Solid-liquid phase equilibria of the quaternary system Na+//Cl-, NO3-, SO42--H2O at 358.15 K

被引:5
作者
Zhu, Li [1 ]
Ma, YuLong [1 ]
Ge, ShaoYing [1 ]
Wang, YuYu [1 ]
机构
[1] Ningxia Univ, Coll Chem & Chem Engn, State Key Lab High Efficiency Utilizat Coal & Gre, Helanshan Rd 539, Yinchuan 750021, Ningxia, Peoples R China
关键词
Phase equilibrium; Phase diagram; Crystallization region; Sodium nitrate; GASIFICATION WASTE-WATER; NA+; DESALINATION; POLLUTION; PHENOL; ACID;
D O I
10.1016/j.jct.2021.106658
中图分类号
O414.1 [热力学];
学科分类号
摘要
The stable (solid + liquid) phase equilibrium and the solution density of the quaternary system Na+//Cl-, NO3-, SO42--H2O and its subsystems at 358.15 K were determined by the isothermal solution saturation method and moist residues. All phase diagrams of ternary systems for Na+//Cl-, SO42--H2O, Na+//Cl-, NO3--H2O, Na+//NO3-, SO42--H2O at 358.15 K contain one invariant point, two invariant curves, and three crystallization regions. Neither double salt nor solid solution is found in the three ternary systems at 358.15 K. When NaCl, NaNO3, and Na2SO4 are analyzed as (7.02, 48.62, 1.58) wt %, respectively, the quaternary system Na+//Cl-, NO3-, SO42--H2O reach saturation at 358.15 K. The phase diagram of the quaternary system at 358.15 K includes one invariant point, three invariant curves, and three crystallization regions. The three crystallization regions correspond to NaCl, NaNO3, and Na2SO4 and the Na2SO4 crystallization region is much bigger than that of the other two salts. Moreover, using the "translation technology", the phase diagram of Na+//Cl-, SO42-, NO3--H2O system can be predicted and constructed. All experimental data, especially the crystalline regions, can provide the fundamental basis for the design and optimization of the crystallization process of NaCl, NaNO3, and Na2SO4 in coal chemical high salinity wastewater. (C) 2021 Elsevier Ltd.
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页数:12
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共 43 条
[1]   Use of evaporation ponds for brine disposal in desalination plants [J].
Ahmed, M ;
Shayya, WH ;
Hoey, D ;
Mahendran, A ;
Morris, R ;
Al-Handaly, J .
DESALINATION, 2000, 130 (02) :155-168
[2]   Substituting freshwater: Can ocean desalination and water recycling capacities substitute for groundwater depletion in California? [J].
Badiuzzaman, Pierre ;
McLaughlin, Eoin ;
McCauley, Darren .
JOURNAL OF ENVIRONMENTAL MANAGEMENT, 2017, 203 :123-135
[3]   Stable Phase Equilibria of the Quaternary System Na+//Cl-, NO3-, SO42--H2O at 353.15 K [J].
Bian, Chao ;
Chen, Hang ;
Song, Xingfu ;
Jin, Yan ;
Yu, Jianguo .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (09) :3305-3314
[4]   Solid-liquid equilibrium for the ternary systems (Na2CO3+ NaCl + H2O) and (Na2CO3+ Na2SO4+ H2O) at 313.15 K and atmospheric pressure [J].
Cao, Jing ;
Ren, Yongsheng ;
Yu, Bingjie ;
Qiu, Lingshu ;
Ma, FeiYan .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2019, 133 :181-193
[5]   Investigation of Solid-Liquid Equilibria on the Na+//CI-, NO3-, SO42--H2O System and the Na+//NO3-, SO42--H2O System at 313.15 K [J].
Cao, Jing ;
Ren, Yongsheng ;
Zhu, Qiunan ;
Ma, Yulong .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (03) :1209-1221
[6]   Solid-Liquid Equilibria for (NaNO3 + NaCl + H2O) and (NaNO3 + Na2CO3 + H2O) Systems at 313.15 K [J].
Cao, Jing ;
Ding, Manxin ;
Ren, Yongsheng .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (03) :884-894
[7]   Liquid-Liquid Equilibrium of Water+1-Butanol + Inorganic Salt Systems at 303.15, 313.15 and 323.15 K: Experiments and Correlation [J].
Chawong, Kanungnit ;
Daengpradab, Boonpradab ;
Rattanaphanee, Panarat .
JOURNAL OF SOLUTION CHEMISTRY, 2017, 46 (05) :1077-1091
[8]   Stable Solid Liquid Equilibrium of the Quaternary System Na+//Cl-, NO3-, and SO42--H2O at 333.15 K [J].
Chen, Hang ;
Bian, Chao ;
Bian, Jiawen ;
Song, Xingfu ;
Yu, Jianguo .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (08) :3569-3575
[10]   New Water Treatment Index System toward Zero Liquid Discharge for Sustainable Coal Chemical Processes [J].
Cui, Peizhe ;
Qian, Yu ;
Yang, Siyu .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2018, 6 (01) :1370-1378