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Chemical Reaction Engineering

Chemical Reaction Engineering
Carrier in a catalyst increases its

None of these
Performance
Activity
Surface area

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Chemical Reaction Engineering
The performance of a cascade of CSTR's can be improved by adding

More CSTR's in parallel
More CSTR's in series
A P.F. reactor in series
A P.F. reactor in parallel

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Chemical Reaction Engineering
The concentration of A in a first order reaction, A → B, decreases

Exponentially with time
Linearly with time
Very abruptly towards the end of the reaction
Logarithmically with time

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Chemical Reaction Engineering
For any reaction, we may write conversion as a function of

All of these
Temperature
Concentration
Time

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Chemical Reaction Engineering
When the reaction occurs in the diffusion controlled region, the apparent activation energy as measured is only __________ the true value.

Equal
Twice
None of these
Half

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Chemical Reaction Engineering
The fractional volume change of the system for the isothermal gas phase reaction, A 3B , between no conversion and complete conversion is

0.5
3
1
2

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