International Journal of Thermophysics· 2026Q2
High-Pressure Solid–Liquid Equilibrium and Volumetric Behavior of Choline Chloride-Based Eutectic Solvents
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- Q2SCImago
- 2026year
Short summary
This study provides the first high-pressure solid-liquid equilibrium (SLE) and volumetric data for choline chloride (ChCl)-based eutectic solvents (ESs) with ethylene glycol, glycerol, 1,3-propanediol, and glycolic acid, expanding the thermodynamic database for these materials.
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Key points
- Reports the first high-pressure solid-liquid equilibrium (SLE) data for ChCl-based ESs (6-25 MPa).
- Provides new density measurements for ChCl-based ESs at high pressures (5-50 MPa) and temperatures (293.15-353.15 K).
- Density data correlated with the modified Tammann–Tait equation showed average relative deviations below 0.45%.
- Calculated isothermal compressibility and isobaric thermal expansivity from density data, showing pressure and temperature dependence.
AI-generated from the title and abstract; the full text is not read.
Abstract
Abstract Over the past two decades, eutectic solvents (ESs) have attracted attention due to their potential in various fields, from chemical processing to materials science. Despite this growing interest, their use is still restricted to fixed stoichiometric mole ratios. This limitation arises from the difficulty in accurately identifying eutectic compositions, a consequence of the scarcity of reliable thermophysical property data. In particular, properties such as density and solid–liquid equilibrium (SLE) remain poorly documented in the literature, especially under elevated pressure. In this context, this work reports SLE and volumetric data for mixtures of choline chloride with four hydrogen-bond donors: ethylene glycol, glycerol, 1,3-propanediol, and glycolic acid. SLE measurements were performed in the pressure range between 6 MPa and 25 MPa and compared with available data at atmospheric pressure. Density measurements were carried out for the ESs at their eutectic compositions over ranges of pressure (5 MPa to 50 MPa) and temperature (293.15 K to 353.15 K). The experimental density data were correlated using the modified Tammann–Tait equation, yielding average relative deviations below 0.45 %. Based on the fitted parameters, the isothermal compressibility ( $${\kappa}_{T}$$ κ T ) and the isobaric thermal expansivity ( $${\alpha}_{T}$$ α T ) were calculated. Both properties exhibited dependence on pressure and temperature, in agreement with the behavior of incompressible liquid systems. This study enlarges the thermodynamic database of ChCl-based ESs by providing the first high-pressure SLE data along with new volumetric measurements. These results improve the understanding of ES phase behavior and offer valuable inputs for thermodynamic modeling, process design, and the development of ES-based applications.
The authors' abstract, as published at the source. International Journal of Thermophysics, 2026 · DOI ↗
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Field: Catalysis
CatalysisChemical Engineering