Biochemical Engineering - Fermentation Kinetics
Exercise : Fermentation Kinetics - Section 2
- Fermentation Kinetics - Section 1
- Fermentation Kinetics - Section 2
26.
The height to diameter ratio (H/D) for the tank fermenters is
27.
The relatively large volume (10 to 40% of total fermenter volume) of the seed culture is employed to
28.
In an airlift bioreactor, the air sparging region is called
29.
The air riser is located on the outside of the draft tube for the large-scale airlift bioreactors because of
30.
At the end of the lag phase, when growth begins, the division rate increases gradually and reaches a maximum value in the exponential growth period. This transitional period is commonly called the accelerated growth phase and is often included as a part of the
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