For the liquid phase zero order irreversible reaction A → B, the conversion of A in a CSTR is found to be 0.3 at a space velocity of 0.1min⁻¹ . What will be the conversion for a PFR with a space velocity of 0.2 min⁻¹? Assume that all the other operating conditions are the same for CSTR and PFR.

Chemical Reaction Engineering
For the liquid phase zero order irreversible reaction A → B, the conversion of A in a CSTR is found to be 0.3 at a space velocity of 0.1min⁻¹ . What will be the conversion for a PFR with a space velocity of 0.2 min⁻¹? Assume that all the other operating conditions are the same for CSTR and PFR.

0.6

0.9

0.3

0.15

0.6

0.9

0.3

0.15

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

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

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

Both forward and backward reactions will be exothermic

Neither of the reactions will be en-dothermic

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

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

Both forward and backward reactions will be exothermic

Neither of the reactions will be en-dothermic

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Chemical Reaction Engineering
The gas phase reaction 2A ⇋ B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is

43833

43959

43898

43864

43833

43959

43898

43864

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Chemical Reaction Engineering
Equilibrium of a chemical reaction as viewed by kinetics is a __________ state.

Static steady

Dynamic steady

Dynamic unsteady

None of these

Static steady

Dynamic steady

Dynamic unsteady

None of these

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Chemical Reaction Engineering
For nearly isothermal operation involving large reaction time in a liquid-phase reaction, the most suitable reactor is a __________ reactor.

Tubular flow

Fixed bed

Stirred tank

Batch

Tubular flow

Fixed bed

Stirred tank

Batch

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Chemical Reaction Engineering
A batch reactor is characterised by

Very low conversion

Variation in extent of reaction and properties of the reaction mixture with time

Variation in reactor volume

Constant residence time

Very low conversion

Variation in extent of reaction and properties of the reaction mixture with time

Variation in reactor volume

Constant residence time

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Chemical Reaction Engineering

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

Chemical Reaction Engineering The gas phase reaction 2A ⇋ B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is

Chemical Reaction Engineering Equilibrium of a chemical reaction as viewed by kinetics is a __________ state.

Chemical Reaction Engineering For nearly isothermal operation involving large reaction time in a liquid-phase reaction, the most suitable reactor is a __________ reactor.

Chemical Reaction Engineering A batch reactor is characterised by

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

Chemical Reaction Engineering
The gas phase reaction 2A ⇋ B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is

Chemical Reaction Engineering
Equilibrium of a chemical reaction as viewed by kinetics is a __________ state.

Chemical Reaction Engineering
For nearly isothermal operation involving large reaction time in a liquid-phase reaction, the most suitable reactor is a __________ reactor.

Chemical Reaction Engineering
A batch reactor is characterised by