Leveraging flow mechanics to determine critical process and scaling parameters in a continuous viral inactivation reactor.


Journal

Biotechnology and bioengineering
ISSN: 1097-0290
Titre abrégé: Biotechnol Bioeng
Pays: United States
ID NLM: 7502021

Informations de publication

Date de publication:
03 2020
Historique:
received: 24 06 2019
revised: 18 10 2019
accepted: 03 11 2019
pubmed: 12 11 2019
medline: 23 2 2021
entrez: 12 11 2019
Statut: ppublish

Résumé

A continuous viral inactivation (CVI) chamber has been designed to operate with acceptable residence time distribution (RTD) characteristics. However, altering the CVI's geometry and operation to accommodate the scale was not obvious. In this work, we elucidate the influence of Dean vortices and leverage the transition into the weak turbulent regime to establish relationships between input variables and process outputs. This study was targeted to understand and quantify the impact of viscosity, Dean number, internal diameter, and path length on the RTD. When the Dean number exceeds 70, radial mixing generated by the Dean vortices began to consistently alter the axial dispersive effects experienced by the pulse injection. Increasing to a Dean number of >100, the axial dispersive effects were dominated by the Dean vortices which allowed the calculation of the minimum and maximum residence time to be generated. This work provides a method to calculate operational solutions for a tubular incubation reactor in terms of path length, internal diameter, flow rate, and target minimum and maximum residence time specifications that assures both viral residence times while also establishing criteria to maximize product quality during continuous operation.

Identifiants

pubmed: 31709510
doi: 10.1002/bit.27223
doi:

Substances chimiques

Antibodies, Monoclonal 0
Biological Products 0

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

637-645

Informations de copyright

© 2019 Wiley Periodicals, Inc.

Références

Aider, A. A., Skali, S., & Brancher, J. (2005). Laminar-turbulent transition in Taylor-Dean flow. Journal of Physics: Conference Series, 14(1), 118-127. https://doi.org/10.1088/1742-6596/14/1/015
Amarikwa, L., Orozco, R., Brown, M., & Coffman, J. (2018). Impact of Dean vortices on the integrity testing of a continuous viral inactivation reactor. Biotechnology Journal, 14(14), e1700726. https://doi.org/10.1002/biot.201700726
ASTM (2012). E2888-12: Standard Practice for Process for Inactivation of Rodent Retrovirus by pH. West Conshohocken, PA: ASTM International. http://www.astm.org
Brorson, K., Krejci, S., Lee, K., Hamilton, E., Stein, K., & Xu, Y. (2003). Bracketed generic inactivation of rodent retroviruses by low pH treatment for monoclonal antibodies and recombinant proteins. Biotechnology and Bioengineering, 82(3), 321-329. https://doi.org/10.1002/bit.10574
Chinniah, S., Hinckley, P., & Connell-Crowley, L. (2016). Characterization of operating parameters for XMuLV inactivation by low pH treatment. Biotechnology Progress, 32(1), 89-97. https://doi.org/10.1002/btpr.2183
Fiadeiro, M., Kublbleck, A., Fahrner, R., & Salm, J. (2016). Enabling continuous low pH viral inactivation with integrated in-line conditioning of protein A streams. American Chemical Society BIOT: San Diego, CA.
Gillespie, C., Holstein, M., Mullin, L., Cotoni, K., Caulmare, J., & Greenhalgh, P. (2019). Continuous in-line virus inactivation for next generation bioprocessing. Biotechnology Journal, 14, e1700718. https://doi.org/10.1002/biot.201700718
Johnson, S., Brown, M., Lute, S., & Brorson, K. (2017). Adapting viral safety assurance strategies to continuous processing of biological products. Biotechnology and Bioengineering, 114(1), 21-32. https://doi.org/10.1002/bit.26060
Klutz, S., Lobedann, M., Bramsiepe, C., & Schembecker, G. (2016). Continuous viral inactivation at low pH value in antibody manufacturing. Chemical Engineering and Processing: Process Intensification, 102, 88-101. https://doi.org/10.1016/j.cep.2016.01.002
Levenspiel, O. (1999). Chemical Reaction Engineering (3rd Edition.). New York, NY: J.W. Sons.
Li, L., Kumar, S., Buck, Burns, C., Lavoie, J., Singh, S., … Boardman, D. (2014). Concentration dependent viscosity of monoclonal antibody solutions: Explaining experimental behavior in terms of molecular properties. Pharmaceutical Research, 31(11), 3161-3178. https://doi.org/10.1007/s11095-014-1409-0
Murai, M. (1991). [Riboflavin Reference Standard (Control 891) of National Institute of Hygienic Sciences]. Eisei Shikenjo Hokoku. Bulletin of National Institute of Hygienic Sciences, 109, 173-175. https://europepmc.org/abstract/med/1364392
Orozco, R., Godfrey, S., Coffman, J., Amarikwa, L., Parker, S., Hernandez, L., … Fiadeiro, M. (2017). Design, construction, and optimization of a novel, modular, and scalable incubation chamber for continuous viral inactivation. Biotechnology Progress, 33(4), 954-965. https://doi.org/10.1002/btpr.2442
Parker, S., Amarikwa, L., Vehar, K., Orozco, R., Godfrey, S., Coffman, J., … Bardliving, C. (2018). Design of a novel continuous flow reactor for low pH viral inactivation. Biotechnology and Bioengineering, 115, 606-616. https://doi.org/10.1002/bit.26497
Xenopoulos, A (2017). Methods for inactivating viruses during a protein purification process. US patent 9809799. Billerica, MA: EMD Millipore Corporation.

Auteurs

Matthew R Brown (MR)

Bioprocess Engineering, Process Science, Boehringer Ingelheim, Fremont, California.

Raquel Orozco (R)

Bioprocess Engineering, Process Science, Boehringer Ingelheim, Fremont, California.

Jon Coffman (J)

Bioprocess Engineering, Process Science, Boehringer Ingelheim, Fremont, California.

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