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TLS Online TPP Program
#Question id: 20013
#Section 5: Bioprocess Engineering and Process Biotechnology
In fed batch bioreactor modelling, the rate of change in the bioreactor volume is assumed to be equal to
TLS Online TPP Program
#Question id: 20014
#Section 5: Bioprocess Engineering and Process Biotechnology
In plug flow tubular reactor the axial velocity profile on cross-section will be
TLS Online TPP Program
#Question id: 20015
#Section 5: Bioprocess Engineering and Process Biotechnology
The concentration of biomass in a continuous stirred tank reactor is 20 g dry weight per litre. What would be the concentration of biomass in the effluent?
TLS Online TPP Program
#Question id: 20043
#Section 4: Fundamentals of Biological Engineering
The exponential phase may be described by the equation _______
TLS Online TPP Program
#Question id: 20044
#Section 4: Fundamentals of Biological Engineering
In a batch sterilization process if ∇overall , ∇heating & ∇cooling are 32.2, 9.8 & 10.1 respectively, THEN the holding time at 121ºC of the process is (given that the specific death rate (k) of microorganisms at 121ºC is 2.54 min-1 ):
TLS Online TPP Program
#Question id: 20265
#Section 4: Fundamentals of Biological Engineering
Which of the following is not an example of disaccharide?