A. Pulse
B. Step
C. Both A. & B.
D. Neither A. nor B.
A. Stirred tank
B. Tubular flow
C. Batch
D. Fixed bed
A. Active at cryogenic temperatures only
B. Prohibitively costly
C. Proteinous in nature
D. Active at very high temperature only
A. Fluidised bed reactor
B. Moving bed reactor
C. Fixed bed reactor
D. None of these
A. Free energy of activation is lowered in the presence of catalyst, which remains unchanged at
the end of reaction
B. A relatively small amount of catalyst can cause the conversion of large amount of reactants
which does not mean that catalyst concentration is important
C. The catalyst does not form an intermediate complex with the reactant
A. Increases
B. Decreases
C. Either A. or B.; depends on the type of catalyst
D. Neither A. nor B.
A. (i) increases (ii) decreases
B. (i) decreases (ii) increases
C. (i) increases (ii) increases
D. (i) decreases (ii) decreases
A. Is same as plug-flow reactor
B. Is same as ideal stirred tank reactor
C. Employs mixing in axial direction only
D. Is most suitable for gas phase reaction
A. (1 + x)
B. (1 – x)
C. (1 + x)2
D. (1 – x)2