Fluid Mechanics and Transport Phenomena
Influence of hydrodynamics on liquid mixing during Taylor flow in a microchannel
Article first published online: 11 JUL 2011
DOI: 10.1002/aic.12698
Copyright © 2011 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Su, Y., Chen, G. and Yuan, Q. (2012), Influence of hydrodynamics on liquid mixing during Taylor flow in a microchannel. AIChE J., 58: 1660–1670. doi: 10.1002/aic.12698
Publication History
- Issue published online: 4 MAY 2012
- Article first published online: 11 JUL 2011
- Accepted manuscript online: 2 JUN 2011 04:18PM EST
- Manuscript Revised: 19 MAY 2011
- Manuscript Received: 3 JAN 2011
Funded by
- National Natural Science Foundation of China. Grant Numbers: 20906087, 20911130358
- Ministry of Science and Technology of China. Grant Number: 2009CB219903
- Fund of Dalian Institute of Chemical Physics, CAS. Grant Number: K2009D01
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Keywords:
- microchannel;
- Taylor flow;
- mixing;
- diffusion;
- multiphase flow;
- hydrodynamics
Abstract
The miscible liquid-liquid two phases based on Taylor flow in microchannels was investigated by high-speed imaging techniques and Villermaux/Dushman reaction. The mixing based on Taylor flow was much better compared with that without introducing gas in microchannels, even the ideal micromixing performance could be obtained under optimized superficial gas and liquid velocities. In the mixing process based on Taylor flow, the superficial gas and liquid velocities affected the lengths and the velocities of Taylor bubble and liquid slug, and finally the micromixing performance. The formation process of Taylor flow in the inlets, the initial uniform distribution of reactants and the internal circulations in the liquid slug, and the thin liquid films all improved the mixing performance. Furthermore, a modified Peclet number that represented the relative importance of diffusion and convection in the mixing process was proposed for explaining and anticipating micromixing efficiency. © 2011 American Institute of Chemical Engineers AIChE J, 58: 1660–1670, 2012

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