TLS Online TPP Program

#Question id: 17660


A pseudoplastic fluid is one in which the viscosity

#Section 4: Fundamentals of Biological Engineering
  1. is constant regardless of the stirrer speed or mixing time
  2. changes during mixing but returns to its original state after mixing
  3. increases with increasing stirrer speed
  4. decreases with increasing stirrer speed
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TLS Online TPP Program

#Question id: 27325

#Section 5: Bioprocess Engineering and Process Biotechnology

if the initial substrate concentration is 15 g/L and initial biomass concentration is 0.1 g/L. The substrate is then consumed completely and produces 6.4 g/L of biomass. The yield coefficient will be

TLS Online TPP Program

#Question id: 27326

#Section 5: Bioprocess Engineering and Process Biotechnology

The growth of a microorganism on glucose is described by the Monod model (µmax = 0.7 h¹ and Ks = 0.1 g L¹). If the initial biomass concentration in the batch fermenter is 0.1 g L¹, the minimum time required to triple the biomass concentration would be

TLS Online TPP Program

#Question id: 27327

#Section 5: Bioprocess Engineering and Process Biotechnology

The product formation kinetics of a biochemical process follows the model qp = au + B. In case of a = 0, the rate of product formation is

TLS Online TPP Program

#Question id: 27328

#Section 5: Bioprocess Engineering and Process Biotechnology

The unit of maintenance coefficient is

TLS Online TPP Program

#Question id: 27329

#Section 5: Bioprocess Engineering and Process Biotechnology

Culture comprising a B. subtlis strain by inoculating 1g of cells into 1 liter bioreactor. Fermentor containing 10g/l of glucose. The maximum specific growth rate of the culture is 1.0 /h. The biomass yield from glucose is 0.5 g/g. If the residual glucose concentration left out is 1g/l, the final cell concentration in g/l achieved would be around

TLS Online TPP Program

#Question id: 27330

#Section 5: Bioprocess Engineering and Process Biotechnology

The ethanol yield per unit mass of substrate consumed (YP/S) in an anaerobic fermentation process can be improved by