Chemical Engineering Thermodynamics
The total change in the enthalpy of a system is independent of the

State of combination and aggregation in the beginning and at the end of the reaction
None of these
Number of intermediate chemical reactions involved
Pressure and temperature

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

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