Chemical Reaction Engineering
A batch reactor suffers from following disadvantage.

High labour and handling cost
Poor product quality control
High shutdown time requirement for emptying, cleaning and refilling
All of these

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Chemical Reaction Engineering
For a tubular reactor with space time 'τ' and residence time 'θ', the following statement holds good.

τ = θ , for a non-isothermal reactor
τ = θ , for an isothermic tubular reactor in which the density of the process fluid is constant
τ = θ , when the fluid density changes in the reactor
τ and θ are always equal

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Chemical Reaction Engineering
The heat of reaction

Depends on both pressure and mechanism of reaction
Depends on the pressure only
Is independent of the mechanism of reaction
Depends on the mechanism of reaction only

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Chemical Reaction Engineering
An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction

Is maximum at the inlet of the reactor
Goes through a minimum along the length of the reactor
Is maximum at the exit of the reactor
Goes through a maximum along the length of the reactor

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