Frontiers of Chemical Science and Engineering >
Simulation of bubble column reactors using CFD coupled with a population balance model
Received date: 12 Oct 2009
Accepted date: 29 Apr 2010
Published date: 05 Jun 2011
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Bubble columns are widely used in chemical and biochemical processes due to their excellent mass and heat transfer characteristics and simple construction. However, their fundamental hydrodynamic behaviors, which are essential for reactor scale-up and design, are still not fully understood. To develop design tools for engineering purposes, much research has been carried out in the area of computational fluid dynamics (CFD) modeling and simulation of gas-liquid flows. Due to the importance of the bubble behavior, the bubble size distribution must be considered in the CFD models. The population balance model (PBM) is an effective approach to predict the bubble size distribution, and great efforts have been made in recent years to couple the PBM into CFD simulations. This article gives a selective review of the modeling and simulation of bubble column reactors using CFD coupled with PBM. Bubble breakup and coalescence models due to different mechanisms are discussed. It is shown that the CFD-PBM coupled model with proper bubble breakup and coalescence models and interphase force formulations has the ability of predicting the complex hydrodynamics in different flow regimes and, thus, provides a unified description of both the homogeneous and heterogeneous regimes. Further study is needed to improve the models of bubble coalescence and breakup, turbulence modification in high gas holdup, and interphase forces of bubble swarms.
Tiefeng WANG . Simulation of bubble column reactors using CFD coupled with a population balance model[J]. Frontiers of Chemical Science and Engineering, 2011 , 5(2) : 162 -172 . DOI: 10.1007/s11705-009-0267-5
1 |
Wang T, Wang J, Jin Y. Slurry reactors for gas-to-liquid processes: a review. Industrial & Engineering Chemistry Research, 2007, 46(18): 5824-5847
|
2 |
Rafique M, Chen P, Dudukovic M P. Computational modeling of gas-liquid flow in bubble columns. Rev Chem Eng, 2004, 20: 225-375
|
3 |
Lehr F, Millies M, Mewes D. Bubble-size distributions and flow fields in bubble columns. AIChE Journal. American Institute of Chemical Engineers, 2002, 48(11): 2426-2443
|
4 |
Jakobsen H A, Lindborg H, Dorao C A. Modeling of bubble column reactors: progress and limitations. Industrial & Engineering Chemistry Research, 2005, 44(14): 5107-5151
|
5 |
Bhole M R, Joshi J B, Ramkrishna D. CFD simulation of bubble columns incorporating population balance modeling. Chemical Engineering Science, 2008, 63(8): 2267-2282
|
6 |
Wang T, Wang J, Jin Y A. CFD-PBM coupled model for gas-liquid flows. AIChE Journal. American Institute of Chemical Engineers, 2006, 52(1): 125-140
|
7 |
Joshi J B. Computational flow modelling and design of bubble column reactors. Chemical Engineering Science, 2001, 56(21-22): 5893-5933
|
8 |
Tomiyama A, Tamai H, Zun I, Hosokawa S. Transverse migration of single bubbles in simple shear flows. Chemical Engineering Science, 2002, 57(11): 1849-1858
|
9 |
Ramkrishna D. Population balances. San Diego: Academic Press, 2000
|
10 |
Kumar S, Ramkrishna D. On the solution of population balance equations by discretization. 1. A fixed pivot technique. Chemical Engineering Science, 1996, 51(8): 1311-1332
|
11 |
Wang T, Wang J, Jin Y. Population balance model for gas-liquid flows: influence of bubble coalescence and breakup models. Industrial & Engineering Chemistry Research, 2005, 44(19): 7540-7549
|
12 |
Liao Y X, Lucas D. A literature review of theoretical models for drop and bubble breakup in turbulent dispersions. Chemical Engineering Science, 2009, 64(15): 3389-3406
