III B.Tech II Semester Supplementary Examinations, Apr/May 2006 CHEMICAL REACTION ENGINEERING-I (Chemical Engineering) Time: 3 hours Max Marks: 80 Answer any FIVE Questions All Questions carry equal marks ????? 1. (a) Define reaction rate constant. Develop an expression that facilitates calculation of units of rate constant for any order. [6] (b) Determine equilibrium conversion of A at 3730K for the following aqueous reaction. k *1 R A) ∆G0 = -3375 K cal/K mole
or ld
k2 ∆Hr0
= -18,000 K cal/K mole Assume specific heats of all solutions are equal to that of water.
[10]
2. The gas reaction 2A → R + 2S is approximately second order with respect to A. When pure A is introduced at 1 atm. into a constant volume batch reactor, the pressure rises 40% in 3 minutes. For a constant pressure batch reactor find [8]
(b) the fractional increase in volume at that time.
[8]
uW
(a) the time required for the same conversion
3. Thermal decomposition of ethane to ethylene, butane and hydrogen is believed to follow the sequence given below. C2 H6 → 2CH3∗
CH3∗ + C2 H6 → CH4 + C2 H5∗ C2 H5∗ → C2 H4 + H ∗
H ∗ + C2 H6 → H2 + C2 H5
nt
2C2 H5∗ → C4 H10
Derive the rate law for formation of ethylene.
[16]
Aj
4. An aqueous reaction is being studied in a mixed flow reactor of 5 lit. volume. The stoichiometry of the reaction is A → 2 R and the reactant A is introduced at a concentration of one mole/liter. Using following data, determine a rate expression for this reaction. [16] Feed rate Temperature 0 C cm3 /sec. 2 13 15 13 15 84
Concentration of R in effluent, mole/liter 1.8 1.5 1.8
1 of 2
NR
Code No: NR320802
5. A liquid reactant stream (1 mol/liter) passes through two mixed flow reactors in a series. The concentration of A in the exit of the first reactor is 0.5 mol/liter. Find the concentration in the exit stream of the second reactor. The reaction is second-order with respect to A and V2/V1 = 2. [16] 6. A 20 lit. mixed reactor is to treat a reactant which decomposes as follows: A → R rR = K1 CA = (4/hr)CA
.in
A → S rS = K2 CA = (1/hr)CA Find the feed rate and conversion of reactant so as to maximize profits. What are there on hourly basis? Data: Feed material A cost Rs. 100/mol at CAO = 1 mol/lit. Product R sells for Rs.500/mol and S has no value. The total operating cost is Rs.2500/hr + Rs.125/mol A fed to the reactor unconverted A is not recycled. [16]
8. Write brief notes on:
uW
(a) Series and parallel reactions
or ld
7. The decomposition of Phosphine is irreversible and first order at 6500C. 4P H 3 (g) → P4 (g) + 6H2 (g) The rate constant s−1 is reported as: Log K = - 18963 + 2 log T + 12.130 where T is in 0 k. T In a closed vessel (constant volume) initially containing Phosphine at 1 atm. pressure, what will be the pressure after 50, 100 and 500s. The temperature is maintained at 6500 C. [16]
Code No: NR320802 III B.Tech II Semester Supplementary ...
Code No: NR320802. NR ... 1. (a) Define reaction rate constant. Develop an expression that facilitates calcula- · tion of units of rate constant for any order.
1.a) Explain with a neat sectional view the operation and advantages of hot blast · cupola. b) Discuss the various types of refractories used for cupola lining.
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320256. III-B.Tech. II Semester Supplementary Examinations December 2002/January 2003 · MODELLING OF POWER SYSTEM COMPONENTS · (Electrical and Electronics Engineering) · Time: 3 hours · Max. Marks: 70 · Answer any FIVE questions · All questions carry
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