Chemical Engineering - Chemical Reaction Engineering
Exercise : Chemical Reaction Engineering - Section 8
- 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
36.
With the same reaction time, initial concentration and feed rate, the reaction 2A
B is carried out separately in CSTR and P.F. reactor of equal volumes. The conversion will be

37.
For any reaction, we may write conversion as a function of
38.
The use of space time is preferred over the mean residence time in the design of a/an
39.
Autocatalytic reactions are best carried out in a
40.
The gas phase reaction 2A
B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is

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