Chemical Reaction Engineering
The space time is equivalent to the holding time in a steady state mixed reactor for

Constant fluid density systems
Variable fluid density systems
Gas reactions with changing no. of moles
Non-isothermal gas reaction

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Chemical Reaction Engineering
In solid catalysed reactions the diffusional effects are more likely to affect the overall rate of reaction for

Fast reaction in catalyst of large pore diameter
Slow reactions in catalyst of small pore diameter
Fast reactions in catalyst of small pore diameter
Slow reactions in catalyst of large pore diameter

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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

7
6
44015
3

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