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Aspen Physical Property System - Physical Property Models

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Parameter Name/<br />

Element<br />

2 Thermodynamic <strong>Property</strong> <strong>Models</strong> 25<br />

Symbol Default MDS Lower<br />

Limit<br />

Upper<br />

Limit<br />

Units<br />

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

PC p ci — — 10 5<br />

RGYR r i gyr<br />

— — 10 -11<br />

10 8<br />

5x10 -9<br />

MUP p i — — 0.0 5x10 -24<br />

HOCETA �� 0.0 X — — —<br />

PRESSURE<br />

LENGTH<br />

DIPOLEMOMENT<br />

The binary parameters HOCETA for many component pairs are available in the<br />

<strong>Aspen</strong> <strong>Physical</strong> <strong>Property</strong> <strong>System</strong>. These parameters are retrieved<br />

automatically when you specify any of the following property methods: NRTL-<br />

HOC, UNIF-HOC, UNIQ-HOC, VANL-HOC, and WILS-HOC.<br />

References<br />

J.G. Hayden and J.P. O'Connell, "A Generalized Method for Predicting Second<br />

Virial Coefficients," Ind. Eng. Chem., Process Des. Dev., Vol. 14,No. 3,<br />

(1975), pp. 209 – 216.<br />

HF Equation-of-State<br />

HF forms oligomers in the vapor phase. The non-ideality in the vapor phase is<br />

found in important deviations from ideality in all thermodynamic properties.<br />

The HF equation accounts for the vapor phase nonidealities. The model is<br />

based on chemical theory and assumes the formation of hexamers.<br />

Species like HF that associate linearly behave as single species. For example,<br />

they have a vapor pressure curve, like pure components. The component on<br />

which a hypothetical unreacted system is based is often called the apparent<br />

(or parent) component. Apparent components react to the true species.<br />

Electrolyte Calculation in <strong>Physical</strong> <strong>Property</strong> Methods discusses apparent and<br />

true species. Abbott and van Ness (1992) provide details and basic<br />

thermodynamics of reactive systems.<br />

The temperature-dependent hexamerization equilibrium constant, can fit the<br />

experimentally determined association factors. The built-in functionality is:<br />

The constants C0 and C1 are from Long et al. (1943), and C2 and C3 are set to<br />

0. The correlation is valid between 270 and 330 K, and can be extrapolated to<br />

about 370 K (cf. sec. 4). Different sets of constants can be determined by<br />

experimental data regression.<br />

Molar Volume Calculation<br />

The non-ideality of HF is often expressed using the association factor, f,<br />

indicating the ratio of apparent number of species to the real number or<br />

species. Assuming the ideal gas law for all true species in terms of (p, V, T)<br />

behavior implies:<br />

(1)

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