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Chemical Reaction Engineering

Chemical Reaction Engineering
The eddy diffusivity for a liquid in plug flow must be

Between 0 and 1
0
1
∞

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Chemical Reaction Engineering
The effect of increasing pressure on the gaseous equilibrium of the reaction 2X+3Y ⇋ 3X+2Y indicates that

Backward reaction is favoured
Pressure has no effect
None of these
Forward reaction is favoured

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Chemical Reaction Engineering
The irreversible reaction, X → Y, is the special case of the reversible reaction, X ⇋ Y, in which the

Fractional conversion of
All of these
Equilibrium constant is infinite
Concentration of

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Chemical Reaction Engineering
Knudsen diffusion is directly proportional to

T₂
√T
1/√T
T

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Chemical Reaction Engineering
A second order reaction of the form A + B → C is called a pseudo-first order reaction, when

CB0 ≥ CB0
CA0 = CB0
CB0 > CA0
CA0 > CB0

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Chemical Reaction Engineering
The use of space time is preferred over the mean residence time in the design of a/an

CSTR
Ideal tubular-flow reactor
Slurry reactor
Batch reactor

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