1971 年 4 巻 2 号 p. 122-128
Thermodynamically exact equations are derived for determining the infinite dilution ternary activity coefficients in liquid phase from isothermal total pressure-concentration data (P-x) and from isobaric bubble temperature-concentration data (T-x), respectively, for a ternary system.
Practical calculations by these equations are illustrated for the dichloroethane-ethanolwater system at 40°C and the ethanol-isopropyl alcohol-water system at 760 mmHg.