Modelos termodinámicos para el equilibrio vapor – liquido a bajas presiones: fase liquida, modelo de wilson


Authors

  • Luis Guillermo Ríos A.

Abstract

El presente artículo tiene que ver con la forma en la cual pueden ser obtenidas las curvas de punto de rocío ó punto de condensación y de punto de burbuja ó punto de ebullición de un sistema binario no ideal, tal como el formado por el etanol (componente más volátil) y el agua, @ bajas presiones (P menor a 10 atm), utilizando la ecuación cúbica de Redlich-Kwong para calcular el coeficiente de fugacidad del gas i en la mezcla gaseosa, i , y el modelo de Wilson, para calcular el coeficiente de actividad del componente i en la mezcla líquida.

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Published

2004-01-05

How to Cite

Ríos A., L. G. (2004). Modelos termodinámicos para el equilibrio vapor – liquido a bajas presiones: fase liquida, modelo de wilson. Scientia Et Technica, 1(24). Retrieved from https://ojs2.utp.edu.co/index.php/revistaciencia/article/view/7359

Issue

Vol. 1 No. 24 (2004)

Section

Ciencias Básicas

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