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Tianlong Deng - One of the best experts on this subject based on the ideXlab platform.
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Solid–Liquid Phase Equilibria of the Quaternary System (Li2SO4 + Na2SO4 + MgSO4 + H2O) at 288.15 K: Experimental and Model Simulation
Journal of Chemical & Engineering Data, 2020Co-Authors: Shiqiang Wang, Yafei Guo, Fei Yuan, Xunian Han, Tianlong DengAbstract:Solubility data for the quaternary system (Li2SO4 + Na2SO4 + MgSO4 + H2O) is very important for the separation of Lithium Sulfate from the salt lake brines in Qaidam Basin. The experimental and cal...
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Solubilities, Densities and Refractive Indices in the Aqueous Quaternary System of Lithium Sulfate, Lithium Metaborate, and Lithium Carbonate at 288.15, 298.15, 308.15 K and 0.1 MPa
Journal of Chemical & Engineering Data, 2016Co-Authors: Yafei Guo, Lina Cao, Shiqiang Wang, Tianlong DengAbstract:Solubilities, densities and refractive indices of the aqueous quaternary system of Lithium Sulfate, Lithium metaborate, and Lithium carbonate at 288.15, 298.15, 308.15 K and 0.1 MPa were determined with isothermal dissolution method. According to the experimental results, the dry-salt phase diagrams, water-phase diagrams, and the diagrams of physicochemical properties including density, pH, and refractive index versus composition of Lithium Sulfate at three temperatures were plotted. In the dry-salt phase diagrams at three temperatures, there are four crystallization regions corresponding to Lithium metaborate octahydrate (LiBO2·8H2O, LB), Lithium carbonate (Li2CO3, LC), and Lithium Sulfate monohydrate (Li2SO4·H2O, LS), and three univariant-solubility curves corresponding to minerals of LS, LB, and LC, and one invariant point of three coexisted minerals (LS + LB + LC). A comparison of the phase diagrams at 288.15, 298.15, and 308.15 K shows that the areas of Lithium Sulfate monohydrate and Lithium metabor...
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Metastable phase equilibria for the ternary aqueous system of Lithium Sulfate and potassium Sulfate at T = 308.15 K: Experimental data and prediction using Pitzer model
Russian Journal of Inorganic Chemistry, 2016Co-Authors: Nan Zhang, Yafei Guo, Tianlong DengAbstract:The metastable solubilities and the physicochemical properties including density, refractive index, pH and conductivity in the ternary system (Li2SO4 + K2SO4 + H2O) at T = 308.15 K were determined experimentally using the isothermal evaporation method, and the metastable phase diagram and the physicochemical properties versus composition diagram were plotted. In the metastable phase diagram, there are two invariant points, three univariant curves and three crystallization regions corresponding to Lithium Sulfate monohydrate (Li2SO4 · H2O), double salt (K2SO4 · Li2SO4) and arcanite (K2SO4). It was found that the double salt of K2SO4·Li2SO4 belongs to the incongruent double salt, and the hydrate of Li2SO4 · H2O belongs to hydrate type I. On the basis of Pitzer model of the electrolyte solution theory, the mixing-ion parameter of θLi,K, \({\Psi _{Li,K,S{O_4}}}\) and the metastable equilibrium constants of the solid phases K2SO4, Li2SO4 · K2SO4 and Li2-SO4 · H2O at 308.15 K were obtained for the first time. The calculated metastable solubility data for this ternary system at 308.15 K agree well with the experimental values, and this result indicates that the mixing-ion parameters and the metastable equilibrium constants obtained in this work are reliable.
