Vapour pressures of (butanenitrile+hexan-1-ol or octan-1-ol) between the temperatures T=288.15 K and 323.15 K were measured by a static method. Excess enthalpies and volumes were also measured at T=298.15 K. Reduction of the vapour pressures to obtain activity coefficients and excess molar Gibbs fre
Excess functions atT= 298.15 K of (butanenitrile +methanol, +pentan-1-ol, +heptan-1-ol, +nonan-1-ol, or +decan-1-ol)
✍ Scribed by R. Garriga; J. Ilarraza; P. P érez; M. Gracia
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 407 KB
- Volume
- 28
- Category
- Article
- ISSN
- 0021-9614
No coin nor oath required. For personal study only.
✦ Synopsis
Vapour pressures, excess enthalpies, and excess volumes of (butanenitrile + methanol, + pentan-1-ol, + heptan-1-ol, + nonan-1-ol, or + decan-1-ol) were measured at a temperature T=298.15 K. Vapour pressures of mixtures containing methanol have also been measured at T=278.15 K, 288.15 K, 308.15 K, and 318.15 K. Reduction of the vapour pressures to obtain activity coefficients and excess molar Gibbs free energies was carried out by Barker's method. All excess molar functions increase with the chain-length of the alcohol. The apparent contribution to excess molar enthalpies H E m and excess molar volumes V E m due to the specific interaction between the hydroxyl hydrogen and the lone electron pair of the nitrogen atom in mixtures of (butanenitrile + hexan-1-ol, + octan-1-ol, or + decan-1-ol) is estimated.
📜 SIMILAR VOLUMES
Vapour pressures of (butanenitrile + propan-1-ol or propan-2-ol) at temperatures T between 278.15 K and 323.15 K were measured by a static method. Excess molar enthalpies and volumes were also measured at T=298.15 K. Following Barker's method, the activity coefficients and the excess molar Gibbs fre
Excess molar volumes V E m at the temperature 298.15 K were obtained as a function of mole fraction ] from measurements of the density by using an Anton-Paar densimeter. Empirical equations have been fitted to the results for both ternary mixtures. The possibilities of predicting excess molar volum
Vapour pressures of (butanenitrile + ethanol or butan-1-ol) between the temperatures T=278.15 K and 323.15 K were measured by a static method. Excess enthalpies and volumes were also measured at T=298.15 K. Reduction of the vapour pressures to obtain activity coefficients and excess molar Gibbs free