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In
chemistry,
Henry's law is a
gas law
that states that the amount of dissolved gas is proportional to its
partial pressure in the gas phase. The proportionality factor is called
the Henry's law constant. It was formulated by the English chemist
William Henry, who studied the topic in the early 19th century. In his publication about the quantity of gases absorbed by water,
[1] he described the results of his experiments:
- ..."water takes up, of gas condensed by one, two, or more
additional atmospheres, a quantity which, ordinarily compressed, would
be equal to twice, thrice, &c. the volume absorbed under the common
pressure of the atmosphere."
An example where Henry's law is at play is in the depth-dependent dissolution of oxygen and nitrogen in the blood of
underwater divers that changes during
decompression, leading to
decompression sickness. An everyday example is given by one's experience with
carbonated soft drinks, which contain dissolved carbon dioxide. Before opening, the gas above the drink in its container is almost pure
carbon dioxide, at a pressure higher than
atmospheric pressure.
After the bottle is opened, this gas escapes, moving the partial
pressure of carbon dioxide above the liquid to be much lower, resulting
in degassing as the dissolved carbon dioxide comes out of solution.
Fundamental types and variants of Henry's law constants
There are many ways to define the proportionality constant of Henry's
law, which can be subdivided into two fundamental types: One
possibility is to put the aqueous phase into the numerator and the
gaseous phase into the denominator ("aq/gas").
[2] This results in the Henry's law solubility constant
.
Its value increases with increased solubility. Alternatively, numerator
and denominator can be switched ("gas/aq"), which results in the
Henry's law volatility constant
. The value of
decreases with increased solubility. There are several variants of both
fundamental types. This results from the multiplicity of quantities
that can be chosen to describe the composition of the two phases. Typical choices for the aqueous phase are
molar concentration (
),
molality (
), and molar
mixing ratio (
). For the gas phase, molar concentration (
) and
partial pressure (
) are often used. It is not possible to use the gas-phase mixing ratio (
) because at a given gas-phase mixing ratio, the aqueous-phase concentration
depends on the total pressure and thus the ratio
is not a constant.
[3]
To specify the exact variant of the Henry's law constant, two
superscripts are used. They refer to the numerator and the denominator
of the definition. For example,
refers to the Henry solubility defined as
.
Henry's law solubility constants
Henry solubility defined via concentration ()
Atmospheric chemists often define the Henry solubility as
- .[2]
Here
is the concentration of a species in the aqueous phase, and
is the partial pressure of that species in the gas phase under equilibrium conditions.
[citation needed]
The
SI unit for
is mol/(m
3 Pa); however, often the unit M/atm is used, since
is usually expressed in M (1 M = 1 mol/dm
3) and
in atm (1 atm = 101325 Pa).
[citation needed]
The dimensionless Henry solubility
The Henry solubility can also be expressed as the dimensionless ratio between the aqueous-phase concentration
of a species and its gas-phase concentration
:
- .[2]
For an ideal gas, the conversion is:
- ,[2]
where
is the
gas constant and
is the temperature.
Sometimes, this dimensionless constant is called the "water-air partitioning coefficient"
.
[4] It is closely related to the various, slightly different definitions of the "Ostwald coefficient"
, as discussed by Battino (1984).
[5]
Henry solubility defined via aqueous-phase mixing ratio ()
Another Henry's law solubility constant is
- .[2]
Here
is the molar mixing ratio in the aqueous phase. For a dilute aqueous solution the conversion between
and
is:
- ,[2]
where
is the density of water and
is the molar mass of water. Thus
- .[2]
The SI unit for
is Pa
−1, although atm
−1 is still frequently used.
[2]
Henry solubility defined via molality ()
It can be advantageous to describe the aqueous phase in terms of
molality instead of concentration. The molality of a solution does not
change with
, since it refers to the
mass of the solvent. In contrast, the concentration
does change with
,
since the density of a solution and thus its volume are
temperature-dependent. Defining the aqueous-phase composition via
molality has the advantage that any temperature dependence of the
Henry's law constant is a true solubility phenomenon and not introduced
indirectly via a density change of the solution. Using molality, the
Henry solubility can be defined as
Here
is used as the symbol for molality (instead of
) to avoid confusion with the symbol
for mass. The SI unit for
is mol/(kg Pa). There is no simple way to calculate
from
, since the conversion between concentration
and molality
involves
all solutes of a solution. For a solution with a total of
solutes with indices
, the conversion is:
where
is the density of the solution, and
are the molar masses. Here
is identical to one of the
in the denominator. If there is only one solute, the equation simplifies to
Henry's law is only valid for dilute solutions where
and
. In this case the conversion reduces further to
and thus
The Bunsen coefficient
According to Sazonov and Shaw, the dimensionless Bunsen coefficient
is defined as "the volume of saturating gas, V1, reduced to T° = 273.15 K, p° = 1 bar, which is absorbed by unit volume V
2* of pure solvent at the temperature of measurement and partial pressure of 1 bar."
