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Chemical Reaction Engineering

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

Tank in series
Dispersion
Plug flow
Mixed flow

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Chemical Reaction Engineering
A reaction which is catalysed by an acid is also catalysed by any substance, which has a tendency to

None of these
Lose a proton
Gain a proton
Lose an electron

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Chemical Reaction Engineering
To maximise the formation of R in the simultaneous reactionA + B → R , rR = 2CA0.5.CB2 A + B → S , rS = 1.5 CA . CB We should have

High CA, high CB
Low CA, low CB
High CA, low CB
Low CA, high CB

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Chemical Reaction Engineering
Carbon particles accummulated on the catalyst used in the gas oil cracking lies in the category of __________ poison.

Deposited
Selectivity
Chemisorbed
Stability

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Chemical Reaction Engineering
Chemical kinetics can predict the __________ of a chemical reaction.

Feasibility
Rate
Both A & B
Neither A nor B

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

Double
None of these
Triple
Equal to

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