When referring to the compilation of Henry's Law Constants, please cite
this publication:
R. Sander: Compilation of Henry's law constants (version 4.0) for
water as solvent, Atmos. Chem. Phys., 15, 4399-4981 (2015),
doi:10.5194/acp-15-4399-2015
|
Hcp |
d ln Hcp / d (1/T) |
Reference |
Type |
Notes |
[mol/(m3Pa)] |
[K] |
|
|
|
7.8×10−6 |
530 |
Fernández-Prini et al. 2003 |
L |
1)
|
7.7×10−6 |
490 |
Wilhelm et al. 1977 |
L |
|
7.9×10−6 |
500 |
Winkler 1891a |
M |
|
7.7×10−6 |
|
Hine and Weimar 1965 |
R |
|
7.7×10−6 |
490 |
Young 1981a |
X |
3)
|
7.7×10−6 |
500 |
Young 1981a |
X |
5)
|
7.7×10−6 |
640 |
Dean 1992 |
? |
6)
|
References
-
Dean, J. A.: Lange's Handbook of Chemistry, McGraw-Hill, Inc., 1992.
-
Fernández-Prini, R., Alvarez, J. L., and Harvey, A. H.: Henry's constants and vapor-liquid distribution constants for gaseous solutes in H2O and D2O at high temperatures, J. Phys. Chem. Ref. Data, 32, 903-916, doi:10.1063/1.1564818, 2003.
-
Hine, J. and Weimar, Jr., R. D.: Carbon basicity, J. Am. Chem. Soc., 87, 3387-3396, doi:10.1021/JA01093A018, 1965.
-
Wilhelm, E., Battino, R., and Wilcock, R. J.: Low-pressure solubility of gases in liquid water, Chem. Rev., 77, 219-262, doi:10.1021/CR60306A003, 1977.
-
Winkler, L. W.: Die Löslichkeit der Gase in Wasser (erste Abhandlung), Ber. Dtsch. Chem. Ges., 24, 89-101, doi:10.1002/CBER.18910240116, 1891a.
-
Young, C. L., ed.: IUPAC Solubility Data Series, vol. 5/6 of Hydrogen and Deuterium , Pergamon Press, Oxford, England, 1981a.
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 (2015) for further details.
Notes
1) |
Vapor pressure data for water from Wagner and Pruss (1993) was needed to calculate H. |
3) |
Value given here as quoted by Fogg and Sangster (2003). |
5) |
Value given here as quoted by Lide and Frederikse (1995). |
6) |
Only the tabulated data between T = 273 K and T = 303 K from Dean (1992) were used to derive H and its temperature dependence. Above T = 303 K, the tabulated data could not be parameterized very well. The partial pressure of water vapor (needed to convert some Henry's law constants) was calculated using the formula given by Sander et al. (1995). The quantities A and α from Dean (1992) were assumed to be identical. |
The numbers of the notes are the same as
in Sander (2015). References cited in the notes can be
found here.
|
* * *
Search Henry's Law Database
* * *
Convert Henry's Law Constants
* * *
|