2019
DOI: 10.1021/acs.jced.9b00561
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Solubility Measurement and Thermodynamic Modeling of Solid–Liquid Equilibria in the MCl–M2B4O7–H2O (M = Li, Na) Systems

Abstract: The solubilities in the MCl–M2B4O7–H2O (M = Li, Na) systems at 323.15 K were studied with the isothermal solid–liquid equilibrium method. Both the phase diagrams in the above systems belong to the simple eutectic type. Combining the Pitzer binary parameters of LiCl and NaCl obtained from the literatures, the lacking Pitzer binary parameters of Li2B4O5(OH)4 and Na2B4O5(OH)4, Pitzer mixing parameters θCl–,B4O5(OH)4 2– , ψLi+,Cl–,B4O5(OH)4 2– , and ψNa+,Cl–,B4O5(OH)4 2– , and the solubility product constants of L… Show more

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Cited by 9 publications
(6 citation statements)
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“… a Standard uncertainties u are u ( T ) = 0.1 K, u ( p ) = 0.005 MPa, u ( w (LiCl)) = 0.003, u ( w (LiBO 2 )) = 0.005, and u ( w (Li 2 B 4 O 7 )) = 0.005. b w, mass fraction. c J, Jänecke index . d Abbreviations: LC: LiCl·H 2 O; LB: LiBO 2 ·2H 2 O; LB4: Li 2 B 4 O 7 ·3H 2 O. e The solubility data were cited from refs , , . …”
Section: Resultsmentioning
confidence: 99%
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“… a Standard uncertainties u are u ( T ) = 0.1 K, u ( p ) = 0.005 MPa, u ( w (LiCl)) = 0.003, u ( w (LiBO 2 )) = 0.005, and u ( w (Li 2 B 4 O 7 )) = 0.005. b w, mass fraction. c J, Jänecke index . d Abbreviations: LC: LiCl·H 2 O; LB: LiBO 2 ·2H 2 O; LB4: Li 2 B 4 O 7 ·3H 2 O. e The solubility data were cited from refs , , . …”
Section: Resultsmentioning
confidence: 99%
“…In Figures and , points A, B, and C are the co-saturation points in the systems LiCl–Li 2 B 4 O 7 –H 2 O, LiCl–LiBO 2 –H 2 O, and LiBO 2 –Li 2 B 4 O 7 –H 2 O. The solubility data for points A, B, and C were cited from the literature by our laboratory. ,, The dry-salt phase diagram in the quaternary system LiCl–LiBO 2 –Li 2 B 4 O 7 –H 2 O at 323.15 K in Figure has one invariant point E (LiCl·H 2 O, Li 2 B 4 O 7 ·3H 2 O, and LiBO 2 ·2H 2 O). The X-ray diffraction patterns of the invariant point E are given in Figure .…”
Section: Resultsmentioning
confidence: 99%
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“…The Pitzer electrolyte solution theory and Harvie–Weare (HW) equations (Pitzer model), , which is described in our previous study, , was widely used in the solubility calculation of the brine systems containing borate. ,, The concentration of various boron species can be calculated if the parameters and standard chemical potentials of boron species are known. In the literature, , the concentration of B­(OH) 3 , B­(OH) 4 – , B 3 O 3 (OH) 4 – , and B 4 O 5 (OH) 4 2– in the solution saturated with Na 2 B 4 O 5 (OH) 4 ·8H 2 O or NaB­(OH) 4 ·2H 2 O and solubilities in the system containing borate or B­(OH) 3 were calculated.…”
Section: Introductionmentioning
confidence: 99%
“…e phase equilibria of water-salt systems can supply theoretical basis for the development of salt lake brine resources [10]. erefore, the research on the phase equilibrium of the brine systems containing boron is meaningful to the comprehensive utilization and development of boron resources from brines [11].…”
Section: Introductionmentioning
confidence: 99%