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metastable phase equilibria for the ternary aqueous system of Lithium Sulfate and potassium Sulfate at t 308 15 k experimental data and prediction using pitzer model
Russian Journal of Inorganic Chemistry, 2016Co-Authors: Nan Zhang, Yafei Guo, Tianlong DengAbstract:The metastable solubilities and the physicochemical properties including density, refractive index, pH and conductivity in the ternary system (Li2SO4 + K2SO4 + H2O) at T = 308.15 K were determined experimentally using the isothermal evaporation method, and the metastable phase diagram and the physicochemical properties versus composition diagram were plotted. In the metastable phase diagram, there are two invariant points, three univariant curves and three crystallization regions corresponding to Lithium Sulfate monohydrate (Li2SO4 · H2O), double salt (K2SO4 · Li2SO4) and arcanite (K2SO4). It was found that the double salt of K2SO4·Li2SO4 belongs to the incongruent double salt, and the hydrate of Li2SO4 · H2O belongs to hydrate type I. On the basis of Pitzer model of the electrolyte solution theory, the mixing-ion parameter of θLi,K, \({\Psi _{Li,K,S{O_4}}}\) and the metastable equilibrium constants of the solid phases K2SO4, Li2SO4 · K2SO4 and Li2-SO4 · H2O at 308.15 K were obtained for the first time. The calculated metastable solubility data for this ternary system at 308.15 K agree well with the experimental values, and this result indicates that the mixing-ion parameters and the metastable equilibrium constants obtained in this work are reliable.
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metastable phase equilibrium in the aqueous ternary system li2so4 mgso4 h2o at 323 15 k
Journal of Chemical & Engineering Data, 2011Co-Authors: Tianlong Deng, Dongchan LiAbstract:The metastable solubilities and physicochemical properties (densities and refractive index) of the aqueous ternary system (Li2SO4 + MgSO4 + H2O) at 323.15 K were determined by the isothermal evaporation method. According to the experimental results, the metastable phase diagram and the diagram of physicochemical properties versus composition were plotted. It was found that there are one eutectic point (Li2SO4·H2O + MgSO4·6H2O), two univariant curves, and two crystallization regions corresponding to Lithium Sulfate monohydrate (Li2SO4·H2O) and hexahydrite (MgSO4·6H2O) in the metastable ternary system. The system belongs to a simple eutectic type, and neither double salts nor solid solutions were found. It can be found that the solution density and refractive index of the metastable ternary system changed regularly with the content change of Lithium Sulfate, and all reach the maximum value at eutectic point. The calculated values of densities and refractive index with empirical equations are in good agreeme...
Teófilo A. Graber - One of the best experts on this subject based on the ideXlab platform.
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Modeling of the density, viscosity and electrical conductivity of aqueous solutions saturated in boric acid in presence of Lithium Sulfate or sodium Sulfate at 293.15 to 313.15 K
Fluid Phase Equilibria, 2021Co-Authors: Wilson Alavia, Jorge A. Lovera, Teófilo A. Graber, Daniela Azúa, Ismael SotoAbstract:Abstract The modeling of the density, viscosity and electrical conductivity of aqueous solutions saturated with boric acid, in the presence of sodium Sulfate or Lithium Sulfate, are presented. The salt concentrations range studied were from (0 to 3.3242) mol·kg−1 for sodium Sulfate and from (0 to 2.9336) mol·kg−1 for Lithium Sulfate at temperatures from (293.15 to 313.15) K and at 1 atm pressure. A model for the density was derived using the Pitzer model. The Eyring's absolute rate theory and the Pitzer model were combined to represent the viscosity. The Casteel-Amis equation was modified to describe the electrical conductivity with temperature and boric acid effects where necessary. The results showed that the models successfully represented the properties studied and are robust for estimation purposes within and beyond the experimental range studied. Also, it was found that short range interactions of boric acid, Sulfate, sodium and Lithium ions with water molecules are relevant to determine the volumetric and transport properties of these solutions and that the electrical conductivity is determined by charged species (Na+, SO42−, NaSO4−, HSO4− and Li+, SO42−, LiSO4−) and the solution viscosity; that is mainly influenced by these salts concentrations, boric acid solubility behavior with these salts and temperature. This is valuable information to improve the processes of boric acid production.
