Transport Phenomena and Fluid Mechanics
Hydrodynamic modeling on the external liquid–solid wetting efficiency in a trickling flow reactor
Article first published online: 27 MAR 2012
DOI: 10.1002/aic.13785
Copyright © 2012 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Cheng, Z.-M., Kong, X.-M., Zhu, J., Wang, Z.-Y., Jin, J. and Huang, Z.-B. (2013), Hydrodynamic modeling on the external liquid–solid wetting efficiency in a trickling flow reactor. AIChE J., 59: 283–294. doi: 10.1002/aic.13785
Publication History
- Issue published online: 21 DEC 2012
- Article first published online: 27 MAR 2012
- Accepted manuscript online: 24 FEB 2012 09:50AM EST
- Manuscript Revised: 7 FEB 2012
- Manuscript Received: 4 DEC 2011
Funded by
- Natural Science Foundation of China. Grant Numbers: 20876043, 21076072
- Fundamental Research Funds for the Central Universities of China
- Abstract
- Article
- References
- Cited By
Keywords:
- trickle-bed reactor;
- liquid flow texture;
- three-region model;
- liquid–solid wetting efficiency correlation
A three-region model was proposed, which considers the bed cross section being composed of a stagnant liquid region, a liquid film region, and a rivulet flow region. To estimate the fractions of the three regions, the fraction of film flow was evaluated first, by transforming the complex trickling flow texture into pure liquid film flow. Through the measurements of liquid holdup and pressure drop for the film flow, a relationship between relative permeability and gas saturation was established, and from which the fraction of film flow region was obtained. It shows packing size is most important to the faction of rivulet flow. The external wetting efficiency of the packing was correlated as the sum of two-third power of the liquid film fraction and the rivulet flow fraction, besides, a correlation based on Reynolds and Galileo numbers of the two phases in the form of
was proposed. © 2012 American Institute of Chemical Engineers AIChE J, 59: 283–294, 2013

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