ArticleApplied microbiology and biotechnology2023
Production of retroviral vectors in continuous high cell density culture.
Article in Applied microbiology and biotechnology, 2023. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 9 papers.
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Who cites it
9 citing papers in PubMed.
- High Cell Density Cultivation of HEK293 Cells Using a 2L Membrane-Stirred Bioreactor.Biotechnology and bioengineering · 2026Article
- Article
- Development of a scalable production bioprocess for HIV-1 virus-like particles coupling continuous VLP harvesting with end-to-end downstream processing.Scientific reports · 2026Article
- Perfusion-Based Production of rAAV via an Intensified Transient Transfection Process.Biotechnology and bioengineering · 2025Article
- Article
- Production of antiviral "OP7 chimera" defective interfering particles free of infectious virus.Applied microbiology and biotechnology · 2024Article
- Digital Twin for Continuous Production of Virus-like Particles toward Autonomous Operation.ACS omega · 2024Article
- A novel multi-stage enrichment workflow and comprehensive characterization for HEK293F-derived extracellular vesicles.Journal of extracellular vesicles · 2024Article
- Intensified Influenza Virus Production in Suspension HEK293SF Cell Cultures Operated in Fed-Batch or Perfusion with Continuous Harvest.Vaccines · 2023Article
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Authors and funding
9 authors.
Funding
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.
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