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MCQs

Total Questions : 114 | Page 6 of 12 pages
Question 51. Which of the following organisms will continue their metabolism at high substrate concentrations?
  1.    Pseudomonas aeruginosa
  2.    Saccharomyces cerevisiae
  3.    Bacillus subtilis
  4.    Escherichia coli
 Discuss Question
Answer: Option A. -> Pseudomonas aeruginosa
Answer: (a).Pseudomonas aeruginosa
Question 52. In a fluidized bed reactor mixing is achieved by
  1.    gravity flow of fluid
  2.    upward movement of the incoming feed
  3.    diffusion
  4.    both (a) and (b)
 Discuss Question
Answer: Option D. -> both (a) and (b)
Answer: (d).both (a) and (b)
Question 53. Two continuous bioreactors containing the same organisms, fed with the same feed at the same dilution rate were compared. Reactor 1 started with an initial concentration of glucose of 10 g.l­¹, while reactor 2 contained 0.1 g.l­¹ of glucose at the start of the process then at steady state
  1.    the concentration of glucose in reactor 1 would be greater than that in reactor 2
  2.    the concentration of glucose in reactor 1 would be equal to reactor 2
  3.    the concentration of glucose in reactor 1 would always be zero.
  4.    the concentration of glucose in reactor 1 would be less than that in reactor 2
 Discuss Question
Answer: Option B. -> the concentration of glucose in reactor 1 would be equal to reactor 2
Answer: (b).the concentration of glucose in reactor 1 would be equal to reactor 2
Question 54. Yeast is typically produced in fed batch reactors because
  1.    yeast cells produce ethanol at low glucose concentrations
  2.    yeast cells ferment at low glucose concentrations
  3.    yeast cells respire at low glucose concentrations
  4.    all of the above
 Discuss Question
Answer: Option C. -> yeast cells respire at low glucose concentrations
Answer: (c).yeast cells respire at low glucose concentrations
Question 55. If biomass yields are constant, then the biomass productivity of a culture grown in continuous reactor will
  1.    always decrease with dilution rate
  2.    increase with dilution rate until washout
  3.    remain constant irrespective of the dilution rate
  4.    decrease with dilution rate until washout
 Discuss Question
Answer: Option B. -> increase with dilution rate until washout
Answer: (b).increase with dilution rate until washout
Question 56. Which of the following is used to calculate mass of substrate in the reactor?
  1.    Flow rate x substrate concentration in the reactor
  2.    Volume of reactor x substrate concentration in reactor
  3.    Flow rate x mass of reactor
  4.    Volume of reactor x Flow rate
 Discuss Question
Answer: Option B. -> Volume of reactor x substrate concentration in reactor
Answer: (b).Volume of reactor x substrate concentration in reactor
Question 57. Low dissolved oxygen concentrations leads to
  1.    low biomass yields
  2.    high biomass yields
  3.    no effect on biomass yields
  4.    none of the above
 Discuss Question
Answer: Option A. -> low biomass yields
Answer: (a).low biomass yields
Question 58. A continuous reactor has a dilution rate of 0.5 h­¹. Its residence time would be
  1.    ln(2)/0.5
  2.    ln(2) x 0.5
  3.    0.5 h
  4.    2 h
 Discuss Question
Answer: Option D. -> 2 h
Answer: (d).2 h
Question 59. In a continuous reactor, the medium contains 40 g.l­¹ of maltose and the medium flow rate is 10 litres per hour and the effluent contains 20 g.l­¹ of lactate. What is the productivity of lactate production from this reactor?
  1.    50 g maltose.l­¹
  2.    50 g lactate.l­¹
  3.    200 g maltose.l­¹
  4.    200 g lactate.l­¹
 Discuss Question
Answer: Option D. -> 200 g lactate.l­¹
Answer: (d).200 g lactate.l­¹
Question 60. A fed-batch reactor containing 1 g.l­¹ of substrate in 2 litre of medium. It is fed with 1 g.l-l of substrate at the rate of 1 litre per hour. After 10 hours, the concentration of substrate in the reactor was 0.5 g.l­¹ . The mass of substrate that was used by the culture in the reactor was
  1.    2g
  2.    6g
  3.    8g
  4.    12g
 Discuss Question
Answer: Option B. -> 6g
Answer: (b).6g

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