This paper investigates a computational study of air bubbles rising in massecuite equivalent non-Newtonian crystal suspensions. Bubble rise motion inside the stagnant liquid of 0.05% xanthan gum crystal suspension was investigated and modelled using computational fluid dynamics (CFD) model to gain an insight into the bubble flow distribution. CFD code FLUENT was used for numerical simulation and bubble rise characteristics were computed through a Volume of Fluid (VOF) model. The influences of the Reynolds number (Re) along with other dimensionless groups such the Weber number (We ), and the Eötvös number (Eo) on bubble velocity and bubble trajectory are discussed. The effects of the vortices on bubble velocity distribution are analyzed. The simulated results of the bubble flow contours were validated by the experimental results. The model developed is capable of predicting the entire flow characteristics of different sizes of bubble inside the liquid column.
Funding
Category 1 - Australian Competitive Grants (this includes ARC, NHMRC)
History
Start Page
1671
End Page
1676
Number of Pages
6
Start Date
2010-01-01
ISBN-13
9781868548187
Location
Antalya, Turkey
Publisher
HEFAT
Place of Publication
Antalya, Turkey
Peer Reviewed
No
Open Access
No
External Author Affiliations
Faculty of Sciences, Engineering and Health; Institute for Resource Industries and Sustainability (IRIS);
Era Eligible
No
Name of Conference
International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics