Thermodynamic modeling of aqueous Na+-K+-Cl--SO42- quaternary system with electrolyte NRTL model

被引:16
作者
Bhattacharia, Sanjoy K. [1 ]
Hossain, Nazir [1 ]
Chen, Chau-Chyun [1 ]
机构
[1] Texas Tech Univ, Dept Chem Engn, Lubbock, TX 79409 USA
关键词
Aqueous brine solution; Electrolyte NRTL model; Potassium sulfate; Solubility; Thermodynamic properties; MINERAL SOLUBILITIES; NA-K-CA-CL-SO4-H2O SYSTEM; OSMOTIC COEFFICIENTS; HIGH-TEMPERATURES; VAPOR-PRESSURES; CO2; ABSORPTION; NATURAL-WATERS; MDEA SOLUTION; PREDICTION; SULFATE;
D O I
10.1016/j.fluid.2015.05.045
中图分类号
O414.1 [热力学];
学科分类号
摘要
A comprehensive thermodynamic model based on electrolyte non-random two-liquid (eNRTL) equation is developed for aqueous Na+-K+-Cl--SO42- quaternary system. To account for the composition dependence of the solution nonideality, the eNRTL model requires two binary interaction parameters for each of the four electrolyte-water and four electrolyte-electrolyte pairs. We obtain the eNRTL binary parameters for (K+SO42-):H2O pair, (K+SO42-):(Ne+SO42-) pair and (K+ Cl-):(K+ SO42-) pair by regressing literature data. The eNRTL binary parameters for the other electrolyte-water and electrolyte-electrolyte pairs are retrieved from the literature. To account for the temperature dependence, each of the eNRTL binary parameter is correlated with a Gibbs-Helmholtz type expression with up to three temperature coefficients. The eNRTL model accurately represents various thermodynamic properties of the aqueous quaternary system and its subsystems with temperatures up to 473.15 K and electrolyte concentrations up to saturation. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 9
页数:9
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