Phase equilibria and excess enthalpy for tetrahydrofuran + 2-methylpyrazine, tetrahydrofuran + 2-methylpyridine and 2-methylpyridine + 2-methylpyrazine: Experimental measurement and predictive modeling

• Consistent VLE data for binaries of THF, 2-methylpyrazine, and 2-methylpyridine • Excess molar enthalpies determined for the binary mixtures at 298.15 K • Vapor pressures of pure components are presented and correlated over a wide temperature range • VLE and H E data simultaneously regressed with NRTL, UNIQUAC and Wilson • COSMO-RS and GC models (UNIFAC, VTPR, PSRK) evaluated for VLE and H E predictive accuracy Knowledge about the vapor–liquid equilibrium (VLE) behavior of systems containing 2-methylpyridine or 2-methylpyrazine is limited in the literature, despite their industrial importance. In this study, consistent VLE data for mixtures of tetrahydrofuran + 2-methylpyrazine and 2-methylpyridine + 2-methylpyrazine at 50 and 75 kPa, as well as the system of tetrahydrofuran + 2-methylpyridine at 50, 75, and 101 kPa are presented. The excess molar enthalpy ( H E ) of these binaries has been measured using an isothermal flow calorimeter at 298.15 K and 101 kPa. The vapor pressure data of the pure components were measured and correlated over the temperature range between 294 and 405 K. The measured VLE and H E data were successfully correlated with NRTL, UNIQUAC, and Wilson activity coefficient models. In addition, the acquired VLE and H E were compared with those predicted by COSMO-RS and different predictive group contribution (GC) based models, including the original UNIFAC, UNIFAC-Dortmund, Volume Translated Peng-Robinson (VTPR) and Predictive Soave–Redlich–Kwong (PSRK). A satisfactory agreement was observed between the calculated results and experimental VLE data for all predictive methods; however, these models exhibited lower accuracy in predicting H E compared to VLE. Attained phase equilibria were checked for thermodynamic consistency using Wisniak’s L-W and Van Ness methods. All binaries exhibit nearly ideal behavior.

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Publication Details

Journal
Fluid Phase Equilibria
Published
2025-10-21
DOI
https://doi.org/10.1016/j.fluid.2025.114609
Citations
1
Primary Topic
Thermodynamic properties of mixtures
Type
article
Field-Weighted Citation Impact
0.72
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article

Phase equilibria and excess enthalpy for tetrahydrofuran + 2-methylpyrazine, tetrahydrofuran + 2-methylpyridine and 2-methylpyridine + 2-methylpyrazine: Experimental measurement and predictive modeling

Juha‐Pekka Pokki, Petri Uusi–Kyyny, Ville Alopaeus, Agung Ari Wibowo et al.
1 citations
Fluid Phase Equilibria
Thermodynamic properties of mixtures
0.72
article

Phase equilibria and excess enthalpy for tetrahydrofuran + 2-methylpyrazine, tetrahydrofuran + 2-methylpyridine and 2-methylpyridine + 2-methylpyrazine: Experimental measurement and predictive modeling

Juha‐Pekka Pokki, Petri Uusi–Kyyny, Ville Alopaeus, Agung Ari Wibowo, Ehsan Asadi, Muhammad Ossama
article en
1 citations

Abstract

• Consistent VLE data for binaries of THF, 2-methylpyrazine, and 2-methylpyridine • Excess molar enthalpies determined for the binary mixtures at 298.15 K • Vapor pressures of pure components are presented and correlated over a wide temperature range • VLE and H E data simultaneously regressed with NRTL, UNIQUAC and Wilson • COSMO-RS and GC models (UNIFAC, VTPR, PSRK) evaluated for VLE and H E predictive accuracy Knowledge about the vapor–liquid equilibrium (VLE) behavior of systems containing 2-methylpyridine or 2-methylpyrazine is limited in the literature, despite their industrial importance. In this study, consistent VLE data for mixtures of tetrahydrofuran + 2-methylpyrazine and 2-methylpyridine + 2-methylpyrazine at 50 and 75 kPa, as well as the system of tetrahydrofuran + 2-methylpyridine at 50, 75, and 101 kPa are presented. The excess molar enthalpy ( H E ) of these binaries has been measured using an isothermal flow calorimeter at 298.15 K and 101 kPa. The vapor pressure data of the pure components were measured and correlated over the temperature range between 294 and 405 K. The measured VLE and H E data were successfully correlated with NRTL, UNIQUAC, and Wilson activity coefficient models. In addition, the acquired VLE and H E were compared with those predicted by COSMO-RS and different predictive group contribution (GC) based models, including the original UNIFAC, UNIFAC-Dortmund, Volume Translated Peng-Robinson (VTPR) and Predictive Soave–Redlich–Kwong (PSRK). A satisfactory agreement was observed between the calculated results and experimental VLE data for all predictive methods; however, these models exhibited lower accuracy in predicting H E compared to VLE. Attained phase equilibria were checked for thermodynamic consistency using Wisniak’s L-W and Van Ness methods. All binaries exhibit nearly ideal behavior.

Fluid Phase EquilibriaVol. 602
Aalto University (FI)
Openalex Percentile: Top 27%
Thermodynamic properties of mixtures
0.72
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