29.09.2024

New publication available online!

PhD candidate Christian Weiland and Professor Michael Schlüter from the Institute of Multiphase Flows Flows at the Hamburg University of Technology together with Professor Alexandra von Kameke from the Department of Mechanical Engineering and Production Management at the Hamburg University of Applied Sciences have presented their latest results on trajectory-based breakup modelling for dense bubbly flows.

The new model predicts the breakup of gaseous bubbles in a continuous liquid phase by treating each bubble as a spring-damper system (Kelvin-Voigt element). The model derives the outer force from Lagrangian analysis of the flow field's stretching rate, adhering to physical principles without arbitrary parameters. Each bubble's individual history is considered, and the model enables numerical simulations across scales from 3 L to 15 m³. Its simplicity offers a favorable cost-benefit ratio. Results are compared to experimental data from optical measurements in a 200 L aerated stirred tank reactor at varying stirrer frequencies.

Weiland, C., von Kameke, A., Schlüter, M. (2024). Trajectory-based breakup modelling for dense bubbly flows. Chemical Engineering Journal 499, 155726.

https://doi.org/10.1016/j.cej.2024.155726