Phase diagram construction and phase chemical analysis of crystallization process for the development of sodium sulfate subtype salt lake brine resources

被引:2
作者
Cui, Rui-Zhi [1 ,2 ]
Nie, Guo-Liang [1 ,2 ]
Yang, Qiu-Ye [1 ,2 ]
Li, Wu [1 ,2 ]
Li, Jun [1 ,2 ]
Zhang, Zhi-Hong [1 ,2 ]
机构
[1] Chinese Acad Sci, Qinghai Inst Salt Lakes, Key Lab Green & High End Utilizat Salt Lake Resour, Xining 810008, Peoples R China
[2] Qinghai Prov Key Lab Resources & Chem Salt Lake, Xining 810008, Peoples R China
基金
中国国家自然科学基金;
关键词
Thermodynamic Model; Solubility; Solid -liquid Phase Equilibrium; Phase diagram; Multi -Stage Freezing; Comprehensive utilization of brine resources; OSMOTIC COEFFICIENTS; LIQUID-EQUILIBRIA; AQUEOUS LITHIUM; THERMODYNAMICS; SYSTEM; ELECTROLYTES; LI+; 25-DEGREES-C; PREDICTION; EXTRACTION;
D O I
10.1016/j.ces.2024.120477
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In view of the composition characteristics of sodium sulfate subtype salt lake brine in Laguocuo, Xizang, and combined with local climate characteristics, the phase equilibria of reciprocal quinary system Li+, Na+, K+/Cl-, SO42--H2O, as well as all subsystems, were predicted under ten temperatures within the range of 248.15 similar to 348.15 K. The corresponding 3D phase diagrams were drawn, and the saturation projection planes and crystallization phase regions were disassembled and analyzed. The isothermal dissolution equilibrium method was used to study the stable phase equilibrium of two ternary subsystems (LiCl-NaCl-H2O and LiCl-KCl-H2O) in the temperature range of 253.15 to 348.15 K, and the comparison between experimental and calculated results verified the applicability of the model selected in this paper. Meanwhile, the isothermal evaporation routes of brine at different temperatures were predicted by using phase diagram of this reciprocal quinary system, and the rules of ion concentration and salt precipitation in liquid phase during isothermal evaporation were obtained. Based on theoretical predictions, and combined with local natural conditions, it is proposed to use multi-stage freezing to make mirabilite crystallize and precipitate from brine, reduce sulfate content in brine, change the composition of brine, and further to achieve comprehensive development and utilization of brine resources. Through the experiment of brine evaporation and theoretical calculations, the effects of freezing temperature and brine composition on solid phase compositions and sulfate removal rate were investigated, and a clean separation process of obtaining high-grade lithium and potassium salts was put forward. The research results of this paper will have important referential significance for guiding the development of brine resources in similar salt lakes.
引用
收藏
页数:25
相关论文
共 41 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]   TOWARDS THE EXTENSION OF UNIFAC TO MIXTURES WITH ELECTROLYTES [J].
CHRISTENSEN, C ;
SANDER, B ;
FREDENSLUND, A ;
RASMUSSEN, P .
FLUID PHASE EQUILIBRIA, 1983, 13 (OCT) :297-309
[3]   INVESTIGATION OF THE AQUEOUS LITHIUM AND MAGNESIUM HALIDE-SYSTEMS [J].
CHRISTOV, C ;
BALAREW, C ;
PETRENKO, S ;
VALYASHKO, V .
JOURNAL OF SOLUTION CHEMISTRY, 1994, 23 (05) :595-604
[4]   (Solid plus liquid) phase equilibria in the quaternary systems LiCl-Li2SO4-MgCl2-MgSO4-H2O and KCl-K2SO4-MgCl2-MgSO4-H2O at 288.15 K [J].
Cui, Rui-Zhi .
JOURNAL OF MOLECULAR LIQUIDS, 2020, 319
[5]   Mineral solubilities of salts in the three quaternary systems: LiCl-NaCl-MgCl2-H2O, LiCl-KCl-MgCl2-H2O and Li2SO4-K2SO4-MgSO4-H2O at 288.15 K [J].
Cui, Rui-Zhi ;
Li, Wu ;
Dong, Ya-Ping ;
Nie, Zhen .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2019, 138 :127-139
[6]   Solubility measurement and prediction of phase equilibria in the quaternary system LiCl plus NaCl + KCl + H2O and ternary subsystem LiCl + NaCl + H2O at 288.15 K [J].
Cui, Ruizhi .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2020, 28 (08) :2137-2141
[7]   Measurements and Calculations of Solid-liquid Equilibria in Quaternary System Li2SO4-Na2SO4-K2SO4-H2O at 288 K [J].
Cui Ruizhi ;
Yang Lei ;
Wang Wei ;
Sang Shihua .
CHEMICAL RESEARCH IN CHINESE UNIVERSITIES, 2017, 33 (03) :460-465
[8]   Solubilities for six ternary systems:: NaCl+NH4Cl+H2O, KCl+NH4Cl+H2O, NaCl+LiCl+H2O, KCl+LiCl+H2O, NaCl+AlCl3+H2O, and KCl+AlCl3+H2O at T = (298 to 333) K [J].
Farelo, F ;
Fernandes, C ;
Avelino, A .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (04) :1470-1477
[9]  
Fu Z.H., 2013, Inorganic Chemicals Industry, V45, P29
[10]   LIQUID-VAPOR EQUILIBRIUM OF AQUEOUS LITHIUM-CHLORIDE, FORM 25DEGREES TO 100DEGREESC AND FROM 1.0 TO 18.5 MOLAL, AND RELATED PROPERTIES [J].
GIBBARD, HF ;
SCATCHAR.G .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1973, 18 (03) :293-298