When referring to the compilation of Henry's Law Constants, please cite
this publication:
R. Sander: Compilation of Henry's law constants (version 5.0.0) for
water as solvent, Atmos. Chem. Phys., 23, 10901-12440 (2023),
doi:10.5194/acp-23-10901-2023
The publication from 2023 replaces that from 2015,
which is now obsolete. Please do not cite the old paper anymore.
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References |
Type |
Notes |
[mol/(m3Pa)] |
[K] |
|
|
|
9.1×10−5 |
2900 |
Abraham and Matteoli (1988) |
L |
|
9.1×10−5 |
2600 |
Clever (1979b) |
L |
1)
|
9.2×10−5 |
2600 |
Wilhelm et al. (1977) |
L |
|
9.4×10−5 |
2600 |
Lewis et al. (1987) |
M |
210)
|
1.0×10−4 |
2700 |
Ramstedt (1911) |
M |
|
1.2×10−4 |
|
Pierotti (1965) |
T |
|
1.0×10−4 |
|
Hayer et al. (2022) |
Q |
20)
|
7.4×10−5 |
2400 |
Linnemann et al. (2020) |
Q |
211)
|
9.1×10−5 |
2600 |
Yaws et al. (1999) |
? |
21)
|
8.3×10−5 |
2800 |
Dean and Lange (1999) |
? |
23)
212)
|
9.1×10−5 |
|
Abraham et al. (1990) |
? |
|
Data
The first column contains Henry's law solubility constant
at the reference temperature of 298.15 K.
The second column contains the temperature dependence
, also at the
reference temperature.
References
-
Abraham, M. H. & Matteoli, E.: The temperature variation of the hydrophobic effect, J. Chem. Soc. Faraday Trans. 1, 84, 1985–2000, doi:10.1039/F19888401985 (1988).
-
Abraham, M. H., Whiting, G. S., Fuchs, R., & Chambers, E. J.: Thermodynamics of solute transfer from water to hexadecane, J. Chem. Soc. Perkin Trans. 2, pp. 291–300, doi:10.1039/P29900000291 (1990).
-
Clever, H. L.: IUPAC Solubility Data Series, Volume 2, Krypton, Xenon and Radon, Pergamon Press, Oxford, ISBN 0080223524 (1979b).
-
Dean, J. A. & Lange, N. A.: Lange’s Handbook of Chemistry, Fifteenth Edition, McGraw-Hill, Inc., ISBN 9780070163843 (1999).
-
Hayer, N., Jirasek, F., & Hasse, H.: Prediction of Henry’s law constants by matrix completion, AIChE J., 68, e17 753, doi:10.1002/AIC.17753 (2022).
-
Lewis, C., Hopke, P. K., & Stukel, J. J.: Solubility of radon in selected perfluorocarbon compounds and water, Ind. Eng. Chem. Res., 26, 356–359, doi:10.1021/IE00062A030 (1987).
-
Linnemann, M., Nikolaychuk, P. A., noz Muñoz, Y. M. M., Baumhögger, E., & Vrabec, J.: Henry’s law constant of noble gases in water, methanol, ethanol, and isopropanol by experiment and molecular simulation, J. Chem. Eng. Data, 65, 1180–1188, doi:10.1021/ACS.JCED.9B00565 (2020).
-
Pierotti, R. A.: Aqueous solutions of nonpolar gases, J. Phys. Chem., 69, 281–288, doi:10.1021/J100885A043 (1965).
-
Ramstedt, E.: Sur la solubilité de l’émanation du radium dans les liquides organiques, Radium (Paris), 8, 253–256, doi:10.1051/RADIUM:0191100807025301 (1911).
-
Wilhelm, E., Battino, R., & Wilcock, R. J.: Low-pressure solubility of gases in liquid water, Chem. Rev., 77, 219–262, doi:10.1021/CR60306A003 (1977).
-
Yaws, C. L., Hopper, J. R., Wang, X., Rathinsamy, A. K., & Pike, R. W.: Calculating solubility & Henry’s law constants for gases in water, Chem. Eng., pp. 102–105 (1999).
Type
Table entries are sorted according to reliability of the data, listing
the most reliable type first: L) literature review, M) measured, V)
VP/AS = vapor pressure/aqueous solubility, R) recalculation, T)
thermodynamical calculation, X) original paper not available, C)
citation, Q) QSPR, E) estimate, ?) unknown, W) wrong. See Section 3.1
of Sander (2023) for further details.
Notes
1) |
A detailed temperature dependence with more than one parameter is available in the original publication. Here, only the temperature dependence at 298.15 K according to the van 't Hoff equation is presented. |
20) |
Calculated using machine learning matrix completion methods (MCMs). |
21) |
Several references are given in the list of Henry's law constants but not assigned to specific species. |
23) |
The partial pressure of water vapor (needed to convert some Henry's law constants) was calculated using the formula given by Buck (1981). The quantities A and α from Dean and Lange (1999) were assumed to be identical. |
210) |
The data from Lewis et al. (1987) were fitted to the three-parameter equation: Hscp= exp( 5.03587 +1555.37916/T −3.42648 ln(T)) mol m−3 Pa−1, with T in K. |
211) |
Calculated employing molecular force field models for the solutes from Mick et al. (2016). |
212) |
The data from Dean and Lange (1999) were fitted to the three-parameter equation: Hscp= exp( −240.66156 +12686.97685/T +33.12171 ln(T)) mol m−3 Pa−1, with T in K. |
The numbers of the notes are the same as
in Sander (2023). References cited in the notes can be
found here.
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