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 Please do not cite the old paper anymore.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: | C4H11NO |
CAS RN: | 124-68-5 |
STRUCTURE
(FROM
NIST):
|
|
InChIKey: | CBTVGIZVANVGBH-UHFFFAOYSA-N |
|
|
References |
Type |
Notes |
[mol/(m3Pa)] |
[K] |
|
|
|
2.1×102 |
|
Du et al. (2017) |
M |
480)
|
7.0×102 |
8500 |
Nguyen (2013) |
M |
11)
|
1.8×102 |
|
Du et al. (2017) |
Q |
551)
|
9.3×101 |
|
Du et al. (2017) |
Q |
|
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
-
Du, Y., Yuan, Y., & Rochelle, G. T.: Volatility of amines for CO2 capture, Int. J. Greenhouse Gas Control, 58, 1–9, doi:10.1016/J.IJGGC.2017.01.001 (2017).
-
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. |
480) |
Value at T = 313 K. |
551) |
Calculated using the method from Nguyen (2013). |
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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