Abstract
A method to design mixing in microfluidic slugs using a modified Peclet number, Pe* = Us ds2 / lD, has been reported by the authors, but it was limited to mixing at constant diffusivity D. This paper reports an improved method to quantitatively determine the effect of D on a relation between Pe* and mixing rates. Computational fluid dynamics (CFD) simulations were used for the investigation. We introduce D into the mixing rate term in the relation between Pe* and mixing rates, and found that (mixing rate × ds2 / D) becomes a function of only Pe*. Thus, slug mixing can be designed using the new dimensionless number, (mixing rate × ds2 / D), and Pe*. This allows us to use mixing rate data at any value of D to estimate mixing rates at another value of D. Though Pe* includes effects of D, l, ds, and Us, effects of initial arrangements of reactants inside a slug and slug cross-sectional shapes are not considered. Thus, the relations between (mixing rate × ds2 / D) and Pe* (referred as Pe* correlation) are quantitatively determined to cover the effects of these parameters. Furthermore, we used the Pe* correlation to show theoretically that channel contraction is an effective microfluidic operation to enhance mixing in slugs.
Original language | English |
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Pages (from-to) | 7386-7392 |
Number of pages | 7 |
Journal | Chemical Engineering Science |
Volume | 61 |
Issue number | 22 |
DOIs | |
Publication status | Published - 2006 Nov 20 |
Keywords
- CFD simulation
- Laminar flow
- Mixing
- Mixing enhancement by channel contraction
- Modified Peclet number
- Multiphase flow
ASJC Scopus subject areas
- Chemistry(all)
- Chemical Engineering(all)
- Industrial and Manufacturing Engineering