Method Article

Process Optimization using High Throughput Automated Micro-Bioreactors in Chinese Hamster Ovary Cell Cultivation

DOI:

10.3791/60577

May 18th, 2020

In This Article

Summary

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Here, we present a detailed procedure to run a Design of Experiment in an automated micro-bioreactor followed by cell harvest and protein quantification using a Protein A column.

Abstract

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Optimization of bioprocesses to increase the yield of desired products is of importance in the biopharmaceutical industry. This can be achieved by strain selection and by developing bioprocess parameters. Shake flasks have been used for this purpose. They, however, lack the capability to control the process parameters such as pH and dissolved oxygen (DO). This limitation can be overcome with the help of an automated micro-bioreactor. These bioreactors mimic cultivation at a larger scale. One of the major advantages of this system is the integration of the Design of Experiment (DOE) in the software. This integration enables establishing a design where multiple process parameters can be varied simultaneously. The critical process parameters and optimum bioprocess conditions can be analyzed within the software. The focus of the work presented here is to introduce the user to the steps involved in process design in the software and incorporation of the DOE within the cultivation run.

Introduction

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The global biopharmaceutical market was worth more than US $250 billion in 2018 and has been continuously expanding1. Pharmaceutical companies are moving away from producing small molecular drugs to biotechnologically produced therapeutics such as recombinant proteins. These alone are responsible for a revenue of more than $150 billion1. Mammalian cells are now extensively used for the production of these pharmaceutical recombinant proteins. In the current period, among the 68 approved products produced by mammalian cells, 57 are produced by Chinese Hamster ovary cells (CHO)2. CHO cells are specif....

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Protocol

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1. Preculture Procedure

NOTE: Recombinant CHO DG44 cells with a viable cell concentration of 1 x 107 cells/mL are used for this protocol.

  1. Thaw the vial containing 1.2 mL of cells to room temperature and immediately transfer the cell suspension to a 15 mL conical centrifuge tube containing 10 mL of cold seed medium.
  2. Centrifuge the conical centrifuge tube for 5 minutes at 190 x g and room temperature and discard the supernatant.
  3. Pre-heat 150 mL of the seed medium in a 500 mL shake flask to 36.8 °C.
  4. Gently resuspend the cell pellet in 10 mL of pre-warmed seed medium....

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Results

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An overview of the cultivation performed in this study is presented in Figure 2.

pH impact on stirrer speed; diagram of experiments at 1050 vs 1300 rpm; buffer solution analysis.
Figure 2: Schematic representation of the experimental conditions to test pH and stirrer speed profiles in the cultur.......

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Discussion

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Optimization of the process to increase the yield is of crucial importance in the biopharmaceutical industry. Shake flasks could potentially be used for the screening of the strain; however, the monitoring of the process parameters such as pH and DO are unavailable in the flasks. The micro-bioreactors have an advantage as they allow continuous monitoring and control of the process. These control loops in the micro-bioreactor also provide a condition similar to those at larger scale and thus, deliver results that are comp.......

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Disclosures

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The authors have nothing to disclose.

Acknowledgements

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The authors would like to thank the Bundesministerium für Bildung und Forschung (BMBF), the Federal Ministry of Education and Research, Germany, and the BioProcessing team of Sartorius Stedim Biotech GmbH, Germany, for their support.

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Materials

List of materials used in this article
NameCompanyCatalog NumberComments
1 mL disposable pipette tips, sterilizedSartorius Stedim Biotech GmbHA-0040
200 mM L-glutamineCorning, Merck25-005-CV
24 Well deep well platesSartorius Stedim Biotech GmbHA-0038
5 mL disposable pipette tips, sterilizedSartorius Stedim Biotech GmbHA-0039
ambr 15 automated microbioreactor systemSartorius Stedim Biotech GmbH001-2804
ambr 15 Cell Culture 24 Disposable Bioreactors - SpargedSartorius Stedim Biotech GmbH001-1B86
Antifoam C EmulsionSigma-Aldrich, MerckA8011
Bottle Top Sterile filterCorning, MerckCLS4314740.1 μm pore size
CEDEX Detergent (3% Mucosol)Roche Innovatis AG05-650-658-001
Cell counterRoche Innovatis AG05-650-216-001CEDEX HiRes
CHO DG44 cell lineCellca, Sartorius Stedim Biotech GmbH
CHOKO Feed Media A (FMA)Sigma-Aldrich, MerckCR80025
CHOKO Feed Media B (FMB)Sigma-Aldrich, MerckCR80026
CHOKO Production MediumSigma-Aldrich, MerckCR80027
CHOKO Stock Culture MeiumSigma-Aldrich, MerckCR80028
Chromaster high pressure liquid chromatography systemVWR International
Conical Centrifuge tubeCorning, MerckSIAL0790
EthanolMerck1070179026
GlycineCarl Roth56-40-6
HPLC VialsVWR InternationalSUPLSU860181
PBSSigma-Aldrich,MerckP4417
Protein A ColumnThermo Fisher Scientific1502226POROS™ A 1.7 mL
Sodium chlorideSigma-Aldrich,Merck7647-14-5
Sodium phosphate dibasic anhydrousSigma-Aldrich,Merck7558-79-4
Trypan BlueVWR InternationalVWRVK940
YSIYSI Inc2900DYSI 2900 Select

References

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  1. Langer, E. S. 15th Annual report and survey of Biopharmaceutical Manufacturing Capacity and Production: A study of Biotherapeutical Developers and Contract Manufacturing Organizations. Bioplan Associates. , Available from: http://bioplanassociates.com/wp-content/uploads/2018/07/15thAnnualBiomfgReport_TABLEOFCONTENTS-LR.pdf (2019).
  2. Walsh, G. Biopharmaceutical benchmarks 2018.....

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Tags

Automated Micro BioreactorDesign of ExperimentChinese Hamster OvaryProcess OptimizationBioprocess ParametersDOE SoftwareCell CultureStirring RPMDissolved OxygenpH Control

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