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Aspen Physical Property System - Physical Property Models

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Parameter Symbol Default MDS Lower<br />

Name/Element<br />

Limit<br />

94 2 Thermodynamic <strong>Property</strong> <strong>Models</strong><br />

Upper<br />

Limit<br />

Units<br />

CSACVL V i — x — — VOLUME (Å 3 )<br />

SGPRF1 A i p i(1-12) — x — — —<br />

SGPRF2 A i p i(13-24) — x — — —<br />

SGPRF3 A i p i(25-36) — x — — —<br />

SGPRF4 A i p i(37-48) — x — — —<br />

SGPRF5 A i p i(49-51) — x — — —<br />

Option Codes<br />

The primary version of COSMO-SAC is the model by Lin and Sandler (2002).<br />

Two other versions are available using an option code, as detailed in the table<br />

below:<br />

Option Description<br />

Code<br />

1 COSMO-SAC model by Lin and Sandler (2002)<br />

2 COSMO-RS model by Klamt (1995)<br />

3 Lin and Sandler model with modified exchange energy (Lin<br />

et al., 2002)<br />

References<br />

A. Klamt, "Conductor-like Screening Model for Real Solvents: A New Approach<br />

to the Quantitative Calculation of Solvation Phenomena," J. Phys. Chem. 99,<br />

2224 (1995).<br />

S.-T. Lin, P. M. Mathias, Y. Song, C.-C. Chen, and S. I. Sandler,<br />

"Improvements of Phase-Equilibrium Predictions for Hydrogen-Bonding<br />

<strong>System</strong>s from a New Expression for COSMO Solvation <strong>Models</strong>," presented at<br />

the AIChE Annual Meeting, Indianapolis, IN, 3-8 November (2002).<br />

S.-T. Lin and S. I. Sandler, "A Priori Phase Equilibrium Prediction from a<br />

Segment Contribution Solvation Model," Ind. Eng. Chem. Res. 41, 899<br />

(2002).<br />

E. Mullins, et al. "Sigma-Profile Database for Using COSMO-Based<br />

Thermodynamic Methods," Ind. Eng. Chem. Res. 45, 4389 (2006).<br />

Electrolyte NRTL Activity Coefficient Model<br />

(GMENRTL)<br />

The Electrolyte NRTL activity coefficient model (GMENRTL) is a versatile<br />

model for the calculation of activity coefficients. Using binary and pair<br />

parameters, the model can represent aqueous electrolyte systems as well as<br />

mixed solvent electrolyte systems over the entire range of electrolyte<br />

concentrations. This model can calculate activity coefficients for ionic species<br />

and molecular species in aqueous electrolyte systems as well as in mixed<br />

solvent electrolyte systems. The model reduces to the well-known NRTL<br />

model when electrolyte concentrations become zero (Renon and Prausnitz,<br />

1969).

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