- (A) 4
- (B) 8
- (C) 12
- (D) 16
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- (A) Uniformity of temperature
- (B) Comparatively smaller equipment
- (C) Very small pressure drop
- (D) Absence of continuous catalyst regeneration facility
- (A) Decreases with increase in temperature
- (B) Increases with increase of pressure of reactants for all reactions
- (C) Decreases with increase of reactant concentration
- (D) None of these
- (A) Converts N2 and H2 into NH3
- (B) Converts CO to CO2 with steam
- (C) Is non-catalytic
- (D) Is highly exothermic
- (A) 1/(1 + k2 . CA0 . t)
- (B) (k2 . CA0 . t)/ (1 + k2 . CA0 . t)
- (C) (k2 . CA0 . t)2/ (1 + k2 . CA0 . t)
- (D) (k2 . CA0 . t)/ (1 + k2 . CA0 . t)2
- (A) Velocity of reaction can be controlled
- (B) Maximum conversion can be controlled
- (C) Both the reactants flow counter-currently
- (D) Residence time is constant
- (A) 2-5 %
- (B) 7-10 %
- (C) 12-15 %
- (D) 20-25 %
- (A) 8987°K
- (B) 9210°K
- (C) 8764°K
- (D) 8621°K
- (A) K α √T.e-E/RT
- (B) K α eE/RT
- (C) K α e-E/RT
- (D) None of these
- (A) Is independent of pressure
- (B) Increases with pressure
- (C) Decreases with pressure
- (D) Increases /decreases with pressure depending on the stoichiometric co-efficients of the reaction
