- (A) Diffusion within the pellet
- (B) Reaction
- (C) External mass transfer
- (D) None of the above
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- (A) Batch reactor
- (B) Ideal tubular-flow reactor
- (C) Slurry reactor
- (D) CSTR
- (A) Ideal plug flow
- (B) Bypass
- (C) Dead zone
- (D) Channelling
- (A) Proportional to
- (B) Independent of
- (C) Inversely proportional to
- (D) Proportional to the square of
- (A) Increases
- (B) Remains unchanged
- (C) Decreases
- (D) Unpredictable from the data
- (A) CSTR of volume V
- (B) PFR of volume V
- (C) CSTR of volume V/X
- (D) PFR of volume V/X
- (A) Equilibrium constant is infinite
- (B) Fractional conversion of ‘A’ at equilibrium is unity
- (C) Concentration of ‘A’ at equilibrium is zero
- (D) All
- (A) 18
- (B) 24
- (C) 6
- (D) 12
- (A) 0.5
- (B) -0.5
- (C) 1
- (D) 1.5
- (A) Surface Kc/(1 + TS) reaction between absorbed A and B in the gas phase
- (B) Surface reaction between absorbed A and absorbed B
- (C) Surface reaction between A in the gas phase and absorbed B
- (D) Desorption of C

