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CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation

Received: 3 January 2024    Accepted: 17 January 2024    Published: 1 February 2024
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Abstract

In most mammalian cell culture operations, the pH is targeted to be close to neutral and the dissolved carbon dioxide [dCO2] concentration is desired to remain between 5 and 15% to avoid any inhibitory effects on cell growth. Typical cell culture scale-up approaches include maintaining constant power by volume (P/V) or a constant tip speed to set the impeller agitation rate or constant vvm to set the gas flow rate. However, these approaches are only focused on keeping the shear in the bioreactor system to a minimum and do not account for controlling the [dCO2] concentration within the desired range. Process engineers across industries have remediated the elevated [dCO2] concentration problem in large scale bioreactors by increasing gas flow rates; however, this approach is often trial and error. Therefore, in this article we review the current understanding of various factors that impact the dCO2 concentration during the scale up of the cell culture process to large-scale bioreactors. This article also describes an easy and practical approach to predict and control the dCO2 concentration in large-scale cell culture bioreactors using a mathematical predictive model developed based on mass-transfer first principles. We demonstrate the effective application and verification of the model by running a CHO cell culture process with a peak cell density of up to 20 x106 Cells/mL in a 15,000 L bioreactor working volume.

Published in Advances in Bioscience and Bioengineering (Volume 12, Issue 1)
DOI 10.11648/abb.20241201.11
Page(s) 1-13
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

Bioreactor Scale Up, CO2 Control, Kla, Cell Culture CO2 Concentration, CO2 Predictive Model, CO2 Bubble Saturation Time

References
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[2] Muralidharan, N., Johnson, T., & Davis, M. (2023, November 16). Identifying False Metabolite Measurements During Cell-Culture Monitoring Effective Application of the Multivariate Hotelling’s T2 Statistic. Bioprocess International, 21(11-12), 29-31. Retrieved from https://bioprocessintl.com/2023/november-december-2023/identifying-false-metabolite-measurements-during-cell-culture-monitoring-effective-application-of-the-multivariate-hotellings-t2-statistic/
[3] Xing, Z., Lewis, A. M., Borys, M. C., & Li, Z. J. (2017). A carbon dioxide stripping model for mammalian cell culture in manufacturing scale bioreactors. Biotechnology and Bioengineering, 114(6), 1184-1194. https://doi.org/10.1002/bit.26232
[4] DeZengotita, V. M., Schmelzer, A. E., & Miller, W. M. (2002). Characterization of hybridoma cell responses to elevated pCO2 and osmolality: Intracellular pH, cell size, apoptosis, and metabolism. Biotechnology and Bioengineering, 77(4), 369-380. https://doi.org/10.1002/bit.10176
[5] Mostafa, S. S., & Gu, X. (2003). Strategies for improved dCO2 removal in large‐scale fed‐batch cultures. Biotechnology Progress, 19(1), 45-51. https://doi.org/10.1021/bp0256263
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[7] Hu, W. "OXYGEN TRANSFER IN CELL CULTURE BIOREACTORS." In Cell Culture Bioprocess Engineering, 2nd ed., 219. CRC Press, 2020.
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[13] Sieblist, C., Hägeholz, O., Aehle, M., Jenzsch, M., Pohlscheidt, M., & Lübbert, A. (2011). Insights into large‐scale cell‐culture reactors: II. gas‐phase mixing and CO2 stripping. Biotechnology Journal, 6(12), 1547-1556. https://doi.org/10.1002/biot.201100153
[14] Liow, K. Y., Thouas, G. A., Tan, B. T., Thompson, M. C., & Hourigan, K. (2009). Modelling the transport of momentum and oxygen in an aerial-disk driven bioreactor used for animal tissue or cell culture. IFMBE Proceedings, 1672-1675. https://doi.org/10.1007/978-3-540-92841-6_415
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[17] Muralidharan, N., Bolduc, E., & Davis, M. (2024, January/February). Characterizing Oxygen Mass Transfer and Shear During Cell Culture Calculating the Maximum Cell Density Supported By a 20,000-Liter Stirred-Tank Bioreactor. Bioprocess International, 22(1-2).
[18] Baz-Rodr'ıguez, S., Aguilar-Corona, A., & Soria, A. (2012). RISING VELOCITY FOR SINGLE BUBBLES IN PURE LIQUIDS. Revista Mexicana de Ingenier'ıa Qu'ımica, 11(2), 269-278. https://www.scielo.org.mx/pdf/rmiq/v11n2/v11n2a6.pdf
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Cite This Article
  • APA Style

