Correlation of mass transfer volumetric coefficient with power input in stirred liquid-liquid dispersions.
- 1 January 1990
- journal article
- Published by Taylor & Francis in JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
- Vol. 23 (4) , 468-474
- https://doi.org/10.1252/jcej.23.468
Abstract
No abstract availableKeywords
This publication has 10 references indexed in Scilit:
- Mass transfer between fine particles and liquids in agitated vessels.JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988
- A physical interpretation of drop sizes in homogenizers and agitated tanks, including the dispersion of viscous oilsChemical Engineering Science, 1987
- Drop breakup in turbulent stirred‐tank contactors. Part II: Relative influence of viscosity and interfacial tensionAIChE Journal, 1986
- Drop size and continuous‐phase mass transfer in agitated vesselsAIChE Journal, 1981
- Sauter mean and maximum drop diameters of liquid-liquid dispersions in turbulent agitated vessels at low dispersed phase hold-upChemical Engineering Science, 1979
- Area‐free mass transfer coefficients for liquid extraction in a continuously worked mixerAIChE Journal, 1969
- Transport of heat and mass between liquids and spherical particles in an agitated tankAIChE Journal, 1969
- Continuous‐phase mass‐transfer coefficients for liquid extraction in agitated vesselsAIChE Journal, 1968
- Mass transfer to particles: Part I. Suspended in agitated tanksAIChE Journal, 1962
- The continuous phase heat and mass-transfer properties of dispersionsChemical Engineering Science, 1961