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Chemical Reaction Engineering

Chemical Reaction Engineering
A catalyst promoter

Itself has very high activity
Improves the activity of a catalyst
Acts as a catalyst support
All of these

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Chemical Reaction Engineering
In an ideal tubular-flow reactor

There is a uniform velocity across the radius
There is no mixing in longitudinal direction
Mixing takes place in radial direction
All of these

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Chemical Reaction Engineering
Which of the following does not produce a change in the value of rate constant of a reaction?

Pressure
None of these
Concentration and catalyst
Temperature

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Chemical Reaction Engineering
A batch reactor suffers from following disadvantage.

High labour and handling cost
All of these
Poor product quality control
High shutdown time requirement for emptying, cleaning and refilling

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Chemical Reaction Engineering
Which of the following is not a unit of reaction rate?

Mole formed/volume of catalyst) (time)
None of these
Moles formed/volume of reactor) (time)
Moles for med/(surface of catalyst) (time)

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Chemical Reaction Engineering
For the liquid phase zero order irreversible reaction A → B, the conversion of A in a CSTR is found to be 0.3 at a space velocity of 0.1min⁻¹ . What will be the conversion for a PFR with a space velocity of 0.2 min⁻¹? Assume that all the other operating conditions are the same for CSTR and PFR.

0.3
0.15
0.6
0.9

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