Aeration constrain is bioreactors
Dissolved oxygen is important in cultivations. Since oxygen is sparingly soluble in water, it may be the growth-limiting factor in these bioreactors. The solubility of oxygen in culture media is ~6.6 µg/mL at 37°C when exposed for a 5 % CO2 / p5% air gas mixture. The typical Oxygen Uptake Rate for mammalian cells are between 3x10-10 and 2x10-8 mg/cell/hour. For optimum growth it is therefore important to maintain the dO2 above this critical level by aeration. Of course, to be effective, the mass transfer rate from the gas bubbles to the liquid broth must equal or exceed the rate at which growing cells Oxygen Uptake Rate. In general terms the air or mixed gas volume required is ranging one litre/working volume/hour.
- The classical aeration method for bioreactors is performed by sparging (bubbling) gas through the bioreactor media. The gas being air or mixed gases by slight overpressure forced through small holes or pores in the sparger tip. The smaller the bubbles the larger surface area and hereby improved oxygen diffusion through the bubble to liquid contact.
- Membrane aeration replaces the need for gas sparging by providing a large interfacial area for oxygen diffusion. Membrane aeration is able to avoid contact between cells and bubbles. Not a method used for re-usable bioreactors as to maintenance issues. Though highly relevant for Single-Use-Bioreactors and will be pursued by CerCell.
Oxygen transfer via sparging is usually limited by the liquid film surrounding the gas bubbles. The rate of transport is given by:
where kL is the oxygen transport coefficient (cm/h), a is the gas-liquid interfacial area (cm2/cm3), kLa the volumetric oxygen transfer coefficient (h-1), C* is saturated dO2 concentration (mg/l) (approx. 8 mg/l at 25 deg. C and 1 atm.), CL is the actual dO2 concentration in the liquid (mg/l), and NO2 is the rate of oxygen transfer (mg O2/ l/h).