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Phase Equilibria and Phase Behaviour

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