchannel. When the Peclet number was less than a constant value, the mixing in liquid slugs was controlled by the molecular diffusion, or else, it was determined by the convective transport.…”
Section: Modified Peclet Number For Micromixedness Ratiomentioning
confidence: 99%
“…In order to investigate such a problem, Sarazin et al [55] considered two kinds of methods in coalescing two droplets of different species subjected to mixing, i.e., coalescing in a longitudinal arrangement and in a side-by-side arrangement. As shown in Figure 27, coalescence of droplets in a longitudinal arrangement provides a much better mixing effect, which is in line with the studies of Tanthapanichakoon et al [53] and Wang et al [54]. As a carrier, fluid oil is most frequently used.…”
Section: Mixing By Dropletssupporting
confidence: 72%
“…When estimating the mixing performance in terms of the distribution of species concentration, care must be given to the initial condition concentration distribution. Tanthapanichakoon et al [53] numerically revealed that the initial concentrations is the most dominant parameter affecting the mixing rate, which was also addressed in the work of Wang et al [54]. This means that the given flow field inside the droplet keeps a symmetric property.…”
Section: Mixing By Dropletsmentioning
confidence: 82%
“…This circular convection is very efficient for the fast transport of particles and molecules and is of particular importance for mixing processes with vesicles, sensor particles, and cells, which are too large to show a significant diffusive contribution to their transport. The segment-internal convection supports the mixing after addition of components into segments (mixing, dosing) as well as homogenization during further procedures [12].…”
Section: Introductionmentioning
confidence: 99%