Chemical Engineering - Chemical Engineering Thermodynamics
Exercise : Chemical Engineering Thermodynamics - Section 8
- Chemical Engineering Thermodynamics - Section 1
- Chemical Engineering Thermodynamics - Section 2
- Chemical Engineering Thermodynamics - Section 3
- Chemical Engineering Thermodynamics - Section 4
- Chemical Engineering Thermodynamics - Section 5
- Chemical Engineering Thermodynamics - Section 6
- Chemical Engineering Thermodynamics - Section 7
- Chemical Engineering Thermodynamics - Section 8
- Chemical Engineering Thermodynamics - Section 9
- Chemical Engineering Thermodynamics - Section 10
- Chemical Engineering Thermodynamics - Section 11
31.
The Joule-Thomson co-efficient is defined as (∂T/∂P)H. Its value at the inversion point is
32.
Fugacity of a component in an ideal gas mixture is euqal to the partial pressure of that component in the mixture. The fugacity of each component in a stable homogeneous solution at contant pressure and temperature __________ as its mole fraction increases.
33.
Entropy is a/an
34.
In the reaction, represented by, 2SO2 + O2
2SO3; ΔH = - 42 kcal; the forward reaction will be favoured by

35.
At triple point (for one component system), vapour pressure of solid as compared to that of liquid will be
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