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Thermodynamic modeling of the solubility of boric acid in the systems boric acid + Lithium Sulfate + water, boric acid + sodium Sulfate + water and boric acid + potassium Sulfate + water at 293.15–313.15 K
Fluid Phase Equilibria, 2015Co-Authors: Wilson Alavia, Jorge A. Lovera, Teófilo A. GraberAbstract:Abstract In this contribution the experimental solubility of boric acid in sodium Sulfate aqueous solution was measured at different temperatures from (293.15 to 313.15) K, and Na2SO4 concentrations ranging from (0 to 3.3795) mol kg−1 H2O. The results were represented using an equation based on Pitzer model for the interactions of nonelectrolytes with electrolytes in aqueous solutions, given by Chanson and Millero (2006) [18]. The model parameter was estimated and validated estimating the solubility of boric acid in Lithium Sulfate, sodium Sulfate and potassium Sulfate aqueous solutions at different temperatures and salt concentrations. The model represented satisfactorily the data for the systems (SD = 0.033 mol kg−1 H2O for H3BO3 + Na2SO4 + H2O, SD = 0.020 mol kg−1 H2O for H3BO3 + Li2SO4 + H2O and SD = 0.030 mol kg−1 H2O for H3BO3 + K2SO4 + H2O). The model parameters are valid to maximum concentration of the salts, 3.380 mol kg−1 for Na2SO4, 3.149 mol kg−1 for Li2SO4 and 1.245 mol kg−1 for K2SO4 from 293.15 K to 313.15 K. Based on the results it was determined that Lithium Sulfate is a precipitant agent for boric acid and its behavior is attributed to the salting out effect of Li+ ion; sodium and potassium Sulfates increase the boric acid solubility; this salting in effect is due to the presence of Na+ and K+ ions. The presence of these salts can be unfavorable for the crystallization of boric acid due to the increase of solubility which decreases the supersaturation, therefore the yield of the process. Comparing the parameters for the system H3BO3 + Na2SO4 + H2O, H3BO3 + Li2SO4 + H2O and H3BO3 + K2SO4 + H2O, it was found that effect of these ions on the decreasing of the solubilty of boric acid in aqueous Sulfate solutions follows the order: Li+ > Na+ > K+, which can be attributed to the increase of their ionic radii, coordinated with 6 water molecules therefore the capacity to form hydration shells.
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liquid liquid equilibrium of the aqueous two phase system water peg 4000 Lithium Sulfate at different temperatures experimental determination and correlation
Journal of Chemical & Engineering Data, 2004Co-Authors: Teófilo A. Graber, And Maria E. Gálvez, Héctor R. Galleguillos, Javier AlvarezbenediAbstract:A study was made of the effect of temperature on the liquid−liquid equilibrium (LLE) in the aqueous biphasic system formed by Lithium Sulfate + polyethylene glycol 4000 + water at 5, 25, and 45 °C. The tie lines and binodal curves as well as the densities and refractive indexes were determined on solutions in equilibrium at each temperature. The LLE experimental data obtained were well correlated to the nonrandom two-liquid thermodynamic model for activity coefficients. When using data from seven equilibrium lines for each temperature, a mean deviation of 1.07% was obtained between experimental compositions and compositions calculated using the model.
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Liquid−Liquid Equilibrium of the Aqueous Two-Phase System Water + PEG 4000 + Lithium Sulfate at Different Temperatures. Experimental Determination and Correlation
Journal of Chemical & Engineering Data, 2004Co-Authors: Teófilo A. Graber, And Maria E. Gálvez, Héctor R. Galleguillos, Javier Álvarez-benedíAbstract:A study was made of the effect of temperature on the liquid−liquid equilibrium (LLE) in the aqueous biphasic system formed by Lithium Sulfate + polyethylene glycol 4000 + water at 5, 25, and 45 °C. The tie lines and binodal curves as well as the densities and refractive indexes were determined on solutions in equilibrium at each temperature. The LLE experimental data obtained were well correlated to the nonrandom two-liquid thermodynamic model for activity coefficients. When using data from seven equilibrium lines for each temperature, a mean deviation of 1.07% was obtained between experimental compositions and compositions calculated using the model.
Luis Antonio Minim - One of the best experts on this subject based on the ideXlab platform.
