D e p a r t m e n t of C h e m i c a l Engineering University of N o t r e Dame, N a t r e Dome, Indiana 46556 Rates of mass transfer during drop formation and coalescence were investigated for three dispersed phase-controlled liquid systems, one binary (ethyl acetate-water) and two ternary (acetic
Mass transfer in the liquid phase during the formation of bubbles
β Scribed by P.H. Calderbank; R.P. Patra
- Publisher
- Elsevier Science
- Year
- 1966
- Tongue
- English
- Weight
- 316 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
Shorter Communications
This equation, if K' is of order unity, produces the correct order of magnitude for u.
In the same way, if the liquid is in laminar flow, we have 566K'G + L a * u=FA 5 0
If in Eqs. ( 6), ( 8) and ( 10) a is substituted by D, all the uncertainty is concentrated in K', which will depend, in general, upon a number of dimensionless groups (E&vi% gp4/pa3, a/D, [(l/pg) (&/&)I), in analogy with the case of vertical tubes [6, 71.
For a free bubble a is of a smaller order of magnitude with respect to D; the pressure gradient effect is therefore expected to be of less importance than in the case of a slug.
π SIMILAR VOLUMES
theoretical model is developed in order to predict the gas absorption rate during gas bubble formation and rise through a shallow liquid pool. The model takes a rather straightforward approach to the hydrodynamics of bubble formation and rise, allows for the general case of mass transfer with simult