Define the terms: Respiratory quotient, Yield, Growth rate limiting reaction.
[3 marks]Discuss the sterilization of air for the fermentation operation.
[4 marks]Afermenter containing microbial culture at 30 0C is used for production of Gmiivcreo abnia al cicnoseucntti coifd eea wchit hw iittsh 2 s0u-iltiatrbel ec aepxapcliatnya. tKionas i.s to be determined. Air flow L is shut off for few minutes and DO level drops the air supply is then reconnected. When steady state is established, the DO tension is 77% air saturation. The following results are obtained. T T12 Time 5 Oxyge 50 66 n tension Where, C = final steady DO concentration and C = DO AL AL Concentration. (a) Estimate Ka. (b) An error is made determining L steady state oxygen level, which instead of 77% is taken as 69%, what is the percentage error in K L a resulting from this error in C AL.
[15 marks]How do the analogy exists between mass and heat transfer?
[3 marks]Discuss the basic steps for designing of a bioreactor.
[4 marks]The fungus Aureobasidium pullulans is used to produce extracellular polysaccharides by fermentation of sucrose. After 120h fermentation, the following measurements of shear stress and shear rate were made with a rotating cylinder viscometer. Shear Stress dyn Shear Rate cm-2 s-1 44.1 10.2 235.3 170 357.1 340 457.1 510 636.8 1020 [1] Plot the rheogram for this fluid. [2] Determine the appropriate Non Newtonian parameters. [3] find the apparent viscosity at the shear rates of ; 15 s-1 and 200 s-1.
[7 marks]Abacterium converts ethanol to acetic acid under aerobic conditions. A continuous fermentation process for vinegar production is proposed using non- viable bacterial cells immobilized on the surface of gelatin beads. The production target is 2 kg h-1acetic acid; however the maximum acetic acid1 concentration tolerated by the cells is 12%. Air is pumped into the fermenter at a rate of 200 mmol h-1.
[7 marks]What minimum amount of ethanol is required?
[ marks]What minimum amount of water must be used to dilute the ethanol to avoid acid inhibition?
[ marks]Derive the equations for Eddie-Hofstee plot and Lineweaver –Burke plot.
[3 marks]Enlist the energy concerns from heat transfer point of view for a bioreactor.
[4 marks]Write about Non- Newtonian fluids with suitable equations. Explain each of them for its stress and strain relation analogous to the law of viscosity.
[7 marks]Discuss the dynamic method to determine Ka. L
[3 marks]Enlist the enzymes which are medical importance.
[4 marks]Discuss the practical considerations for bioreactor constructions.
[7 marks]Write a note on: Orifice and Nozzle spargers
[3 marks]Discuss aseptic operation by giving schematic to show operating procedures.
[4 marks]Explain the concept of air lift bioreactor. Compare it with fluidized bed bioreactor.
[7 marks]What is the importance of modeling? Where and how does it help in fermentation plants?
[3 marks]Explain the measurement of DO concentrations.
[4 marks]Justify the statement: “Chemostate culture evaluates the kinetic and yield parameters.”
[7 marks]Derive equation to narrate death kinetics of cell culture.
[3 marks]How cells grow? Which factors affect?
[4 marks]Define bioprocess engineering. Explain the role of biotechnology in that.
[7 marks]What are the effects of conditions on Enzyme reaction rate?
[3 marks]Write a note on: Assessing mixing effectiveness
[4 marks]Write the transfer of oxygen from gas bubbles to cell.
[7 marks]