A. Activation
B. Potential
C. Binding
D. Threshold
A. m
B. 1/m
C. √m
D. m2
A. Zero
B. One
C. Two
D. Three
A. k ∝ T1.5
B. k ∝ exp(-E/RT)
C. k ∝ √T
D. k ∝ T
A. Suitable for gas phase reactions
B. Ideal at very low conversion
C. Same as plug flow reactor (PFR)
D. Same as ideal stirred tank reactor
A. Increase in the number of effective collisions
B. Decrease in activation energy
C. Increase in the average kinetic energy of the reacting molecules
D. None of these
A. Increase of temperature
B. Decrease of temperature
C. Increase in initial concentration of A
D. Decrease in initial concentration of A
A. Pore volume
B. Solid density
C. Porosity
D. All A., B., & C.
A. Batch reactor
B. Tubular flow reactor
C. Stirred tank reactor
D. Fluidised bed reactor
A. (atm)-1
B. (hr)-1
C. (atm)-1.(hr)-1
D. atm.(hr)-1