An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction

Chemical Reaction Engineering
An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction

Is maximum at the inlet of the reactor

Goes through a minimum along the length of the reactor

Is maximum at the exit of the reactor

Goes through a maximum along the length of the reactor

Is maximum at the inlet of the reactor

Goes through a minimum along the length of the reactor

Is maximum at the exit of the reactor

Goes through a maximum along the length of the reactor

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Chemical Reaction Engineering
From collison theory, the reaction rate constant is proportional to

√T

Exp(- E/RT)

Tm.exp(- E/RT)

Exp(- E/2RT)

√T

Exp(- E/RT)

Tm.exp(- E/RT)

Exp(- E/2RT)

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Chemical Reaction Engineering
The reaction A → B is conducted in an isothermal batch reactor. If the conversion of A increases linearly with holding time, then the order of the reaction is

1.5

2

0

1

1.5

2

0

1

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Chemical Reaction Engineering
The decomposition of A into B is represented by the exothermic reaction, A ⇋ 2B. To achieve maximum decomposition, it is desirable to carry out the reaction.

At low P and high T

At high P and high T

At high P and low T

At low P and low T

At low P and high T

At high P and high T

At high P and low T

At low P and low T

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Chemical Reaction Engineering
A liquid decomposes by irreversible first order kinetics and the half life period of this reaction is 8 minutes. The time required for 75% conversion of the liquid will be __________ minutes.

4

8

16

12

4

8

16

12

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Chemical Reaction Engineering
In an ideal P.F.R. at steady state conditions

There is no lateral mixing of fluid

The composition of reactants remains constant along a flow path

The conversion of the reactant varies from point to point along a flow path

There may be diffusion along the flow path

There is no lateral mixing of fluid

The composition of reactants remains constant along a flow path

The conversion of the reactant varies from point to point along a flow path

There may be diffusion along the flow path

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Chemical Reaction Engineering

Chemical Reaction Engineering An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction

Chemical Reaction Engineering From collison theory, the reaction rate constant is proportional to

Chemical Reaction Engineering The reaction A → B is conducted in an isothermal batch reactor. If the conversion of A increases linearly with holding time, then the order of the reaction is

Chemical Reaction Engineering The decomposition of A into B is represented by the exothermic reaction, A ⇋ 2B. To achieve maximum decomposition, it is desirable to carry out the reaction.

Chemical Reaction Engineering A liquid decomposes by irreversible first order kinetics and the half life period of this reaction is 8 minutes. The time required for 75% conversion of the liquid will be __________ minutes.

Chemical Reaction Engineering In an ideal P.F.R. at steady state conditions

Chemical Reaction Engineering
An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction

Chemical Reaction Engineering
From collison theory, the reaction rate constant is proportional to

Chemical Reaction Engineering
The reaction A → B is conducted in an isothermal batch reactor. If the conversion of A increases linearly with holding time, then the order of the reaction is

Chemical Reaction Engineering
The decomposition of A into B is represented by the exothermic reaction, A ⇋ 2B. To achieve maximum decomposition, it is desirable to carry out the reaction.

Chemical Reaction Engineering
A liquid decomposes by irreversible first order kinetics and the half life period of this reaction is 8 minutes. The time required for 75% conversion of the liquid will be __________ minutes.

Chemical Reaction Engineering
In an ideal P.F.R. at steady state conditions