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

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

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Chemical Reaction Engineering
In an ideal mixed reactor (at steady state), the

Composition throughout the reactor remains same
Space time is equivalent to holding time for constant density systems
All of these
Exit stream has the same composition as the fluid within the reactor

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Chemical Reaction Engineering
A batch reactor is

Suitable for liquid phase reactions involving small production rate
Most suitable for very large production rate
Suitable for gas-phase reactions on commercial scale
Least expensive to operate for a given rate

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Chemical Reaction Engineering
For a heterogenous catalytic reaction, A + B → C, with equimole feed of A and B, the initial rate - rA0 is invariant with total pressure. The rate controlling step is

Surface reaction between absorbed A and absorbed B
Desorption of C
Surface reaction between A in the gas phase and absorbed B
Surface Kc/(1 + TS) reaction between absorbed A and B in the gas phase

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