Liquid + liquid) equilibrium data are presented for (acetonitrile + acetic acid, or propanoic acid, or butanoic acid, or 2-methylpropanoic acid, or pentanoic acid, or 3methylbutanoic acid + cyclohexane) at T = 298.15 K. The relative mutual solubility of each of the carboxylic acids is higher in the
(Solid  +  liquid) equilibria in (polynuclear aromatic +  tertiary amide) systems
✍ Scribed by Zygmunt Lisicki; Małgorzata E. Jamróz
- Publisher
- Elsevier Science
- Year
- 2000
- Tongue
- English
- Weight
- 226 KB
- Volume
- 32
- Category
- Article
- ISSN
- 0021-9614
No coin nor oath required. For personal study only.
✦ Synopsis
The solubility of selected polynuclear aromatic compounds (anthracene, phenanthrene, carbazole, fluorene, dibenzothiophene, and dibenzofuran) in three N -substituted amide systems (N ,N -dimethylacetamide, N -methyl-2-pyrrolidinone, N -methyl-ε-caprolactam) has been measured by a dynamic method over the whole concentration range. In the case of N -methyl-ε-caprolactam systems the measurements were carried out from T = 280 K up to the melting temperatures of the aromatic compounds, because of a rapid increase of viscosity resulting in glass formation in the supercooled liquid phases. The incongruently melting compounds were found to exist only in the systems with carbazole. The other systems were simple eutectics. To estimate the activity coefficients, the liquidus curves were approximated with the Wilson, Redlich-Kister, NRTL, and UNIQUAC equations. For all calculated results the root-mean-square deviations of solubility temperatures vary from 0.1 K to 2.8 K, depending on the equation used.
📜 SIMILAR VOLUMES
The experimental results are compared with values calculated by means of the Wilson, UNIQUAC and NRTL equations utilizing parameters derived from the experimental s.l.e. The existence of a (solid + solid) first-order phase transition in hydrocarbons has been taken into consideration in the solubilit
Liquid + liquid) equilibrium data of (tert amyl ethyl ether + ethanol + water) were determined experimentally at T = (298. 15, 308.15, and 318.15) K. The experimental results were correlated with the NRTL and UNIQUAC equations. The correlations were made at each temperature and for the three tempera
Consistent (vapour + liquid) equilibrium data for the ternary system (benzene + cyclohexane + anisole) at p = 101.32 kPa are reported. The results indicate that the mixture deviates positively from ideality and that only the minimum binary azeotrope (benzene + cyclohexane) exists. The activity coeff
Vapour + liquid) equilibrium data are presented for (methanol + ethyl tert-butyl ether) and (methanol + ethyl tert-butyl ether + toluene) at T = 328.15 K. The experimental results were measured by using a Boublik recirculation still. The binary results for (methanol + ethyl tert-butyl ether) and for
The isothermal and isobaric (vapour + liquid) equilibria (v.l.e.) for (N ,N -dimethylformamide + 2-propanol + 1-butanol) and the binary constituent mixtures were measured with an inclined ebulliometer. The experimental results are analyzed using the UNIQUAC equation with temperature-dependent binary