๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Dispersion during bubble-train flow in capillaries

โœ 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.

โœฆ 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.


๐Ÿ“œ SIMILAR VOLUMES


Radial mass-transfer enhancement in bubb
โœ Rainer Gruber; Thomas Melin ๐Ÿ“‚ Article ๐Ÿ“… 2003 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 201 KB

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 in flow through a network of
โœ P.G. Saffman ๐Ÿ“‚ Article ๐Ÿ“… 1959 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 430 KB

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

Bubble dispersion in free shear flows
โœ C.W. Stewart; C.T. Crowe ๐Ÿ“‚ Article ๐Ÿ“… 1993 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 476 KB
Void wave dispersion in bubbly flows
โœ J-W. Park; D.A. Drew; R.T. Lahey Jr.; A. Clausse ๐Ÿ“‚ Article ๐Ÿ“… 1990 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 488 KB
Dispersed bubble flow in horizontal pipe
โœ Paolo Andreussi; Alessandro Paglianti; Florencio Sanchez Silva ๐Ÿ“‚ Article ๐Ÿ“… 1999 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 230 KB

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