Code No: 45053

R07

Set No - 1

in

III B.Tech I Semester Regular Examinations,Nov/Dec 2009 BIOCHEMICAL REACTION ENGINEERING-1 Bio-Technology Time: 3 hours Max Marks: 80 Answer any FIVE Questions All Questions carry equal marks ????? 1. Write short notes on

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(a) enzyme specificity (b) active site

[8+8]

[16]

3. Describe about the product formation stoichiometry of fermentation.

[16]

4. Derive the design equation for a batch reactor. Write the advantages and disadvantages using batch reactors in bioprocessing?

[16]

or

2. Explain the mass transfer limitations in immobilized enzyme systems.

5. Explain the significance of type of carrier, concentrations, pH, temperature, and reaction time in immobilization of enzymes. [16]

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6. Explain the concept of search for a biochemical reaction mechanism taking enzyme-substrate as example.

[16]

7. Given that the maximum specific growth rate of an organism is µmax = 1 h-1 and its Ks = 1.5 g/cm3. If the input substrate concentration is 145 g/cm3 and concentration of product at this maximum output rate is 10 g/cm3, determine the maximum output rate of the product. [16]

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8. Discuss in detail about applications of RTD Measurements.

1

[16]

Code No: 45053

R07

Set No - 2

1. What is Han-Levenspiel model? Explain it in detail.

in

III B.Tech I Semester Regular Examinations,Nov/Dec 2009 BIOCHEMICAL REACTION ENGINEERING-1 Bio-Technology Time: 3 hours Max Marks: 80 Answer any FIVE Questions All Questions carry equal marks ????? [16]

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2. Describe about online data analysis for measurement of biochemical parameters. [16] 3. Explain the concept of enzyme stability and immobilization?

[16]

4. Derive an expression for the concentration profile of a substrate following first order kinetics and spherical geometry considering internal mass transfer. [16]

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or

5. Michaelis-Menton kinetics are used to describe intracellular reactions. Yet [E0 ] ≈ [S0 ]. In invitro batch reactors, the quasi steady state hypothesis does not hold for [E0 ] ≈ [S0 ]. The rapid equilibrium assumption will not hold. Explain why Michalis-Menten kinetics and the quasi-steady-state approximation are still reasonable descriptions of intracellular enzyme reactions. [16] 6. (a) What are the factors that contribute to increase specific growth rate? (b) A batch fermenter is being used for the production of yeart cell from glucose. The number of yeart cells is found to double in 1.5h. Find the specific growth rate of cells. [8+8] 7. (a) Explain about various variables affecting the rate of biochemical reaction. (b) Describe various methods of expressing rate of a biochemical reaction. [8+8]

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8. “RTD as a diagnostic tool for detecting and characterizing flow behavior” Explain. [16]

2

Code No: 45053

R07

Set No - 3

1. Describe about the cell growth stoichiometry of fermentation.

in

III B.Tech I Semester Regular Examinations,Nov/Dec 2009 BIOCHEMICAL REACTION ENGINEERING-1 Bio-Technology Time: 3 hours Max Marks: 80 Answer any FIVE Questions All Questions carry equal marks ????? [16]

ld .

2. Describe Typical batch growth curve of a microbial culture. Explain about various growth phases in the curve. [16] 3. Discuss the various physical and chemical techniques used for enzyme immobilization.

[16]

4. (a) Describe the effect of substrate on growth inhibition.

or

(b) Describe the effect of product on growth inhibition.

[8+8]

5. (a) Explain how activation energy and temperature dependency are interdependable for a biochemical reaction. (b) Explain the role of Arrhenius law on a bio chemical reaction.

[8+8]

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6. Establish relation ship between the equilibrium constant and its relation to G0 .[16] 7. Write short notes on

(a) ENZYME CATALYSIS

(b) Nature and Examples of Enzyme Catalysis

[8+8]

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nt

8. You are working for a company A and you join a research group working on immobilized enzymes. Harry, the head of the lab, claims that immobilization improves the stability of the enzyme. His proof is that the enzyme has a half life of 10 days in free solution, but under identical conditions of temperature, pH , and medium composition, the measured half life of a packed column is 30 days. The enzymes immobilized in a porous sphere 5 mm in diameter. Is Harrys reasoning right? Do u agree with him? Why or why not? [16] ?????

3

Code No: 45053

R07

Set No - 4

1. Explain about overall growth stoichiometry of fermentation.

in

III B.Tech I Semester Regular Examinations,Nov/Dec 2009 BIOCHEMICAL REACTION ENGINEERING-1 Bio-Technology Time: 3 hours Max Marks: 80 Answer any FIVE Questions All Questions carry equal marks ????? [16]

ld .

2. Derive the design equation for a CST reactor. Write the advantages and disadvantages using batch reactors in bioprocessing? [16] 3. Explain the application of immobilized enzymes in industry and medicine.

[16]

or

4. Milk is pasteurized if it is heated to 630 C for 30 min, but if it is heated to 740 C it only needs 15 s for the same result. Find the activation energy of this sterilization process? [16] 5. Disuss in detail about the effects of temperature and pressure changes on the equilibrium constant for a reaction. [16]

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6. Given that the maximum specific growth rate of an organism is max = 1 h-1 and its Ks = 1.5 g/cm3. If the input substrate concentration is 145 g/cm3, determine the maximum output rate for this system in a CFSTR. [16] 7. Derive Michaelis-Menten reaction rate expression with different assumptions. (a) Equilibrium Assumption

(b) Sequential irrevesible Reaction Assumption (c) Quasi-Steady State Assumption

[5+5+6]

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8. Discuss the external diffusional effects on the immobilized enzyme kinetics on non-porus supports. [16]

4

R07 Set No - 1

Code No: 45053. R07. Set No - 1. III B.Tech I Semester Regular Examinations,Nov/Dec 2009 · BIOCHEMICAL REACTION ENGINEERING-1 · Bio-Technology.

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