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               Chapter 12                    The two freezing-point curves intersect at point E. For a solution with x to the
                                                                                                           B
               Multicomponent Phase Equilibrium  left of E, solid C will freeze out as T is lowered. For x to the right of E, solid B will
                                                                                       l
                                                                                       B
                                                                       l
                                         freeze out. At the values of T and x corresponding to point E, the chemical potentials
                                                                       B
                                         of B and C in the solution equal the chemical potentials of pure solid B and C, re-
                                         spectively, and both B and C freeze out when a solution with the eutectic composition
                                         x  is cooled. Point E is the eutectic point (Greek eutektos, “easily melted”).
                                          B
                                             The portion of line DE with x very close to 1 can be calculated from the ideally
                                                                      B
                                         dilute–solution equation (12.14) with A and B replaced by B and C, respectively.
                                         Likewise, the portion of line AFGE with x very close to 0 (and hence x very close
                                                                             B                         C
                                         to 1) can be calculated from (12.14) with A and B replaced by C and B, respectively.
                                         Away from the ends of these lines, Eq. (12.7) with A replaced by B or C applies. This
                                         exact equation is hard to use to find the freezing point T as a function of x or x . To
                                                                                         f              B    C
                                         get a rough idea of the shape of the curves DE and AE, we neglect the temperature de-
                                         pendences of   H   and   H    ; and we approximate g and g as 1 over the full
                                                      fus  m,B   fus  m,C                  B     C
                                         range of solution composition (this ideal-solution approximation is usually quite
                                         poor). Thus the very approximate equation for DE is
                                                                              1    1
                                                           R  ln  x   ¢ H m,B a     b   for DE             (12.46)
                                                                B
                                                                      fus
                                                                             T*    T
                                                                               B
                                         The approximate equation for AE is obtained by replacing B with C in (12.46).
                                             Suppose we start at point R in Fig. 12.19 and isobarically cool a liquid solution of
                                         B and C with composition x
. The overall composition of the closed system remains
                                                                 B
                                         constant at x
, and we proceed vertically down from R. When T reaches T , solid C
                                                                                                         1
                                                    B
                                                                          l
                                         starts to freeze out. As C freezes out, x increases and (since B is the solute here) the
                                                                          B
                                         freezing point is lowered further. To freeze out more of the solvent (C), we therefore
                                         must lower the temperature further. At a typical temperature T , there is an equilibrium
                                                                                             2
                                         between a solution whose composition is given by point G as x  and solid C, whose
                                                                                               B
                                         composition is given by point I as x   0. As usual, the points at the ends of the tie
                                                                        B
                                         line (GHI) give the compositions of the two phases in equilibrium. The lever rule gives
                                                                    s
                                                       l
                                          s
                                                  l
                                         n HI    (n   n )HG ,  where n is the number of moles of solid C in equilibrium with
                                          C       B    C            C
                                         a solution of n moles of B plus n moles of C. At point F, the lever rule gives n
                                                      l
                                                                                                              s
                                                                      l
                                                      B               C                                       C
                                         0. As T drops along the line FHK, the horizontal distance to the line AFGE increases,
                                                                s
                                         indicating an increase in n .
                                                                C
                                             As T is lowered further, we finally reach the eutectic temperature T at point K.
                                                                                                       3
                                         Here, the solution has composition x  (point E), and now both solid C and solid B
                                                                         B
                                         freeze out, since both solids freeze out when a solution with the eutectic composition
                                         is cooled. The relative amounts of B and C that freeze out at E correspond to the eu-
                                         tectic composition x , and the entire remaining solution freezes at T with no further
                                                          B                                        3
                                         change in composition. At K, three phases are in equilibrium (solution, solid B, and
                                         solid C), so the lever rule (12.41) does not apply. With three phases, we have f   2
                                         3   2   1 degree of freedom; this degree of freedom has been eliminated by the spec-
                                         ification that P is fixed at 1 atm. Hence there are no degrees of freedom for the three-
                                         phase system, and the temperature must remain constant at T until all the solution has
                                                                                            3
                                         frozen and the number of phases has dropped to 2. Below T , we are simply cooling a
                                                                                           3
                                         mixture of solid B plus solid C. The endpoints of a horizontal tie line drawn through
                                         point S lie at x   0 and x   1, and these are the compositions of the phases [pure
                                                      B         B
                                         C(s) and pure B(s)] present at S.
                                             If we reverse the process and start at point S with solid B plus solid C, the first
                                         liquid formed will have the eutectic composition x . The system will remain at point K
                                                                                   B
                                         until all the B has melted, along with enough C to give a solution with eutectic composi-
                                         tion. Then the remaining solid C will melt over the temperature range T to T . (Sharpness
                                                                                                  3    1
                                         of melting point is one test organic chemists use for the purity of a compound.) A solid
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