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Liquid−Liquid Phase Equilibrium of Triblock Copolymer F68, Poly(ethylene oxide)-b-poly(propylene oxide)-b-poly(ethylene oxide), with Sulfate Salts
Journal of Chemical & Engineering Data, 2010Co-Authors: João Paulo Martins, Luis Henrique Mendes Da Silva, Jane Sélia Dos Reis Coimbra, Maria Do Carmo Hespanhol Da Silva, Tonimar Domiciano Arrighi Senra, Guilherme Max Dias Ferreira, Luis Antonio MinimAbstract:Phase diagrams of aqueous two-phase systems (ATPS) composed of triblock copolymer (F68) 8460 g·mol−1, sodium Sulfate, Lithium Sulfate, zinc Sulfate, or ammonium Sulfate were determined at (278.2, 288.2, and 298.2) K. The temperature effect on the biphasic area is very small, indicating a strong entropic contribution associating to the phase separation. The ability of these four salts in inducing the formation of the ATPS with F68 followed the order: sodium Sulfate > zinc Sulfate > ammonium Sulfate > Lithium Sulfate.
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Partitioning of caseinomacropeptide in aqueous two-phase systems.
Journal of chromatography. B Analytical technologies in the biomedical and life sciences, 2007Co-Authors: César A Sodré Da Silva, Luis Antonio Minim, Jane S R Coimbra, Edwin E Garcia Rojas, Luis Henrique Mendes Da SilvaAbstract:This study evaluates the influence of type of salt and temperature on the partition coefficient of caseinomacropetide (CMP) to determine the best conditions for the recovery of CMP in aqueous two-phase systems (ATPS) composed by poly(ethylene glycol) (PEG) 1500 and an inorganic salt (potassium phosphate, sodium citrate, Lithium Sulfate or sodium Sulfate). In all systems, CMP presented affinity for the PEG-rich phase. The PEG1500+Lithium Sulfate showed the highest values of partitioning coefficient. In addition, thermodynamic parameters (DeltaH degrees , DeltaS degrees , DeltaG degrees) as a function of temperature, were calculated for the system PEG1500-sodium citrate at different PEG concentrations and the results imply thermodynamic differences between partitioning of CMP in this system.
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density electrical conductivity kinematic viscosity and refractive index of binary mixtures containing poly ethylene glycol 4000 Lithium Sulfate and water at different temperatures
Journal of Chemical & Engineering Data, 2007Co-Authors: Regina Maria Marques Da Silva, Edwin Garcia E Rojas, Luis Antonio Minim, Luis Henrique Mendes Da Silva, Jane Sélia Dos Reis Coimbra, Valeria Paula Rodrigues MinimAbstract:Kinematic viscosity, density, refractive index, and electrical conductivity of aqueous solutions of poly(ethylene glycol) and of Lithium Sulfate were experimentally determined at (278.1, 298.1, 308.1, and 318.1) K. The density and refractive index followed a linear behavior with temperature and solute concentration, but kinematic viscosity and electrical conductivity followed a nonlinear relationship. Models were fitted to the data, which gave good agreement with the experimental data.
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Equilibrium Data for PEG 4000 + Salt + Water Systems from (278.15 to 318.15) K
Journal of Chemical & Engineering Data, 2007Co-Authors: Carolina P. Carvalho, Luis Antonio Minim, Jane Sélia Dos Reis Coimbra, Isabele Andressa F. Costa, And Luís Henrique M. Silva, Maria Cristina MaffiaAbstract:Liquid−liquid equilibrium data of aqueous two-phase systems composed of PEG 4000 + sodium Sulfate, PEG 4000 + Lithium Sulfate, and PEG 4000 + potassium phosphate were determined from (278.15 to 318.15) K. When the temperature was increased, the slope of the tie line (STL) tended to increase, reducing the quantity of salt necessary for phase splitting. From (308.15 to 318.15) K, for the aqueous systems PEG 4000 + Lithium Sulfate or potassium phosphate, a small decrease of the STL was verified. In spite of producing a phase diagram with a larger biphasic area, the sodium Sulfate showed higher capability for inducing the phase splitting as compared to potassium phosphate and Lithium Sulfate.
Angel Carton - One of the best experts on this subject based on the ideXlab platform.
