Chapter 10. Solid–Liquid Mixing
- Edward L. Paul3,
- Victor A. Atiemo-Obeng4,
- Suzanne M. Kresta5
Published Online: 30 JAN 2004
DOI: 10.1002/0471451452.ch10
Copyright © 2004 John Wiley & Sons, Inc.
Book Title

Handbook of Industrial Mixing: Science and Practice
Additional Information
How to Cite
Atiemo-Obeng, V. A., Penney, W. R. and Armenante, P. (2004) Solid–Liquid Mixing, in Handbook of Industrial Mixing: Science and Practice (eds E. L. Paul, V. A. Atiemo-Obeng and S. M. Kresta), John Wiley & Sons, Inc., Hoboken, NJ, USA. doi: 10.1002/0471451452.ch10
Editor Information
- 3
Merck & Co., Inc. (retired); 308 Brooklyn Boulevard, Sea Girt, NJ 08750, USA
- 4
The Dow Chemical Company, Building 1776, Midland, MI 48674, USA
- 5
Department of Chemical and Materials Engineering, University of Alberta, Edmonton, AB, Canada T6G 2G6
Publication History
- Published Online: 30 JAN 2004
- Published Print: 14 NOV 2003
ISBN Information
Print ISBN: 9780471269199
Online ISBN: 9780471451457
- Summary
- Chapter
Keywords:
- solid–liquid systems;
- off-bottom suspension;
- just suspended state;
- Njs;
- solid dispersion;
- solids distribution;
- solid–liquid mass transfer coefficient;
- solid dissolution;
- solid distribution;
- floating solids;
- non-wetting solids
Summary
The focus of this chapter is on mixing operations in mechanically stirred vessels which involve dispersion of solids in liquids. The minimum agitation speed to achieve the just off-bottom suspended state, Njs, is defined, and experimental approaches to its determinations are provided. Correlations for the prediction of Njs are provided for different impeller-vessel configurations, geometric and physical parameters, and operating conditions. Correlations for the determination of solid–liquid mass transfer coefficients are also given, as well as the equations to determine the rate of solid dissolution, and the time to achieve complete dissolution. Limitations on the draw down of floating solids, and on the distribution of solids throughout the vessel are discussed. Examples for the calculation of Njs and other variables of importance in solid–liquid systems are provided.
