- (A) d(VCA)/dt = -F (CAF – CA) – kCA2V
- (B) d(VCA)/dt = F (CAF – CA) – kCA2V
- (C) d(VCA)/dt = -FCA – kCA2V
- (D) d(VCA)/dt = FCAF – kCA2V
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- (A) Catalyst size is reduced or the catalyst diffusivity is reduced
- (B) Catalyst size is reduced or the catalyst diffusivity is increased
- (C) Catalyst size is increased or the catalyst diffusivity is reduced
- (D) Catalyst size is increased or the catalyst diffusivity is increased
- (A) Operating conditions (e.g. pressure and temperature)
- (B) Rate constant
- (C) Density of mixture
- (D) None of these
- (A) E
- (B) E + ΔHA
- (C) E + ΔHA – ΔHR)
- (D) ΔHA + ΔHR
- (A) 190
- (B) 290
- (C) 390
- (D) 490
- (A) Decreases the activation energy
- (B) Alters the reaction mechanism
- (C) Increases the frequency of collisions of reacting species
- (D) All
- (A) CA = 1.2 CA0 (1 – X)/(1 – 0.33X)
- (B) CA = 1.2 CA0 (1 – X)/(1 – 0.5X)
- (C) CA = 0.83 CA0 (1 – X)/(1 – 0.33X)
- (D) CA = 0.83 CA0 (1 – X)/(1 – 0.5X)
- (A) The feed rate is measured at temperature and pressure in the reactor
- (B) The temperature, pressure and the density of reaction mixture remains constant throughout the reactor
- (C) There is no change in number of moles in gaseous reaction
- (D) All
- (A) CA
- (B) CA2
- (C) CA3
- (D) CA4
- (A) T
- (B) √T
- (C) 1/√T
- (D) T2

