The system comprises substances with saturation pressure dependence p s1(T), p s2(T) a smooth line presents bubble points and dash ones relates to dew points. By way of example, Figure 1 shows a typical shape of the curve which bounds the two-phase vapor-liquid region of a binary system for a given composition χ ≡ χ 2, χ 1 = 1 − χ. (6) to (8) together with either temperature T d(p, χ) or pressure p d(T, χ) which correspond to a dew point. Conversely, at the dew point which relates to a starting point of condensation, it is known that z" = 1, χ (6) to (8) define a bubble point temperature T b(p, χ) if the pressure is known or a bubble point pressure p b(T, χ) if temperature is known in both cases the vapor phase composition χ At the bubble point, the liquid phase fraction z' = 1 and the phase composition of the liquid phase and the total composition of the system are equal: In contrast to the case of a pure substance, for the multicomponent two phase system these lines do not coincide as soon as the system is a polyvariant one (a number of degrees of freedom f = ν > 1), and the lines bound a field of two-phase equilibrium. The equations under consideration allow the calculation of a bubble point line as well as a dew point line. The system of Equations (6)-(8) is a base for analysis of vapor-liquid equilibrium in mixtures (solutions). Where z' and z" are a mole fraction of the liquid and the vapor phases. In general, it may be presented in the form So it is reasonable to use the correlations only for predicting the properties a priori as a first approximation.Īn alternative way in describing thermodynamic properties is based on using an equation of state which may present the properties of both liquid and gaseous states. It should be noted, however, that such correlations are essentially less precise than experimental data to be described. Actually all of them have been based on the three parameter corresponding states law, therefore to calculate any of the properties mentioned above it is necessary that critical parameters T c, p c as well as Pitzer Ґ (acentric) factor need to be known. To estimate thermodynamic properties of the phases which are in equilibrium, it is possible to use generalized equations such as Lee-Kesler, Gunn and Yamada for density, as well as the equations by Carruth and Kobayashi for heat of evaporation. The best of them provide a discrepancy of 1-2% in describing experimental data of p s(T) (the equations by Frost-Kalkwarf-Thodos, Lee-Kesler, etc.). (p 0 = 101325 Pa, T b is the normal boiling point temperature), which is a base for derivation of the majority of empirical correlations to describe the vapor pressure versus temperature.
0 Comments
Leave a Reply. |
AuthorWrite something about yourself. No need to be fancy, just an overview. ArchivesCategories |