    Muralidharan, N., Johnson, T., Bolduc, E., Davis, M. (2024). CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation. Advances in Bioscience and Bioengineering, 12(1), 1-13. https://doi.org/10.11648/abb.20241201.11

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    ACS Style

    Muralidharan, N.; Johnson, T.; Bolduc, E.; Davis, M. CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation. Adv. BioSci. Bioeng. 2024, 12(1), 1-13. doi: 10.11648/abb.20241201.11

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    AMA Style

    Muralidharan N, Johnson T, Bolduc E, Davis M. CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation. Adv BioSci Bioeng. 2024;12(1):1-13. doi: 10.11648/abb.20241201.11

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  • @article{10.11648/abb.20241201.11,
      author = {Naveenganesh Muralidharan and Thatsinee Johnson and Emma Bolduc and Mark Davis},
      title = {CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation},
      journal = {Advances in Bioscience and Bioengineering},
      volume = {12},
      number = {1},
      pages = {1-13},
      doi = {10.11648/abb.20241201.11},
      url = {https://doi.org/10.11648/abb.20241201.11},
      eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.abb.20241201.11},
      abstract = {In most mammalian cell culture operations, the pH is targeted to be close to neutral and the dissolved carbon dioxide [dCO2] concentration is desired to remain between 5 and 15% to avoid any inhibitory effects on cell growth. Typical cell culture scale-up approaches include maintaining constant power by volume (P/V) or a constant tip speed to set the impeller agitation rate or constant vvm to set the gas flow rate. However, these approaches are only focused on keeping the shear in the bioreactor system to a minimum and do not account for controlling the [dCO2] concentration within the desired range. Process engineers across industries have remediated the elevated [dCO2] concentration problem in large scale bioreactors by increasing gas flow rates; however, this approach is often trial and error. Therefore, in this article we review the current understanding of various factors that impact the dCO2 concentration during the scale up of the cell culture process to large-scale bioreactors. This article also describes an easy and practical approach to predict and control the dCO2 concentration in large-scale cell culture bioreactors using a mathematical predictive model developed based on mass-transfer first principles. We demonstrate the effective application and verification of the model by running a CHO cell culture process with a peak cell density of up to 20 x106 Cells/mL in a 15,000 L bioreactor working volume.},
     year = {2024}
    }
    

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  • TY  - JOUR
    T1  - CO2 Control Strategy for Large-Scale Cell Culture Bioreactor Operation
    AU  - Naveenganesh Muralidharan
    AU  - Thatsinee Johnson
    AU  - Emma Bolduc
    AU  - Mark Davis
    Y1  - 2024/02/01
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    N1  - https://doi.org/10.11648/abb.20241201.11
    DO  - 10.11648/abb.20241201.11
    T2  - Advances in Bioscience and Bioengineering
    JF  - Advances in Bioscience and Bioengineering
    JO  - Advances in Bioscience and Bioengineering
    SP  - 1
    EP  - 13
    PB  - Science Publishing Group
    SN  - 2330-4162
    UR  - https://doi.org/10.11648/abb.20241201.11
    AB  - In most mammalian cell culture operations, the pH is targeted to be close to neutral and the dissolved carbon dioxide [dCO2] concentration is desired to remain between 5 and 15% to avoid any inhibitory effects on cell growth. Typical cell culture scale-up approaches include maintaining constant power by volume (P/V) or a constant tip speed to set the impeller agitation rate or constant vvm to set the gas flow rate. However, these approaches are only focused on keeping the shear in the bioreactor system to a minimum and do not account for controlling the [dCO2] concentration within the desired range. Process engineers across industries have remediated the elevated [dCO2] concentration problem in large scale bioreactors by increasing gas flow rates; however, this approach is often trial and error. Therefore, in this article we review the current understanding of various factors that impact the dCO2 concentration during the scale up of the cell culture process to large-scale bioreactors. This article also describes an easy and practical approach to predict and control the dCO2 concentration in large-scale cell culture bioreactors using a mathematical predictive model developed based on mass-transfer first principles. We demonstrate the effective application and verification of the model by running a CHO cell culture process with a peak cell density of up to 20 x106 Cells/mL in a 15,000 L bioreactor working volume.
    VL  - 12
    IS  - 1
    ER  - 

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Author Information
  • Manufacturing Science and Technology (MSAT), AGC Biologics, Boulder, USA

  • Manufacturing Science and Technology (MSAT), AGC Biologics, Boulder, USA

  • Manufacturing Science and Technology (MSAT), AGC Biologics, Boulder, USA

  • Manufacturing Science and Technology (MSAT), AGC Biologics, Boulder, USA

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