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Scalable process development for rAAV transient transfection production using computational fluid dynamics modeling.

Jianfa Ou1, Yawen Tang1, Alexander Williams1

  • 1Biologics Development, Global Product Development and Supply, Bristol Myers Squibb, Devnes, Massachusetts, USA.

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|April 4, 2025
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Summary
This summary is machine-generated.

This study optimized recombinant adeno-associated virus (rAAV) production by controlling shear stress in bioreactors. Scale-up to 250L achieved consistent cell growth and rAAV production, overcoming previous challenges.

Keywords:
computational fluid dynamics modelrAAVrobustnessscale‐upshear stresstransfection production

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Area of Science:

  • Biotechnology and Bioprocessing
  • Gene Therapy Manufacturing
  • Cell and Molecular Biology

Background:

  • Recombinant adeno-associated virus (rAAV) is a key vector for gene therapies.
  • Current upstream development for rAAV faces challenges in productivity and consistency.
  • Scale-up of rAAV production requires careful management of process parameters.

Purpose of the Study:

  • To design and implement a robust scale-up process for rAAV production at a 250L scale.
  • To investigate and mitigate the impact of mechanical shear forces on rAAV production in bioreactors.
  • To identify critical process attributes for consistent and high-yield rAAV manufacturing.

Main Methods:

  • Process development in shake flasks to optimize plasmid ratios.
  • Computational fluid dynamics (CFD) modeling (M-STAR) and empirical correlations (Dynochem) to characterize bioreactor hydrodynamics.
  • Determination of optimal power per unit volume (P/V) for different bioreactor scales.
  • Assessment of shear protectants (Poloxamer-188) and critical attributes like pre-transfection viable cell density (VCD).

Main Results:

  • Initial optimization in shake flasks improved rAAV production, but scale-up to stirred-tank bioreactors showed a significant decrease in genome titer due to shear stress.
  • CFD modeling guided the selection of optimal P/V values (71 W/m³ at 250mL, 20 W/m³ at 5-50L, and 15 W/m³ at 250L) to minimize shear.
  • Addition of Poloxamer-188 and control of pre-transfection VCD enhanced process robustness.
  • The final 250L scale process, incorporating a 30% cell culture dilution and controlled DNA complexation, demonstrated consistent cell growth and rAAV production.

Conclusions:

  • Mechanical shear stress is a critical factor limiting rAAV production during bioreactor scale-up.
  • A scale-up strategy based on CFD modeling and hydrodynamic characterization enables robust rAAV manufacturing.
  • Optimized process parameters, including shear stress control and critical attribute management, are essential for consistent rAAV production at the 250L scale.