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Aspen Physical Property System - Physical Property Models

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However, q(�) can only be written explicitly for � = 5.8. Only an<br />

approximation is possible below that threshold. Dahl and Michelsen use a<br />

second order polynomial fitted to the analytical solution for 10 < � < 13 that<br />

can be extrapolated to low alpha:<br />

Since q(�)is a universal function (for each equation-of-state), the<br />

combination of equations 6 and 7 form the MHV2 mixing rule. Excess Gibbs<br />

energies, from any activity coefficient model with parameters optimized at<br />

low pressures, can be used to determine �, if �i, bi, and b are known. To<br />

compute b, a linear mixing rule is assumed as in the original Huron-Vidal<br />

mixing rules:<br />

This equation is equivalent to the assumption of zero excess molar volume.<br />

The MHV2 mixing rule was the first successful predictive mixing rule for<br />

equations of state. This mixing rule uses previously determined activity<br />

coefficient parameters for predictions at high pressures. UNIFAC was chosen<br />

as a default for its predictive character. The Lyngby modified UNIFAC<br />

formulation was chosen for optimum performance (see UNIFAC (Lyngby<br />

Modified)). However, any activity coefficient model can be used when its<br />

binary interaction parameters are known.<br />

Like the Huron-Vidal mixing rules, the MHV2 mixing rules are not flexible in<br />

the description of the excess molar volume. The MHV2 mixing rules are<br />

theoretically incorrect at the low pressure limit. But the practical<br />

consequences of this drawback are minimal (see Huron-Vidal Mixing Rules,<br />

this chapter).<br />

Reference: S. Dahl and M.L. Michelsen, "High-Pressure Vapor-Liquid<br />

Equilibrium with a UNIFAC-based Equation-of-state," AIChE J., Vol. 36,<br />

(1990), pp. 1829-1836.<br />

Predictive Soave-Redlich-Kwong-Gmehling<br />

Mixing Rules<br />

These mixing rules by Holderbaum and Gmehling (1991) use a relationship<br />

between the excess Helmholtz energy and equation-of-state. They do not use<br />

a relationship between equation-of-state properties and excess Gibbs energy,<br />

as in the Huron-Vidal mixing rules. The pressure-explicit expression for the<br />

equation-of-state is substituted in the thermodynamic equation:<br />

The Helmholtz energy is calculated by integration. A E is obtained by:<br />

82 2 Thermodynamic <strong>Property</strong> <strong>Models</strong><br />

(7)<br />

(8)<br />

(1)<br />

(2)

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