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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2011, Vol. 5 Issue (3): 343-348   https://doi.org/10.1007/s11705-010-1029-0
  RESEARCH ARTICLE 本期目录
Caloric evaporation of the brine in Zangnan Salt Lake
Caloric evaporation of the brine in Zangnan Salt Lake
Shiqiang WANG1, Yafei GUO1, Nan ZHANG2, Lingzhong BU3, Tianlong DENG1,3,4(), Mianping ZHENG3
1. Tianjin Key Laboratory of Marine Resources and Chemistry, Tianjin University of Science and Technology, Tianjin 300457, China; 2. Tianjin Centre of China Geological Survey at CGS, Tianjin 300170, China; 3. Key Laboratory of Saline Lake Resources and Environment in Ministry of Land and Resources, Institute of Mineral Resources at Chinese Academy of Geological Sciences, Beijing 100037, China; 4. CAS Key Laboratory of Salt Lake Resources and Chemistry, Qinghai Institute of Salt Lakes at CAS, Xining 810008, China
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Abstract

Zangnan Salt Lake on the south of the Tibet is a type of carbonate lake with high concentrations of lithium, boron, and potassium and obviously it differs from seawater in its chemical composition. An experimental simulation of the caloric evaporation of the lake’s brine was conducted by first freezing the brine and then performing isothermal evaporation at 288.15 K. The freezing path and the physicochemical properties of the brine were determined. The crystallization sequence was natron, hydrohalite, halite, sylvite, zabuyelite, trona, aphthitalite, thermonatrite, and borax. Rubidium and cesium salts did not crystallized out but concentrated in the mother solution. The physicochemical properties (density, refractive index, conductivity, and pH) of the liquid phase changed as the evaporation progressed. In the beginning of the evaporation processes, the concentration of potassium ions in the liquid phase gradually increased but later it decreased. A peak value of 55.21 g/L was obtained when the evaporation was 88% complete. When the mineral aphthitalite began to crystallize; the concentrations of B2O3, Li+, Rb+, and Cs+ gradually increased as the evaporation progressed. When the evaporation was 98% complete, their concentrations in the mother liquor were 40.77 g/L, 4.838 g/L, 400.17 mg/L and 31.95 mg/L, respectively. This essential fundamental study can provide an important reference for the comprehensive utilization of brines in Zangnan Salt Lake.

Key wordsZangnan Salt Lake    evaporation    crystallization path    freezing
收稿日期: 2010-12-28      出版日期: 2011-09-05
Corresponding Author(s): DENG Tianlong,Email:tldeng@tust.edu.cn   
 引用本文:   
. Caloric evaporation of the brine in Zangnan Salt Lake[J]. Frontiers of Chemical Science and Engineering, 2011, 5(3): 343-348.
Shiqiang WANG, Yafei GUO, Nan ZHANG, Lingzhong BU, Tianlong DENG, Mianping ZHENG. Caloric evaporation of the brine in Zangnan Salt Lake. Front Chem Sci Eng, 2011, 5(3): 343-348.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-010-1029-0
https://academic.hep.com.cn/fcse/CN/Y2011/V5/I3/343
No.Evaporation /%Chemical components of the liquid phases
Concentration /(g·L-1)Concentration /(mg·L-1)Ja?necke index Jb /mol·(100 mol dry salt)-1
Li+Na+K+Mg2+Cl-SO42-B2O3CO32-HCO3-Rb+Cs+2K+CO32-SO42-
L00.000.26157.2410.040.1069.355.512.7119.392.2221.541.19024.3664.7610.88
L15.100.27354.9810.700.1168.756.272.8715.734.5925.131.5727.2659.7313.00
L263.170.629134.9923.630.06171.0913.306.4637.936.8161.963.9026.7760.9612.27
L378.300.907132.1537.620.06164.0520.6210.0247.793.2193.525.8931.6854.1814.13
L488.431.463136.9255.210.06146.8824.3616.9180.121.21167.3210.7530.6358.3711.00
L593.912.961146.0655.860.03139.8219.9625.07104.580.35175.0011.4426.7765.447.79
L698.314.838137.8751.510.03131.6417.2840.77100.660.02400.1731.9526.1866.677.15
Tab.1  
No.Chemical components of solid phase /%Solid phase
Li+K+Na+Cl-SO42-B2O3CO32-HCO3-Rb+Cs+
S10.00120.001477.941.450.940.03218.041.591.56 × 10-71.03 × 10-8NaCO3·10H2O+ NaCl·2H2O
S 20.620.9475.6221.310.590.380.540.002.60 × 10-61.62 × 10-7NaCl+ KCl+ Li2CO3
S30.0571.2167.1925.390.400.0573.263.545.18 × 10-73.42 × 10-8NaCl+ KCl+ NaCO3·NaHCO3·2H2O
S40.553.2938.850.824.340.101.031.072.64 × 10-69.38 × 10-9NaCl+ NaCO3·NaHCO3·2H2O+ Li2CO3 + Na2SO4·3K2SO4
S50.2811.4340.1835.935.140.354.640.359.87 × 10-61.70 × 10-7NaCl+ NaCO3·H2O+ Na2SO4·3K2SO4
S60.319.9846.4229.844.983.15.370.001.84 × 10-55.27 × 10-7NaCl+ NaCO3·H2O+ Na2SO4·3K2SO4 + Na2B4O7·10H2O
Tab.2  
Fig.1  
ExperimentTemperature /KStageSequence of salt precipitation
Refrigeration263.15L0-L1/S1NaCO3·10H2O+ NaCl·2H2O
Isothermal evaporation288.15L2/S2NaCl+ KCl+ Li2CO3
288.15L3/S3NaCl+ KCl+ NaCO3·NaHCO3·2H2O
288.15L4/S4NaCl+ NaCO3·NaHCO3·2H2O+ Li2CO3 + Na2SO4·3K2SO4
288.15L5/S5NaCl+ NaCO3·H2O+ Na2SO4·3K2SO4
288.15L6/S6NaCl+ NaCO3·H2O+ Na2SO4·3K2SO4 + Na2B4O7·10H2O
Tab.3  
Fig.2  
No.Evaporation /%Salinity /(g·L-1)Density ρ /(g·cm-3)pHnDConductivity κ /(S·m-1)
L00.00166.721.10339.261.355114.01
L1/S15.10164.161.11159.641.358213.77
L2/S263.17394.841.26509.641.389020.28
L3/S378.30416.371.28239.911.391519.33
L4/S488.43463.071.311810.571.397016.38
L5/S593.91494.661.349811.051.400512.92
L6/S698.31484.591.395711.891.40818.64
Tab.4  
Fig.3  
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