[6] If the gas is ideal, the pressure cancels out, and the conversion to
is simply
- ,
with
= 273.15 K. Note, that according to this definition, the conversion factor is
not temperature-dependent.
[citation needed] Independent of the temperature that the Bunsen coefficient refers to, 273.15 K is always used for the conversion.
[citation needed] The Bunsen coefficient, which is named after
Robert Bunsen, has been used mainly in the older literature.
[citation needed]
The Kuenen coefficient
According to Sazonov and Shaw, the Kuenen coefficient
is defined as "the volume of saturating gas V(g), reduced to T° =
273.15 K, p° = bar, which is dissolved by unit mass of pure solvent at
the temperature of measurement and partial pressure 1 bar."
[6] If the gas is ideal, the relation to
is
- ,[citation needed][original research?]
where
is the density of the solvent, and
= 273.15 K. The SI unit for
is m
3/kg.
[6] The Kuenen coefficient, which is named after
Johannes Kuenen, has been used mainly in the older literature, and
IUPAC considers it to be obsolete.
[7]
Henry's law volatility constants
The Henry volatility defined via concentration ()
A common way to define a Henry volatility is dividing the partial pressure by the aqueous-phase concentration:
The SI unit for
is Pa m
3/mol.
The Henry volatility defined via aqueous-phase mixing ratio ()
Another Henry volatility is
The SI unit for
is Pa. However, atm is still frequently used.
The dimensionless Henry volatility
The Henry volatility can also be expressed as the dimensionless ratio between the gas-phase concentration
of a species and its aqueous-phase concentration
:
In
chemical engineering and
environmental chemistry, this dimensionless constant is often called the
air–water partitioning coefficient .
Values of Henry's law constants
A large compilation of Henry's law constants has been published by Sander (2015).
[2] A few selected values are shown in the table below:
Henry's law constants (gases in water at 298.15 K)
equation: |
|
|
|
|
unit: |
|
|
|
(dimensionless) |
O2 |
770 |
1.3×10−3 |
4.3×104 |
3.2×10−2 |
H2 |
1300 |
7.8×10−4 |
7.1×104 |
1.9×10−2 |
CO2 |
29 |
3.4×10−2 |
1.6×103 |
8.3×10−1 |
N2 |
1600 |
6.1×10−4 |
9.1×104 |
1.5×10−2 |
He |
2700 |
3.7×10−4 |
1.5×105 |
9.1×10−3 |
Ne |
2200 |
4.5×10−4 |
1.2×105 |
1.1×10−2 |
Ar |
710 |
1.4×10−3 |
4.0×104 |
3.4×10−2 |
CO |
1100 |
9.5×10−4 |
5.8×104 |
2.3×10−2 |
Temperature dependence
When the temperature of a system changes, the Henry constant also
changes. The temperature dependence of equilibrium constants can
generally be described with the
van 't Hoff equation, which also applies to Henry's law constants:
where
is the enthalpy of dissolution. Note that the letter
in the symbol
refers to enthalpy and is not related to the letter
for Henry's law constants. Integrating the above equation and creating an expression based on
at the reference temperature
= 298.15 K yields:
The van 't Hoff equation in this form is only valid for a limited temperature range in which
does not change much with temperature.
The following table lists some temperature dependencies:
Values of (in K)
O2 |
H2 |
CO2 |
N2 |
He |
Ne |
Ar |
CO |
1700 |
500 |
2400 |
1300 |
230 |
490 |
1300 |
1300 |
Solubility of permanent gases usually decreases with increasing
temperature at around room temperature. However, for aqueous solutions,
the Henry's law solubility constant for many species goes through a
minimum. For most permanent gases, the minimum is below 120 °C. Often,
the smaller the gas molecule (and the lower the gas solubility in
water), the lower the temperature of the maximum of the Henry's law
constant. Thus, the maximum is at about 30 °C for helium, 92 to 93 °C
for argon, nitrogen and oxygen, and 114 °C for xenon.
[8]
Effective Henry's law constants Heff
The Henry's law constants mentioned so far do not consider any
chemical equilibria in the aqueous phase. This type is called the
"intrinsic" (or "physical") Henry's law constant. For example, the
intrinsic Henry's law solubility constant of
formaldehyde can be defined as
In aqueous solution, methanal is almost completely hydrated:
The total concentration of dissolved methanal is
Taking this equilibrium into account, an effective Henry's law constant
can be defined as
For acids and bases, the effective Henry's law constant is not a useful quantity because it depends on the
pH of the solution.
