Slurry reactors are characterised by the

Chemical Reaction Engineering
Slurry reactors are characterised by the

Neither A nor B

Both A and B

Presence of two mobile phases

Lack of intraparticle diffusion resistance

Neither A nor B

Both A and B

Presence of two mobile phases

Lack of intraparticle diffusion resistance

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Chemical Reaction Engineering
A trickle bed reactor is the one, which

Has altogether three streams either entering or leaving

Employs all the three phases (i.e.. .solid, liquid and gas)

Processes three reactants with same flow rate

Processes three reactants at different flow rates

Has altogether three streams either entering or leaving

Employs all the three phases (i.e.. .solid, liquid and gas)

Processes three reactants with same flow rate

Processes three reactants at different flow rates

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Chemical Reaction Engineering
n' number of plug flow reactors (P.F.R) in series with a total volume 'V' gives the same conversion as one P.F.R. of volume

1/V

V

V/n

V.n

1/V

V

V/n

V.n

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Chemical Reaction Engineering
For a heterogeneous catalytic reaction

Free energy of activation is lowered in the presence of catalyst, which remains unchanged at the end of reaction

The catalyst does not form an intermediate complex with the reactant

The surface of the catalyst does not play an important role during reaction

A relatively small amount of catalyst can cause the conversion of large amount of reactants which does not mean that catalyst concentration is important

Free energy of activation is lowered in the presence of catalyst, which remains unchanged at the end of reaction

The catalyst does not form an intermediate complex with the reactant

The surface of the catalyst does not play an important role during reaction

A relatively small amount of catalyst can cause the conversion of large amount of reactants which does not mean that catalyst concentration is important

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Chemical Reaction Engineering
A batch reactor is suitable for

Achieving cent percent conversion of reactants into products

Liquid phase reactions

Large scale gaseous phase reactions

Obtaining uniform polymerisation products in highly exothermic reactions

Achieving cent percent conversion of reactants into products

Liquid phase reactions

Large scale gaseous phase reactions

Obtaining uniform polymerisation products in highly exothermic reactions

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Chemical Reaction Engineering
In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume.

More than

Same as

Data insufficient; can't be predicted

Less than

More than

Same as

Data insufficient; can't be predicted

Less than

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Chemical Reaction Engineering

Chemical Reaction Engineering Slurry reactors are characterised by the

Chemical Reaction Engineering A trickle bed reactor is the one, which

Chemical Reaction Engineering n' number of plug flow reactors (P.F.R) in series with a total volume 'V' gives the same conversion as one P.F.R. of volume

Chemical Reaction Engineering For a heterogeneous catalytic reaction

Chemical Reaction Engineering A batch reactor is suitable for

Chemical Reaction Engineering In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume.

Chemical Reaction Engineering
Slurry reactors are characterised by the

Chemical Reaction Engineering
A trickle bed reactor is the one, which

Chemical Reaction Engineering
n' number of plug flow reactors (P.F.R) in series with a total volume 'V' gives the same conversion as one P.F.R. of volume

Chemical Reaction Engineering
For a heterogeneous catalytic reaction

Chemical Reaction Engineering
A batch reactor is suitable for

Chemical Reaction Engineering
In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume.