Mixing and oxygen transfer characteristics of a microplate bioreactor with surface-attached microposts.

Bioprocess optimization for cell-based therapies is a resource heavy activity. To reduce the associated cost and time, process development may be carried out in small volume systems, with the caveat that such systems be predictive for process scale-up. The transport of oxygen from the gas phase into the culture medium, characterized using the volumetric mass transfer coefficient, k a, has been identified as a critical parameter for predictive process scale-up.