Densities and viscosities were measured for anisole + 1-butanol, + 1-pentanol, + 1-hexanol, + 1-heptanol, and + 1-octanol at 303.15 K, 313.15 K, and 323.15 K. The excess volumes and viscosity deviations from the mole fraction average were calculated and correlated by a Redlich−Kister type equation. While the excess volumes of anisole + 1-butanol are negative, those of the remaining binary mixtures are positive. The viscosity deviations are negative for all systems.

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Densities and viscosities were measured for anisole with 2-butanol, 2-methyl-1-propanol, and 2-methyl-2-propanol binary liquid mixtures with a vibrating-tube densimeter and Cannon-Fenske routine viscometers over the temperature range between 303.15 and 323.15 K and at atmospheric pressure. Excess molar volumes and viscosity deviations were calculated at various temperatures. Both excess molar volumes and the viscosity deviations are negative for all investigated systems. The isothermal excess molar volumes and viscosity deviations were fitted to a Redlich-Kister type equation, and the kinematic viscosity data were correlated with the McAllister equation.

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Densities and viscosities were measured for the binary mixtures of butylamine with 1-butanol, 1-pentanol, 1-hexanol, 1-heptanol, and 1-octanol at 303.15 K, 313.15 K, and 323.15 K over the entire composition range. Excess molar volumes and viscosity deviations were calculated at various temperatures. Both excess molar volumes and viscosity deviations are negative for all investigated systems. A Redlich−Kister type equation was applied to fit the isothermal excess volumes and viscosity deviations, and McAllister's three-body and four-body interaction models were also used to correlate the kinematic viscosities.