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Aspen Physical Property System - Physical Property Models

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Where:<br />

wi = Liquid phase weight fraction of component i<br />

�i *,l = Pure component liquid thermal conductivity of component i<br />

Where n is determined from two option codes on model KL2VR:<br />

If option code 1 is Then n is determined by<br />

0 (default) Option code 2, always<br />

1<br />

If option code 2 is Then n is<br />

0 (default) -2<br />

1 0.4<br />

280 3 Transport <strong>Property</strong> <strong>Models</strong><br />

Option code 2, unless . In this case n is<br />

set to 1.<br />

2 1 (This uses a weighted average of liquid thermal<br />

conductivities.)<br />

For most systems, the ratio of maximum to minimum pure component liquid<br />

thermal conductivity is between 1 and 2, where the exponent -2 is<br />

recommended, and is the default value used.<br />

Pure component liquid thermal conductivity �i *,l is calculated by the General<br />

Pure Component Liquid Thermal Conductivity model.<br />

Reference: R.C. Reid, J.M. Prausnitz, and T.K. Sherwood, The Properties of<br />

Gases and Liquids, 4th ed., (New York: McGraw-Hill, 1977), p. 533.<br />

TRAPP Thermal Conductivity Model<br />

The general form for the TRAPP thermal conductivity model is:<br />

Where:<br />

Cpi *,ig<br />

= Mole fraction vector<br />

= Ideal gas heat capacity calculated using the<br />

General pure component ideal gas heat capacity<br />

model<br />

fcn = Corresponding states correlation based on the<br />

model for vapor and liquid thermal conductivity<br />

made by the National Bureau of standards (NBS,<br />

currently NIST)<br />

The model can be used for both pure components and mixtures. The model<br />

should be used for nonpolar components only.

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