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Chemical Reaction Engineering

Chemical Reaction Engineering
Promoter is added to the catalyst to improve its

None of these
Porosity
Sensitivity
Surface area

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Chemical Reaction Engineering
Holding time for flow reactors is __________ the space time, for constant fluid density

Double
Equal to
None of these
Triple

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

Dispersion
Plug flow
Mixed flow
Tank in series

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Chemical Reaction Engineering
N' plug flow reactors in series with a total volume 'V' gives the same conversion as a single plug flow reactor of volume 'V' for __________ order reactions.

Third
Any
Second
First

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Chemical Reaction Engineering
The catalyst in a second order reversible reaction increases the rate of the forward reaction

To a greater extent than that of the backward reaction
And decreases that of backward reaction
And backward reaction equally
Only

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Chemical Reaction Engineering
Non-catalytic fluid-solid reactions are represented by __________ model.

Neither A and B
Unreacted core
Continuous reaction
Both A and B

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