Liquid-liquid equilibria for glycols plus hydrocarbons: Data and correlation

Samer Derawi, Georgios Kontogeorgis, Erling Halfdan Stenby, Toril Haugum, A.O. Fredheim

Research output: Contribution to journalJournal articleResearchpeer-review

Abstract

Liquid-liquid equilibrium data for seven binary glycol-hydrocarbon systems have been measured in the temperature range 32 degreesC to 80 degreesC and at the pressure 1 bar. The measured systems are monoethylene glycol (MEG) + heptane, methyleyclohexane (MCH) + hexane, propylene glycol (PG) + heptane, diethylene glycol (DEG) + heptane, triethylene glycol (TEG) + heptane, and tetraethylene glycol (TETRA) + heptane. The data obtained were correlated with the NRTL model and two different versions of the UNIQUAC equation. The NRTL model and one of the UNIQUAC equations (UQ 4) have a linear temperature-dependent interaction parameter term, while the other UNIQUAC equation (UQ 2) has an interaction parameter that is independent of the temperature. There was a fairly good agreement between the experimental data and the models with an average deviation in the composition for both phases of 3% for both NRTL and UQ 4 and 15% for UQ 2. These results indicate the necessity of using the linearly dependent interaction parameters.
Original languageEnglish
JournalJournal of Chemical and Engineering Data
Volume47
Issue number2
Pages (from-to)169-173
ISSN0021-9568
DOIs
Publication statusPublished - 2002

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