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Aspen Physical Property System - Physical Property Models

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Dean-Stiel Pressure Correction<br />

The residual vapor viscosity or the pressure correction to low pressure vapor<br />

viscosity by Dean and Stiel is:<br />

Where � v (p = 0) is obtained from a low pressure viscosity model (for<br />

example, General Pure Component Vapor Viscosity). The dimensionlessmaking<br />

factor � is:<br />

�<br />

Tc<br />

262 3 Transport <strong>Property</strong> <strong>Models</strong><br />

=<br />

=<br />

M =<br />

pc<br />

Vcm<br />

Zcm<br />

=<br />

=<br />

=<br />

�rm = Vcm / Vm v<br />

The parameter Vm v is obtained from Redlich-Kwong equation-of-state.<br />

Parameter<br />

Name/Element<br />

Symbol Default MDS Lower<br />

Limit<br />

Upper<br />

Limit<br />

MW M i — — 1.0 5000.0 —<br />

Units<br />

VC V ci — — 0.001 3.5 MOLE-VOLUME<br />

IAPS Viscosity for Water<br />

The IAPS viscosity models, developed by the International Association for<br />

Properties of Steam, calculate vapor and liquid viscosity for water and steam.<br />

These models are used in option sets STEAMNBS and STEAM-TA.<br />

The general form of the equation for the IAPS viscosity models is:<br />

�w=fcn(T, p)<br />

Where:<br />

fcn = Correlation developed by IAPS<br />

The models are only applicable to water. There are no parameters required<br />

for the models.

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