Hydrodynamics in spray and packed liquid-liquid extraction columns: A review

Authors

  • Milan N. Sovilj University of Novi Sad, Faculty of Technology, Novi Sad
  • Branislava G. Nikolovski University of Novi Sad, Faculty of Technology, Novi Sad
  • Momčilo Đ. Spasojević University of Novi Sad, Faculty of Technical Sciences, Novi Sad

DOI:

https://doi.org/10.20450/mjcce.2019.1519

Keywords:

spray and packed bed columns, slip velocity, Sauter mean drop diameter, axial dispersion coefficient

Abstract

This work provides a review of hydrodynamic characteristics such as the slip velocity, the dispersed-phase holdup, mean drop size, and axial dispersion of non-mechanically agitated liquid-liquid (L-L) extractors, with special reference to spray and packed bed columns. The complexity and importance of hydrodynamic behavior in designing and scaling up L-L extractors was a driving force to analyze, compare and discuss some important experimental findings available in the literature. The effects of phase velocities and the dispersed-phase holdup on the slip velocity, the mean drop size and the axial dispersion coefficient were studied and presented. Empirical correlations for slip velocity, the Sauter mean drop diameter and the axial dispersion coefficient, which were taken from the literature, were commented in terms of their applicability.

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Published

2019-12-30

How to Cite

Sovilj, M. N., Nikolovski, B. G., & Spasojević, M. Đ. (2019). Hydrodynamics in spray and packed liquid-liquid extraction columns: A review. Macedonian Journal of Chemistry and Chemical Engineering, 38(2), 267–282. https://doi.org/10.20450/mjcce.2019.1519

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Chemical Engineering

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