Adam Skrzecz
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
5.918e-01
Mass fraction (1)
4
5.918
1
-2
1.43e-02
Mass fraction (2)
3
1.43
1
1
-1
3.683e-01
Mole fraction - Liquid (1)
4
3.683
1
-3
4.8e-03
Mole fraction - Liquid (2)
2
4.8
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
7.122e-01
Mass fraction (1)
4
7.122
1
-1
1.778e-01
Mass fraction (2)
4
1.778
1
2
-1
6.543e-01
Mole fraction - Liquid (1)
4
6.543
1
-2
8.73e-02
Mole fraction - Liquid (2)
3
8.73
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
6.949e-01
Mass fraction (1)
4
6.949
1
-1
2.308e-01
Mass fraction (2)
4
2.308
1
3
-1
6.892e-01
Mole fraction - Liquid (1)
4
6.892
1
-1
1.224e-01
Mole fraction - Liquid (2)
4
1.224
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
5.697e-01
Mass fraction (1)
4
5.697
1
-1
3.805e-01
Mass fraction (2)
4
3.805
1
4
-1
6.327e-01
Mole fraction - Liquid (1)
4
6.327
1
-1
2.259e-01
Mole fraction - Liquid (2)
4
2.259
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
4.732e-01
Mass fraction (1)
4
4.732
1
-1
4.809e-01
Mass fraction (2)
4
4.809
1
5
-1
5.582e-01
Mole fraction - Liquid (1)
4
5.582
1
-1
3.033e-01
Mole fraction - Liquid (2)
4
3.033
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
3.891e-01
Mass fraction (1)
4
3.891
1
-1
5.841e-01
Mass fraction (2)
4
5.841
1
6
-1
5.054e-01
Mole fraction - Liquid (1)
4
5.054
1
-1
4.056e-01
Mole fraction - Liquid (2)
4
4.056
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
3.728e-01
Mass fraction (1)
4
3.728
1
-1
6.017e-01
Mass fraction (2)
4
6.017
1
7
-1
4.907e-01
Mole fraction - Liquid (1)
4
4.907
1
-1
4.234e-01
Mole fraction - Liquid (2)
4
4.234
1
1
2.0e+01
Ambient temperature
2
2.0
°C
2
2.932e+02
Ambient temperature
4
2.932
$\pu{K}$
-1
3.615e-01
Mass fraction (1)
4
3.615
1
-1
6.155e-01
Mass fraction (2)
4
6.155
1
8
-1
4.824e-01
Mole fraction - Liquid (1)
4
4.824
1
-1
4.391e-01
Mole fraction - Liquid (2)
4
4.391
1
1
Compositions along the saturation curve
Solubility, Solubility data series
The titration method was used to determine the binodal curve. The refraction indexes of mixtures were measured to construct the calibration curve, which was then used to find the concentration of ethanol in both phases at equilibrium.
The International Union of Pure and Applied Chemistry
Mertslin, R. V.; Nikurashina, N. I.; Petrov, V. A.; Zh. Fiz. Khim. 35, 2770 (1961).
paper
64-17-5
1
C2H6O
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
46.0684
Ethanol
Source not specified, dehydrated; distilled; BP = 78.0°C, $n_{D}^{20}$ = 1.3596.
110-54-3
2
C6H14
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
VLKZOEOYAKHREP-UHFFFAOYSA-N
86.1754
Hexane
Source not specified; doubly distilled; BP = 68.5°C, $n_{D}^{26}$ = 1.3751.
7732-18-5
3
H2O
InChI=1S/H2O/h1H2
XLYOFNOQVPJJNP-UHFFFAOYSA-N
18.0153
Water
Doubly distilled.
Ethanol with n-Hexane with Water
Solubility data from IUPAC SDS Volume 69 (page ?) - Ethanol with n-Hexane with Water