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Chemical Reaction Engineering

Chemical Reaction Engineering
Fluid flow in a real packed bed can be approximated as __________ model.

Tank in series
Mixed flow
Dispersion
Plug flow

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Chemical Reaction Engineering
Slurry reactors are characterised by the

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

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Chemical Reaction Engineering
A catalyst in a chemical reaction

All of these
Increases the frequency of collisions of reacting species
Alters the reaction mechanism
Decreases the activation energy

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Chemical Reaction Engineering
An exothermic reaction takes place in an adiabatic reactor. The product temperature __________ reactor feed temperature.

May be greater or less than
Is always less than
Is always greater than
Is always equal to

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Chemical Reaction Engineering
Non-catalytic fluid-solid reactions are represented by __________ model.

Unreacted core
Continuous reaction
Both A and B
Neither A and B

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Chemical Reaction Engineering
In case of a/an __________ chemical reaction, conversion increases with the rise in temperature.

Reversible endothermic
Irreversible exothermic
Reversible exothermic
Irreversible endothermic

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