Cargando…
Production of retroviral vectors in continuous high cell density culture
ABSTRACT: Retroviral vectors derived from murine leukemia virus (MLV) are used in somatic gene therapy applications e.g. for genetic modification of hematopoietic stem cells. Recently, we reported on the establishment of a suspension viral packaging cell line (VPC) for the production of MLV vectors....
Autores principales: | , , , , , , , , |
---|---|
Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Springer Berlin Heidelberg
2023
|
Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10485120/ https://www.ncbi.nlm.nih.gov/pubmed/37542575 http://dx.doi.org/10.1007/s00253-023-12689-9 |
_version_ | 1785102725426446336 |
---|---|
author | Hein, Marc D. Kazenmaier, Daniel van Heuvel, Yasemin Dogra, Tanya Cattaneo, Maurizio Kupke, Sascha Y. Stitz, Jörn Genzel, Yvonne Reichl, Udo |
author_facet | Hein, Marc D. Kazenmaier, Daniel van Heuvel, Yasemin Dogra, Tanya Cattaneo, Maurizio Kupke, Sascha Y. Stitz, Jörn Genzel, Yvonne Reichl, Udo |
author_sort | Hein, Marc D. |
collection | PubMed |
description | ABSTRACT: Retroviral vectors derived from murine leukemia virus (MLV) are used in somatic gene therapy applications e.g. for genetic modification of hematopoietic stem cells. Recently, we reported on the establishment of a suspension viral packaging cell line (VPC) for the production of MLV vectors. Human embryonic kidney 293-F (HEK293-F) cells were genetically modified for this purpose using transposon vector technology. Here, we demonstrate the establishment of a continuous high cell density (HCD) process using this cell line. First, we compared different media regarding the maximum achievable viable cell concentration (VCC) in small scale. Next, we transferred this process to a stirred tank bioreactor before we applied intensification strategies. Specifically, we established a perfusion process using an alternating tangential flow filtration system. Here, VCCs up to 27.4E + 06 cells/mL and MLV vector titers up to 8.6E + 06 transducing units/mL were achieved. Finally, we established a continuous HCD process using a tubular membrane for cell retention and continuous viral vector harvesting. Here, the space-time yield was 18-fold higher compared to the respective batch cultivations. Overall, our results clearly demonstrate the feasibility of HCD cultivations for high yield production of viral vectors, especially when combined with continuous viral vector harvesting. KEY POINTS: • A continuous high cell density process for MLV vector production was established • The tubular cell retention membrane allowed for continuous vector harvesting • The established process had a 18-fold higher space time yield compared to a batch SUPPLEMENTARY INFORMATION: The online version contains supplementary material available at 10.1007/s00253-023-12689-9. |
format | Online Article Text |
id | pubmed-10485120 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2023 |
publisher | Springer Berlin Heidelberg |
record_format | MEDLINE/PubMed |
spelling | pubmed-104851202023-09-09 Production of retroviral vectors in continuous high cell density culture Hein, Marc D. Kazenmaier, Daniel van Heuvel, Yasemin Dogra, Tanya Cattaneo, Maurizio Kupke, Sascha Y. Stitz, Jörn Genzel, Yvonne Reichl, Udo Appl Microbiol Biotechnol Biotechnological Products and Process Engineering ABSTRACT: Retroviral vectors derived from murine leukemia virus (MLV) are used in somatic gene therapy applications e.g. for genetic modification of hematopoietic stem cells. Recently, we reported on the establishment of a suspension viral packaging cell line (VPC) for the production of MLV vectors. Human embryonic kidney 293-F (HEK293-F) cells were genetically modified for this purpose using transposon vector technology. Here, we demonstrate the establishment of a continuous high cell density (HCD) process using this cell line. First, we compared different media regarding the maximum achievable viable cell concentration (VCC) in small scale. Next, we transferred this process to a stirred tank bioreactor before we applied intensification strategies. Specifically, we established a perfusion process using an alternating tangential flow filtration system. Here, VCCs up to 27.4E + 06 cells/mL and MLV vector titers up to 8.6E + 06 transducing units/mL were achieved. Finally, we established a continuous HCD process using a tubular membrane for cell retention and continuous viral vector harvesting. Here, the space-time yield was 18-fold higher compared to the respective batch cultivations. Overall, our results clearly demonstrate the feasibility of HCD cultivations for high yield production of viral vectors, especially when combined with continuous viral vector harvesting. KEY POINTS: • A continuous high cell density process for MLV vector production was established • The tubular cell retention membrane allowed for continuous vector harvesting • The established process had a 18-fold higher space time yield compared to a batch SUPPLEMENTARY INFORMATION: The online version contains supplementary material available at 10.1007/s00253-023-12689-9. Springer Berlin Heidelberg 2023-08-05 2023 /pmc/articles/PMC10485120/ /pubmed/37542575 http://dx.doi.org/10.1007/s00253-023-12689-9 Text en © The Author(s) 2023 https://creativecommons.org/licenses/by/4.0/Open Access This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article's Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article's Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) . |
spellingShingle | Biotechnological Products and Process Engineering Hein, Marc D. Kazenmaier, Daniel van Heuvel, Yasemin Dogra, Tanya Cattaneo, Maurizio Kupke, Sascha Y. Stitz, Jörn Genzel, Yvonne Reichl, Udo Production of retroviral vectors in continuous high cell density culture |
title | Production of retroviral vectors in continuous high cell density culture |
title_full | Production of retroviral vectors in continuous high cell density culture |
title_fullStr | Production of retroviral vectors in continuous high cell density culture |
title_full_unstemmed | Production of retroviral vectors in continuous high cell density culture |
title_short | Production of retroviral vectors in continuous high cell density culture |
title_sort | production of retroviral vectors in continuous high cell density culture |
topic | Biotechnological Products and Process Engineering |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10485120/ https://www.ncbi.nlm.nih.gov/pubmed/37542575 http://dx.doi.org/10.1007/s00253-023-12689-9 |
work_keys_str_mv | AT heinmarcd productionofretroviralvectorsincontinuoushighcelldensityculture AT kazenmaierdaniel productionofretroviralvectorsincontinuoushighcelldensityculture AT vanheuvelyasemin productionofretroviralvectorsincontinuoushighcelldensityculture AT dogratanya productionofretroviralvectorsincontinuoushighcelldensityculture AT cattaneomaurizio productionofretroviralvectorsincontinuoushighcelldensityculture AT kupkesaschay productionofretroviralvectorsincontinuoushighcelldensityculture AT stitzjorn productionofretroviralvectorsincontinuoushighcelldensityculture AT genzelyvonne productionofretroviralvectorsincontinuoushighcelldensityculture AT reichludo productionofretroviralvectorsincontinuoushighcelldensityculture |