𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Liquid Dispersion in Large Diameter Bubble Columns, with and without Internals

✍ Scribed by Ann Forret; Jean-Marc Schweitzer; Thierry Gauthier; Rajamani Krishna; Daniel Schweich


Publisher
John Wiley and Sons
Year
2008
Tongue
English
Weight
625 KB
Volume
81
Category
Article
ISSN
0008-4034

No coin nor oath required. For personal study only.

✦ Synopsis


Abstract

Liquid mixing has been studied in a 1 m diameter bubble column, with and without internals (vertical cooling tubes). The presence of internals significantly affects both large scale recirculation and local dispersion. The most common approach to model liquid mixing is the one‐dimensional axial dispersion model, validated many times in small bubble columns without internals. This paper shows that this model is still appropriate to large columns, but without internals. A two‐dimensional model, taking into account a radially dependent axial velocity profile, and both axial and radial dispersion, is required to account for the internals on liquid mixing.


πŸ“œ SIMILAR VOLUMES


Liquid mixing based on convection and tu
✍ S. Degaleesan; S. Roy; S.B. Kumar; M.P. DudukoviΔ‡ πŸ“‚ Article πŸ“… 1996 πŸ› Elsevier Science 🌐 English βš– 583 KB

A phenomenological model for liquid mixing, that captures the essence of the ob-Served physical phenomena in bubble columns, is presented. In this model, mixing of the liquid phase is considered to be primarily due to convective recirculation and turbulence caused by the rising gas bubbles. The mixi

Gas-liquid mass transfer in bubble colum
✍ Arto Laari; Juha Kallas; Seppo Palosaari πŸ“‚ Article πŸ“… 1997 πŸ› John Wiley and Sons 🌐 English βš– 565 KB

Bubble break-up, gas holdup, and the gas-liquid volumetric mass transfer coefficient are studied in a bubble column reactor with simultaneous injection of a gas and liquid through a T-junction nozzle. The theoretical dependence of bubble break-up and the volumetric mass transfer coefficient on liqui