The Wong–Sandler mixing rule is a thermodynamic mixing rule used for vapor–liquid equilibrium and liquid-liquid equilibrium calculations.[1] __TOC__
The first boundary condition is
b-
a | |
RT |
=\sumi\sumjxixj\left(bij-
aij | |
RT |
\right)
which constrains the sum of a and b. The second equation is
\underline
ex | |
A | |
EOS |
(T,P\toinfty,\underlinex)=\underline
ex | |
A | |
\gamma |
(T,P\toinfty,\underlinex)
with the notable limit as
P\toinfty
\underline{V}i\tob,
\underline{V}mix\tob
\underline
ex | |
A | |
EOS |
=C*\left(
a | |
b |
-\sumxi
ai | |
bi |
\right).
The mixing rules become
a | |
RT |
=Q
D | |
1-D |
, b=
Q | |
1-D |
Q=\sumi\sumjxixj\left(bij-
aij | |
RT |
\right)
D=\sumixi
ai | |
biRT |
+
\underline{G | |
ex |
\gamma(T,P,\underlinex)}{C*RT}
The cross term still must be specified by a combining rule, either
bij-
aij | |
RT |
=\sqrt{\left(bii-
aii | |
RT |
\right)\left(bjj-
ajj | |
RT |
\right)}(1-kij)
or
bij-
aij | |
RT |
=
1 | |
2 |
(bii+bjj)-
\sqrt{aiiajj | |