Vapor-Phase Solubility of Decane in Nitrogen as Functions of Temperature and Pressure
This Demonstration computes the solubility of a high-temperature boiling fluid (-decane) in supercritical nitrogen at various high pressures for user-set values of the temperature. Two approximate methods for solubility prediction are compared: (1) the ideal gas assumption (blue curve); and (2) real gas behavior, described by the virial equation of state (red curve). Here, the fugacity coefficients are computed using the virial equation.
The first snapshot corresponds to a temperature of 50 °C and shows excellent agreement with Figure 5-41 in . The value of the virial coefficient at 50 °C given in , determined by fitting the model to experimental solubility data, compares favorably with obtained in the present calculation at the same temperature.