6.1 Ideal Solutions 245
If the pressure is taken as an independent variable, the mole fractions in the two phases,
represented by the ends of the tie line, are dependent variables.Temperature–Composition Phase Diagrams
In this type of phase diagram the pressure is held fixed. For two components the mole
fraction of one component is plotted on the horizontal axis and the temperature is plot-
ted on the vertical axis. Figure 6.3 shows the liquid–vapor temperature–composition
diagram of benzene and toluene at 1.000 atm. The upper curve gives the boiling tem-
perature at the given pressure as a function of the mole fraction of benzene in the vapor
phase, and the lower curve gives the boiling temperature at the given pressure as a func-
tion of the mole fraction of benzene in the liquid phase. The tie lines drawn between
the two curves connect values of the mole fraction in the two phases at equilibrium
with each other, giving the composition of one phase as a function of the composition
of the other phase at the temperature given by the height of the tie line. Each tie line
in this diagram must be the same as the tie line in a pressure–composition diagram
corresponding to the temperature of this diagram.Area of
vapor states400390380370360350340
0 0.2 0.4 0.6 0.8 10
Mole fraction of benzeneT/KArea of
liquid states Tie
line
areaPoints
representing
coexisting
phasesFigure 6.3 The Liquid–Vapor Tem-
perature–Composition Phase Dia-
gram of Benzene and Toluene at 1.000
atm.Drawn from data of M. A. Rosanoff,
C. W. Bacon, and F. W. Schulze,J. Am.
Chem. Soc., 36 , 1993 (1914).In order to represent the full equilibrium pressure-temperature-composition behav-
ior of a two-component system, a three-dimensional graph is required, as schematically
represented in Figure 6.4 for a nearly ideal liquid solution. There are two surfaces in this
diagram, and they coincide at the edges of the graph. A pressure–composition diagram
is created by passing a plane of constant temperature through the three-dimensionalPressure at
constantT
Temperature
at constant PTie lines Plane of
constantPPlane of
constantTRegion of
vapor statesX T
2PFigure 6.4 Perspective View of the Three-Dimensional Liquid–Vapor Phase Diagram
for an Ideal Solution (Schematic).