TLS Online TPP Program
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TLS Online TPP Program
#Question id: 26678
#Unit 12. Biochemical Engineering
The shear stress responsible for cell death in airlift fermentors CANNOT be reduced by
TLS Online TPP Program
#Question id: 26778
#Unit 12. Biochemical Engineering
For a chemostat culture operating under steady state. which of the following statements is NOT true?
TLS Online TPP Program
#Question id: 23270
#Unit 12. Biochemical Engineering
If in a bioreactor, the gas hold up (r) is 0.1 and the average diameter of the air bubbles is 1 mm; then the interfacial area (of the air bubble —liquid interface), per unit reactor volume is:
TLS Online TPP Program
#Question id: 21398
#Unit 12. Biochemical Engineering
To have an extended late log/ stationary phase so that secondary metabolites may be produced, you will prefer to use:
TLS Online TPP Program
#Question id: 21401
#Unit 12. Biochemical Engineering
Scaling up a reactor while keeping the power consumption per unit volume constant will lead to:
TLS Online TPP Program
#Question id: 21406
#Unit 12. Biochemical Engineering
S. cerevisiae produces ethanol at a yield of 0.5 g/g glucose. The strain ferments 20g/l glucose in 24 hours. Calculate productivity of ethanol in this fermentation.
