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Chemical Reaction Engineering

Chemical Reaction Engineering
Bulk diffusion in catalyst pore __________ with increase in pressure.

Decreases
Remains unchanged
Increases
Increases exponentially

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Chemical Reaction Engineering
Kinetics of a catalytic reaction can be best studied on a/an __________ reactor.

Integral (plug flow)
Mixed
Either A, B and C
Differential (flow)

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Chemical Reaction Engineering
The conversion in a mixed reactor/accomplishing a reaction A 3R is 50% when gaseous reactant 'A' is introduced at the rate of 1 litre/second and the leaving flow rate is 2 litres/second. The holding time for this operation is __________ second.

3
0.5
2
1

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Chemical Reaction Engineering
Slurry reactors are characterised by the

Both A and B
Neither A nor B
Lack of intraparticle diffusion resistance
Presence of two mobile phases

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Chemical Reaction Engineering
A chemical reaction, A → 3B, is conducted in a constant pressure vessel. Starting with pure A, the volume of the reaction mixture increases 3 times in 6 minutes. The fractional conversion is

0.5
1
Data insufficient, can't be predicted
0.33

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Chemical Reaction Engineering
For identical flow rate and feed composition, X plug flow reactors (PER) in series with a total volume V gives the same conversion as single

CSTR of volume V/X
PFR of volume V
PFR of volume V/X
CSTR of volume V

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