Chemical Reaction Engineering
With the same reaction time, initial concentration and feed rate, the reaction 2A → B is carried out separately in CSTR and P.F. reactor of equal volumes. The conversion will be

Same in both the reactors
Data insufficient; can't be predicted
Higher in P.F. reactor
Higher in CSTR

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Chemical Reaction Engineering
A pollutant P degrades according to first order kinetics. An aqueous stream containing P at 2 kmole/m³ and volumetric flow rate 1m³ /h requires a mixed flow reactor of volume V to bring down the pollutant level to 0.5 kmole/m³ . The inlet concentration of the pollutant is now doubled and the volumetric flow rate is tripled. If the pollutant level is to be brought down to the same level of 0.5 kmole/m³ , the volume of the mixed flow reactor should be increased by a factor of

3
7
6
44015

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Chemical Reaction Engineering
A batch reactor is suitable for

Achieving cent percent conversion of reactants into products
Large scale gaseous phase reactions
Obtaining uniform polymerisation products in highly exothermic reactions
Liquid phase reactions

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