- (A) Film diffusion
- (B) Diffusion through ash layer
- (C) Chemical reaction
- (D) Either
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- (A) keff = k + kg
- (B) keff = (k+ kg)/2
- (C) keff = (kkg)1/2
- (D) 1/keff = 1/k + 1/kg
- (A) K1 . CX
- (B) (K1 + K2 + K3) CX
- (C) (K1 + K2) CX
- (D) (K2 + K3) CX
- (A) 15, 10, 5
- (B) 5, 10, 15
- (C) 10, 5, 15
- (D) 10, 15, 5
- (A) 103.01
- (B) 10-0.67
- (C) 10-3.01
- (D) 100.67
- (A) Homogeneous
- (B) Non-Homogeneous
- (C) Heterogeneous
- (D) Non-Heterogeneous
- (A) (1/η) exp (-t/η)
- (B) η exp (-t/η)
- (C) exp (-t/η)
- (D) (1/η) (-t/η)
- (A) Moles for med/(surface of catalyst) (time)
- (B) Moles formed/volume of reactor) (time)
- (C) Mole formed/volume of catalyst) (time)
- (D) None of these
- (A) Zero order
- (B) Third order
- (C) Consecutive
- (D) None of these
- (A) Poor product quality control
- (B) High labour and handling cost
- (C) High shutdown time requirement for emptying, cleaning and refilling
- (D) All

