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Aspen Physical Property System - Physical Property Models

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<strong>Property</strong> Model Model Name Phase(s)Pure Mixture<br />

Redlich-Kister GMREDKIS L S — X<br />

Scatchard-Hildebrand GMXSH L — X<br />

Symmetric Electrolyte NRTL GMENRTLS L — X<br />

Three-Suffix Margules GMMARGUL L S — X<br />

UNIFAC GMUFAC L L1 L2 — X<br />

UNIFAC (Lyngby modified) GMUFLBY L L1 L2 — X<br />

UNIFAC (Dortmund modified) GMUFDMD L L1 L2 — X<br />

UNIQUAC GMUQUAC L L1 L2 — X<br />

Unsymmetric Electrolyte NRTL GMENRTLQ L — X<br />

van Laar GMVLAAR L — X<br />

Wagner interaction parameter GMWIP S — X<br />

Wilson GMWILSON L — X<br />

Wilson model with liquid molar<br />

volume<br />

2 Thermodynamic <strong>Property</strong> <strong>Models</strong> 13<br />

GMWSNVOL L — X<br />

Vapor Pressure and Liquid Fugacity <strong>Models</strong><br />

<strong>Property</strong> Model Model<br />

Name<br />

General Pure Component Liquid<br />

Vapor Pressure<br />

<strong>Property</strong> Phase(s)Pure Mixture<br />

PL0XANT PL L L1 L2 X —<br />

API Sour SWEQ PHILMX L — X<br />

Braun K-10 BK10 PHILMX L — X<br />

Chao-Seader PHL0CS PHIL L X —<br />

Grayson-Streed PHL0GS PHIL L X —<br />

Kent-Eisenberg ESAMINE PHILMX,<br />

GLMX,<br />

HLMX,<br />

SLMX<br />

L — X<br />

Maxwell-Bonnell PL0MXBN PL L L1 L2 X —<br />

Solid Antoine PS0ANT PS S X —<br />

Heat of Vaporization <strong>Models</strong><br />

These models calculate DHVL.<br />

<strong>Property</strong> Model Model Name Phase(s)Pure Mixture<br />

General Pure Component Heat<br />

of Vaporization<br />

DHVLWTSN L X —<br />

Clausius-Clapeyron Equation DHVLCC L X —<br />

Molar Volume and Density <strong>Models</strong><br />

These models calculate VL (pure liquid), VLMX (liquid mixture), or VS (pure<br />

solid), except for Brelvi-O'Connell which calculates VLPM.<br />

<strong>Property</strong> Model Model Name Phase(s)Pure Mixture<br />

API Liquid Volume VL2API L — X<br />

Brelvi-O'Connell VL1BROC L — X

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