New experimental VLE-data for alkanol/alkane mixtures and their description by an extended real association (ERAS) model.

(Vapour+liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T=298.15K

“…To our knowledge, there is not any isothermal VLE study on the ternary systems presented here, although there are some previous reports on the constituent binary systems at different temperatures: 1-butanol + n-hexane [14][15][16][17][18][19], 2-butanol + n-hexane [19][20][21][22], 1-butanol or 2-butanol + 1-chlorobutane [23,24], and n-hexane + 1-chlorobutane [25,26].…”

Thermodynamics of fluid‐phase equilibria for standard chemical engineering operations

“…These calculations use two binary "physical" (UNIQUAC) parameters and two "chemical" parameters (Nagata and Kawamura, 1979). A more detailed "chemical plus physical" model is the ERAS model developed by Heintz and coworkers (Heintz et al, 1986;Letcher et al, 1995); "chemical plus physical" solution theory is frequently used for describing the properties of electrolyte solutions (for example, Lu and Maurer, 1993).…”

Prediction of viscosity of alcohol+hydrocarbon systems by 1H NMR and activity coefficients at infinite dilution

“…3. The viscosity prediction for the 1-octanol (1)+hexane (2) system at 298.15 K by 1 H NMR chemical shift and ∞ 2 at 298.55 K (Gmehling and Onken, 1977) (---); VLE data (Heintz et al, 1986) (-); and experimental data at 298.15 K (Franjo et al, 1995) Experimental data (Chowdhury et al,2001) Prediction data of this work Prediction data from VLE…”