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 Please do not cite the old paper anymore.
|
FORMULA: | HOC2H4NH2 |
CAS RN: | 141-43-5 |
STRUCTURE
(FROM
NIST):
|
|
InChIKey: | HZAXFHJVJLSVMW-UHFFFAOYSA-N |
|
|
References |
Type |
Notes |
[mol/(m3Pa)] |
[K] |
|
|
|
4.2×103 |
8300 |
Kim et al. (2008) |
M |
552)
|
6.0×104 |
|
Bone et al. (1983) |
M |
12)
|
1.1×104 |
|
Modarresi et al. (2007) |
Q |
68)
|
9.7×102 |
5800 |
Nguyen (2013) |
? |
11)
567)
|
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
-
Bone, R., Cullis, P., & Wolfenden, R.: Solvent effects on equilibria of addition of nucleophiles to acetaldehyde and the hydrophilic character of diols, J. Am. Chem. Soc., 105, 1339–1343, doi:10.1021/JA00343A044 (1983).
-
Kim, I., Svendsen, H. F., & Børresen, E.: Ebulliometric determination of vapor-liquid equilibria for pure water, monoethanolamine, N-methyldiethanolamine, 3-(methylamino)-propylamine, and their binary and ternary solutions, J. Chem. Eng. Data, 53, 2521–2531, doi:10.1021/JE800290K (2008).
-
Modarresi, H., Modarress, H., & Dearden, J. C.: QSPR model of Henry’s law constant for a diverse set of organic chemicals based on genetic algorithm-radial basis function network approach, Chemosphere, 66, 2067–2076, doi:10.1016/J.CHEMOSPHERE.2006.09.049 (2007).
-
Nguyen, T.: Amine Volatility in CO2 Capture, Ph.D. thesis, The University of Texas at Austin, USA, URL https://rochelle.che.utexas.edu/files/2015/02/Nguyen-2013-Amine-Volatility-in-CO2-Capture.pdf (2013).
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
11) |
Measured at high temperature and extrapolated to T⊖ = 298.15 K. |
12) |
Value at T = 293 K. |
68) |
Modarresi et al. (2007) use different descriptors for their calculations. They conclude that a genetic algorithm/radial basis function network (GA/RBFN) is the best QSPR model. Only these results are shown here. |
552) |
Calculated from the slope of y1P vs x1, using the tabulated VLE data from Kim et al. (2008) between 40 °C and 100 °C. Only dilute solutions with x1 ≤ 0.1 were considered. |
567) |
Nguyen (2013) refer to Kim et al. (2008) as the source, but this value cannot be found there. |
The numbers of the notes are the same as
in Sander (2023). References cited in the notes can be
found here.
|
* * *
Search Henry's Law Database
* * *
Convert Henry's Law Constants
* * *
|