The isopiestic molalities for the systems LiBr-HO,CaBr-HO and LiBr-CaBr-HO were measured at 373.15 K with the isopiestic method using the Oak Ridge National Laboratory(ORNL)high-temperature gravimetric isopiestic appa...
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The isopiestic molalities for the systems LiBr-HO,CaBr-HO and LiBr-CaBr-HO were measured at 373.15 K with the isopiestic method using the Oak Ridge National Laboratory(ORNL)high-temperature gravimetric isopiestic apparatus[1].The osmotic coefficients and water activities were determined based on the lithium chloride,calcium chloride and sodium chloride reference *** behavior of the osmotic coefficients and the saturated vapor pressure for the ternary system as a function of molality was demonstrated.A chemical model for the LiBr-HO system that calculates solute and water activities,and solid-liquid equilibria from 273.15 to 523.15 K,was constructed by combining our experimental results with other experimental data available in the literature[2].The mixed ion-interaction parameters of θ and Ψ were fitted for ionic strengths to 36.0 mol·kg by using the least-square *** calculated osmotic coefficients for the ternary system agree well with the experimental *** thermodynamic data obtained in this study are essential for development of universal thermodynamic models for brine systems containing lithium bromide and calcium bromide.
Lithium borates not only occupy an important position in the modern inorganic industry,but also have been widely used in agriculture,metal smelting and chemical analysis for their excellent characteristics [1].In the ...
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Lithium borates not only occupy an important position in the modern inorganic industry,but also have been widely used in agriculture,metal smelting and chemical analysis for their excellent characteristics [1].In the west of china,some salt-lake brines contain abundant lithium and boron,and consist of several types of hydrated lithium borates *** to the complex structure of lithium borates,it is highly desirable to study the thermodynamic properties and behaviors of its aqueous electrolyte solution,and fully understand ion-interactions among each *** this work,water activities and osmotic coefficients for the ternary system(LiBO + LiBO + HO) and its subsystem at 288.15 K with various ionic strength 0.056-0.566 mol·kg were measured using an improved isopiestic *** experimental results were treated by the Pitzer ion-interaction model,then,a serious of parameters were obtained to describe the model.
The phase diagram of the system LiCl+NaCl+KCl+HO is of great importance to the process of extracting LiCl from nature *** this work,the complete phase diagram of the system LiCl+NaCl+KCl+HO at 298.15(shown in Fig.1a) ...
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The phase diagram of the system LiCl+NaCl+KCl+HO is of great importance to the process of extracting LiCl from nature *** this work,the complete phase diagram of the system LiCl+NaCl+KCl+HO at 298.15(shown in Fig.1a) and 323.15 K(shown in Fig.1b) were predicted by Pitzer-Clegg- Simmoson(PSC) *** standard water activity and solubility data of binary systems LiCl+HO,NaCl+HO,KCl+HO and solubility data of ternary systems NaCl+KCl+HO, LiCl+KCl+HO,LiCl+NaCl+HO were fitted to obtain PSC model *** the solubility and water activity of three ternary systems NaCl+KCl+HO,LiCl+KCl+HO,LiCl+NaCl+HO and quaternary system LiCl+NaCl+KCl+HO were predicted over a wide range of temperature with the binary and ternary model ***,the experimental data of solubility and water activity of the system and sub-ternary system of LiCl+NaCl+KCl+HO was evaluated by checking the consistency of predicted data with the experimental *** predicted phase diagram proved to be trustworthy and reliable for the industrial process design of extracting LiCl from nature brine.
The thermodynamic properties of the ternary system Mg Cl2-Na Cl-H2 O are instructive for magnesium chloride purification from crude bischofite in salt lakes. According to our experience, the sodium content in bischofi...
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The thermodynamic properties of the ternary system Mg Cl2-Na Cl-H2 O are instructive for magnesium chloride purification from crude bischofite in salt lakes. According to our experience, the sodium content in bischofite cannot be decreased by recrystallization method. In order to explain this abnormal phenomenon, we need profound understanding the multi-temperature phase diagram of the ternary system Mg Cl2-Na Cl-H2 O. Since the crystallization field of Mg Cl2·6H2O is very narrow, the determination of the eutectic line between the Mg Cl2·6H2O and Na Cl phases is a challenge. Although a lot of solubility experiments have been reported by many authors, a great discrepancy exists among them. So we determined the water activities of the system Mg Cl2-Na Cl-H2 O at 323.15 and 348.15 K, and constructed the phase diagrams and the eutectic line between the Mg Cl2·6H2O and Na Cl phases of the system Mg Cl2-Na Cl-H2 O with the Pitzer’s ion interaction model from 298.15 K to 373.15 K, as shown in Figure 1. We carried out purification test using a new fractional crystallization method according to the simulated results, the sodium content in bischofite decreased from 1.21 % to 0.17 %.
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