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  3. Volume 4, Number 2
  4. PHASE VAPOR–LIQUID EQUILIBRIUM FOR THE SOLUTIONS OF DIETHYL SELENIDE AND DIETHYLZINC

PHASE VAPOR–LIQUID EQUILIBRIUM FOR THE SOLUTIONS OF DIETHYL SELENIDE AND DIETHYLZINC

CTAS.
2021;
Volume 4, Number 2
: 10-16
https://doi.org/10.23939/ctas2021.02.010
Authors:
  1. Serhiy Gerasymchuk
  2. Ihor Poliuzhyn
  3. H. V. Mel’nyk
  4. Yu. P. Pavlovskiy
  5. Valentyn Serheyev
1
Lviv Polytechnic National University
2
Lviv Polytechnic National University
3
Lviv Polytechnic National University
4
Lviv Polytechnic National University
5
Lviv Polytechnic National University

Using a semi-empirical Wilson’s model, the vapor-liquid equilibrium in the “diethylzinc - diethyl selenide” system is described: the activity coefficients of the solution components, the separation coefficient, the excess functions of the solution (HE, GE, TSE) are calculated, and isothermal P-X diagrams are obtained. The parameters of the Wilson’s model were calculated on the basis of our data on measuring the temperature dependence for saturated vapor pressure of high-purity samples of diethylzinc, diethyl selenide and their equimolecular solution using iterations from the mathematical software package Mathsad 14. Peculiarities of intermolecular interaction in the “diethylzinc – diethyl selenide” system and the presence of a negative deviation from Raoul's law have been found. The studied system is homogeneous in the whole concentration range. The concentration dependence of the enthalpy of mixing is alternating for the researched temperature range (280-340 K).

diethylzinc
diethyl selenide; the Wilson’s model; azeotrope; saturated vapor pressure; activity coefficients; excessed mixing functions

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