Solution
Refer to Figure 7.17. Using the tie lines to connect the vapor composition
for each liquid phase composition, we ultimately find ourselves at a compo-
sition consisting ofx 1 0. Therefore, the pure component 2 is our ultimate
product.
As an additional example, what is the expected outcome if the solution had
an initial mole fraction x 1 of 0.1? Is your conclusion the same as the conclu-
sion for the additional example in Example 7.7?If deviations from ideality are large enough, then two liquids won’t even
make a solution at certain mole fractions: they will be immiscible.As long as
there is enough of each component to establish an equilibrium with a vapor
phase in the system, the pressure-composition phase diagram will look some-
thing like Figure 7.18. Between points A and B, we are implying that the two182 CHAPTER 7 Equilibria in Multiple-Component Systems
T(BP 2 )T(BP 1 )Temperature0.5
x 1 , y 10.0 1.0Final composition
of distillate:
pure component 2Initial composition
of liquid phaseFigure 7.17 See Example 7.8. If one starts with a liquid having the composition indicated, the
ultimate product will be one of the pure components.p* 2p* 1Pressure0.5
x 10.0 A 1.0BRegion of immiscibilityTotal pressurePartial pressure of component 2Partial pressure of component 1Figure 7.18 For very nonideal solutions, there may be ranges of immiscibility. In those ranges,
the vapor composition will not change. Here, the region between points A and B is a region of
immiscibility. The vapor pressure is constant in that range.