期刊
FLUID PHASE EQUILIBRIA
卷 537, 期 -, 页码 -出版社
ELSEVIER
DOI: 10.1016/j.fluid.2021.112989
关键词
electrolyte thermodynamics; solubility product; ionic liquids; predictions; Bjerrum; Born
资金
- German Science Foundation (DFG) within the priority program SPP 1708 Material Synthesis Near Room Temperature [HE 7165/7-1]
The application of electrolyte thermodynamic models in non-aqueous systems can help reduce experimental efforts and gain insights into molecular interactions, particularly valuable for designing advanced battery electrolytes.
The applications of electrolyte thermodynamic models to non-aqueous systems is of great value to reduce experimental effort and gain inside into molecular interactions. A large-scale application is for example the design of advanced battery electrolytes. For non-aqueous electrolyte systems, the Born term was found to be important, as it accounts for the transfer of ions from water into non-aqueous medium. In part one of this study [Bulow et al., Fluid Phase Equilibria 2021, 112967] the Born term was combined with a concentration-dependent dielectric constant within the ePC-SAFT framework (electrolyte Perturbed-Chain Statistical Associating Fluid Theory). In the present work, the Bjerrum treatment for ion pairing was included in the Debye-Huckel framework within ePC-SAFT. The approach was validated by experimental data for the dissociation of salts in organic solvents derived from conductivity measurements. Further, solubility was modeled of alkali halides in organic solvents and in ionic liquids. Modeling solubility required access to the solubility product K-SP, which does not depend on the solvent. The approach within this work was to first determine K-SP using experimental solubility data in water and the respective ePC-SAFT predicted activity coefficients prior to predict activity coefficients in non-aqueous medium, finally yielding solubility. The so-determined solubility values were found to be in reasonable agreement with the experimental data without fitting model parameters to any data of the non-aqueous solutions. The solubility product requires the solid form of the precipitating salt to be equal for all solvents; as alkali salts precipitate from aqueous solutions as hydrates, the method cannot be applied. Therefore, a methodology is presented to extrapolate the high-temperature K-SP of anhydrates to lower temperature. Using the so-extrapolated K-SP allowed predicting solubility of non-solvates in other solvents. (C) 2021 Elsevier B.V. All rights reserved.
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