Thermodynamics and phase equilibrium of the high concentration solid solution-aqueous solution system KCl–RbCl–H2O from T = 298.15 K to T = 323.15 K
- 1. National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190 (China)
- 2. Qinghai Institute of Salt Lakes, Chinese Academy of Sciences, Xining 810008 (China)
Description
Highlights: • The water activities of the solid solution-aqueous solution (SS-AS) system KCl–RbCl–H2O at T = 298.15 K and T = 323.15 K were measured by the isopiestic method. • The solubility of this ternary system have been measured with the Flow-Cloud-Point method at T = (298.15, 308.15 and 323.15) K. • The Pitzer model was selected to correlate the measured water activity and the solubility data. • The model calculated results indicate that the equilibrium solid phase in the ternary system is (K, Rb)Cl(ss) regular solid solution. • The Lippman log ∑ K − Xs − Xact and Φ ∑ m − Xs − Xaq equilibrium diagrams indicate again that the equilibrium solid phase was regular solid solution. - Abstract: Water activities of the high concentration solid solution-aqueous solution system (SS-AS) KCl–RbCl–H2O and its sub-binary systems at T = 298.15 K and T = 323.15 K have been elaborately measured by an isopiestic method. The solubility of this ternary system at T = (298.15, 308.15 and 323.15) K was also measured by a Flow-Cloud-Point method. A Pitzer model was used to estimate the reliability of the solubility reported in the literature, and to judge the type of solid phase, by correlating the measured water activity and the reported solubility values. The binary model parameters as a function of temperature between T = 298.15 K and T = 323.15 K were obtained by fitting the water activities in the binary systems. The predicted water activities at T = 298.15 K and T = 323.15 K with the obtained binary parameters only, are in good agreement with the experimental values, which indicate that the Pitzer model can reliably represent the properties of the ternary system, with binary parameters only within the temperature range from T = 298.15 K to T = 323.15 K. Under the different assumptions that the equilibrium solid phase involved the pure salts (KCl(s) and RbCl(s)) for the ideal solid solution or regular solid solution (K, Rb)Cl(ss), the solubility isotherms at T = (298.15, 308.15 and 323.15) K were calculated and compared to experimental results, respectively. It was found that only the calculated solubility isotherms for (K, Rb)Cl(ss) regular solid solution are consistent with the corresponding experimental values. The solid phase equilibrated with the aqueous solution in the KCl–RbCl–H2O ternary system should be a regular solid solution (K, Rb)Cl(ss). This conclusion also can be verified from the Lippman log ∑ K − Xs − Xact and Φ ∑ m − Xs − Xaq equilibrium diagrams.
Availability note (English)
Available from http://dx.doi.org/10.1016/j.jct.2016.12.003Additional details
Identifiers
- DOI
- 10.1016/j.jct.2016.12.003;
- PII
- S0021-9614(16)30400-1;
Publishing Information
- Journal Title
- Journal of Chemical Thermodynamics
- Journal Volume
- 106
- Journal Page Range
- p. 285-294
- ISSN
- 0021-9614
- CODEN
- JCTDAF
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 49002265
- Subject category
- S37: INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY; S36: MATERIALS SCIENCE;
- Resource subtype / Literary indicator
- Numerical Data
- Descriptors DEI
- AQUEOUS SOLUTIONS; EXPERIMENTAL DATA; POTASSIUM CHLORIDES; RUBIDIUM CHLORIDES; SOLID SOLUTIONS; SOLUBILITY; TEMPERATURE DEPENDENCE; TEMPERATURE RANGE 0273-0400 K
- Descriptors DEC
- ALKALI METAL COMPOUNDS; CHLORIDES; CHLORINE COMPOUNDS; DATA; DISPERSIONS; HALIDES; HALOGEN COMPOUNDS; HOMOGENEOUS MIXTURES; INFORMATION; MIXTURES; NUMERICAL DATA; POTASSIUM COMPOUNDS; POTASSIUM HALIDES; RUBIDIUM COMPOUNDS; RUBIDIUM HALIDES; SOLUTIONS; TEMPERATURE RANGE
Optional Information
- Copyright
- Copyright (c) 2016 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.