Henry's law

This article is about one of the gas laws in chemistry. For the chemist, see William Henry (chemist). For all other uses, see Law (disambiguation).

In chemistry, Henry's law is one of the gas laws formulated by William Henry in 1803. It states:

"At a constant temperature, the amount of a given gas that dissolves in a given type and volume of liquid is directly proportional to the partial pressure of that gas in equilibrium with that liquid."

An equivalent way of stating the law is that the solubility of a gas in a liquid is directly proportional to the partial pressure of the gas above the liquid.

An everyday example of Henry's law is given by carbonated soft drinks. Before the bottle or can of carbonated drink is opened, the gas above the drink is almost pure carbon dioxide at a pressure slightly higher than atmospheric pressure. The drink itself contains dissolved carbon dioxide. When the bottle or can is opened, this gas escapes, giving the characteristic hiss. Because the partial pressure of carbon dioxide above the liquid is now much lower, some of the dissolved carbon dioxide comes out of solution as bubbles. If a glass of the drink is left in the open, the concentration of carbon dioxide in solution will come into equilibrium with the carbon dioxide in the air, and the drink will go "flat".

A slightly more exotic example of Henry's law is in the decompression and decompression sickness of underwater divers.

Formula and the Henry's law constant

Henry's law can be put into mathematical terms (at constant temperature) as

p = k_{\mathrm{H}} c

where p is the partial pressure of the gaseous solute above the solution, c is the concentration of the dissolved gas and kH is a constant with the dimensions of pressure divided by concentration. The constant, known as the Henry's law constant, depends on the solute, the solvent and the temperature.

Some values for kH for gases dissolved in water at 298 K include:

oxygen (O2) : 769.2 L·atm/mol
carbon dioxide (CO2) : 29.41 L·atm/mol
hydrogen (H2) : 1282.1 L·atm/mol

There are various other forms of Henry's Law which define the constant kH differently and require different dimensional units.[1] In particular, the "concentration" of the solute in solution may also be expressed as a mole fraction or as a molarity.[2]

Other forms of Henry's law

The various other forms of Henry's law are discussed in the technical literature.[1][3][4]

Table 1: Some forms of Henry's law and constants (gases in water at 298.15 K)[4]
equation: k_{\mathrm{H,pc}} = \frac{p}{c_\mathrm{aq}} k_{\mathrm{H,cp}} = \frac{c_\mathrm{aq}}{p} k_{\mathrm{H,px}} = \frac{p}{x} k_{\mathrm{H,cc}} = \frac{c_{\mathrm{aq}}}{c_{\mathrm{gas}}}
units: \frac{\mathrm{L} \cdot \mathrm{atm}}{\mathrm{mol}} \frac{\mathrm{mol}}{\mathrm{L} \cdot \mathrm{atm}} \rm atm\, dimensionless
O2 769.23 1.3×10−3 4.259×104 3.181×10−2
H2 1282.05 7.8×10−4 7.099×104 1.907×10−2
CO2 29.41 3.4×10−2 0.163×104 0.8317
N2 1639.34 6.1×10−4 9.077×104 1.492×10−2
He 2702.7 3.7×10−4 14.97×104 9.051×10−3
Ne 2222.22 4.5×10−4 12.30×104 1.101×10−2
Ar 714.28 1.4×10−3 3.955×104 3.425×10−2
CO 1052.63 9.5×10−4 5.828×104 2.324×10−2
where:
caq = concentration (or molarity) of gas in solution (in mol/L)
cgas = concentration of gas above the solution (in mol/L)
p = partial pressure of gas above the solution (in atm)
x = mole fraction of gas in solution (dimensionless)

As can be seen by comparing the equations in the above table, the Henry's law constant kH,pc is simply the inverse of the constant kH,cp. Since all kH may be referred to as Henry's law constants, readers of the technical literature must be quite careful to note which version of the equation is being used.[1]

It should also be noted, the 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. Typically, Henry's law is only applicable to gas solute mole fractions less than 0.03.[5]

It also only applies simply for solutions where the solvent does not react chemically with the gas being dissolved. A common example of a gas that does react with the solvent is carbon dioxide, which forms carbonic acid (H2CO3) to a certain degree with water.

Temperature dependence of the Henry constant

When the temperature of a system changes, the Henry constant will also change.[1] This is why some people prefer to name it Henry coefficient. Multiple equations assess the effect of temperature on the constant. These forms of the van 't Hoff equation are examples:[4]

k_{\rm H,pc}(T) = k_{\rm H,pc}(T^\ominus)\, \exp{ \left[ -C \, \left( \frac{1}{T}-\frac{1}{T^\ominus}\right)\right]}\,
k_{\rm H,cp}(T) = k_{\rm H,cp}(T^\ominus)\, \exp{ \left[ C \, \left( \frac{1}{T}-\frac{1}{T^\ominus}\right)\right]}\,

where

kH for a given temperature is Henry's constant (as defined in this article's first section). Note that the sign of C depends on whether kH,pc or kH,cp is used.
T is any given temperature, in K
T o refers to the standard temperature (298 K).

This equation is only an approximation, and should be used only when no better, experimentally derived formula is known for a given gas.

