Aspen Physical Property System - Physical Property Models

Solvents
The contribution from solvents can be written as follows:
168 2 Thermodynamic Property Models
(103)
(104)
(105)
(106)
(107)
(108)
where is the liquid fugacity coefficient of pure solvent
component i, pi sat is the vapor pressure of pure component at the system
temperature T, �i v is the vapor fugacity coefficient of pure component at T
and pi sat (normally calculated from an equation-of-state model), and
is the Poynting pressure correction from pi sat to p,
and Vi l is the liquid molar volume at T and p.
Henry components
The contribution from Henry components can be written as follows:
(109)
(110)
(111)
(112)
(113)