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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Honeywell Hi Spec Solut, Proc Modeling & Real Time Optimizat Grp, London, ON N6B 1V5, CanadaHoneywell Hi Spec Solut, Proc Modeling & Real Time Optimizat Grp, London, ON N6B 1V5, Canada
Zhao, E
Saha, S
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Honeywell Hi Spec Solut, Proc Modeling & Real Time Optimizat Grp, London, ON N6B 1V5, CanadaHoneywell Hi Spec Solut, Proc Modeling & Real Time Optimizat Grp, London, ON N6B 1V5, Canada
机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Yang, Jianyong
Peng, Changjun
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Peng, Changjun
Liu, Honglai
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Liu, Honglai
Hu, Ying
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China