A batch adiabatic reactor at an initial temperature of 373°K is being used for the reaction, A → B. Assume the heat of reaction is - 1kJ/mole at 373°K and heat capacity of both A and B to be constant and equal to 50J/mole.K. The temperature rise after a conversion of 0.5 will be

Chemical Reaction Engineering
A batch adiabatic reactor at an initial temperature of 373°K is being used for the reaction, A → B. Assume the heat of reaction is - 1kJ/mole at 373°K and heat capacity of both A and B to be constant and equal to 50J/mole.K. The temperature rise after a conversion of 0.5 will be

5°C

100°C

10°C

20°C

5°C

100°C

10°C

20°C

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Chemical Reaction Engineering
The rate of the chemical reaction A → B doubles as the concentration of A i.e.., CA is doubled. If rate of reaction is proportional to CAn, then what is the value of n for this reaction?

1

0.5

2

1

0.5

2

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Chemical Reaction Engineering
Oil is hydrogenated using nickel catalyst in a __________ reactor.

Slurry

Fluidised bed

Fixed bed

Batch

Slurry

Fluidised bed

Fixed bed

Batch

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Chemical Reaction Engineering
In an ideal tubular-flow reactor

There is a uniform velocity across the radius

There is no mixing in longitudinal direction

Mixing takes place in radial direction

All of these

There is a uniform velocity across the radius

There is no mixing in longitudinal direction

Mixing takes place in radial direction

All of these

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Chemical Reaction Engineering
Catalyst is a substance, which __________ chemical reaction.

Alters the value of equilibrium constant in a reversible

Decreases the speed of a

Can either increase or decrease the speed of a

Increases the speed of a

Alters the value of equilibrium constant in a reversible

Decreases the speed of a

Can either increase or decrease the speed of a

Increases the speed of a

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Chemical Reaction Engineering
The experimentally determined overall order of the reaction, A + B → C + D, is two. Then the

Reaction may be elementary with molecularity of 2

Molecularity of the reaction is 2, but the reaction may not be elementary

Reaction is elementary but the molecularity may not be 2

Reaction is elementary with a molecularity of 2

Reaction may be elementary with molecularity of 2

Molecularity of the reaction is 2, but the reaction may not be elementary

Reaction is elementary but the molecularity may not be 2

Reaction is elementary with a molecularity of 2

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Chemical Reaction Engineering

Chemical Reaction Engineering The rate of the chemical reaction A → B doubles as the concentration of A i.e.., CA is doubled. If rate of reaction is proportional to CAn, then what is the value of n for this reaction?

Chemical Reaction Engineering Oil is hydrogenated using nickel catalyst in a __________ reactor.

Chemical Reaction Engineering In an ideal tubular-flow reactor

Chemical Reaction Engineering Catalyst is a substance, which __________ chemical reaction.

Chemical Reaction Engineering The experimentally determined overall order of the reaction, A + B → C + D, is two. Then the

Chemical Reaction Engineering
The rate of the chemical reaction A → B doubles as the concentration of A i.e.., CA is doubled. If rate of reaction is proportional to CAn, then what is the value of n for this reaction?

Chemical Reaction Engineering
Oil is hydrogenated using nickel catalyst in a __________ reactor.

Chemical Reaction Engineering
In an ideal tubular-flow reactor

Chemical Reaction Engineering
Catalyst is a substance, which __________ chemical reaction.

Chemical Reaction Engineering
The experimentally determined overall order of the reaction, A + B → C + D, is two. Then the