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Chemical Reaction Engineering

Chemical Reaction Engineering
For a mixed flow reactor operating at steady state, the rate of reaction is given by

FA0/V - dCsub>A/dt
- dCsub>A/dt
FA0/V . Xsub>A
FA0/V + dCsub>A/dt

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Chemical Reaction Engineering
Fluid flow in a real packed bed can be approximated as __________ model.

Plug flow
Tank in series
Dispersion
Mixed flow

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Chemical Reaction Engineering
Helium-mercury method can be used to determine the __________ of the catalyst particle.

All of these
Pore volume
Porosity
Solid density

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Chemical Reaction Engineering
Which of the following is the most suitable for very high pressure gas phase reaction?

Fluidised bed reactor
Tubular flow reactor
Batch reactor
Stirred tank reactor

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Chemical Reaction Engineering
If Thiele modulus is __________ , then the pore diffusion resistance in a catalyst may be considered as negligible.

∞
> 0.5
0
< 0.5

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Chemical Reaction Engineering
In a/an __________ vessel, the fluid enters and leaves following plug flow.

Close-opened
Open-closed
Closed
Open

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