Chemical Engineering - Chemical Reaction Engineering
Exercise : Chemical Reaction Engineering - Section 4
- Chemical Reaction Engineering - Section 1
- Chemical Reaction Engineering - Section 2
- Chemical Reaction Engineering - Section 3
- Chemical Reaction Engineering - Section 4
- Chemical Reaction Engineering - Section 5
- Chemical Reaction Engineering - Section 6
- Chemical Reaction Engineering - Section 7
- Chemical Reaction Engineering - Section 8
- Chemical Reaction Engineering - Section 9
- Chemical Reaction Engineering - Section 10
41.
Second order consecutive irreversible reactions
were carried out in a constant volume isothermal batch reactor with different initial feed compositions. Reactor temperature was same in all the cases. In experiments where the ratio of concentration of B to that of A in the initial feed was less than 0.5, the concentration of B increased first, reached a maximum and then declined with time. However, for all experiments where this concentration ratio was 0.5 or above, concentration of B decreased monotonically with time right from the beginning. What is the ratio of the two rate constants (k1/k2)?

42.
Pick out the wrong statement.
43.
There is no correspondence between stoichiometry and the rate equation in case of a/an __________ reaction.
44.
A spherical porous catalyst particle of radius R is subjected to reactant A which reacts to form B by a zero order surface reaction A
B. Film mass transfer resistance is negligible and pore diffusion of A is rate controlling. The effectiveness factor of the catalyst is reported as 7/8. Which of the following statement is true?

45.
Which of the following is used for calcination of limestone and dolomite in industrial practice ?
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