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Chemical Reaction Engineering

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

Plug flow
Dispersion
Mixed flow
Tank in series

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

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Chemical Reaction Engineering
A reactor is generally termed as an autoclave, when it is a

Atmospheric pressure tank reactor
High pressure batch reactor
Atmospheric pressure CSTR
High pressure tubular reactor

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Chemical Reaction Engineering
Arrhenious equation represents graphically the variation between the __________ and temperature.

Frequency factor
Activation energy
Rate of reaction
Rate constant

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

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

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Chemical Reaction Engineering
Which of the following is an independent variable for a batch tank reactor with uniform concentration and temperature?

Useful volume of the tank
Diameter of the reactor
None of these
Time

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