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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
Fugacity and pressure are numerically not equal for the gases

In ideal state
At standard state
At low temperature and high pressure
Both A and B

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Chemical Engineering Thermodynamics
The equation Tds = dE - PdV applies to

Single phase fluid of constant composition
Single phase fluid of varying composition
Both B and C
Open as well as closed systems

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Chemical Engineering Thermodynamics
For an ideal gas, the chemical potential is given by

R dlnP
R dlnf
None of these
RT dlnP

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Chemical Engineering Thermodynamics
A solid is transformed into vapour without going to the liquid phase at

Triple point
Boiling point
Always
Below triple point

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Chemical Engineering Thermodynamics
In case of a reversible process (following pvn = constant), work obtained for trebling the volume (v₁ = 1 m³ and v₂ 3 m³ ) is max imum, when the value of 'n' is

1.66
1
1.44

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Chemical Engineering Thermodynamics
Compressibility factor for almost all the gases are approximately same at the same

Critical pressure and critical temperature
Pressure and temperature
Reduced pressure and reduced temperature
None of these

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