Table 2.
Table summarizing the advantages and limitations of the described large-scale systems.
Device | Max Capacitya | Cell density (ml−1) | Features | Disadvantages |
---|---|---|---|---|
Wave bioreactor (associated with microcarriers) | 20 L/0.02 m3 | 2 × 106 | • Tool for intensified scaling-up • Low shear stress • Operation in different batch modes |
• Scale-up to >100 L is challenging • Large space is needed |
Stirred tank (associated with microcarriers) | 2,000 L/2 m3 | 2 × 106 | • Easy of scaling up from benchtop to factory • Bioprocessing is well-understood • Flexible and automatic platform for very high-volume bioprocess |
• Require optimization with cell line and microcarriers • Large volumes required • High shear stress |
Packed bed | 500 m2/ 0.03m3 | 3 × 106 | • High density cell culture due to large surface available • Operation in different batch modes • Cell passage less frequent |
• Packing material difficult cell harvest • Concentration of gradients |
Hollow fiber bioreactorb | 150 cm2/ml−1 0.00007 m3 | 1 × 109 | • Increased surface to volume ratio • In vivo-like tissue structure (blood vessels) |
• Difficult to harvest cells • Concentration of gradients |
Commercially available.
Variable maximum capacity, as various cartridges can be connected in parallel.