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Aspen Physical Property System - Physical Property Models

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The pure component dielectric constant coefficients of nonaqueous solvents<br />

and Born radius of ionic species are required only for mixed-solvent<br />

electrolyte systems.<br />

The temperature dependency relations of these parameters are given in<br />

Electrolyte NRTL Activity Coefficient Model.<br />

Heat of mixing is calculated from temperature derivatives of activity<br />

coefficients. Heat capacity is calculated from secondary temperature<br />

derivative of the activity coefficient. As a result, the temperature dependent<br />

parameters are critical for modeling enthalpy correctly. It is recommended<br />

that enthalpy data and heat capacity data be used to obtain these<br />

temperature dependency parameters. See also Electrolyte NRTL Enthalpy and<br />

Electrolyte NRTL Gibbs Energy.<br />

Obtaining Parameters<br />

In the absence of electrolytes, the electrolyte NRTL model reduces to the<br />

NRTL equation which is widely used for non-electrolyte systems. Therefore,<br />

molecule-molecule binary parameters can be obtained from binary<br />

nonelectrolyte systems.<br />

Electrolyte-molecule pair parameters can be obtained from data regression of<br />

apparent single electrolyte systems.<br />

Electrolyte-electrolyte pair parameters are required only for mixed<br />

electrolytes with a common ion. Electrolyte-electrolyte pair parameters can<br />

affect trace ionic activity precipitation. Electrolyte-electrolyte pair parameters<br />

can be obtained by regressing solubility data of multiple component<br />

electrolyte systems.<br />

When the electrolyte-molecule and electrolyte-electrolyte pair parameters are<br />

zero, the electrolyte NRTL model reduces to the Debye-Hückel limiting law.<br />

Calculation results with electrolyte-molecule and electrolyte-electrolyte pair<br />

parameters fixed to zero should be adequate for very dilute weak electrolyte<br />

systems; however, for concentrated systems, pair parameters are required<br />

for accurate representation.<br />

See <strong>Physical</strong> <strong>Property</strong> Data, Chapter 1, for the pair parameters available from<br />

the electrolyte NRTL model databank. The table contains pair parameters for<br />

some electrolytes in aqueous solution at 100�C. These values were obtained<br />

by using the <strong>Aspen</strong> <strong>Physical</strong> <strong>Property</strong> Data Regression <strong>System</strong> (DRS) to<br />

regress vapor pressure and mole fraction data at T=100�C with SYSOP15S<br />

(Handbook of Chemistry and Physics, 56th Edition, CRC Press, 1975, p. E-1).<br />

In running the DRS, standard deviations for the temperature (�C), vapor<br />

pressure (mmHg), and mole fractions were set at 0.2, 1.0, and 0.001,<br />

respectively. In addition, complete dissociation of the electrolyte was<br />

assumed for all cases.<br />

Option Codes for Electrolyte NRTL Activity<br />

Coefficient Model (GMENRTL)<br />

The electrolyte NRTL activity coefficient model (GMENRTL) has three option<br />

codes and the option codes can affect the performance of this model.<br />

2 Thermodynamic <strong>Property</strong> <strong>Models</strong> 107

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