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Enrolment No.GUJARAT TECHNOLOGICAL UNIVERSITY
E - SEMESTER-VII (NEW) EXAMINATION — WINTER 2018
Subject Code: 2172602/2172607 Date: 19/11/2018
Subject Name: Polymer Kinetics
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Time: 10:30 AM TO 01:00 PM Total Marks: 70Instructions:
1. Attempt all questions.
2. Make suitable assumptions wherever necessary.
3. Figures to the right indicate full marks.
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- The rate constants for a certain reaction are 1.6*107 and 1.625*107 (second)-1 at 10°C and 30°C respectively. Calculate the activation energy. 03
- Compare collision theory to transition state theory. 04
- The primary reaction occurring in the homogeneous decomposition of nitrous oxide is found to be N2O—N2+1/2O2, with a rate -rN2O= k1*[N2O]/1+k2*[N2O].Devise a mechanism to explain this observed rate. 07
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OR
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- Give classification of reactors based on it’s thermal behavior. 03
- Differentiate integral method of analysis and differential method of analysis. 04
- Derive integral rate expression for second order irreversible bimolecular reaction A+B?P for variable volume system. 07
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- The decomposition of NH3 on tungsten wire at 856°C yield the following result:
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Total Pressure,(Torr) 228 250 273 318
Time(s) 200 400 600 1000
Determine the order of reaction and calculate value of the rate constant. 07 - Write a brief note on term ‘molecularity’ 03
- With the suitable examples, explain the term space time and space velocity respectively. 04
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- The decomposition of NH3 on tungsten wire at 856°C yield the following result:
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OR
- Assuming a stoichiometry A?R for first order gas reaction, we calculate the size of plug flow reactor needed for given duty (99%conversion of pure feed) to be V=32 liters. Infact, however, the reactions stoichoimetry is A?3R with this corrected stoichiometry, what is the required reactor volume? 07
- Write a brief note on order of reaction. 03
- Consider a gaseous feed CA0=100, CB0=200 to a steady flow reactor operated at constant temperature and pressure. The isothermal gas phase reaction taking place is A+B?R+S. For XA=0.8, find CA, CB, and XB. 04
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- The homogeneous gas phase decomposition of phosphine proceeds at 649°C, 4PH3? P4 +6H2 with the first order rate r PH3=(10/hr)*C PH3.What size of plug flow reactor for operating at 649°C and 4.6 atmosphere can produce 80% conversion of feed consisting of 2 kgmoles of pure phosphine per hour? 07
- Write down the practical significance of chain modifier with suitable rubber reaction chemistry. 03
- Explain the kinetics of non-catalyzed polycondensation reaction. 04
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OR
- Discuss the kinetics of cationic polymerization. 07
- With reaction chemistry explain the term ‘telomerization’. 03
- Explain the kinetics of catalyzed polycondensation reaction. 04
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- Discuss the kinetics of anionic polymerization. 07
- Explain the principle of membrane osmometry method to determine the polymer molecular weight. 03
- Write about the methods used to determine the reactivity ratio. 04
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OR
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- The following data were obtained on the osmotic pressure of solution of B-globulin in 0.1SMNacl a1 37°C
C, grammole/100ml 19.27 12.53 5.81
p, mmH2O 453 253 112
Calculate the polymer weight of polymer. - - Write down the full form of USLV. Also give it’s major advantages. 03
- Write in brief about the effect of reactivity ratio on copolymerization behavior. 04
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- The following data were obtained on the osmotic pressure of solution of B-globulin in 0.1SMNacl a1 37°C
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- Calculate the intrinsic viscosity of polystyrene sample in toluene from the following relative viscosity data obtained at 25°C.
C*103Kgmole/m3 0.002 0.004 0.006 0.008 0.010
?r 1.102 1.208 1.317 1.430 1.548--- Content provided by FirstRanker.com ---
Calculate M if the Mark Houwink constants are a=0.69 and K=1.7*10-5m3/Kgmole
- Calculate the intrinsic viscosity of polystyrene sample in toluene from the following relative viscosity data obtained at 25°C.
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