A physical interpretation of drop sizes in homogenizers and agitated tanks, including the dispersion of viscous oils
- 1 January 1987
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 42 (7) , 1671-1676
- https://doi.org/10.1016/0009-2509(87)80172-0
Abstract
No abstract availableKeywords
This publication has 12 references indexed in Scilit:
- Drop breakup in turbulent stirred‐tank contactors. Part III: Correlations for mean size and drop size distributionAIChE Journal, 1986
- Drop breakup in turbulent stirred‐tank contactors. Part I: Effect of dispersed‐phase viscosityAIChE Journal, 1986
- Drop sizes of emulsions related to turbulent energy dissipation ratesChemical Engineering Science, 1985
- The effect of viscosity on droplet splitting in ARD and RDC extractorsCollection of Czechoslovak Chemical Communications, 1982
- Sauter mean and maximum drop diameters of liquid-liquid dispersions in turbulent agitated vessels at low dispersed phase hold-upChemical Engineering Science, 1979
- Effect of impeller geometry on drop break-up in a stirred liquid—liquid contactorChemical Engineering Science, 1974
- Distribution of drop sizes produced in turbulent liquid—liquid dispersionChemical Engineering Science, 1967
- Flow and turbulence in a stirred tankAIChE Journal, 1966
- Maximum stable drop size in turbulent flowAIChE Journal, 1962
- Fundamentals of the hydrodynamic mechanism of splitting in dispersion processesAIChE Journal, 1955