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Chemical Reaction Engineering

Chemical Reaction Engineering
The residence time distribution of an ideal CSTR is

1/τ (-t/τ)
1/τ exp (-t/τ)
Τ exp (-t/τ)
Exp(-t/τ)

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Chemical Reaction Engineering
In a semi-batch reactor

Residence time is constant
Velocity of reaction can be controlled
Maximum conversion can be controlled
Both the reactants flow counter-currently

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Chemical Reaction Engineering
The dispersion number of perfect mixed flow is

< 2100
> 150
∞

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Chemical Reaction Engineering
The decomposition of A into B is represented by the exothermic reaction, A ⇋ 2B. To achieve maximum decomposition, it is desirable to carry out the reaction.

At high P and low T
At low P and low T
At low P and high T
At high P and high T

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Chemical Reaction Engineering
In a/an __________ vessel, the fluid enters and leaves following plug flow.

Close-opened
Open
Closed
Open-closed

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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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