Insights in hydrodynamics of bubbling fluidized beds at elevated pressure by DEM-CFD approach

• Published in: Particuology Vol. 8; no. 5; pp. 407 - 414
• Main Author: Zahra Mansourpour Sedighe Karimi Reza Zarghami Navid Mostoufi Rahmat Sotudeh-Gharebagh
• Format: Journal Article
• Language: English
• Published: Elsevier B.V 01.10.2010; Process Design and Simulation Research Center, Oil and Gas Centre of Excellence, School of Cheraical Engineering, University of Tehran, P.O. Box 11155-4563, Tehran, Iran
• Subjects: Bubble; Bubbles; Computational fluid dynamic; Computational fluid dynamics; Computer simulation; DEM; Discrete element method; Elevated; Elevated pressure; Fluid flow; Fluidized bed; Fluidized beds; Hydrodynamics; Mathematical models; Pressure fluctuations; 力学方法; 加压流化床; 气泡动力学; 水动力特性; Bubble; Elevated pressure; Discrete element method; Computational fluid dynamic; Pressure fluctuations; Fluidized bed
• ISSN: 1674-2001; 1672-2515; 2210-4291
• DOI: 10.1016/j.partic.2010.03.017

A numerical simulation was conducted to study the effect of pressure on bubble dynamics in a gas-solid fluidized bed. The gas flow was modeled using the continuum theory and the solid phase, by the discrete element method （DEM）. To validate the simulation results, calculated local pressure fluctuations were compared with corresponding experimental data of 1-mm polyethylene particles. It was shown that the model successfully predicts the hydrodynamic features of the fluidized bed as observed in the experiments. Influence of pressure on bubble rise characteristics such as bubble rise path, bubble stability, average bubbles diameter and bubble velocity through the bed was investigated. The simulation results are in conformity with current hydrodynamic theories and concepts for fluidized beds at high pressures. The results show further that elevated pressure reduces bubble growth, velocity and stability and enhances bubble gyration through the bed, leading to change in bed flow structure.