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Chemical Reaction Engineering

Chemical Reaction Engineering
The conversion for a first order liquid phase reaction. A → B in a CSTR is 50%. If another CSTR of the same volume is connected in series, then the % conversion at the exit of the second reactor will be

100
90
75
60

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Chemical Reaction Engineering
From among the following, choose one which is not an exothermic process.

Methanol synthesis
Catalytic cracking
Oxidation of sulphur
Ammonia synthesis

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Chemical Reaction Engineering
Molecularity of an elementary reaction, P + Q → R + S is

2
3
1
4

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Chemical Reaction Engineering
Higher free energy of activation of a chemical reaction (at a given temperature) implies

Both B and C
Slower rate of reaction
Higher rate of reaction
Higher equilibrium conversion

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Chemical Reaction Engineering
A stirred tank reactor compared to tubular-flow reactor provides

All of these
Higher overall selectivity for a first order consecutive reaction
More uniform operating conditions
Permits operation at the optimum temperature for a long reaction time

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Chemical Reaction Engineering
If the time required for half change is inversely proportional to the square of initial concentration and the velocity depends on the units in which the concentration term is expressed, then the order of reaction is

0
3
1
2

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