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Chemical Reaction Engineering

Chemical Reaction Engineering
If a solid-gas non-catalytic reaction occurs at very high temperature, the rate controlling step is the __________ diffusion.

Film
None of these
Ash layer
Pore

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Chemical Reaction Engineering
The concentration of A in a first order reaction, A → B, decreases

Linearly with time
Exponentially with time
Logarithmically with time
Very abruptly towards the end of the reaction

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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

100°C
20°C
5°C
10°C

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Chemical Reaction Engineering
A reaction in which one of the products of reaction acts as a catalyst is called a/an __________ reaction.

Catalytic
Autocatalytic
Photochemical
None of these

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Chemical Reaction Engineering
A stirred tank reactor compared to tubular-flow reactor provides

More uniform operating conditions
Permits operation at the optimum temperature for a long reaction time
All of these
Higher overall selectivity for a first order consecutive reaction

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Chemical Reaction Engineering
For every 10°C rise in temperature, the rate of chemical reaction doubles. When the temperature is increased from 30 to 70°C, the rate of reaction increases __________ times.

8
12
32
16

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