Abstract
The gas–liquid flow behavior of the stirred flow field, the different positions of a single bubble, the initial velocity, the surface tension and the agglomeration of multiple bubbles were studied by CFD numerical simulation. The results show that the pressure distribution and velocity distribution inside the fluid during agitation indicate that the velocity difference between the liquid and the gas phase and the collision between the bubbles caused by the turbulent behavior of the liquid are the important conditions leading to the bubble breakage. Different initial bubble positions and initial bubble velocities have important effects on single bubble breakage. The surface tension is an important condition that affects the bubble breakage. When the surface tension coefficient is 0.7, the bubble will be stretched to the smallest degree; when the surface tension coefficient is 0.1, the bubble will be stretched to the largest degree and it will be easily broken into smaller bubbles. The multi-bubble results show the states and trajectories of coalescence between bubbles. The research results can provide data support for the engineering application of desulfurization process and theoretical guidance for the research of bubble breaking mechanism.
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Acknowledgements
This research was supported by the National Natural Science Foundation of China (51904069), the Fundamental Research Funds for the Central Universities (N2223026), and the Scientific Research Fund Project of Northeastern University at Qinhuangdao (XNY201808).
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Lv, C., Chen, Xx., Ji, Zx. et al. Simulation of bubble breaking process in a jet mixing reactor for desulfurization of molten iron. J. Iron Steel Res. Int. 30, 1117–1127 (2023). https://doi.org/10.1007/s42243-023-00984-8
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DOI: https://doi.org/10.1007/s42243-023-00984-8