Gases In most laboratory situations, the difference in behaviour between a real gas and an ideal gas is dependent only on the pressure and the temperature, not on the presence of any other gases. At a given temperature, the "effective" pressure of a gas is given by its
fugacity : this may be higher or lower than its mechanical pressure. By historical convention, fugacities have the dimension of pressure, so the dimensionless activity is given by: :a_i = \frac{f_i}{p^{\ominus}} = \varphi_i y_i \frac{p}{p^{\ominus}} where is the dimensionless fugacity coefficient of the species, is its
mole fraction in the gaseous mixture ( for a pure gas) and is the total pressure. The value {p^{\ominus}} is the standard pressure: it may be equal to 1
atm (101.325
kPa) or 1
bar (100 kPa) depending on the source of data, and should always be quoted.
Mixtures in general The most convenient way of expressing the composition of a generic mixture is by using the
mole fractions (written in the gas phase) of the different components (or chemical species: atoms or molecules) present in the system, where : x_i = \frac{n_i}{n}\,, \qquad n =\sum_i n_i\,, \qquad \sum_i x_i = 1\, : with , the number of moles of the component
i, and , the total number of moles of all the different components present in the mixture. The standard state of each component in the mixture is taken to be the pure substance,
i.e. the pure substance has an activity of one. When activity coefficients are used, they are usually defined in terms of
Raoult's law, : a_i = f_i x_i\, where is the Raoult's law activity coefficient: an activity coefficient of one indicates ideal behaviour according to Raoult's law.
Dilute solutions (non-ionic) A solute in dilute solution usually follows
Henry's law rather than Raoult's law, and it is more usual to express the composition of the solution in terms of the molar concentration (in mol/L) or the molality (in mol/kg) of the solute rather than in mole fractions. The standard state of a dilute solution is a hypothetical solution of concentration = 1 mol/L (or molality = 1 mol/kg) which shows ideal behaviour (also referred to as "infinite-dilution" behaviour). The standard state, and hence the activity, depends on which measure of composition is used. Molalities are often preferred as the volumes of non-ideal mixtures are not strictly additive and are also temperature-dependent: molalities do not depend on volume, whereas molar concentrations do. The activity of the solute is given by: :\begin{align} a_{c,i} &= \gamma_{c,i}\, \frac{c_i}{c^{\ominus}} \\[6px] a_{b,i} &= \gamma_{b,i}\, \frac{b_i}{b^{\ominus}} \end{align}
Ionic solutions When the solute undergoes ionic dissociation in solution (for example a salt), the system becomes decidedly non-ideal and we need to take the dissociation process into consideration. One can define activities for the cations and anions separately ( and ). In a liquid solution the activity coefficient of a given
ion (e.g. Ca2+) isn't measurable because it is experimentally impossible to independently measure the electrochemical potential of an ion in solution. (One cannot add cations without putting in anions at the same time). Therefore, one introduces the notions of ;mean ionic activity : ;mean ionic molality : ;mean ionic activity coefficient : where represent the stoichiometric coefficients involved in the ionic dissociation process Even though and cannot be determined separately, is a measurable quantity that can also be predicted for sufficiently dilute systems using
Debye–Hückel theory. For electrolyte solutions at higher concentrations, Debye–Hückel theory needs to be extended and replaced, e.g., by a
Pitzer electrolyte solution model (see
external links below for examples). For the activity of a strong ionic solute (complete dissociation) we can write: : ==Measurement==