1984
DOI: 10.1002/jps.2600730104
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Excess Free Energy Approach to the Estimation of Solubility in Mixed Solvent Systems I: Theory

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Cited by 61 publications
(19 citation statements)
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“…When selecting a model, factors such as model applicability (liquid-liquid equilibria, solid-liquid equilibria, or vapor-liquid equilibria), treatment of the electrolyte solution chemistry (completely dissociated, undissociated, or speciated), type of ion-interactions (short-range, long-range, electrostatic), and reference state (symmetrical vs. unsymmetrical conventions) need to be taken into consideration. Other mathematical models, often referred to as cosolvency models, are published in the pharmaceutical literature (Acree et al, 1991;Adjei et al, 1980;Barzegar-Jalali and Jouyban-Gharamaleki, 1997;Jouyban-Gharamaleki, 1998;Khossravi, 1992;Ochsner et al, 1985;Williams and Amidon, 1984;Yalkowsky and Roseman, 1981). An evaluation of these models was presented by Jouyban-Gharamaleki et al (1999) and Pinho and Macedo (1996).…”
Section: Solubility and Solubility Productmentioning
confidence: 99%
“…When selecting a model, factors such as model applicability (liquid-liquid equilibria, solid-liquid equilibria, or vapor-liquid equilibria), treatment of the electrolyte solution chemistry (completely dissociated, undissociated, or speciated), type of ion-interactions (short-range, long-range, electrostatic), and reference state (symmetrical vs. unsymmetrical conventions) need to be taken into consideration. Other mathematical models, often referred to as cosolvency models, are published in the pharmaceutical literature (Acree et al, 1991;Adjei et al, 1980;Barzegar-Jalali and Jouyban-Gharamaleki, 1997;Jouyban-Gharamaleki, 1998;Khossravi, 1992;Ochsner et al, 1985;Williams and Amidon, 1984;Yalkowsky and Roseman, 1981). An evaluation of these models was presented by Jouyban-Gharamaleki et al (1999) and Pinho and Macedo (1996).…”
Section: Solubility and Solubility Productmentioning
confidence: 99%
“…[24] V terms are presented as the molar volume differences between solvent, cosolvent and solute. The solute-solvent interaction terms are estimated from experimental solubility data.…”
Section: Theoretical Basementioning
confidence: 99%
“…In &(,deal) = -Ahf(l -T/T,)/RT -ACp(Tt -T ) / R T + AC,.ln (T,/T)/R (9) where Ahf is the latent heat of fusion, AC, is the difference between the heat capacity of the solid and that of the pure subcooled liquid a t temperature T, T, is the triple point, and T is the temperature of the solution. If the melting point is <1OO"C above the solution temperature, the terms including AC, may be neglected, and if the normal melting point is substituted for the triple point, the commonly used approximation to calculate ideal solubility results:"…”
Section: Theoretical Sectionmentioning
confidence: 99%