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
6.
The rate controlling step for the heterogeneous irreversible catalytic reaction A(g) + B(g) C(g) is the surface reaction of absorbed A with absorbed B to give adsorbed C. The rate expression for this reaction can then be written as (where, KA, KB and KC are the equilibrium constants and is the rate constant of the rate controlling step.)
7.
The optimum performance for reactors operating in parallel is obtained when the feed stream is distributed in such a way, that the
8.
A catalyst is said to be a negative catalyst, ifit
9.
For the non catalytic reaction of particles with surrounding fluid, the same needed to achive the same fractional conversion for particles of different unchanging sizes is proportional to the particle diameter, when the __________ is the controlling resistance.
10.
Pure ethanol vapor is fed to a reactor packed with alumina catalyst, at the rate of 100 kmole / hr. The reactor products comprise: ethylene :95 kmole / hr, water vapour: 97.5 k mole / hr and diethyl ether :2.5 kmole/hr. The reactions occuring can be represented by:
C2H5OH C2H4 + H2O
2C2H5OH C2H5 - O - C2H5 + H2O
The percent conversion of ethanol in the reactor is
C2H5OH C2H4 + H2O
2C2H5OH C2H5 - O - C2H5 + H2O
The percent conversion of ethanol in the reactor is
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