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Chemical Reaction Engineering

Chemical Reaction Engineering
In case of a P.F.R., there

Both A and B
May be lateral mixing of fluid
Neither A nor B
Should not be any mixing along the flow path

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Chemical Reaction Engineering
Rate constant 'k' and absolute temperature 'T' are related by collision theory (for bimolecular) as

k ∝ √T
k ∝ T
k ∝ exp(-E/RT)
k ∝ T1.5

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Chemical Reaction Engineering
The conversion of a reactant, undergoing a first order reaction, at a time equal to three times the half life of the reaction is

0.425
Data insufficient to calculate
0.5
0.875

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Chemical Reaction Engineering
Fluidised bed reactor is characterised by

Very small pressure drop
Absence of continuous catalyst regeneration facility
Comparatively smaller equipment
Uniformity of temperature

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Chemical Reaction Engineering
Reverse reaction in a chemical equilibrium is favoured by the

Removal of one of the products regularly
None of these
Increase in the concentration of one of the reactants
Increase in the concentration of oneof the products

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Chemical Reaction Engineering
For the liquid phase parallel reactions:R, rR = K?.CA2; E? = 80 KJ/moleS, rS = K?.CA ; E? = 120 KJ/mole The desired product is R. A higher selectivity of R will be achieved, if the reaction is conducted at

High temperature in a PFR
Low temperature in a PFR
High temperature in a CSTR
Low temperature in a CSTR

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