Detailed modelling of hydrodynamics, mass transfer and chemical reactions in a bubble column using a discrete bubble model: Chemisorption of CO 2 into NaOH solution, numerical and experimental study
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Darmana et al. [254] found that their model reproduces qualitatively very well the entire process, but time-averaged velocities, plume meandering period, and gas hold-up only match well with experiments if mass transfer is neglected; if mass transfer is taken into account, the average bubble size computed numerically is higher than experimentally found, leading to higher gas hold-up, higher flow,
“Although the model reproduces qualitatively very well the entire process, timeaveraged averaged velocities, plume meandering period, and gas hold-up only match well with experiments if mass transfer is neglected. If mass transfer is taken into account, the average bubble size computed numerically is higher compared to the one found experimentally, leading to a higher gas hold-up, higher flow”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [254]
Taborda and Sommerfeld [138] found that their numerical results are in reasonable agreement with the experimental data of [254] in terms of time averaged gas hold-up, equivalent bubble diameter, time averaged bubble velocity and decrease of pH with time.
“The numerical results are in reasonable agreement with the experimental data of [254] in terms of time averaged gas hold-up, equivalent bubble diameter, time averaged bubble velocity and decrease of pH with time.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [254]
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- Authors
- Darmana, D., Henket, R. L. B., Deen, N. G., & Kuipers, J. A. M.
- Affiliations
- University of Twente (NL)
- Corresponding author
- Deen, N.G.
- Venue
- Chemical Engineering Science
- Publisher
- Elsevier BV
- Published
- 2007-05
- Volume
- 62
- Issue
- 9
- Pages
- 2556-2575
- ISSN
- 0009-2509 (ISSN-L)
- OpenAlex
- W1986600499
- Cited by
- 146
- References
- 34
- Citations by year
- 2026: 11 · 2025: 11 · 2024: 10 · 2023: 15 · 2022: 16 · 2021: 17 · 2020: 11 · 2019: 4 · 2018: 10 · 2017: 6 · 2016: 5 · 2015: 7 · 2014: 6 · 2013: 2 · 2012: 2
- FWCI
- 2.63
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Chemical Engineering Science (publishedVersion)
- University of Twente Research Information (publishedVersion)
- TU/e Research Portal (submittedVersion)
- University of Twente Research Information (submittedVersion)
- Funders
- Shell
- Technische Universiteit Delft
- 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, chemisorption, CO2 absorption, NaOH solution, Euler-Lagrange model, discrete bubble model, mass transfer, chemical reactions, bubble hydrodynamics, bubble size distribution, gas holdup, bubble velocity, particle image velocimetry
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