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 Please do not cite the old paper anymore.
|
Converting Henry's Law Constants
Your input: = 1 (aq-concentration / partial pressure)
Conversion to Henry's law solubility constants
yields:
= |
1 |
|
(aq-concentration / partial pressure) |
= |
101.325 |
|
(aq-concentration / partial pressure) |
= |
2478.96 |
|
(aq-concentration / gas-concentration) |
= |
0.00100301 |
|
(molality / partial pressure) |
= |
101.63 |
|
(molality / partial pressure) |
= |
1.83089 |
|
(molar fraction / partial pressure) |
= |
2271.1 |
|
(Bunsen coefficient) |
Conversion to Henry's law volatility constants
yields:
= |
0.546182 |
|
(partial pressure / molar fraction) |
= |
1 |
|
(partial pressure / aq-concentration) |
= |
9.86923E-06 |
|
(partial pressure / aq-concentration) |
= |
0.000403395 |
|
(gas-concentration / aq-concentration) |
All conversions are calculated at a temperature of
T = 298.15 K and a solution density
of ϱ = 997 kg/m3, using
the conversion factors from
Sander (2023) as shown in the following tables.
Table 1: Conversion factors between several Henry's law solubility
constants .
|
= ...
|
= ...
|
= ...
|
= ...
|
= ...
|
= ...
|
α = ...
|
= 1
|
1.00000 |
101.325 |
2478.96 |
1.00301E-3 |
101.630 |
1.83089 |
2271.10 |
= 1
|
9.86923E-3 |
1.00000 |
24.4654 |
9.89893E-6 |
1.00301 |
0.0180695 |
22.4140 |
= 1 |
4.03395E-4 |
0.0408740 |
1.00000 |
4.04609E-7 |
0.0409970 |
7.38573E-4 |
0.916150 |
= 1
|
997.000 |
1.01021E5 |
2.47152E6 |
1.00000 |
1.01325E5 |
1825.40 |
2.26428E6 |
= 1
|
9.83962E-3 |
0.997000 |
24.3920 |
9.86923E-6 |
1.00000 |
0.0180153 |
22.3467 |
= 1
|
0.546182 |
55.3419 |
1353.96 |
5.47826E-4 |
55.5084 |
1.00000 |
1240.43 |
α = 1 |
4.40316E-4 |
0.0446150 |
1.09152 |
4.41641E-7 |
0.0447493 |
8.06171E-4 |
1.00000 |
Table 2: Conversion factors between several Henry's law volatility
constants .
|
= ...
|
= ...
|
= ...
|
= ...
|
= 1
|
1.00000 |
1.83089 |
1.80695E-5 |
7.38573E-4 |
= 1
|
0.546182 |
1.00000 |
9.86923E-6 |
4.03395E-4 |
= 1
|
55341.9 |
1.01325E5 |
1.00000 |
40.8740 |
= 1
|
1353.96 |
2478.96 |
0.0244654 |
1.00000 |
Table 3: Products of Henry's law solubility constants
and Henry's law volatility constants
.
For example, if
= 11.1 atm, then
≈
5 mol/(kg atm) because 11.1 *
5 ≈ 55.5084.
|
|
|
|
|
|
|
|
|
0.546182 |
55.3419 |
1353.96 |
5.47826E-4 |
55.5084 |
1.00000 |
1240.43 |
|
1.00000 |
101.325 |
2478.96 |
1.00301E-3 |
101.630 |
1.83089 |
2271.10 |
|
9.86923E-6 |
1.00000E-3 |
0.0244654 |
9.89893E-9 |
1.00301E-3 |
1.80695E-5 |
0.0224140 |
|
4.03395E-4 |
0.0408740 |
1.00000 |
4.04609E-7 |
0.0409970 |
7.38573E-4 |
0.916150 |
|
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