Compared with single-phase laminar pipe flow, two-phase bubble-train flow shows a significantly increased rate of mass transfer between liquid and wall. The present work is a study of this effect over a wide range of the governing variables. The problem has been numerically simulated and experimenta
Dispersion during bubble-train flow in capillaries
โ Scribed by T.C. Thulasidas; M.A. Abraham; R.L. Cerro
- Publisher
- Elsevier Science
- Year
- 1999
- Tongue
- English
- Weight
- 284 KB
- Volume
- 54
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
โฆ Synopsis
The name bubble-train flow is used to identify the cocurrent flow of gas bubbles and liquid slugs through a capillary. A model was developed to analyze mass transfer between bubbles and liquid slugs during bubble train flow. This mass transfer model, derived from the equations of transport, is based on the fluid flow profiles and has no adjustable parameters. A comprehensive account of the experiments designed to test the model is presented. The single capillary model was used to analyze mass transfer of a passive saline solution introduced as a pulse signal. Theoretical results were used to determine the concentration vs time distribution of the saline solution inside the capillary channels. These results were compared with experimental residence times determined using a conductimetric technique. Very good agreement between theory and experiments was found for single capillaries. The mass transfer model, however, must be modified to take into account macroscopic flow distribution effects before it can be used for the analysis of mass transfer and chemical reaction inside the monolith froth reactor.
๐ SIMILAR VOLUMES
Ibis paper presents the results of an anaIysis of dispersion in a porous medium, for the case when Dorcy's law is valid and the P&let number is large. It is shown tbat, after a sufficiently long time, the effective longitudinal diffusivity is a logarithmic function of the Pellet number. RBsume-Analy
A set of experiments has been performed to analyse gas-phase distribution in horizontal bubble flow. The experimental data have been obtained by means of conductance probes and include measurements of the local void fraction and the bubble diameter and velocity. Present observations show large varia