For Phase Equilibria
T_\text{liq} = T_\text{vap}
p_\text{liq} = p_\text{vap}
f^\text{liq} = f^\text{vap}
Relative Volatility
K_i = \frac{y_i}{x_i}
\alpha_{ij} = \frac{K_i}{K_j}
Eutectic
L \rightarrow \alpha(s) + \beta(s)
Peritectic
\alpha(s) + L \rightarrow \beta(s)
Azeotrope
y_i = x_i
At an azeotrope the vapour and liquid compositions are the same. Therefor, the components can’t be separated by distillation
dG_i = RT d\left( \ln \hat{f_i} \right), \quad \lim_{p \to 0} \left( \frac{\hat{f_i}}{x_i p} \right) = 1