TLS Online TPP Program

#Question id: 31200


Which of the following tools is NOT commonly used for Multiple Sequence Alignment?

#Section 7: Recombinant DNA technology and Other Tools in Biotechnology
  1. BLAST
  2. MUSCLE
  3. T-Coffee
  4. ClustalW
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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: 412

#Section 4: Fundamentals of Biological Engineering

All of the following contribute to the large, negative, free-energy change upon hydrolysis of “high-energy” compounds except:

TLS Online TPP Program

#Question id: 1910

#Section 2: General Biology

Hyperacute graft rejection is caused by:

TLS Online TPP Program

#Question id: 27471

#Section 5: Bioprocess Engineering and Process Biotechnology

In which of the following method, the enzyme is bound to a suitable adsorbent material rendering it immobile?

TLS Online TPP Program

#Question id: 14200

#Section 5: Bioprocess Engineering and Process Biotechnology

A fluidized-bed, immobilized-cell bioreactor is used for the conversion of glucose to ethanol by Z. mobilis cells immobilized in k-carrageenan gel beads. The dimensions of the bed are 10 cm (diameter) by 200 cm. Since the reactor is fed from the bottom of the column and because of CO2 gas evolution, substrate and cell concentrations decrease with the height of the column. The average cell concentration at the bottom of the column is X0 = 45 g/l, and the average cell concentration decreases with the column height according to the following equation:

                             

where Z is the column height (cm). The specific rate of substrate consumption is qS = 2 g S/g cells . h. The feed flow rate and glucose concentration in the feed are 5 l/h and 160 g glucose/l, respectively.

Determine the ethanol concentration in the effluent (g/l . h) if YP/S = 0.48 g ethanol/g glucose