Theoretical prediction of volumetric mass transfer coefficients in bubble columns for Newtonian and non-Newtonian fluids
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Kawase et al. correlation predictions agree with experimental data with a percentage of 25% for Newtonian fluids and 24% for non-Newtonian fluids.
“The comparison between the predictions given by their correlation agrees with experimental data available in the literature with a percentage of 25% in the case of Newtonian fluids and 24% in the case of non-Newtonian fluids for quite a wide range of conditions.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [338]
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- Authors
- Kawase, Y., Halard, B., & Moo-Young, M.
- Affiliations
- University of Waterloo (CA)
- ORCID
- Kawase, Y.
- Venue
- Chemical Engineering Science
- Publisher
- Elsevier BV
- Published
- 1987
- Volume
- 42
- Issue
- 7
- Pages
- 1609-1617
- ISSN
- 0009-2509 (ISSN-L)
- OpenAlex
- W2059714664
- Cited by
- 224
- References
- 24
- Citations by year
- 2026: 10 · 2025: 9 · 2024: 6 · 2023: 4 · 2022: 12 · 2021: 3 · 2020: 10 · 2019: 12 · 2018: 11 · 2017: 6 · 2016: 14 · 2015: 7 · 2014: 7 · 2013: 7 · 2012: 5
- FWCI
- 3.31
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Chemical Engineering Science (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
- volumetric mass transfer coefficient, bubble column, Higbie penetration theory, non-Newtonian fluids, Newtonian fluid, mass transfer modeling
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