Mole fraction is used very frequently in the construction of
phase diagrams. It has a number of advantages: • it is not temperature dependent (as is
molar concentration) and does not require knowledge of the densities of the phase(s) involved • a mixture of known mole fraction can be prepared by weighing off the appropriate masses of the constituents • the measure is
symmetric: in the mole fractions
x = 0.1 and
x = 0.9, the roles of 'solvent' and 'solute' are reversed. • In a mixture of
ideal gases, the mole fraction can be expressed as the ratio of
partial pressure to total
pressure of the mixture • In a ternary mixture one can express mole fractions of a component as functions of other components mole fraction and binary mole ratios: • : \begin{align} x_1 &= \frac{1 - x_2}{1 + \frac{x_3}{x_1}} \\[2pt] x_3 &= \frac{1 - x_2}{1 + \frac{x_1}{x_3}} \end{align} Differential quotients can be formed at constant ratios like those above: : \left(\frac{\partial x_1}{\partial x_2}\right)_{\frac{x_1}{x_3}} = -\frac{x_1}{1 - x_2} or : \left(\frac{\partial x_3}{\partial x_2}\right)_{\frac{x_1}{x_3}} = -\frac{x_3}{1 - x_2} The ratios
X,
Y, and
Z of mole fractions can be written for ternary and multicomponent systems: : \begin{align} X &= \frac{x_3}{x_1 + x_3} \\[2pt] Y &= \frac{x_3}{x_2 + x_3} \\[2pt] Z &= \frac{x_2}{x_1 + x_2} \end{align} These can be used for solving PDEs like: : \left(\frac{\partial\mu_2}{\partial n_1}\right)_{n_2, n_3} = \left(\frac{\partial\mu_1}{\partial n_2}\right)_{n_1, n_3} or : \left(\frac{\partial\mu_2}{\partial n_1}\right)_{n_2, n_3, n_4, \ldots, n_i} = \left(\frac{\partial\mu_1}{\partial n_2}\right)_{n_1, n_3, n_4, \ldots, n_i} This equality can be rearranged to have differential quotient of mole amounts or fractions on one side. : \left(\frac{\partial\mu_2}{\partial\mu_1}\right)_{n_2, n_3} = -\left(\frac{\partial n_1}{\partial n_2}\right)_{\mu_1, n_3} = -\left(\frac{\partial x_1}{\partial x_2}\right)_{\mu_1, n_3} or : \left(\frac{\partial\mu_2}{\partial\mu_1}\right)_{n_2, n_3, n_4, \ldots, n_i} = -\left(\frac{\partial n_1}{\partial n_2}\right)_{\mu_1, n_2, n_4, \ldots, n_i} Mole amounts can be eliminated by forming ratios: : \left(\frac{\partial n_1}\right)_{n_3} = \left(\frac{\partial\frac{n_1}{n_3}}{\partial\frac{n_2}{n_3}}\right)_{n_3} = \left(\frac{\partial\frac{x_1}{x_3}}{\partial\frac{x_2}{x_3}}\right)_{n_3} Thus the ratio of chemical potentials becomes: : \left(\frac{\partial\mu_2}{\partial\mu_1}\right)_{\frac{n_2}{n_3}} = -\left(\frac{\partial\frac{x_1}{x_3}}{\partial\frac{x_2}{x_3}}\right)_{\mu_1} Similarly the ratio for the multicomponents system becomes : \left(\frac{\partial\mu_2}{\partial\mu_1}\right)_{\frac{n_2}{n_3}, \frac{n_3}{n_4}, \ldots, \frac{n_{i-1}}{n_i}} = -\left(\frac{\partial\frac{x_1}{x_3}}{\partial\frac{x_2}{x_3}}\right)_{\mu_1, \frac{n_3}{n_4}, \ldots, \frac{n_{i-1}}{n_i}} ==Related quantities==