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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
The partial molar enthalpy of a component in an ideal binary gas mixture of composition Z, at a temperature T and pressure P, is a function only of

T
T and P
T and Z
T, P and Z

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Chemical Engineering Thermodynamics
The molar excess Gibbs free energy, gE, for a binary liquid mixture at T and P is given by, (gE/RT) = A . x₁. x₂, where A is a constant. The corresponding equation for ln y₁, where y₁ is the activity co-efficient of component 1, is

Ax₁
A . x₂²
Ax₁²
Ax₂

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Chemical Engineering Thermodynamics
At absolute zero temperature, the __________ of the gas is zero.

Volume
Pressure
None of these
Mass

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Chemical Engineering Thermodynamics
When a system is in equilibrium for all possible processes, the differential or finite change of entropy is

None of these
> 0
< 0
= 0

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Chemical Engineering Thermodynamics
Partial molal quantities are important in the study of

Ideal solutions
A pure component
Ideal gases
Non-ideal mixtures

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Chemical Engineering Thermodynamics
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.

Decreases
Decreases exponentially
Remains constant
Increases

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