Walter Hayduk
2
2.7315e+02
Ambient temperature
5
2.7315
$\pu{K}$
0
0e+00
Ambient temperature
0
0
°C
-2
1.455e-02
Mole fraction - Liquid (1)
4
1.455
1
1
6.871e+01
Henry's Law Solubility Coefficient
4
6.871
$\pu{atm-1}$
3
2.43e+03
Enthalpy change
3
2.43
$\pu{cal mol-1}$
1
2
2.9315e+02
Ambient temperature
5
2.9315
$\pu{K}$
1
2.0e+01
Ambient temperature
2
2.0
°C
-2
1.084e-02
Mole fraction - Liquid (1)
4
1.084
1
1
9.224e+01
Henry's Law Solubility Coefficient
4
9.224
$\pu{atm-1}$
3
2.3e+03
Enthalpy change
2
2.3
$\pu{cal mol-1}$
2
2
2.9815e+02
Ambient temperature
5
2.9815
$\pu{K}$
1
2.5e+01
Ambient temperature
2
2.5
°C
-2
1.013e-02
Mole fraction - Liquid (1)
4
1.013
1
1
9.873e+01
Henry's Law Solubility Coefficient
4
9.873
$\pu{atm-1}$
3
2.27e+03
Enthalpy change
3
2.27
$\pu{cal mol-1}$
3
2
3.0315e+02
Ambient temperature
5
3.0315
$\pu{K}$
1
3.0e+01
Ambient temperature
2
3.0
°C
-3
9.51e-03
Mole fraction - Liquid (1)
3
9.51
1
2
1.051e+02
Henry's Law Solubility Coefficient
4
1.051
$\pu{atm-1}$
3
2.24e+03
Enthalpy change
3
2.24
$\pu{cal mol-1}$
4
2
3.1315e+02
Ambient temperature
5
3.1315
$\pu{K}$
1
4.0e+01
Ambient temperature
2
4.0
°C
-3
8.53e-03
Mole fraction - Liquid (1)
3
8.53
1
2
1.173e+02
Henry's Law Solubility Coefficient
4
1.173
$\pu{atm-1}$
3
2.18e+03
Enthalpy change
3
2.18
$\pu{cal mol-1}$
5
2
3.3315e+02
Ambient temperature
5
3.3315
$\pu{K}$
1
6.0e+01
Ambient temperature
2
6.0
°C
-3
6.93e-03
Mole fraction - Liquid (1)
3
6.93
1
2
1.442e+02
Henry's Law Solubility Coefficient
4
1.442
$\pu{atm-1}$
3
2.08e+03
Enthalpy change
3
2.08
$\pu{cal mol-1}$
6
2
3.5315e+02
Ambient temperature
5
3.5315
$\pu{K}$
1
8.0e+01
Ambient temperature
2
8.0
°C
-3
5.79e-03
Mole fraction - Liquid (1)
3
5.79
1
2
1.728e+02
Henry's Law Solubility Coefficient
4
1.728
$\pu{atm-1}$
3
1.995e+03
Enthalpy change
4
1.995
$\pu{cal mol-1}$
7
1
Solubility, Solubility data series
Two calibrated glass spheres, one larger than the other, immersed in a bath connected to a mercury manometer were used. Approximately 200 mL of solvent was placed in the larger sphere and both were thoroughly evacuated. A supply of ethene was charged to the smaller flask to 2 atm pressure. Ethene was admitted to the flask containing the solvent and allowed to reach equilibrium by stirring. The pressures were read and material balances made to determine the solubility. Solubilities were measured for equilibrium pressures between 50 and 1300 mm of mercury pressure and Henry's law was found to apply in all cases.
The International Union of Pure and Applied Chemistry
Truchard, A. M.; Harris, H. G.; Himmelblau, D. M.; J. Phys. Chem. 1961, 65, 575-576.
paper
https://doi.org/10.1021/j100821a513
64-67-5
2
C4H10O4S
InChI=1S/C4H10O4S/c1-3-7-9(5,6)8-4-2/h3-4H2,1-2H3
DENRZWYUOJLTMF-UHFFFAOYSA-N
154.185
Diethyl sulfate
Diethyl sulfate was Eastman practical grade purified by washing with $\ce{Na2CO3}$ solution and drying with $\ce{CaCl2}$.
74-85-1
1
C2H4
InChI=1S/C2H4/c1-2/h1-2H2
VGGSQFUCUMXWEO-UHFFFAOYSA-N
28.0532
Ethene
Ethene source and purity not given.
Ethene and Diethyl sulfate
Solubility data from IUPAC SDS Volume 57 (page ?) - Ethene and Diethyl sulfate