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Furthermore, the ternary systems could be represented using the binary parameters of the thermodynamic model with a function of temperature.
Pure substance parameters of the Peng Robinson EOS are taken from the literature, whereas the binary parameters of the Van der Waals one-fluid mixing rule are adjusted to experimental binary VLE data.
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In liquid liquid extraction column, UNIFAC-LL (Table 1) was used because in Aspen Plus® the binary parameters of NRTL or UNIQUAC for the extractants studied in this paper are not based on experimental data, and UNIFAC-LL has a high accuracy in the prediction of butanol extraction by decanol and oleyl alcohol [Table 1; (Kurkijärvi et al. 2014)].
If the binary parameters for a ternary solution are not accessible, a model based upon the binary parameters of binary solutions may provide a very acceptable means of predicting the flash points for the ternary solution as revealed by a comparison between predicted and experimental data.
Binary parameters of activity coefficients are regressed from experimental vapor pressure data while default constants are used for the solubility expressions.
Binary parameters of butanol water from Aspen Plus V7.3® are not adequate for simulation of vacuum units (Mariano et al. 2011).
This strategy is based on the analysis of the distillation column phase equilibrium sensitivity and leads to an unique matrix of equation of state dominant binary parameters for the whole fractionation train.
The equation also gives excellent results when modeling the solubility of supercritical CO2 in fatty acid esters, with two binary parameters, independent of the temperature and composition, in this case.
Adjustable parameters and binary interaction parameters of the UNIQUAC model were estimated from experimental data for Caribbean pine and Hoop pine as well as data available in the literature.
To obtain the model binary interaction parameters of the hyperbranched polymer + water the subsystem hyperbranched polymer + water was experimentally estimated, and for the subsystem PEG8000 water experimental data from literature were used, the parameters were fitted in both cases.
The binary interaction parameters of the model were estimated by correlating vapor-liquid equilibrium (VLE) data and, for some systems, successful predictions of the critical loci were obtained even when VLE data far from the critical point were used.
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