A population-balance-equation model is employed for the analysis of liquid-liquid extraction columns. This model considers drop breakage, coalescence, and exit phenomena for the drop phase caused by drop-drop and drop-continuous phase interactions. Drop breakage and coalescence rates are employed fr
β¦ LIBER β¦
Flooding, holdup, and drop size measurements in a multistage column extractor
β Scribed by V. I. Kirou; L. L. Tavlarides; J. C. Bonnet; C. Tsouris
- Publisher
- American Institute of Chemical Engineers
- Year
- 1988
- Tongue
- English
- Weight
- 869 KB
- Volume
- 34
- Category
- Article
- ISSN
- 0001-1541
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