Abstract
Convective micromixers allow fast mixing with characteristic times below 1 ms by creating vortices in bends or junctions of microchannels. Their robustness and comparatively high throughput make them suitable for process intensification purposes. In this contribution, T-shaped micromixers with rectangular cross section and meandering structures as basic elements are numerically investigated for Reynolds numbers from 0.01 to 1000 in the mixing channel. Static and transient mixing regimes in T-mixers are described up to the transition to turbulence, where a worsening of mixing is found. Different experimental results confirm the simulations and lead to the convective lamination model. This model links the energy dissipation to mixing similar to a modeling of turbulent mixing. Additional to mixing of two fluids, also wall contact of fluids in channel flow is investigated with a catalyzed chemiluminescence reaction. With this method, dead zones can be made visible.
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Dreher, S., Engler, M., Kockmann, N., Woias, P. (2010). Theoretical and Experimental Investigations of Convective Micromixers and Microreactors for Chemical Reactions. In: Bockhorn, H., Mewes, D., Peukert, W., Warnecke, HJ. (eds) Micro and Macro Mixing. Heat and Mass Transfer. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-04549-3_18
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DOI: https://doi.org/10.1007/978-3-642-04549-3_18
Publisher Name: Springer, Berlin, Heidelberg
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