Eulerian-Lagrangian simulations of unsteady gas-liquid flows in bubble columns
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Vieira et al. [308] found time-averaged axial liquid velocity and gas hold-up compare well against experimental results; modified k-# model delivers the best results, being a good compromise between simplicity and accuracy.
“Nevertheless, the time-averaged axial liquid velocity and the gas hold-up compare well against experimental results [158,309,310]. They conclude that the modified k -# model delivers the best results, being a good compromise between simplicity of modeling and accuracy of the predictions.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [309]
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- Authors
- Buwa, V. V., Deo, D. S., & Ranade, V. V.
- Affiliations
- National Chemical Laboratory (IN)
- Corresponding author
- Ranade, Vivek V.
- Venue
- International Journal of Multiphase Flow
- Publisher
- Elsevier BV
- Published
- 2006-07
- Volume
- 32
- Issue
- 7
- Pages
- 864-885
- ISSN
- 0301-9322 (ISSN-L)
- OpenAlex
- W1978913313
- Cited by
- 160
- References
- 29
- Citations by year
- 2026: 7 · 2024: 10 · 2023: 5 · 2022: 5 · 2021: 9 · 2020: 10 · 2019: 20 · 2018: 7 · 2017: 6 · 2016: 8 · 2015: 7 · 2014: 16 · 2013: 8 · 2012: 4
- FWCI
- 5.37
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- International Journal of Multiphase Flow (publishedVersion)
- 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, gas-liquid two-phase flow, Eulerian-Lagrangian simulation, bubble dynamics, superficial gas velocity, height-to-width ratio, lift force, numerical diffusion, wall pressure, bubble size, mass transfer
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