Chemical Engineering Thermodynamics
A reasonably general expression for vapour-liquid phase equilibrium at low to moderate pressure is Φi yi P = Yi xi fi° where, Φ is a vapor fugacity component, Yi is the liquid activity co-efficient and fi° is the fugacity of the pure component i. the Ki value (Yi = Ki xi) is therefore, in general a function of

Temperature and pressure only
Temperature, pressure, liquid composition xi and vapour composition yi
Temperature, pressure and liquid composition xi only
Temperature only

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Chemical Engineering Thermodynamics
Absolute zero temperature signifies the

None of these
Minimum temperature attainable
Temperature of the heat reservoir to which a Carnot engine rejects no heat
Temperature of the heat reservoir to which a Carnot engine rejects all the heat that is taken in

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