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Chemical Reaction Engineering

Chemical Reaction Engineering
Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is

43833
43832
43835
43834

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Chemical Reaction Engineering
For a fluidised bed reactor, the most suitable/relevant model is a __________ model.

Bubbling bed
Plug flow
Tank in series
None of these

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Chemical Reaction Engineering
The rate of a gas phase reaction is given by K . CA . CB. If the volume of the reaction vessel is reduced to l/4th of its initial volume, then the reaction rate compared to the original rate will be __________ times.

8
16
2
4

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Chemical Reaction Engineering
Transition state theory relates the above quantities as

K ∝ e-E/RT
K ∝ √T
K ∝ T1.5
K ∝ T.eE/RT

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Chemical Reaction Engineering
Half-life period for a first order reaction is __________ the initial concentration of the reactant.

Independent of
None of these
Inversely proportional to
Directly proportional to

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Chemical Reaction Engineering
When a catalyst increases the rate of chemical reaction, the rate constant

Becomes infinite
Remains constant
Decreases
Increases

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