Abstract
In this work we present a numerical model to predict the bubble size distribution in turbulent bubbly flows. The continuous phase is described by the volume-averaged Navier–Stokes equations, which are solved on an Eulerian grid, whereas the dispersed or bubble phase is treated in a Lagrangian manner, where each individual bubble is tracked throughout the computational domain. Collisions between bubbles are described by means of a hard-sphere model. Coalescence of bubbles is modeled via a stochastic inter-particle encounter model. A break-up model is implemented with a break-up constraint on the basis of a critical Weber value augmented with a model for the daughter size distribution. A numerical parameter study is performed of the bubble break-up model implemented in the deterministic Euler–Lagrange framework and its effect on the bubble size distribution (BSD) is reported. A square bubble column operated at a superficial gas velocity of 2 cm/s is chosen as a simulation base case to evaluate the parameters. The parameters that are varied are the values of the critical Weber number (WecritWecrit), the daughter size distribution (β ) and the superficial gas velocity (vsupvsup). Changes in the values of WecritWecrit and vsupvsup have a significant impact on the overall BSD, while a different shaped β did not show a significant difference.
Original language | English |
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Pages (from-to) | 9-22 |
Number of pages | 14 |
Journal | Chemical Engineering Science |
Volume | 108 |
DOIs | |
Publication status | Published - 28 Apr 2014 |
Keywords
- Euler-Lagrange model
- Bubble columns
- Coalescence
- Break-up
- Daughter size distribution