In an air-water-only system under batch operation, a bubble interface was created in a laboratory column by introducing a step change in gas flow, and the rise velocity of this interface, u~n, was measured using a novel method based on electrical conductivity with a custom-designed fast-response con
Bubble swarm velocity in a column: a two-dimensional approach
โ Scribed by G. Shen; J.A. Finch
- Publisher
- Elsevier Science
- Year
- 1997
- Tongue
- English
- Weight
- 470 KB
- Volume
- 52
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
โฆ Synopsis
The average gas velocity, ug, is widely used as a measure of bubble swarm velocity in a column. However, it is only correct in the ideal case: i.e. uniform distribution of uni-sized bubbles. Under real conditions, i.e. a non-uniform distribution of multi-sized bubbles, the hindered velocity, Uh, obtained by interpolating the interface rise velocity, was identified with the real bubble swarm velocity by the authors (Shen and Finch, 1996, Chem. Engng Sci. 51, 3665-3674).
The ideal case is akin to a one-dimensional domain. In the two-dimensional domain, with a knowledge of the radial gas holdup profile and liquid circulation velocity over the cross section of the column, Uh was simulated using the model of Richardson and Zaki with the coefficient me describing the system characteristics. The observation that uh <<. Ug was mathematically proved by an inequality assuming a parabolic gas holdup profile of order n = 2.
๐ SIMILAR VOLUMES
This paper develops a procedure for estimation of the rise velocity of a swarm of large gas bubbles in a bubble column operating in the churn-turbulent flow regime. The large bubble swarm velocity is estimated by introducing two correction factors into the classical relation for rise of a single sp
This paper reports on LDA experiments in bubble columns 15.2, 23.4, and 38.4 cm in diameter. The gas fraction ranges up to 25%, but the columns are still in the bubbly regime, i.e. coalescence of bubbles is minor. It is shown that both the axial and tangential liquid velocity components can be measu