[verification needed] In order to obtain a pH-independent constant, the product of the intrinsic Henry's law constant
and the acidity constant
is often used for strong acids like
hydrochloric acid (HCl):
Although
is usually also called a Henry's law constant, it should be noted that
it is a different quantity and it has different units than
.
Dependence on ionic strength (Sechenov equation)
Values of Henry's law constants for aqueous solutions depend on the
composition of the solution, i.e., on its ionic strength and on
dissolved organics. In general, the solubility of a gas decreases with
increasing salinity ("
salting out"). However, a "
salting in" effect has also been observed, for example for the effective Henry's law constant of
glyoxal. The effect can be described with the Sechenov equation, named after the Russian physiologist
Ivan Sechenov
(sometimes the German transliteration "Setschenow" of the Cyrillic name
Се́ченов is used). There are many alternative ways to define the
Sechenov equation, depending on how the aqueous-phase composition is
described (based on concentration, molality, or molar fraction) and
which variant of the Henry's law constant is used. Describing the
solution in terms of molality is preferred because molality is invariant
to temperature and to the addition of dry salt to the solution. Thus,
the Sechenov equation can be written as
where
is the Henry's law constant in pure water,
is the Henry's law constant in the salt solution,
is the molality-based Sechenov constant, and
is the molality of the salt.
Non-ideal solutions
Henry's law has been shown to apply to a wide range of solutes in the limit of "infinite dilution" (
x → 0), including non-volatile substances such as
sucrose. In these cases, it is necessary to state the law in terms of
chemical potentials.
For a solute in an ideal dilute solution, the chemical potential
depends only on the concentration. For non-ideal solutions, the activity
coefficients of the components must be taken into account:
- ,
where
for a volatile solute;
c° = 1 mol/L.
For non-ideal solutions, the
activity coefficient γc
depends on the concentration and must be determined at the
concentration of interest. The activity coefficient can also be obtained
for non-volatile solutes, where the vapor pressure of the pure
substance is negligible, by using the
Gibbs-Duhem relation:
By measuring the change in vapor pressure (and hence chemical
potential) of the solvent, the chemical potential of the solute can be
deduced.
The
standard state for a dilute solution is also defined in terms of infinite-dilution behavior. Although the standard concentration
c°
is taken to be 1 mol/l by convention, the standard state is a
hypothetical solution of 1 mol/l in which the solute has its limiting
infinite-dilution properties. This has the effect that all non-ideal
behavior is described by the activity coefficient: the activity
coefficient at 1 mol/l is not necessarily unity (and is frequently quite
different from unity).
All the relations above can also be expressed in terms of
molalities b rather than concentrations, e.g.:
where
for a volatile solute;
b° = 1 mol/kg.
The standard chemical potential
μm°, the activity coefficient
γm and the Henry's law constant
KH,b all have different numerical values when molalities are used in place of concentrations.
Solvent mixtures
Henry law constant H
2, M for a gas 2 in a mixture of solvents 1 and 3 is related to the constants for individual solvents H
21 and H
23:
where a
13 is the interaction parameter of the solvents from Wohl expansion of the excess chemical potential of the ternary mixtures.
Miscellaneous
In geochemistry
In
geochemistry, a version of Henry's law applies to the solubility of a
noble gas in contact with
silicate melt. One equation used is
where
- C is the number concentrations of the solute gas in the melt and gas phases,
- β = 1/kBT, an inverse temperature parameter (kB is the Boltzmann constant),
- µE is the excess chemical potentials of the solute gas in the two phases.
Comparison to Raoult's law
Henry's
law is a limiting law that only applies for "sufficiently dilute"
solutions. The range of concentrations in which it applies becomes
narrower the more the system diverges from ideal behavior. Roughly
speaking, that is the more chemically "different" the solute is from the
solvent.
For a dilute solution, the concentration of the solute is approximately proportional to its
mole fraction x, and Henry's law can be written as
This can be compared with
Raoult's law:
where
p* is the vapor pressure of the pure component.
At first sight, Raoult's law appears to be a special case of Henry's law, where
KH =
p*. This is true for pairs of closely related substances, such as
benzene and
toluene, which obey Raoult's law over the entire composition range: such mixtures are called "ideal mixtures".
The general case is that both laws are
limit laws,
and they apply at opposite ends of the composition range. The vapor
pressure of the component in large excess, such as the solvent for a
dilute solution, is proportional to its mole fraction, and the constant
of proportionality is the vapor pressure of the pure substance (Raoult's
law). The vapor pressure of the solute is also proportional to the
solute's mole fraction, but the constant of proportionality is different
and must be determined experimentally (Henry's law). In mathematical
terms:
- Raoult's law:
- Henry's law:
Raoult's law can also be related to non-gas solutes.