Chemical Reaction Engineering
In an ideal tubular-flow reactor

There is a uniform velocity across the radius
There is no mixing in longitudinal direction
All of these
Mixing takes place in radial direction

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Chemical Reaction Engineering
In a zero order reaction, reactants concentration does not change with time and the

Reaction rate is trebled when the initial concentration is trebled
Time for completion of the reaction is independent of the initial concentration
Time for half change is independent of the initial concentration
Time for half change is half the time taken for completion of the reaction

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Chemical Reaction Engineering
The rate expression for a heterogenous catalytic reaction is given by, - rA = K.KA PA(1 + KA.PA + Kr.PR), where K is surface reaction rate constant and KA and KR are absorption equilibrium constants of A and R respectively. If KR PR >> (1 + KA PA), the apparent activation energy EA is equal to (given E is the activation energy for the reaction and ΔHR and ΔHA are the activation energies of adsorption of R and A)

E + ΔHA - ΔHR
ΔHA + ΔHR
E + ΔHA
E

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

Goes through a maximum along the length of the reactor
Is maximum at the exit of the reactor
Goes through a minimum along the length of the reactor
Is maximum at the inlet of the reactor

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