Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 2—parameter fitting and the use of the multiblock model for dense dispersions
- 1 May 2002
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 57 (10) , 1815-1825
- https://doi.org/10.1016/s0009-2509(02)00067-2
Abstract
No abstract availableThis publication has 15 references indexed in Scilit:
- Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 1 Description and qualitative validation of the modelChemical Engineering Science, 1999
- Alternative mechanisms of drop breakup in stirred vesselsChemical Engineering Science, 1998
- Steady‐state drop‐size distributions in high holup fraction dispersion systemsAIChE Journal, 1995
- Transient drop size in agitated liquid-liquid systems, as influenced by the direction of mass transfer and surfactant concentrationIndustrial & Engineering Chemistry Research, 1992
- Dynamic simulation of bimodal drop size distributions in low-coalescence batch dispersion systemsChemical Engineering Science, 1992
- Drop breakup in turbulent stirred‐tank contactors. Part I: Effect of dispersed‐phase viscosityAIChE Journal, 1986
- Changes of the average drop sizes during the initial period of liquid-liquid dispersions in agitated vesselsIndustrial & Engineering Chemistry Process Design and Development, 1985
- Breakage and coalescence of drops in a batch stirred vessel—II comparison of model and experimentsChemical Engineering Science, 1981
- A model for transitional breakage probability of droplets in agitated lean liquid-liquid dispersionsChemical Engineering Science, 1979
- Description of interaction processes in agitated liquid-liquid dispersionsChemical Engineering Science, 1977