Abstract
In recent years, several automated scale-down bioreactor systems have been developed to increase efficiency in cell culture process development. ambr™ is an automated workstation that provides individual monitoring and control of culture dissolved oxygen and pH in single-use, stirred-tank bioreactors at a working volume of 10–15 mL. To evaluate the ambr™ system, we compared the performance of four recombinant Chinese hamster ovary cell lines in a fed-batch process in parallel ambr™, 2-L bench-top bioreactors, and shake flasks. Cultures in ambr™ matched 2-L bioreactors in controlling the environment (temperature, dissolved oxygen, and pH) and in culture performance (growth, viability, glucose, lactate, Na+, osmolality, titer, and product quality). However, cultures in shake flasks did not show comparable performance to the ambr™ and 2-L bioreactors.
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References
Bareither R, Pollard D (2011) A review of advanced small-scale parallel bioreactor technology for accelerated process development: current state and future need. Biotechnol Prog 27:2–14
Betts JI, Baganz F (2006) Miniature bioreactors: current practices and future opportunities. Microb Cell Fact 5:21
Chisti Y (1993) Animal cell culture in stirred bioreactors: observations on scale-up. Process Biochem 28:511–517
Cohen SA, Michaud DP (1993) Synthesis of a fluorescent derivatizing reagent, 6-aminoquinolyl-N-hydroxysuccinimidyl carbamate, and its application for the analysis of hydrolysate amino acids via high-performance liquid chromatography. Anal Biochem 211:279–287
Cook JA, Fox MH (1988) Effects of chronic pH 6.6 on growth, intracellular pH, and response to 42.0 °C hyperthermia of Chinese Hamster Ovary cells. Cancer Res 48:2417–2420
Gennaro LA, Salas-Solano O (2008) On-line CE-LIF-MS technology for the direct characterization of N-linked glycans from therapeutic antibodies. Anal Chem 80:3838–3845
Guo D, Gao A, Michels DA, Feeney L, Eng M, Chan B, Laird MW, Zhang B, Yu XC, Joly J, Snedecor B, Shen A (2010) Mechanisms of unintended amino acid sequence changes in recombinant monoclonal antibodies expressed in Chinese hamster ovary (CHO) cells. Biotechnol Bioeng 107:163–171
Hopp J, Pritchett R, Darlucio M, Ma J, Chou JH (2009) Development of a high throughput protein a well-plate purification method for monoclonal antibodies. Biotechnol Prog 25:1427–1432
Keane JT, Ryan D, Gray PP (2003) Effect of shear stress on expression of a recombinant protein by Chinese Hamster Ovary cells. Biotechnol Bioeng 81:211–220
Kondragunta B, Drew JL, Brorson KA, Moreira AR, Rao G (2010) Advances in clone selection using high-throughput bioreactors. Biotechnol Prog 26:1095–1103
Kumar S, Wittmann C, Heinzle E (2004) Minibioreactors. Biotechnol Lett 26:1–10
Lewis G, Lugg R, Lee K, Wales R (2010) Novel automated micro-scale bioreactor technology: a qualitative and quantitative mimic for early process development. Bioprocess J 9:22–25
Lin AA, Kimura R, Miller WM (1993) Production of tPA in recombinant CHO cells under oxygen-limited conditions. Biotechnol Bioeng 42:339–350
Restelli V, Wang MD, Huzel N, Ethier M, Perreault H, Butler M (2006) The effect of dissolved oxygen on the production and the glycosylation profile of recombinant human erythropoietin produced from CHO cells. Biotechnol Bioeng 94:481–494
Sauer PW, Burky JE, Wesson MC, Sternard HD, Qu L (2000) A high-yielding, generic fed-batch cell culture process for production of recombinant antibodies. Biotechnol Bioeng 67:585–597
Tissot S, Oberbek A, Reclari M, Dreyer M, Hacker DL, Baldi L, Farhat M, Wurm FM (2011) Efficient and reproducible mammalian cell culture bioprocesses without probes and controllers? N Biotechnol 28:382–390
Trummer E, Fauland K, Seidinger S, Schriebl K, Lattenmayer C, Kunert R, Vorauer-Uhl K, Weik R, Borth N, Katinger H, Muller D (2006) Process parameter shifting: part I. Effect of DOT, pH, and temperature on the performance of Epo-Fc expressing CHO cells cultivated in controlled batch bioreactors. Biotechnol Bioeng 94:1033–1044
Tsao Y-S, Cardoso AG, Condon RGG, Voloch M, Lio P, Lagos JC, Kearns BG, Liu Z (2005) Monitoring Chinese hamster ovary cell culture by the analysis of glucose and lactate metabolism. J Biotechnol 118:316–327
Varley J, Birch J (1999) Reactor design for large scale suspension animal cell culture. Cytotechnology 29:177–205
Yoon SK, Choi SL, Song JY, Lee GM (2005) Effect of culture pH on Erythropoietin production by Chinese Hamster Ovary cells grown in suspension at 32.5 and 37.0 °C. Biotechnol Bioeng 89:345–356
Yuk IH, Baskar D, Duffy PH, Hsiung J, Leung S, Lin AA (2011) Overcoming challenges in WAVE bioreactors without feedback controls for pH and dissolved oxygen. Biotechnol Prog 27:1397–1406
Zhang L, Lilyestrom W, Li C, Scherer T, van Reis R, Zhang B (2011) Revealing a positive charge patch on a recombinant monoclonal antibody by chemical labeling and mass spectrometry. Anal Chem 83:8501–8508
Acknowledgments
The authors thank cell line development groups for generating the CHO cell lines evaluated; B6 media preparation group for supplying all the media and solutions used; cell banking group for supplying ampoules; Peter Harms and Louis Cheung for discussions on methods of higher throughput for off-line analysis; Analytical Operations group, especially Yun Tang, Kevin Lin, and Renee Yang, for providing analytical support for titer, product quality and amino acid assays; Andy Lin and John Joly for guidance and support.
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Hsu, WT., Aulakh, R.P.S., Traul, D.L. et al. Advanced microscale bioreactor system: a representative scale-down model for bench-top bioreactors. Cytotechnology 64, 667–678 (2012). https://doi.org/10.1007/s10616-012-9446-1
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DOI: https://doi.org/10.1007/s10616-012-9446-1
Keywords
- Scale-down system
- Chinese hamster ovary
- Cell culture automation
- ambr™
- Single-use bioreactor