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Chemical Reaction Engineering

Chemical Reaction Engineering
Carrier in a catalyst increases its

Performance
Surface area
None of these
Activity

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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
An autothermal reactor is

Most suitable for a second order reaction
Isothermal in nature
Most suitable for a reversible reaction
Completely self-supporting in its thermal energy requirements

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

Porosity
Pore volume
Solid density
All of these

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Chemical Reaction Engineering
For a fluidised bed reactor, the most suitable/relevant model is a __________ model.

Tank in series
None of these
Plug flow
Bubbling bed

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Chemical Reaction Engineering
6 gm of carbon is burnt with an amount of air containing 18 gm oxygen. The product contains 16.5 gms COâ‚‚ and 2.8 gms CO besides other constituents. What is the degree of conversion on the basis of disappearance of limiting reactant?

1
0.75
0.95
0.2

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