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

5°C
20°C
10°C
100°C

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Chemical Reaction Engineering
In an ideal P.F.R. at steady state conditions

There may be diffusion along the flow path
The conversion of the reactant varies from point to point along a flow path
There is no lateral mixing of fluid
The composition of reactants remains constant along a flow path

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