期刊
CHEMICAL ENGINEERING SCIENCE
卷 246, 期 -, 页码 -出版社
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ces.2021.117007
关键词
CFD; Bubbly flow; Drag force coefficient; Turbulence; Vortex; Hybrid drag model
The study compared several drag models for high-turbulent gas-liquid flows and found that most models performed well upstream of the obstacle but overestimated the void fraction downstream. A hybrid drag model was proposed to improve the prediction of void fraction based on the results.
The accuracy of the modelling of gas-liquid flows depends strongly on a suitable modelling of the inter-facial forces. Among these, drag is dominant. Most drag models reported in the literature have been derived and validated only for laminar or low-turbulent flow conditions. In this study, we numerically evaluated several drag models from the literature for high-turbulent gas-liquid flow around an obstacle in a pipe that creates a distinct vortex region. We performed Computational Fluid Dynamics (CFD) sim-ulations and compared the void fraction and gas velocity profiles with experimental data obtained by ultrafast X-ray computed tomography. We found that all models, except Schiller&Naumann and Feng, predicted the void fraction well compared to experimental data upstream of the obstacle, i.e., for a devel-oped two-phase pipe flow with axial symmetry. However, the void fraction downstream is greatly over-estimated by all models except those that appropriately consider the turbulence effects. Based on the results, a hybrid drag model is proposed that significantly improves the prediction of the void fraction. (c) 2021 Elsevier Ltd. All rights reserved.
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