The following table lists some values for constant C (in Kelvins) in the equation above:

Table 2: Values of C (in K)
 Gas  O2 H2 CO2 N2 He Ne Ar CO
C  1700   500   2400   1300   230   490   1300   1300 

Because solubility of permanent gases usually decreases with increasing temperature at around room temperature, the partial pressure a given gas concentration has in liquid must increase. While heating water (saturated with nitrogen) from 25 to 95 °C, the solubility will decrease to about 43% of its initial value. This can be verified when heating water in a pot; small bubbles evolve and rise long before the water reaches boiling temperature. Similarly, carbon dioxide from a carbonated drink escapes much faster when the drink is not cooled because the required partial pressure of CO2 to achieve the same solubility increases in higher temperatures. Partial pressure of CO2 in the gas phase in equilibrium with seawater doubles with every 16 K increase in temperature.[6]

The constant C may be regarded as:

C = -\frac{\Delta_{\rm solv}H}{R} = -\frac{{\rm d}\left[ \ln k_{\rm H}(T)\right]}{{\rm d}(1/T)}

where

ΔsolvH is the enthalpy of solution
R is the gas constant.

The solubility of gases does not always decrease with increasing temperature. For aqueous solutions, the Henry's law constant usually goes through a maximum (i.e., the solubility 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 about 30 °C for helium, 92 to 93 °C for argon, nitrogen and oxygen, and 114 °C for xenon.[7]

Influence of electrolytes

The influence of electrolytes on the solubility of gases is sometimes given by Sechenov (often spelled Setschenow) equation which accounts for the "salting out" (i.e., decreasing the solubility) or "salting in" (i.e., increasing the solubility) effect (see the article on activity coefficient). The Sechenov equation can be written as:[8]

\log(*z_1/z_1) = k_{syz} y

where:

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

C_{\rm melt}/C_{\rm gas} = \exp\left[-\beta(\mu^{\rm E}_{\rm melt} - \mu^{\rm E}_{\rm gas})\right]\,

where:

C = the number concentrations of the solute gas in the melt and gas phases
β = 1/kBT, an inverse temperature scale: kB = the Boltzmann constant
µE = the excess chemical potentials of the solute gas in the two phases.

Comparison to Raoult's law

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:

p = k_{\rm H}\,x

This can be compared with Raoult's law:

p = p^\star\,x

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: \lim_{x\to 1}\left( \frac{p}{x}\right) = p^\star
Henry's law: \lim_{x\to 0}\left( \frac{p}{x}\right) = k_{\rm H}

Raoult's law can also be related to non-gas solutes.

Standard chemical potential

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 on the concentration:

\mu = \mu_c^\ominus + RT\ln{\left( \frac{\gamma_c c}{c^\ominus}\right)}\,, where \gamma_c = \frac{k_{{\rm H,}c}}{p^\star} for a volatile solute; co = 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:

\sum_i n_i\, {\rm d}\mu_i = 0

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 co 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.:

\mu = \mu_b^\ominus + RT\ln{\left( \frac{\gamma_b b}{b^\ominus}\right)}\,, where \gamma_b = \frac{k_{{\rm H,}b}}{p^\star} for a volatile solute; bo = 1 mol/kg.

The standard chemical potential μmo, 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.

See also

References

  1. ↑ 1.0 1.1 1.2 1.3 Smith, Francis L.; Harvey, Allan H. (September 2007). "Avoid Common Pitfalls When Using Henry's Law" (PDF). Chemical Engineering Progress. ISSN 0360-7275.
  2. ↑ Lee, F. F. (2007), Comprehensive analysis, Henry's law constant determination, and photocatalytic degradation of polychlorinated biphenyls (PCBs) and/or other persistent organic pollutants (POPs), Ph.D. dissertation, State University of New York at Albany, pp. 199–201
  3. ↑ North Carolina State University CH 431/Lecture 14
  4. ↑ 4.0 4.1 4.2 Sander, R. (2014), "Compilation of Henry's law constants, version 3.99", Atmos. Chem. Phys. Discuss. 14: 29615–30521, doi:10.5194/acpd-14-29615-2014
  5. ↑ Prausnitz, John M; Lichtenthaler, Rudiger N.; de Azevedo, Edmundo Gomes (1999). Molecular Thermodynamics of Fluid Phase Equilibria (3rd ed.). Prentice Hall. p. 586. ISBN 0-13-977745-8.
  6. ↑ Takahashi, Taro; Sutherland, Stewart C.; Sweeney, Colm; Poisson, Alain; Metzl, Nicolas; Tilbrook, Bronte; Bates, Nicolas; Wanninkhof, Rik; Feely, Richard A. (2002). "Global sea–air CO2 flux based on climatological surface ocean pCO2, and seasonal biological and temperature effects". Deep Sea Research Part II: Topical Studies in Oceanography 49 (9–10): 1601– 1622. Bibcode:2002DSRII..49.1601T. doi:10.1016/S0967-0645(02)00003-6.
  7. ↑ Cohen, P., ed. (1989). The ASME Handbook on Water Technology for Thermal Power Systems. The American Society of Mechanical Engineers. p. 442. ISBN 978-0-7918-0634-0.
  8. ↑ Letcher, Trevor M., ed. (2007). Developments and applications in solubility (1st ed.). Royal Society of Chemistry. p. 71. ISBN 978-0854043729.

Further reading

External links