Cited by 15Fluid Dynamics and MixingMinerals Flotation and Separation TechniquesGranular flow and fluidized beds

Flow Simulation in a 2D Bubble Column with the Euler-lagrange and Euler-euler Method

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Weber, Andreas, Bart, Hans-Jörg·2018·The Open Chemical Engineering Journal

Abstract

Object: Bubbly flows, as present in bubble column reactors, can be simulated using a variety of simulation techniques. It is presented, how Computational Fluid Dynamics (CFD) methods are used to simulate a pseudo 2D bubble column using Euler-Lagrange (EL) and Euler-Euler (EE) techniques. Method: The presented EL method uses the open access software OpenFOAM to solve bubble dynamics with bubble interactions computedviaMonte Carlo methods. The estimated bubble size distribution and the predicted hold-up are compared with experimental data and other simulative EE work with a reasonable consensus for both. Benchmarks with state of the art EE simulations shows that the EL approach shows good performance if the bubble number stays at a certain level, as the EL approach scales linearly with the number of bubbles simulated. Therefore, different computational meshes have been used to account for influence of the resolution quality. Conclusion: The EL approach indicated faster solution for all realistic cases, only deliberate decrease of coalescence rates could push CPU time to the limits. Critical bubble number - when EE becomes superior to the EL approach - was estimated to be 40.000 in this particular case.

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Crossref · 10.2174/1874123101812010001

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  • Weber and Bart [243] found that for low-to-moderate values of gas superficial velocity, the results of numerical simulations match well with the experimental results of Diaz et al. [245], while significant deviations are found for high values of gas superficial velocity.

    “They found that for low-to moderate values of gas superficial velocity, the results of numerical simulations match well with the experimental results of Diaz et al. [245]. On the contrary, significant deviations are found in case of high values of gas superficial velocity.”

    From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [243]

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  • Weber and Bart [243] stated that the Euler-Lagrange approach may be advantageous over the Euler-Euler one if the number of bubbles does not exceed 40,000, and recommended using Euler-Euler if the gas hold-up is high (>5%) and if the bubble size is small (<4 mm).

    “stating that the Euler-Lagrange approach may be advantageous over the Euler-Euler one if the number of bubbles does not exceed 40,000. Besides, they recommend to use the Euler-Euler if the gas hold-up is high (&gt;5%) and if the bubble size is small (&lt;4 mm).”

    From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [243]

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Research works printed but not linked: 4

  1. K. Akita, and F. Yoshida, "Bubble Size, Interfacial Area, and Liquid-Phase Mass Transfer Coefficient in Bubble Columns", Ind. Eng. Chem. Process Des. Dev., vol. 13, no. 1, pp. 84-91, 1974.
  2. A. Weber, and H-J. Bart, "Euler-Lagrange simulation of bubble hydrodynamics using a stochastic approach", Young Researchers Symposium 2016 (YRS 2016): Proceedings: April, 14th-15th 2016, Fraunhofer-Zentrum Kaiserslautern, 2016pp. 154-159
  3. A. Tomiyama, "Drag, Lift and Virtual Mass Force Acting on a Single Bubble", 3rd International Symposium on Two-Phase Flow Modelling and Experimentation, 2004 Pisa, Italy
  4. M. Ishii, S. Kim, and J. Kelly, "Development of Interfacial Area Transport Equation", Nucl. Eng. Technol., vol. 2005, no. 37, pp. 525-536, 2005.

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Authors
Weber, A., & Bart, H.-J.
Affiliations
University of Kaiserslautern (DE)
Corresponding author
Bart, Hans-Jörg
Venue
The Open Chemical Engineering Journal
Published
2018-01-25
Volume
12
Issue
1
Pages
1-13
ISSN
1874-1231 (ISSN-L)
OpenAlex
W2648229383
Cited by
15
References
33
Citations by year
2026: 1 · 2025: 1 · 2024: 1 · 2023: 4 · 2022: 3 · 2021: 1 · 2020: 2 · 2019: 1 · 2018: 1
FWCI
0.50
Type
journal article
Language
en
Open access
Locations
  • The Open Chemical Engineering Journal (publishedVersion, cc-by)
  • arXiv (Cornell University) (submittedVersion)
  • arXiv (Cornell University)
Funders
  • Technische Universität Kaiserslautern
  • Deutsche Forschungsgemeinschaft (RTG GrK 1932)
Topics
  • Physical Sciences › Engineering › Biomedical Engineering › Fluid Dynamics and Mixing
  • Physical Sciences › Environmental Science › Water Science and Technology › Minerals Flotation and Separation Techniques
  • Physical Sciences › Engineering › Computational Mechanics › Granular flow and fluidized beds
Keywords
bubble column, bubbly flow, Euler-Lagrange method, bubble dynamics, bubble coalescence, bubble size distribution, void fraction, computational cost, grid resolution, OpenFOAM

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