Modelling of mass transfer from falling droplets

Citation
J. Petera et Lr. Weatherley, Modelling of mass transfer from falling droplets, CHEM ENG SC, 56(16), 2001, pp. 4929-4947
Citations number
38
Categorie Soggetti
Chemical Engineering
Journal title
CHEMICAL ENGINEERING SCIENCE
ISSN journal
00092509 → ACNP
Volume
56
Issue
16
Year of publication
2001
Pages
4929 - 4947
Database
ISI
SICI code
0009-2509(200108)56:16<4929:MOMTFF>2.0.ZU;2-I
Abstract
The prediction of mass transfer rates to and from moving drops has traditio nally used the Whitman two-film theory approach in which the resistances to mass transfer on each side of the interface are described by film mass tra nsfer coefficients. These are correlated in terms of the hydrodynamic condi tions, the physical properties of the fluids, and the geometry of the syste m. The performance of liquid-liquid contactors in which mass transfer occur s between swarms of moving droplets of one phase and the other liquid phase as the continuous phase, has similarly been correlated in terms of mass tr ansfer coefficients. These lump together the combined effects of interfacia l mass transfer resistances and those associated with the bulk phases, the effects of interfacial disturbances, coalescence and break-up phenomena, sp ecific surface area, and the effects of axial mixing. In this paper we buil d upon earlier work and other published research which uses finite element methods to quantitatively calculate flow field data and trajectory predicti ons for single particles and drops in a two phase system. The differential equations were discretised using the finite element approach employing a pr ocedure based on the Lagrangian framework developed earlier. Here we extend the approach to calculate mass transfer rates between single aqueous drops and a continuous immiscible solvent phase. The calculated values of drop v elocity and mass transfer rates are compared with experimental values deter mined for single drops of ethanol/water mixtures extracting into a continuo us phase of n-decanol. Good agreement between the experimental and predicte d values was obtained, thus demonstrating that in this case, interfacial ma ss transfer in liquid-liquid systems can be predicted from the fundamental transport equations. The results of the work indicate the potential of furt her development of this approach for swarming drops and hence quantitative prediction of the behaviour of liquid-liquid contactors. (C) 2001 Elsevier Science Ltd. All rights reserved.