- (A) 1/(time)n
- (B) (Concentration)1 – n/(time)
- (C) (Concentration)n – 1/(time)
- (D) None of these
Chemical Engineering Mcqs
- (A) Diffusion within the pellet
- (B) Reaction
- (C) External mass transfer
- (D) None of the above
- (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

