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Total Questions : 114 | Page 4 of 12 pages
Question 31. Production of organic acids in batch culture is generally growth associated phase followed by non-growth associated production. The probable reason for this is that
  1.    organic acids uncouple catabolism from anabolism
  2.    biomass yields increase as the fermentation proceeds
  3.    organic acids are secondary metabolites
  4.    high concentrations of organic acid promote the growth of the microbial population
 Discuss Question
Answer: Option A. -> organic acids uncouple catabolism from anabolism
Answer: (a).organic acids uncouple catabolism from anabolism
Question 32. 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?
  1.    Greater than 20 g dry weight per litre
  2.    Approximately 20 g dry weight per litre
  3.    Lesser than 20 g dry weight per litre
  4.    More than 30 g dry weight per litre
 Discuss Question
Answer: Option B. -> Approximately 20 g dry weight per litre
Answer: (b).Approximately 20 g dry weight per litre
Question 33. Pseudo-steady state in a continuous reactor refers to a reactor in which
  1.    Pseudomonads are being cultured
  2.    concentration oscillate around a mean value
  3.    concentration increase with time
  4.    concentration decrease with time
 Discuss Question
Answer: Option B. -> concentration oscillate around a mean value
Answer: (b).concentration oscillate around a mean value
Question 34. The ideal tubular-flow fermenter without radial variations is called a
  1.    plug flow fermenter
  2.    continuous stirred tank fermenter (CSTF)
  3.    column fermenter
  4.    any intensity of dilution rate near the wash out points
 Discuss Question
Answer: Option A. -> plug flow fermenter
Answer: (a).plug flow fermenter
Question 35. The toxicity of organic acids to cells
  1.    enhances as the pH falls
  2.    reduces as the pH falls
  3.    is not affected by pH
  4.    is highest at pH 7.0
 Discuss Question
Answer: Option A. -> enhances as the pH falls
Answer: (a).enhances as the pH falls
Question 36. The main reason for production of antibiotics in fed batch reactors is
  1.    the presence of precursors is often toxic to the cells
  2.    higher yields when cells enter the stationary phase
  3.    higher yields when cell growth slows
  4.    all of the above
 Discuss Question
Answer: Option D. -> all of the above
Answer: (d).all of the above
Question 37. Fed batch reactors is used to produce vinegar because
  1.    it can maintain low ethanol concentrations
  2.    it can maintain low acetic acid concentrations
  3.    acetic acid bacteria tend to ferment at high ethanol concentrations
  4.    all of the above
 Discuss Question
Answer: Option A. -> it can maintain low ethanol concentrations
Answer: (a).it can maintain low ethanol concentrations
Question 38. When a culture of fermenting yeast becomes metabolically uncoupled, ethanol
  1.    becomes a secondary metabolite
  2.    production becomes growth associated
  3.    production becomes non-growth associated
  4.    becomes a growth nutrient
 Discuss Question
Answer: Option C. -> production becomes non-growth associated
Answer: (c).production becomes non-growth associated
Question 39. On a glucose medium, the growth of an organism is characterized by the following Monod model and stoichiometric parameters μm = 0.3 h­¹, Ks =0.05 g.l­¹ and Yxs = 0.3 g.g­¹ When this organism is grown in a 2 litre continuous on a medium containing 10 g.l­¹ of glucose added at 1 l.h­¹, the steady state concentration of biomass in the reactor will be
  1.    0 g.l­¹
  2.    0.4 g.l­¹
  3.    0.5 g.l­¹
  4.    10 g.l­¹
 Discuss Question
Answer: Option A. -> 0 g.l­¹
Answer: (a).0 g.l­¹
Question 40. Mixing profiles closest to plug flow are observed in
  1.    continuous packed bed reactor
  2.    stirred tank reactor with biomass recycles
  3.    continuous fluidized bed bioreactor
  4.    all of these
 Discuss Question
Answer: Option A. -> continuous packed bed reactor
Answer: (a).continuous packed bed reactor

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