Consider two binary mixtures: (1) ethanol and water and (2) ethanol and ethyl acetate. This Demonstration computes the isobaric vapor-liquid diagram as well as the equilibrium curve at user-set values of the total pressure (expressed in ). The modified Raoult's law is used along with the van Laar model and Antoine equation. Both systems present a positive pressure-sensitive azeotrope. When present, this azeotrope is indicated on the equilibrium curve by a red dot. The loci of the azeotrope versus pressure is given in a separate plot. In both cases, the azeotrope disappears at a low enough total pressure. One particular feature of the present calculation is that it uses the arc length continuation method (see the Details section) to find the bubble/dew point temperatures versus liquid/vapor phase compositions. This takes advantage of a new function as of Mathematica 9.0, WhenEvent, which determines the loci of the azeotropes; indeed they verify , where is the arc length parameter.