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Aspen Physical Property System - Physical Property Models

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Note: Reduced temperature Tr is always calculated using absolute<br />

temperature units.<br />

Parameter Symbol Default MDS Lower Upper Units<br />

Name/Element<br />

Limit Limit<br />

TC T ci — — 5.0 2000.0 TEMPERATURE<br />

PC p ci — — 10 5<br />

Soave Modification<br />

74 2 Thermodynamic <strong>Property</strong> <strong>Models</strong><br />

10 8<br />

(4)<br />

PRESSURE<br />

The parameter �i is a temperature function introduced by Soave in the<br />

Redlich-Kwong equation-of-state to improve the correlation of the pure<br />

component vapor pressure:<br />

Equation 3 still holds. The parameter mi can be correlated with the acentric<br />

factor:<br />

Equations 1, 2, 3, 5 and 6 are the standard Redlich-Kwong-Soave<br />

formulation. The Soave alpha function is adequate for hydrocarbons and other<br />

nonpolar compounds, but is not sufficiently accurate for polar compounds.<br />

Parameter<br />

Name/Element<br />

Symbol Default MDS Lower<br />

Limit<br />

(5)<br />

(6)<br />

Upper<br />

Limit<br />

Units<br />

TCRKS T ci TC X 5.0 2000.0 TEMPERATURE<br />

PCRKS p ci PC X 10 5<br />

OMGRKS � i OMEGA X -0.5 2.0 —<br />

Boston-Mathias Extrapolation<br />

10 8<br />

PRESSURE<br />

For light gases at high reduced temperatures (> 5), equation 5 gives<br />

unrealistic results. The boundary conditions are that attraction between<br />

molecules should vanish for extremely high temperatures, and reduces<br />

asymptotically to zero. Boston and Mathias derived an alternative function for<br />

temperatures higher than critical:<br />

With<br />

di<br />

ci<br />

=<br />

=<br />

Where:<br />

(7)

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