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  4. Modeling and validating of oxygen transport in wave bioreactors: optimized experimental mass transfer method and novel Lattice-Boltzmann CFD approach
 
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Modeling and validating of oxygen transport in wave bioreactors: optimized experimental mass transfer method and novel Lattice-Boltzmann CFD approach

Citation Link: https://doi.org/10.15480/882.16715
Publikationstyp
Journal Article
Date Issued
2026-01-21
Sprache
English
Author(s)
Piontek, Sina
Fitschen, Jürgen 
Weiland, Christian  
Mehrphasenströmungen V-5  
Habicher, Tobias  
Schlüter, Michael  orcid-logo
Mehrphasenströmungen V-5  
Wucherpfennig, Thomas  
TORE-DOI
10.15480/882.16715
TORE-URI
https://hdl.handle.net/11420/61554
Journal
Frontiers in bioengineering and biotechnology  
Volume
13
Article Number
1688774
Citation
Frontiers in Bioengineering and Biotechnology 13: 1688774 (2026)
Publisher DOI
10.3389/fbioe.2025.1688774
Scopus ID
2-s2.0-105029223303
Publisher
Frontiers Media SA
Wave bioreactors are commonly used in biopharmaceutical upstream processes as an intermediate stage between shake flasks and stirred tanks within the seed train. They offer a controlled environment for cell cultivation while minimizing shear stress. Accurate characterization of these systems is essential for optimizing cell culture performance, particularly as state of the art cell lines require higher volumetric mass transfer coefficients k<inf>L</inf>a. This study aims to determine the volumetric mass transfer coefficient through experiments and computational fluid dynamics (CFD) simulations. An improved experimental method for the measurements of the volumetric mass transfer is presented, with results correlated to key process parameters: rocking angle, rocking rate, and filling volume. In addition, CFD simulations were caried out using M-Star CFD by means of a Lattice-Boltzmann Method-based solver. The mass transfer was calculated using Higbie’s penetration theory, incorporating the Kolmogorov scale to define contact time. The analysis also integrates concepts from Friedl and the surface renewal model, introducing the surface normal velocity as an additional parameter in the mass transfer coefficient k<inf>L</inf> calculation. Analyzes were carried out for 10 and 50 L wave bioreactors, with one degree of freedom movement. Optimized process parameters were identified and validated in biological cultivations, resulting in increased dissolved oxygen levels in the medium. These findings contribute to improved characterization and control of wave bioreactors, enabling more accurate prediction of process parameter effects.
Subjects
CFD
process optimization
rocked bioreactor
single use
volumetric mass transfer coefficient
wave bioreactor
DDC Class
660: Chemistry; Chemical Engineering
577: Ecology
620.1: Engineering Mechanics and Materials Science
Lizenz
https://creativecommons.org/licenses/by/4.0/
Publication version
publishedVersion
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