A. Diffusion within the pellet
B. Reaction
C. External mass transfer
D. None of the above
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., B. and C.
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