A. Decreases
B. Increases
C. Is at the highest allowable temperature throughout
D. First increases and then decreases
A. Suitable for gas-phase reactions on commercial scale
B. Suitable for liquid phase reactions involving small production rate
C. Least expensive to operate for a given rate
D. Most suitable for very large production rate
A. First
B. Second
C. Third
D. Zero
A. Tank in series
B. Dispersion
C. Both A. & B.
D. Neither A. nor B.
A. It is a reversible reaction
B. It is an exothermic reaction
C. The energy of reacting molecules exceeds the activation energy by absorption of light
D. None of these
A. Achieving cent percent conversion of reactants into products
B. Large scale gaseous phase reactions
C. Liquid phase reactions
D. Obtaining uniform polymerisation products in highly exothermic reactions
A. Is same as plug-flow reactor
B. Is same as ideal stirred tank reactor
C. Employs mixing in axial direction only
D. Is most suitable for gas phase reaction
A. Physical
B. Chemical
C. Both A. and B.
D. Neither A. nor B.
A. Both forward and backward reactions will be exothermic
B. Neither of the reactions will be endothermic
C. The combination reaction will be exothermic, while the dissociation reaction will be
endothermic
D. The combination reaction will be endothermic, while the dissociation reaction will be
exothermic
A. 100
B. 1000
C. 10000
D. 100000