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Chemical Reaction Engineering

Chemical Reaction Engineering
reactant and product streams). The amount of heat to be removed is

5/3 kW
2/3 kW
4kW
1kW

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Chemical Reaction Engineering
Which of the following is not a theory of homogeneous reaction?

Collision theory and activated complex theory
None of these
Radiation hypothesis
Chain reaction theory

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Chemical Reaction Engineering
In case of calcination of limestone, CaCO₃ CaO + CO₂, the addition of more of CaO will result in __________ in the concentration of CO₂.

Increase
Unpredictable from the data
No change
Decrease

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Chemical Reaction Engineering
A pulse tracer is introduced in an ideal CSTR (with a mean residence time ι) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be

τ/0.693
2τ
0.5τ
0.693τ

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Chemical Reaction Engineering
A first order reaction A → B occurs in an isothermal porous catalyst pellet of spherical shape. If the concentration of A at the centre of the pellet is much less than at the external surface, the process is limited by

None of these
Diffusion within the pellet
External mass transfer
Reaction

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Chemical Reaction Engineering
__________ gas is normally employed in B.E.T.method of finding out the surface area of catalyst.

H₂
He
N₂
CO₂

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