Vapor-liquid and liquid-liquid equilibrium calculations in mixtures containing non-ionic glycol ether surfactant using PHSC equation of state

被引:9
|
作者
Khoshsima, Ali [1 ]
Dehghani, Mohammad Reza [1 ]
机构
[1] Iran Univ Sci & Technol, Sch Chem Engn, Thermodynam Res Lab, Tehran 1684613114, Iran
关键词
Phase behavior; Surfactant; Glycol ether; Binary interaction parameter; PHSC; SPHERE-CHAIN EQUATION; ORGANIC-SOLVENT MIXTURES; EXCESS MOLAR VOLUMES; THERMODYNAMIC PROPERTIES; PHASE-EQUILIBRIA; BINARY-MIXTURES; PRESSURE MEASUREMENTS; PERTURBATION-THEORY; AQUEOUS-SOLUTIONS; METHYL ACETATE;
D O I
10.1016/j.fluid.2014.05.041
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this study, vapor-liquid and liquid-liquid equilibrium in mixtures containing glycol ether surfactant, non-polar and polar compounds are calculated using Perturbed Hard Sphere Chain (PHSC) equation of state (EoS). Pure liquid density and vapor pressure of surfactants are used for parameter estimation of glycol ether surfactants. The PHSC parameters are calculated for both ethylene glycol ether and propylene glycol ether surfactants. Glycol ether surfactant molecules are modeled as associating components by considering two association sites for each molecule. The results show that the PHSC model is capable of correlating thermodynamic behavior of binary (polar + surfactant) and (non-polar + surfactant) systems. Upper critical solution temperature (UCST) for hydrocarbon + surfactant and lower critical solution temperature (LCST) for water + surfactant systems are accurately calculated. The critical temperatures and the extent of immiscibility are in good agreement with the available experimental data. (C) 2014 Elsevier B.V. All rights reserved.
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页码:16 / 26
页数:11
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