TLS Online TPP Program

#Question id: 19022


Calculate the degree of reduction for ethanol, where the degree of reduction of C=4, H=1, O=-2.

#Section 4: Fundamentals of Biological Engineering
  1. γ = 9
  2. γ = 6
  3. γ = 3
  4. γ = 2
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TLS Online TPP Program

#Question id: 14322

#Section 5: Bioprocess Engineering and Process Biotechnology

Production of recombinant protein by a geneticallyengineered strain of Escherichia coli is proportional to cell growth. Ammonia is used as nitrogen source for aerobic respiration of glucose. The recombinant protein has an overall formula CHI.5500.31N0.25. The yield ofbiomass from glucose is measured at 0.48 g g-1; the yield of recombinant protein from glucose is about 20% that for cells. How much ammonia is required per gmol glucose?

TLS Online TPP Program

#Question id: 14323

#Section 5: Bioprocess Engineering and Process Biotechnology

Production of recombinant protein by a geneticallyengineered strain of Escherichia coli is proportional to cell growth. Ammonia is used as nitrogen source for aerobic respiration of glucose. The recombinant protein has an overall formula CHI.5500.31N0.25. The yield ofbiomass from glucose is measured at 0.48 g g-1; the yield of recombinant protein from glucose is about 20% that for cells. What is the oxygen demand per gmol glucose?

TLS Online TPP Program

#Question id: 14324

#Section 5: Bioprocess Engineering and Process Biotechnology

Production of recombinant protein by a geneticallyengineered strain of Escherichia coli is proportional to cell growth. Ammonia is used as nitrogen source for aerobic respiration of glucose. The recombinant protein has an overall formula CHI.5500.31N0.25. The yield of biomass from glucose is measured at 0.48 g g-1; the yield of recombinant protein from glucose is about 20% that for cells. If the biomass yield remains at 0.48 g g- l, how much change in oxygen requirement for wild-type E. coli unable to synthesise recombinant protein?

TLS Online TPP Program

#Question id: 14325

#Section 5: Bioprocess Engineering and Process Biotechnology

Production of recombinant protein by a geneticallyengineered strain of Escherichia coli is proportional to cell growth. Ammonia is used as nitrogen source for aerobic respiration of glucose. The recombinant protein has an overall formula CHI.5500.31N0.25. The yield ofbiomass from glucose is measured at 0.48 g g-1; the yield of recombinant protein from glucose is about 20% that for cells. If the biomass yield remains at 0.48 g g- l, how much change in ammonia requirement for wild-type E. coliunable to synthesise recombinant protein?

TLS Online TPP Program

#Question id: 14326

#Section 5: Bioprocess Engineering and Process Biotechnology

The chemical reaction equation for conversion of ethanol (C2H60) to acetic acid (C2H402) is:



Acetic acid is produced from ethanol during growth of Acetobacter aceti, which has the composition CH1.800.5N0.2. Biomass yield from substrate is 0.14 g g- 1; product yield from substrate is 0.92 g g-1. Ammonia is used as nitrogen source. How much gmol of oxygen is demanded for acetic acid production?

TLS Online TPP Program

#Question id: 14327

#Section 5: Bioprocess Engineering and Process Biotechnology

Bakers' yeast is produced in a 50 000-litre fermenter under aerobic conditions. The carbon substrate is sucrose; ammonia is provided as nitrogen source. The average biomass composition is CH1.8300.55N0.17 with 5% ash. Under efficient growth conditions, biomass is the only major product; the biomass yield from sucrose is 0.5 g g-I. If the specific growth-rate is 0.45 h-l, estimate the rate of heat removal required to maintain constant temperature in the fermenter when the yeast concentration is 10 g l- 1     _______________________.10^6