Liquid Activity Methods

 

These methods use liquid activity coefficients to model the liquid phase behavior. The Poynting correction for pressure may be applied to the liquid phase and the standard state liquid fugacities and vapor phase fugacity coefficients may be computed with an equation of state. For super-critical gases and for trace solutes, Henry's constants may be used to define the standard state fugacity. The activity methods work best for mixtures of components which do not differ greatly in volatility and have strongly non-ideal liquid interactions. See Liquid Activity Coefficients for further information on this approach to phase equilibria.

 

The following systems are provided in this category. The name for each system is defined from the Equilibrium K-value method.

 

Non-random Two-liquid Equation (NRTL)

K-values: NRTL method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Universal Quasi-chemical (UNIQUAC)

K-values: UNIQUAC method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

van Laar (VANLAAR)

K-values: VANLAAR method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Wilson (WILSON)

K-values: WILSON method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Margules (MARGULES)

K-values: MARGULES method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Regular Solution Theory (REGULAR)

K-values: REGULAR method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Flory-Huggins Theory (FLORY)

K-values: FLORY method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Universal Functional Activity Coefficient (UNIFAC)

K-values: UNIFAC method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Lyngby-modified UNIFAC (UNIFAC TDep-1)

K-values: UNIFAC TDep-1 method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Dortmund-modified UNIFAC (UNIFAC TDep-2)

K-values: UNIFAC TDep-2 method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Modified UNIFAC method (UNIFAC TDep-3)

K-values: UNIFAC TDep-3 method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Free volume modification to UNIFAC (Free Volume)

K-values: Free Volume method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Ideal (IDEAL)

K-values: Ideal method

Enthalpies, entropies, densities, vapor fugacities: Ideal method

 

Additional Information

Many options are provided when calculating K-values with liquid activity methods. These options may be reached via the Thermodynamics System - Modification Window and include the following: fill options for missing liquid phase activity coefficients, Poynting correction options, Henry's law options, selection of LLE key components and databank search order for liquid activity coefficient data. The method used for the standard state liquid fugacity coefficients and vapor phase fugacity coefficients may also be selected and modified in this window.

 

Descriptions of the individual thermodynamic methods may be accessed from the Thermodynamic System - Modification Window by selecting the current property method and pushing the Help button. Further description may be obtained by selecting the property method under Related Topics in the help screen which is displayed.

 

Detailed information on the liquid activity coefficient methods, including complete descriptions of the equation forms may be obtained in PRO/II Reference Manual under the topic Liquid Activity Methods.

 

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Related Topics

 

Thermodynamics - General Information

Binary Data Fill for Liquid Activity Methods