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Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production

Modified Vaccinia Ankara (MVA) virus is a promising vector for vaccination against various challenging pathogens or the treatment of some types of cancers, requiring a high amount of virions per dose for vaccination and gene therapy. Upstream process intensification combining perfusion technologies,...

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Autores principales: Gränicher, Gwendal, Tapia, Felipe, Behrendt, Ilona, Jordan, Ingo, Genzel, Yvonne, Reichl, Udo
Formato: Online Artículo Texto
Lenguaje:English
Publicado: John Wiley and Sons Inc. 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7435511/
https://www.ncbi.nlm.nih.gov/pubmed/32762152
http://dx.doi.org/10.1002/biot.202000024
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author Gränicher, Gwendal
Tapia, Felipe
Behrendt, Ilona
Jordan, Ingo
Genzel, Yvonne
Reichl, Udo
author_facet Gränicher, Gwendal
Tapia, Felipe
Behrendt, Ilona
Jordan, Ingo
Genzel, Yvonne
Reichl, Udo
author_sort Gränicher, Gwendal
collection PubMed
description Modified Vaccinia Ankara (MVA) virus is a promising vector for vaccination against various challenging pathogens or the treatment of some types of cancers, requiring a high amount of virions per dose for vaccination and gene therapy. Upstream process intensification combining perfusion technologies, the avian suspension cell line AGE1.CR.pIX and the virus strain MVA‐CR19 is an option to obtain very high MVA yields. Here the authors compare different options for cell retention in perfusion mode using conventional stirred‐tank bioreactors. Furthermore, the authors study hollow‐fiber bioreactors and an orbital‐shaken bioreactor in perfusion mode, both available for single‐use. Productivity for the virus strain MVA‐CR19 is compared to results from batch and continuous production reported in literature. The results demonstrate that cell retention devices are only required to maximize cell concentration but not for continuous harvesting. Using a stirred‐tank bioreactor, a perfusion strategy with working volume expansion after virus infection results in the highest yields. Overall, infectious MVA virus titers of 2.1–16.5 × 10(9) virions/mL are achieved in these intensified processes. Taken together, the study shows a novel perspective on high‐yield MVA virus production in conventional bioreactor systems linked to various cell retention devices and addresses options for process intensification including fully single‐use perfusion platforms.
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spelling pubmed-74355112020-08-19 Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production Gränicher, Gwendal Tapia, Felipe Behrendt, Ilona Jordan, Ingo Genzel, Yvonne Reichl, Udo Biotechnol J Research Articles Modified Vaccinia Ankara (MVA) virus is a promising vector for vaccination against various challenging pathogens or the treatment of some types of cancers, requiring a high amount of virions per dose for vaccination and gene therapy. Upstream process intensification combining perfusion technologies, the avian suspension cell line AGE1.CR.pIX and the virus strain MVA‐CR19 is an option to obtain very high MVA yields. Here the authors compare different options for cell retention in perfusion mode using conventional stirred‐tank bioreactors. Furthermore, the authors study hollow‐fiber bioreactors and an orbital‐shaken bioreactor in perfusion mode, both available for single‐use. Productivity for the virus strain MVA‐CR19 is compared to results from batch and continuous production reported in literature. The results demonstrate that cell retention devices are only required to maximize cell concentration but not for continuous harvesting. Using a stirred‐tank bioreactor, a perfusion strategy with working volume expansion after virus infection results in the highest yields. Overall, infectious MVA virus titers of 2.1–16.5 × 10(9) virions/mL are achieved in these intensified processes. Taken together, the study shows a novel perspective on high‐yield MVA virus production in conventional bioreactor systems linked to various cell retention devices and addresses options for process intensification including fully single‐use perfusion platforms. John Wiley and Sons Inc. 2020-09-08 2021-01 /pmc/articles/PMC7435511/ /pubmed/32762152 http://dx.doi.org/10.1002/biot.202000024 Text en © 2020 The Authors. Biotechnology Journal published by Wiley‐VCH GmbH https://creativecommons.org/licenses/by/4.0/This is an open access article under the terms of the http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) License, which permits use, distribution and reproduction in any medium, provided the original work is properly cited.
spellingShingle Research Articles
Gränicher, Gwendal
Tapia, Felipe
Behrendt, Ilona
Jordan, Ingo
Genzel, Yvonne
Reichl, Udo
Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title_full Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title_fullStr Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title_full_unstemmed Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title_short Production of Modified Vaccinia Ankara Virus by Intensified Cell Cultures: A Comparison of Platform Technologies for Viral Vector Production
title_sort production of modified vaccinia ankara virus by intensified cell cultures: a comparison of platform technologies for viral vector production
topic Research Articles
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7435511/
https://www.ncbi.nlm.nih.gov/pubmed/32762152
http://dx.doi.org/10.1002/biot.202000024
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