CFD-PBM simulation with EMMS correctors for bubble column reactors

被引:0
|
作者
Wang J. [1 ,2 ]
Yang N. [1 ]
机构
[1] State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing
[2] University of Chinese Academy of Sciences, Beijing
来源
Huagong Xuebao/CIESC Journal | 2017年 / 68卷 / 07期
基金
中国国家自然科学基金;
关键词
Bubble column; Bubble size distribution; CFD; Gas holdup; Population balance modeling;
D O I
10.11949/j.issn.0438-1157.20170025
中图分类号
学科分类号
摘要
The energy-minimization multi-scale (EMMS) model has been introduced to improve the population balance modeling (PBM) of gas-liquid flows. The energy for bubble breakup and coalescence can be obtained from the EMMS model and then used to derive a correction factor for the coalescence rate. This new model is applied in this study to simulate the bubble columns of high flow rates. Simulations using the three different models, namely, the constant-bubble-size model, the CFD-PBM model and the CFD-PBM-EMMS model, are compared with experimental data. The simulation of CFD-PBM-EMMS gives better prediction for bubble size distribution and liquid axial velocity at different heights as well as the overall and local gas holdup. The relative error of global gas holdup reduces to 5% or 15%, and the mean relative error of local gas holdup reduces to 8% or 17% for 0.16 m·s-1 or 0.25 m·s-1 of superficial gas velocity. © All Right Reserved.
引用
收藏
页码:2667 / 2677
页数:10
相关论文
共 35 条
  • [1] Kantarci N., Borak F., Ulgen K.O., Bubble column reactors, Process Biochem., 40, 7, pp. 2263-2283, (2005)
  • [2] Simcik M., Mota A., Ruzicka M.C., Et al., CFD simulation and experimental measurement of gas holdup and liquid interstitial velocity in internal loop airlift reactor, Chem. Eng. Sci., 66, 14, pp. 3268-3279, (2011)
  • [3] Hibiki T., Ishii M., Lift force in bubbly flow systems, Chem. Eng. Sci., 62, 22, pp. 6457-6474, (2007)
  • [4] Sanyal J., Vasquez S., Roy S., Et al., Numerical simulation of gas-liquid dynamics in cylindrical bubble column reactors, Chem. Eng. Sci., 54, 21, pp. 5071-5083, (1999)
  • [5] Van Baten J.M., Krishna R., CFD simulations of a bubble column operating in the homogeneous and heterogeneous flow regimes, Chem. Eng. Technol., 25, 11, pp. 1081-1086, (2002)
  • [6] Krishnar, Van Baten J.M., Urseanu M.I., Three-phase Eulerian simulations of bubble column reactors operating in the churn-turbulent regime: a scale up strategy, Chem. Eng. Sci., 55, 16, pp. 3275-3286, (2000)
  • [7] Scargiali F., D'Orazio A., Grisafi F., Et al., Modelling and simulation of gas-liquid hydrodynamics in mechanically stirred tanks, Chem. Eng. Res. Des., 85, A5, pp. 637-646, (2007)
  • [8] Wang T.F., Wang J.F., Jin Y., A novel theoretical breakup kernel function for bubbles/droplets in a turbulent flow, Chem. Eng. Sci., 58, 20, pp. 4629-4637, (2003)
  • [9] Qin C.P., Yang N., Population balance modeling of breakage and coalescence of dispersed bubbles of droplets in multiphase systems, Progress in Chemistry, 8, pp. 1207-1233, (2016)
  • [10] Ramkrishna D., Population Balances: Theory and Applications to Particulate Systems in Engineering, (2000)