Abstract
Population balance equations with different bubble diameters are combined with classical Euler/Euler hydrodynamic simulation to investigate turbulent bubble flow in a vertical pipe in the present work. The universal basic averaged equations for bubble flow are developed by applying the volume-averaging operator to the local instantaneous flow equations. Based on the analysis of the motion of the bubbles in the flow field and the influence of bubble coalescence and break-up, the constitutive relation is determined. Comparison of the available experimental data with the present model prediction shows that the model can be used to predict the local volume fraction, radial velocity profiles, turbulence kinetic energy, mean bubble diameter and the evolution of mean bubble diameter due to the reasonable consideration of the interaction between the two phases and the influence of bubble coalescence and break-up.
| Original language | English |
|---|---|
| Pages (from-to) | 563-568 |
| Number of pages | 6 |
| Journal | Huagong Xuebao/Journal of Chemical Industry and Engineering (China) |
| Volume | 55 |
| Issue number | 4 |
| State | Published - Apr 2004 |
Keywords
- Bubble coalescence and break-up
- Turbulent bubbly flow
- Two-phase flow model
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