|
13 |
Lasheras J C, Eastwood C, Martinez-Bazan C, Montanes J L. A review of statistical models for the break-up of an immiscible fluid immersed into a fully developed turbulent flow. International Journal of Multiphase Flow, 2002, 28(2): 247-278
|
14 |
Wang T F, Wang J F, Jin Y. A novel theoretical breakup kernel function for bubbles/droplets in a turbulent flow. Chemical Engineering Science, 2003, 58(20): 4629-4637
|
15 |
Alopaeus V, Koskinen J, Keskinen K I, Majander J. Simulation of the population balances for liquid-liquid systems in a nonideal stirred tank. Part 2. Parameter fitting and the use of the multiblock model for dense dispersions. Chemical Engineering Science, 2002, 57(10): 1815-1825
|
16 |
Luo H, Svendsen H F. Theoretical model for drop and bubble breakup in turbulent dispersions. AIChE Journal. American Institute of Chemical Engineers, 1996, 42(5): 1225-1233
|
17 |
Kostoglou M, Karabelas A J. Toward a unified framework for the derivation of breakage functions based on the statistical theory of turbulence. Chemical Engineering Science, 2005, 60(23): 6584-6595
|
18 |
Wang T F, Wang J F, Jin J. An efficient numerical algorithm for “A novel theoretical breakup kernel function of bubble/droplet in a turbulent flow”. Chemical Engineering Science, 2004, 59(12): 2593-2595
|
19 |
Martínez-Bazán C, Montanes J L, Lasheras J C. On the breakup of an air bubble injected into a fully developed turbulent flow. Part 2. Size PDF of the resulting daughter bubbles. Journal of Fluid Mechanics, 1999, 401: 183-207
|
20 |
Fu X Y, Ishii M. Two-group interfacial area transport in vertical air-water flow. I. Mechanistic model. Nuclear Engineering and Design, 2003, 219(2): 143-168
|
21 |
Wang T, Wang J, Jin Y. Theoretical prediction of flow regime transition in bubble columns by the population balance model. Chemical Engineering Science, 2005, 60(22): 6199-6209
|
22 |
Prince M J, Blanch H W. Bubble coalescence and break-up in air-sparged bubble-columns. AIChE Journal. American Institute of Chemical Engineers, 1990, 36(10): 1485-1499
|
23 |
Sha Z, Laari A, Turunen I. Multi-phase-multi-size group model for the inclusion of population balances into the CFD simulation of gas-liquid bubbly flows. Chemical Engineering & Technology, 2006, 29(5): 550-559
|
24 |
Wang T, Wang J. Numerical simulations of gas-liquid mass transfer in bubble columns with a CFD-PBM coupled model. Chemical Engineering Science, 2007, 62(24): 7107-7118
|
25 |
Ekambara K, Nandakumar K, Joshi J B. CFD simulation of bubble column reactor using population balance. Industrial & Engineering Chemistry Research, 2008, 47(21): 8505-8516
|
26 |
Degaleesan S, Dudukovic M, Pan Y. Experimental study of gas-induced liquid-flow structures in bubble columns. AIChE Journal. American Institute of Chemical Engineers, 2001, 47(9): 1913-1931
|
27 |
Koynov A, Khinast J G, Tryggvason G. Mass transfer and chemical reactions in bubble swarms with dynamic interfaces. AIChE Journal. American Institute of Chemical Engineers, 2005, 51(10): 2786-2800
|
28 |
Zhao H, Ge W. A theoretical bubble breakup model for slurry beds or three-phase fluidized beds under high pressure. Chemical Engineering Science, 2007, 62(1-2): 109-115
|
29 |
Troshko A A, Zdravistch F. CFD modeling of slurry bubble column reactors for Fisher-Tropsch synthesis. Chemical Engineering Science, 2009, 64(5): 892-903
|
30 |
Cheung S C P, Yeoh G H, Tu J Y. Population balance modeling of bubbly flows considering the hydrodynamics and thermomechanical processes. AIChE Journal. American Institute of Chemical Engineers, 2008, 54(7): 1689-1710
|
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