A mathematical treatment of the effect of particle size distribution on mass transfer in dispersions
- 1 May 1966
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 12 (3) , 499-508
- https://doi.org/10.1002/aic.690120320
Abstract
No abstract availableKeywords
This publication has 13 references indexed in Scilit:
- Relative velocities of bubbles to liquid in an agitated gas‐liquid contractorAIChE Journal, 1965
- Droplet characteristics in a countercurrent contactorAIChE Journal, 1964
- Mass transfer from gas bubbles in an agitated vessel with and without simultaneous chemical reactionChemical Engineering Science, 1964
- The effect of diffusivities and surface films on rates of gas absorptionChemical Engineering Science, 1964
- On mass transfer in the continuous phase from spherical bubbles or dropsChemical Engineering Science, 1964
- The effect of interfacial films on mass transfer rates in liquid-liquid extractionChemical Engineering Science, 1961
- The continuous phase heat and mass-transfer properties of dispersionsChemical Engineering Science, 1961
- Film‐penetration model for mass and heat transferAIChE Journal, 1958
- Turbulent exchange of mass and momentum with a boundaryAIChE Journal, 1956
- The effect of surface active agents in liquid extraction processesChemical Engineering Science, 1953