Thermodynamic solid-liquid equilibrium model for mixed systems HF-NaF-H2O and HF-KF-H2O up to 2 m HF at T = 25oC
In this study we developed thermodynamic models for solid-liquid equilibrium for mixed systems HF-NaF-H O and HF-KF-H O up to 2 m HF at T = 25 C. Models are developed on the basis of Pitzer ion interactions approach. The recommendations on mean activity coefficients ( ) have been used to construct t...
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Veröffentlicht in: | Acta Scientifica Naturalis 2023-03, Vol.10 (1), p.1-15 |
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Hauptverfasser: | , , |
Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | In this study we developed thermodynamic models for solid-liquid equilibrium for mixed systems HF-NaF-H
O and HF-KF-H
O up to 2 m HF at T = 25
C. Models are developed on the basis of Pitzer ion interactions approach. The recommendations on mean activity coefficients (
) have been used to construct the model for HF-H
O system. The models for binary systems NaF-H
O and KF-H
O are taken from our previous study in the same journal [Donchev et al. ASN (2021) 8(2), 1-15]. To parameterize models for ternary systems we used the available solubility data, i.e. on the basis of solubility approach. The thermodynamic solubility products (as ln K
) of precipitating in mixed systems double salts [NaF.HF(cr), and KF.HF(cr)] have been determined on the basis of evaluated model ion interaction parameters and using experimental m(sat) solubility data. The model is in a good agreement with experimewnt solubility data in the systems HF–NaF–H
O and HF–NaF–H
O up to maximum HF molality of 2 mol·kg
. At higher acid molality the model predicts much higher solubility of double salts (NaF.HF(cr) and KF.HF(cr) for both mixed systems. It was concluded that not a correct raw data for binary HF–H
O system used in parameterization are the main reason for concentration restriction of mixed HF models presented here. |
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ISSN: | 2603-347X |
DOI: | 10.2478/asn-2023-0002 |