Table 3.
Relevant challenges encountered during plate screen development and proposed potential solutions
| Common challenges in plate screen | 96-well plate | Lab-scale bioreactor | Details | Potential solutions |
|---|---|---|---|---|
| Population size (total number of cells) | 107 cells | 1012 cells | Tank processes allow for an extended growth phase due to controlled environment | Match number of generations by adjusting the volume or density of the seed culture |
| pH control | Uncontrolled | Controlled base and/or acid addition | One-sided pH control is required for most fermentation process | Addition of buffering solutions, reduction of substrate/product concentration or biomass |
| Aeration | Uncontrolled | DO control through air/oxygen spargers and impeller speed adjustment | Oxygen transfer in plates is typically lower than in tanks | Characterize potential impact of oxygen limitation on strain performance. Reduction of oxygen uptake rate by adjustment of substrate concentration and cell density |
| Substrate load | Low | High | Strains may be sensitive to excess carbon and produce unwanted byproducts leading to changes in pH | Employ a glucose-limited main plate fermentation, either as batch or using glucose release system |
| Biomass concentration | Low | High | Oxygen transfer and process control capabilities in plates are limited | Include a scale-down factor in plate media composition |
| Carbon supply | Uncontrolled | Controlled | Bioreactors are equipped with controlled feeding mechanisms | Employ glucose release system and modify enzyme and substrate concentration to optimize release rate to generate fed-batch regimen |
| Evaporation | High risk | Low risk | Evaporation in plates can lead to significant differences in a culture volume | Determine the impact of evaporation on well-to-well CV at different time points. Minimize incubation time |