2000
DOI: 10.1016/s0009-2509(99)00534-5
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Extended UNIQUAC model for correlation and prediction of vapour–liquid–solid equilibria in aqueous salt systems containing non-electrolytes. Part A. Methanol–water–salt systems

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Cited by 96 publications
(99 citation statements)
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“…Instead of using mixing rules to estimate the density and dielectric constant of the solvent mixture, we use water properties for all solvent components. Similar assumptions were made for the LR part of other mixed solvent models (Iliuta et al, 2000). With this constraint, the corresponding LR activity coefficient expressions for the solvents γ LR,(x) s and the ions γ LR,(x),∞ i are:…”
Section: Long-range Contributionmentioning
confidence: 97%
“…Instead of using mixing rules to estimate the density and dielectric constant of the solvent mixture, we use water properties for all solvent components. Similar assumptions were made for the LR part of other mixed solvent models (Iliuta et al, 2000). With this constraint, the corresponding LR activity coefficient expressions for the solvents γ LR,(x) s and the ions γ LR,(x),∞ i are:…”
Section: Long-range Contributionmentioning
confidence: 97%
“…In a real mixture, solvents have densities and dielectric properties different from those of pure water. For this reason, these simplifications of the LR part were made in other mixed solvent models in chemical engineering and technical chemistry applications (see Iliuta et al, 2000). The uncertainties that occurred due to the adopted assumptions to derive the LR and SR activity coefficients with respect to approximations of parameters, were described in the semi-empirical SR part as in the original AIOMFAC (Zuend et al, 2008).…”
Section: The Long-range Contributionmentioning
confidence: 99%
“…More information can be found in the literature [15][16][17]. Extended UNIQUAC volume and surface area parameters and interaction parameters are reported in Table 2, 3 and 4 [18].…”
Section: Calculations Of Phase Diagram By Extended Uni-quac Modelmentioning
confidence: 99%