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Chemical Reaction Engineering

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

Tank in series
Bubbling bed
Plug flow
None of these

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Chemical Reaction Engineering
When all the limiting reactant is consumed in the reaction, the operational yield __________ the relative yield.

Equals
Is smaller than
Can be either greater or smaller than (depends on the type of reaction)
Is greater than

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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 CO₂ and 2.8 gms CO besides other constituents. What is the degree of conversion on the basis of disappearance of limiting reactant?

0.75
1
0.2
0.95

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Chemical Reaction Engineering
Catalytic action in a catalytic chemical reaction follows from the ability of catalyst to change the

Activation energy
Equilibrium constant
Heat of reaction
None of these

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Chemical Reaction Engineering
A batch reactor is characterised by

Constant residence time
Variation in reactor volume
Very low conversion
Variation in extent of reaction and properties of the reaction mixture with time

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Chemical Reaction Engineering
In case of a/an __________ chemical reaction, conversion increases with the rise in temperature.

Reversible endothermic
Irreversible exothermic
Irreversible endothermic
Reversible exothermic

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