c09 JWBS043-Rogers September 13, 2010 11:26 Printer Name: Yet to Come
140 THE PHASE RULE
-1/T (K-1)
-0.0037 -0.0036 -0.0035 -0.0034 -0.0033 -0.0032 -0.0031 -0.0030
Vapor Pressure (kPa)
0
2
4
6
8
10
12
14
FIGURE 9.13 The liquid–vapor coexistence curve of water leading tovapH(H 2 O)=
44 .90 kJ mol−^1.
The vapor pressures over pure water were selected at 10 K intervals
from 273 to 323 K, plotted, and submitted to a standard curve-fitting rou-
tine (SigmaPlot 11.0). A two-parameter exponential curve fit of pvap vs.
− 1 /T(Statistics → Nonlinear → Regression Wizard→ Ex-
ponential Growth → Single, 2-Parameter) gave the empirical con-
stantb(Outputb 5400.6916) K, where the unit of the empirical constant is kelvins
in order to make the exponent−b/Tunitless. The curve fit is good, having a mean
residual (difference between calculated and experimental values) of 1 part per thou-
sand or 0.1% over a range of about 12 kPa. We have the relationship between the
parameterbandvapH:
b=
vapH
R
which gives us
vapH=R(b)= 8. 314
(
5. 401 × 103
)
= 44. 90 × 103 = 44 .90 kJ mol−^1
This value is “averaged out” by the curve fitting technique over the temperatures
symmetrically distributed around 298 K. The handbook value ofvapHof water at
298 K is 43.99 kJ mol−^1.
Example 9.2 Ternary Phase Diagrams
The ternary phase diagram ABC in which A is completely miscible with B and C but
B and C are only partially miscible in each other looks like a combination of Figs.
9.9 and 9.12 except that the tie lines are not horizontal.