Sauter mean and maximum drop diameters of liquid-liquid dispersions in turbulent agitated vessels at low dispersed phase hold-up
- 31 December 1979
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 34 (3) , 432-434
- https://doi.org/10.1016/0009-2509(79)85081-2
Abstract
No abstract availableThis publication has 6 references indexed in Scilit:
- The effect of coalescence on drop size distribution in an agitated liquid-liquid dispersionChemical Engineering Science, 1975
- Effect of impeller geometry on drop break-up in a stirred liquid—liquid contactorChemical Engineering Science, 1974
- Velocity profiles and pumping capacities for turbine type impellersThe Canadian Journal of Chemical Engineering, 1968
- Drop size distribution in agitated liquid‐liquid systemsAIChE Journal, 1967
- Distribution of drop sizes produced in turbulent liquid—liquid dispersionChemical Engineering Science, 1967
- Fundamentals of the hydrodynamic mechanism of splitting in dispersion processesAIChE Journal, 1955