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Chemical Reaction Engineering

Chemical Reaction Engineering
The vessel dispersion number (D/μL) for plug flow is

500
∞
750

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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?

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

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

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

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Chemical Reaction Engineering
A batch adiabatic reactor at an initial temperature of 373°K is being used for the reaction, A → B. Assume the heat of reaction is - 1kJ/mole at 373°K and heat capacity of both A and B to be constant and equal to 50J/mole.K. The temperature rise after a conversion of 0.5 will be

100°C
20°C
10°C
5°C

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

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Chemical Reaction Engineering
The energy of activation of a chemical reaction

Both B and C
Varies as fifth power of the temperature
Is same as heat of reaction at constant pressure
Is the minimum energy which the molecules must have before the reaction can take place

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