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Chemical Reaction Engineering

Chemical Reaction Engineering
For a packed bed reactor; the presence of a long tail in the residence time distribution curve is an indication of

Bypass
Chanelling
Dead zone
Ideal plug flow

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

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

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Chemical Reaction Engineering
For every 10°C rise in temperature, the rate of chemical reaction doubles. When the temperature is increased from 30 to 70°C, the rate of reaction increases __________ times.

16
12
32
8

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Chemical Reaction Engineering
The use of space time is preferred over the mean residence time in the design of a/an

CSTR
Ideal tubular-flow reactor
Batch reactor
Slurry reactor

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Chemical Reaction Engineering
The 'E' curve for a non-ideal reactor defines the fraction of fluid having age between t and t + dt

At the outlet
In the reactor
At the inlet
Averaged over the inlet and outlet

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Chemical Reaction Engineering
The role of a catalyst in a chemical reaction is to change the

Activation energy
Heat of reaction
Final products
Equilibrium constant

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