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

10°C

5°C

20°C

100°C

10°C

5°C

20°C

100°C

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Chemical Reaction Engineering
In the gaseous phase ammonia formation reaction (N₂ + 3H₂ ⇋ 2NH₃), the value of the equilibrium constant depends on the

Initial concentration of N₂ and H₂

Volume of the reactor

Total pressure of the system

Temperature

Initial concentration of N₂ and H₂

Volume of the reactor

Total pressure of the system

Temperature

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Chemical Reaction Engineering
Differential method for analysing the kinetic data is used

When rate expressions are very simple

When the data are scattered

None of these

For testing complicated mechanisms

When rate expressions are very simple

When the data are scattered

None of these

For testing complicated mechanisms

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Chemical Reaction Engineering
In the reversible reaction of the type, A + B ⇋ AB, in general

The combination reaction will be exothermic, while the dissociation reaction will be endothermic

The combination reaction will be endothermic, while the dissociation reaction will be exothermic

Both forward and backward reactions will be exothermic

Neither of the reactions will be en-dothermic

The combination reaction will be exothermic, while the dissociation reaction will be endothermic

The combination reaction will be endothermic, while the dissociation reaction will be exothermic

Both forward and backward reactions will be exothermic

Neither of the reactions will be en-dothermic

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Chemical Reaction Engineering
If pore diffusion is the controlling step in a solid catalysed reaction, the catalyst

Porosity is of less importance

Porosity is very important

None of these

Internal surface area is utilised efficiently

Porosity is of less importance

Porosity is very important

None of these

Internal surface area is utilised efficiently

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Chemical Reaction Engineering
An imbalanced chemical reaction equation is against the law of

Multiple proportion

Conservation of mass

Constant proportion

None of these

Multiple proportion

Conservation of mass

Constant proportion

None of these

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Chemical Reaction Engineering

Chemical Reaction Engineering In the gaseous phase ammonia formation reaction (N₂ + 3H₂ ⇋ 2NH₃), the value of the equilibrium constant depends on the

Chemical Reaction Engineering Differential method for analysing the kinetic data is used

Chemical Reaction Engineering In the reversible reaction of the type, A + B ⇋ AB, in general

Chemical Reaction Engineering If pore diffusion is the controlling step in a solid catalysed reaction, the catalyst

Chemical Reaction Engineering An imbalanced chemical reaction equation is against the law of

Chemical Reaction Engineering
In the gaseous phase ammonia formation reaction (N₂ + 3H₂ ⇋ 2NH₃), the value of the equilibrium constant depends on the

Chemical Reaction Engineering
Differential method for analysing the kinetic data is used

Chemical Reaction Engineering
In the reversible reaction of the type, A + B ⇋ AB, in general

Chemical Reaction Engineering
If pore diffusion is the controlling step in a solid catalysed reaction, the catalyst

Chemical Reaction Engineering
An imbalanced chemical reaction equation is against the law of