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

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Chemical Reaction Engineering
For the same residence time, which one will give the maximum conversion?

Single tubular flow reactor (v = 5 litres)
Two stirred tank (each of 2.5 litres) in series
Stirred tank followed by tubular flow reactor (each of 2.5 litres)
Single stirred tank (v = 5 litres)

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Chemical Reaction Engineering
A batch reactor is

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

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