TLS Online TPP Program

#Question id: 16572


During the casting of polyacrylamide gel acrylamide and bis-acrylamide are joined by 

#Section 7: Recombinant DNA technology and Other Tools in Biotechnology
  1. Free radical catalysis
  2. Polymerization reaction
  3. Dehydration reaction
  4. Condensation reaction
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TLS Online TPP Program

#Question id: 27341

#Section 5: Bioprocess Engineering and Process Biotechnology

In a chemostat, under steady state condition, if the feed media is sterile and endogenous metabolism is negligible compared to growth rate, then the specific growth rate (μ) will be

TLS Online TPP Program

#Question id: 27342

#Section 5: Bioprocess Engineering and Process Biotechnology

A culture of Rhizobium sp. is grown in a chemostat (200 m³ bioreactor). The feed contains 12 g/L sucrose, Ks for the organism is 0.2 g/L and Hmax = 0.3 h¹. The flow rate required to obtain steady state concentration of sucrose as 2 g/L in the bioreactor

TLS Online TPP Program

#Question id: 27343

#Section 5: Bioprocess Engineering and Process Biotechnology

Cell wash out condition in the bioreactor occurs when

TLS Online TPP Program

#Question id: 27344

#Section 5: Bioprocess Engineering and Process Biotechnology

In a chemostat, evaluate the dilution rate at the cell wash-out condition by applying Monod's model with the given set of data: μmax = 1 h-1; YX/S = 0.5 g g-1; Ks = 0.2 g/L; S0 = 10 g/L

TLS Online TPP Program

#Question id: 27345

#Section 5: Bioprocess Engineering and Process Biotechnology

For running a Continuous Stirred Tank Reactor, critical dilution rate is:

TLS Online TPP Program

#Question id: 27346

#Section 5: Bioprocess Engineering and Process Biotechnology

Continuous cultivation is carried out in 10 L working volume. If 0.2 h-1 dilution rate has to be maintained, then the feed rate will be