Thermodynamic solid-liquid equilibrium model for mixed systems HF-NaF-H2O and HF-KF-H2O up to 2 m HF at T = 25 o C

In this study we developed thermodynamic models for solid-liquid equilibrium for mixed systems HF-NaF-H 2 O and HF-KF-H 2 O up to 2 m HF at T = 25 o C. Models are developed on the basis of Pitzer ion interactions approach. The recommendations on mean activity coefficients ( γ ± ) have been used to c...

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Veröffentlicht in:Acta Scientifica Naturalis 2023-03, Vol.10 (1), p.1-15
Hauptverfasser: Donchev, Stanislav, Tsenov, Tsvetan V., Christov, Christomir
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Sprache:eng
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Zusammenfassung:In this study we developed thermodynamic models for solid-liquid equilibrium for mixed systems HF-NaF-H 2 O and HF-KF-H 2 O up to 2 m HF at T = 25 o C. Models are developed on the basis of Pitzer ion interactions approach. The recommendations on mean activity coefficients ( γ ± ) have been used to construct the model for HF-H 2 O system. The models for binary systems NaF-H 2 O and KF-H 2 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 o sp ) 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 2 O and HF–NaF–H 2 O up to maximum HF molality of 2 mol·kg −1 . 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 2 O system used in parameterization are the main reason for concentration restriction of mixed HF models presented here.
ISSN:2603-347X
2603-347X
DOI:10.2478/asn-2023-0002