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Aspen Physical Property System - Physical Property Models

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where R is the gas constant.<br />

Linear extrapolation of Cp *,ig versus T is performed outside temperature<br />

bounds.<br />

Parameter<br />

Name/Element<br />

222 2 Thermodynamic <strong>Property</strong> <strong>Models</strong><br />

Symbol Default MDS Lower<br />

Limit<br />

Upper<br />

Limit<br />

Units<br />

CPIGDS/1 C 1i — — — — TEMPERATURE<br />

CPIGDS/2, …, 8 C 2i, ..., C 8i 0 — — — —<br />

CPIGDS/9 C 9i 0 — — — TEMPERATURE<br />

CPIGDS/10 C 10i 1000 — — — TEMPERATURE<br />

IK-CAPE Heat Capacity Polynomial<br />

The equation is:<br />

Linear extrapolation of Cp *,ig versus T is performed outside temperature<br />

bounds.<br />

Parameter<br />

Name/Element<br />

Symbol Default MDS Lower<br />

Limit<br />

Upper<br />

Limit<br />

Units<br />

CPIGPO/1 C 1i — X — — MOLE-CAPACITY<br />

CPIGPO/2,…,10 C 2i, ..., C 10i 0 X — — MOLE-CAPACITY<br />

TEMPERATURE<br />

CPIGPO/11 C 11i 0 X — — TEMPERATURE<br />

CPIGPO/12 C 12i 1000 X — — TEMPERATURE<br />

References<br />

Data for the Ideal Gas Heat Capacity Polynomial: Reid, Prausnitz and Poling,<br />

The Properties of Gases and Liquids, 4th ed., (New York: McGraw-Hill, 1987).<br />

The <strong>Aspen</strong> <strong>Physical</strong> <strong>Property</strong> <strong>System</strong> combustion data bank, JANAF<br />

Thermochemical Data, Compiled and calculated by the Thermal Research<br />

Laboratory of Dow Chemical Company.<br />

F. A. Aly and L. L. Lee, "Self-Consistent Equations for Calculating the Ideal<br />

Gas Heat Capacity, Enthalpy, and Entropy, Fluid Phase Eq., Vol. 6, (1981), p.<br />

169.

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