Walter Hayduk
2
3.7315e+02
Ambient temperature
5
3.7315
$\pu{K}$
2
1.00e+02
Ambient temperature
3
1.00
°C
-1
9.00e-01
Mole fraction - Vapor (1)
3
9.00
1
-1
1.44e-01
Equilibrium Constant (Component 1)
3
1.44
1
-1
3.06e-01
Mole fraction - Liquid (1)
3
3.06
1
0
4.05e+00
Ambient pressure
3
4.05
$\pu{MPa}$
0
2.95e+00
Equilibrium Constant (Component 2)
3
2.95
1
1
2
3.7315e+02
Ambient temperature
5
3.7315
$\pu{K}$
2
1.00e+02
Ambient temperature
3
1.00
°C
-1
9.19e-01
Mole fraction - Vapor (1)
3
9.19
1
-1
1.48e-01
Equilibrium Constant (Component 1)
3
1.48
1
-1
4.50e-01
Mole fraction - Liquid (1)
3
4.50
1
0
6.08e+00
Ambient pressure
3
6.08
$\pu{MPa}$
0
2.04e+00
Equilibrium Constant (Component 2)
3
2.04
1
2
2
3.7315e+02
Ambient temperature
5
3.7315
$\pu{K}$
2
1.00e+02
Ambient temperature
3
1.00
°C
-1
9.05e-01
Mole fraction - Vapor (1)
3
9.05
1
-1
2.37e-01
Equilibrium Constant (Component 1)
3
2.37
1
-1
5.99e-01
Mole fraction - Liquid (1)
3
5.99
1
0
8.11e+00
Ambient pressure
3
8.11
$\pu{MPa}$
0
1.51e+00
Equilibrium Constant (Component 2)
3
1.51
1
3
2
3.7315e+02
Ambient temperature
5
3.7315
$\pu{K}$
2
1.00e+02
Ambient temperature
3
1.00
°C
-1
8.37e-01
Mole fraction - Vapor (1)
3
8.37
1
-1
7.24e-01
Equilibrium Constant (Component 1)
3
7.24
1
-1
7.75e-01
Mole fraction - Liquid (1)
3
7.75
1
1
1.013e+01
Ambient pressure
4
1.013
$\pu{MPa}$
0
1.08e+00
Equilibrium Constant (Component 2)
3
1.08
1
4
2
4.2315e+02
Ambient temperature
5
4.2315
$\pu{K}$
2
1.50e+02
Ambient temperature
3
1.50
°C
-1
7.75e-01
Mole fraction - Vapor (1)
3
7.75
1
-1
2.98e-01
Equilibrium Constant (Component 1)
3
2.98
1
-1
2.45e-01
Mole fraction - Liquid (1)
3
2.45
1
0
4.05e+00
Ambient pressure
3
4.05
$\pu{MPa}$
0
3.16e+00
Equilibrium Constant (Component 2)
3
3.16
1
5
2
4.2315e+02
Ambient temperature
5
4.2315
$\pu{K}$
2
1.50e+02
Ambient temperature
3
1.50
°C
-1
8.22e-01
Mole fraction - Vapor (1)
3
8.22
1
-1
2.83e-01
Equilibrium Constant (Component 1)
3
2.83
1
-1
3.71e-01
Mole fraction - Liquid (1)
3
3.71
1
0
6.08e+00
Ambient pressure
3
6.08
$\pu{MPa}$
0
2.21e+00
Equilibrium Constant (Component 2)
3
2.21
1
6
2
4.2315e+02
Ambient temperature
5
4.2315
$\pu{K}$
2
1.50e+02
Ambient temperature
3
1.50
°C
-1
9.25e-01
Mole fraction - Vapor (1)
3
9.25
1
-1
3.54e-01
Equilibrium Constant (Component 1)
3
3.54
1
-1
5.06e-01
Mole fraction - Liquid (1)
3
5.06
1
0
8.11e+00
Ambient pressure
3
8.11
$\pu{MPa}$
0
1.63e+00
Equilibrium Constant (Component 2)
3
1.63
1
7
2
4.2315e+02
Ambient temperature
5
4.2315
$\pu{K}$
2
1.50e+02
Ambient temperature
3
1.50
°C
-1
7.64e-01
Mole fraction - Vapor (1)
3
7.64
1
-1
7.16e-01
Equilibrium Constant (Component 1)
3
7.16
1
-1
6.70e-01
Mole fraction - Liquid (1)
3
6.70
1
1
1.013e+01
Ambient pressure
4
1.013
$\pu{MPa}$
0
1.14e+00
Equilibrium Constant (Component 2)
3
1.14
1
8
2
4.7315e+02
Ambient temperature
5
4.7315
$\pu{K}$
2
2.00e+02
Ambient temperature
3
2.00
°C
-1
5.20e-01
Mole fraction - Vapor (1)
3
5.20
1
-1
5.96e-01
Equilibrium Constant (Component 1)
3
5.96
1
-1
1.95e-01
Mole fraction - Liquid (1)
3
1.95
1
0
4.05e+00
Ambient pressure
3
4.05
$\pu{MPa}$
0
2.67e+00
Equilibrium Constant (Component 2)
3
2.67
1
9
2
4.7315e+02
Ambient temperature
5
4.7315
$\pu{K}$
2
2.00e+02
Ambient temperature
3
2.00
°C
-1
5.86e-01
Mole fraction - Vapor (1)
3
5.86
1
-1
5.95e-01
Equilibrium Constant (Component 1)
3
5.95
1
-1
3.04e-01
Mole fraction - Liquid (1)
3
3.04
1
0
6.08e+00
Ambient pressure
3
6.08
$\pu{MPa}$
0
1.93e+00
Equilibrium Constant (Component 2)
3
1.93
1
10
2
4.7315e+02
Ambient temperature
5
4.7315
$\pu{K}$
2
2.00e+02
Ambient temperature
3
2.00
°C
-1
6.02e-01
Mole fraction - Vapor (1)
3
6.02
1
-1
7.02e-01
Equilibrium Constant (Component 1)
3
7.02
1
-1
4.33e-01
Mole fraction - Liquid (1)
3
4.33
1
0
8.11e+00
Ambient pressure
3
8.11
$\pu{MPa}$
0
1.39e+00
Equilibrium Constant (Component 2)
3
1.39
1
11
1
Solubility, Solubility data series
A high pressure apparatus employing a glass capillary tube immersed in mercury was used. Agitation was by means of a magnetically-operated agitation system. A cathetometer was used to determine the quantity of solvent charged and a microburette was used to measure the volumes of gas dissolved.
The International Union of Pure and Applied Chemistry
Paratella, A.; Riv. Combust. 1963, 17, 334-341.
paper
74-85-1
1
C2H4
InChI=1S/C2H4/c1-2/h1-2H2
VGGSQFUCUMXWEO-UHFFFAOYSA-N
28.0532
Ethene
Ethene was prepared by reaction of Zn with dibromoethane in an alcohol solution. The purity was determined at 99.5%.
142-82-5
2
C7H16
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
IMNFDUFMRHMDMM-UHFFFAOYSA-N
100.202
Heptane
Heptane was from Phillips Petroleum of the highest purity grade (unspecified).
Ethene with Heptane
Solubility data from IUPAC SDS Volume 57 (page ?) - Ethene with Heptane