Literature DB >> 26231834

Equipment characterization to mitigate risks during transfers of cell culture manufacturing processes.

Christian Sieblist1, Marco Jenzsch2, Michael Pohlscheidt2.   

Abstract

The production of monoclonal antibodies by mammalian cell culture in bioreactors up to 25,000 L is state of the art technology in the biotech industry. During the lifecycle of a product, several scale up activities and technology transfers are typically executed to enable the supply chain strategy of a global pharmaceutical company. Given the sensitivity of mammalian cells to physicochemical culture conditions, process and equipment knowledge are critical to avoid impacts on timelines, product quantity and quality. Especially, the fluid dynamics of large scale bioreactors versus small scale models need to be described, and similarity demonstrated, in light of the Quality by Design approach promoted by the FDA. This approach comprises an associated design space which is established during process characterization and validation in bench scale bioreactors. Therefore the establishment of predictive models and simulation tools for major operating conditions of stirred vessels (mixing, mass transfer, and shear force.), based on fundamental engineering principles, have experienced a renaissance in the recent years. This work illustrates the systematic characterization of a large variety of bioreactor designs deployed in a global manufacturing network ranging from small bench scale equipment to large scale production equipment (25,000 L). Several traditional methods to determine power input, mixing, mass transfer and shear force have been used to create a data base and identify differences for various impeller types and configurations in operating ranges typically applied in cell culture processes at manufacturing scale. In addition, extrapolation of different empirical models, e.g. Cooke et al. (Paper presented at the proceedings of the 2nd international conference of bioreactor fluid dynamics, Cranfield, UK, 1988), have been assessed for their validity in these operational ranges. Results for selected designs are shown and serve as examples of structured characterization to enable fast and agile process transfers, scale up and troubleshooting.

Entities:  

Keywords:  Cell culture; Large scale bioreactors; Mixing; Oxygen mass transfer; Scale up

Year:  2015        PMID: 26231834      PMCID: PMC4960186          DOI: 10.1007/s10616-015-9899-0

Source DB:  PubMed          Journal:  Cytotechnology        ISSN: 0920-9069            Impact factor:   2.058


  36 in total

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Journal:  Nat Biotechnol       Date:  2004-11       Impact factor: 54.908

2.  Scale-up methodologies for Escherichia coli and yeast fermentation processes.

Authors:  Beth Helene Junker
Journal:  J Biosci Bioeng       Date:  2004       Impact factor: 2.894

3.  Physiological responses of CHO cells to repetitive hydrodynamic stress.

Authors:  Ruben Godoy-Silva; Jeffrey J Chalmers; Susan A Casnocha; Laura A Bass; Ningning Ma
Journal:  Biotechnol Bioeng       Date:  2009-08-15       Impact factor: 4.530

4.  Reactor design for large scale suspension animal cell culture.

Authors:  J Varley; J Birch
Journal:  Cytotechnology       Date:  1999-05       Impact factor: 2.058

5.  Animal cells in turbulent fluids: details of the physical stimulus and the biological response.

Authors:  R S Cherry
Journal:  Biotechnol Adv       Date:  1993       Impact factor: 14.227

6.  Insights into large-scale cell-culture reactors: I. Liquid mixing and oxygen supply.

Authors:  Christian Sieblist; Marco Jenzsch; Michael Pohlscheidt; Andreas Lübbert
Journal:  Biotechnol J       Date:  2011-09-13       Impact factor: 4.677

Review 7.  Cells and bubbles in sparged bioreactors.

Authors:  J J Chalmers
Journal:  Cytotechnology       Date:  1994       Impact factor: 2.058

8.  CO(2) in large-scale and high-density CHO cell perfusion culture.

Authors:  D R Gray; S Chen; W Howarth; D Inlow; B L Maiorella
Journal:  Cytotechnology       Date:  1996-01       Impact factor: 2.058

Review 9.  Large-scale mammalian cell culture.

Authors:  W S Hu; J G Aunins
Journal:  Curr Opin Biotechnol       Date:  1997-04       Impact factor: 9.740

10.  Cell inactivation in the presence of sparging and mechanical agitation.

Authors:  J D Yang; N S Wang
Journal:  Biotechnol Bioeng       Date:  1992-10-05       Impact factor: 4.530

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  3 in total

1.  Numerical and Experimental Investigation of the Hydrodynamics in the Single-Use Bioreactor Mobius® CellReady 3 L.

Authors:  Diana Kreitmayer; Srikanth R Gopireddy; Tomomi Matsuura; Yuichi Aki; Yuta Katayama; Taihei Sawada; Hirofumi Kakihara; Koichi Nonaka; Thomas Profitlich; Nora A Urbanetz; Eva Gutheil
Journal:  Bioengineering (Basel)       Date:  2022-05-11

2.  Development of a miniature bioreactor model to study the impact of pH and DOT fluctuations on CHO cell culture performance as a tool to understanding heterogeneity effects at large-scale.

Authors:  Roman Zakrzewski; Kenneth Lee; Gary J Lye
Journal:  Biotechnol Prog       Date:  2022-05-07

3.  Enzyme-based lignocellulose hydrolyzation - Brief data survey for cellulase performance characterization on behalf of the Sauter mean diameter of raw material particles.

Authors:  Robert Glaser
Journal:  Data Brief       Date:  2015-11-18
  3 in total

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