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Solubilities of testosterone propionate in non-polar solvents at 100°

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Abstract THE solubilities of the formate to valerate esters of testosterone in non-polar solvents at 25° were determined by James & Roberts (1968) who also compared them with ideal mole fraction solubilities (X2), calculated from the equation, (Hildebrand & Scott 1962). ΔHF is the heat of fusion of the solute and TM the melting point. Changes in solubility as the homologous series is ascended were predicted by equation (1), but the individual experimental results did not agree with the calculated values. ΔHF was calculated from the heat of fusion at the melting point, ΔHFM, by correcting for the differences in heat capacity of the solid and the supercooled liquid between TM and T. The correction was estimated with a differential scanning calorimeter by extrapolating the liquid enthalpy line back to 25° and measuring the area between the extrapolation and the enthalpy line of the solid. The method was considered questionable, however, because it assumed that the enthalpy line of the supercooled liquid decreased linearly over the whole range of temperature. This theory is tested below by comparing the measured and calculated solubilities of testosterone propionate at a temperature just below its melting point, where the heat capacity correction is small and ΔHFM can be used for ΔHF. The solvents examined by James & Roberts (1968) had smaller molar volumes than the testosterone esters, and it was suggested that the difference in molar volume between solute and solvent could prevent the random distribution assumed by regular solution theory. Prediction of solubility would thus improve as the molar volume of the solvent approached that of the solute. The test is applied below by determining the solubility of testosterone propionate in a range of solvents.
Title: Solubilities of testosterone propionate in non-polar solvents at 100°
Description:
Abstract THE solubilities of the formate to valerate esters of testosterone in non-polar solvents at 25° were determined by James & Roberts (1968) who also compared them with ideal mole fraction solubilities (X2), calculated from the equation, (Hildebrand & Scott 1962).
ΔHF is the heat of fusion of the solute and TM the melting point.
Changes in solubility as the homologous series is ascended were predicted by equation (1), but the individual experimental results did not agree with the calculated values.
ΔHF was calculated from the heat of fusion at the melting point, ΔHFM, by correcting for the differences in heat capacity of the solid and the supercooled liquid between TM and T.
The correction was estimated with a differential scanning calorimeter by extrapolating the liquid enthalpy line back to 25° and measuring the area between the extrapolation and the enthalpy line of the solid.
The method was considered questionable, however, because it assumed that the enthalpy line of the supercooled liquid decreased linearly over the whole range of temperature.
This theory is tested below by comparing the measured and calculated solubilities of testosterone propionate at a temperature just below its melting point, where the heat capacity correction is small and ΔHFM can be used for ΔHF.
The solvents examined by James & Roberts (1968) had smaller molar volumes than the testosterone esters, and it was suggested that the difference in molar volume between solute and solvent could prevent the random distribution assumed by regular solution theory.
Prediction of solubility would thus improve as the molar volume of the solvent approached that of the solute.
The test is applied below by determining the solubility of testosterone propionate in a range of solvents.

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