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Liquid−Liquid Equilibria for Aqueous Solutions of Lithium Sulfate or Lithium Formate and Triethylamine or Diisopropylamine
Journal of Chemical & Engineering Data, 2000Co-Authors: Angel Carton, Silvia Bolado, Mar MarcosAbstract:Measurements of liquid-liquid equilibria were performed in order to study the suitability of triethylamine and diisopropylamine for the extractive crystallization of Lithium Sulfate or Lithium formate from its aqueous solutions. In the temperature range studied, two liquid phases exist in all ternary-salt-saturated systems. Both amines selectively extract water from saturated Lithium Sulfate or Lithium formate solutions at low temperatures, causing salt crystals to precipitate. Ranges of possible crystallization temperatures are given for each system. The variation with temperature of the two liquid phases compositions allows the amine recovery from the mother liquor. In all cases, a regeneration temperature of 20 °C is chosen.
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Density, Viscosity, and Electrical Conductivity of Aqueous Solutions of Lithium Sulfate
Journal of Chemical & Engineering Data, 1995Co-Authors: Angel Carton, F. Sobron, Silvia Bolado, Jose I. GerbolesAbstract:The density, viscosity, and electrical conductivity of aqueous Lithium Sulfate solutions has been determined over the concentration range 0.4-3.2 m. This range covered both undersaturated and supersaturated solutions. Apparent molal volumes of electrolyte are given along with equations for the properties as a function of temperature and composition.
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Viscosity, Conductivity, and Refractive Index of Saturated Solutions of Lithium Sulfate + Water + Methanol
Journal of Chemical & Engineering Data, 1995Co-Authors: Angel Carton, F. Sobron, Silvia Bolado, Jose I. GerbolesAbstract:The viscosity, electrical conductivity, and refractive index of saturated solutions of Lithium Sulfate in water and water + methanol have been determined over the temperature range 283.15-313.15 K and in the mass fraction of methanol range 0-0.9. Equations are given for these properties as a function of temperature and the mass fraction of methanol.
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Composition and density of saturated solutions of Lithium Sulfate + water + ethanol
Journal of Chemical & Engineering Data, 1994Co-Authors: Angel Carton, F. Sobron, Silvia Bolado, Javier TabaresAbstract:The solubilities of Lithium Sulfate in water and in aqueous ethanol have been determined over the temperature range 283.15-323.15 K and at 0-0.6 mass fraction of ethanol. The densities of the saturated solutions are also reported. Equations are given for the solubility and the density of the saturated solutions as a function of temperature and mass fraction of ethanol
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composition and density of saturated solutions of Lithium Sulfate water ethanol
Journal of Chemical & Engineering Data, 1994Co-Authors: Angel Carton, F. Sobron, Silvia Bolado, Javier TabaresAbstract:The solubilities of Lithium Sulfate in water and in aqueous ethanol have been determined over the temperature range 283.15-323.15 K and at 0-0.6 mass fraction of ethanol. The densities of the saturated solutions are also reported. Equations are given for the solubility and the density of the saturated solutions as a function of temperature and mass fraction of ethanol
Dongchan Li - One of the best experts on this subject based on the ideXlab platform.
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metastable phase equilibrium in the aqueous ternary system li2so4 mgso4 h2o at 323 15 k
Journal of Chemical & Engineering Data, 2011Co-Authors: Tianlong Deng, Dongchan LiAbstract:The metastable solubilities and physicochemical properties (densities and refractive index) of the aqueous ternary system (Li2SO4 + MgSO4 + H2O) at 323.15 K were determined by the isothermal evaporation method. According to the experimental results, the metastable phase diagram and the diagram of physicochemical properties versus composition were plotted. It was found that there are one eutectic point (Li2SO4·H2O + MgSO4·6H2O), two univariant curves, and two crystallization regions corresponding to Lithium Sulfate monohydrate (Li2SO4·H2O) and hexahydrite (MgSO4·6H2O) in the metastable ternary system. The system belongs to a simple eutectic type, and neither double salts nor solid solutions were found. It can be found that the solution density and refractive index of the metastable ternary system changed regularly with the content change of Lithium Sulfate, and all reach the maximum value at eutectic point. The calculated values of densities and refractive index with empirical equations are in good agreeme...