无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ
研究与开发

水盐体系汽液平衡的热力学模型研究

  • 刘治国 ,
  • 张娜 ,
  • 陈川 ,
  • 徐显朕
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  • 1.海军航空大学青岛校区,山东青岛 266000
    2.青岛大学化学化工学院
刘治国(1976—),男,博士,副教授,主要研究方向:化工热力学,金属材料环境适应性研究,电化学腐蚀特性分析;E-mail: qdnuaalzg@163.com

收稿日期: 2020-10-19

  网络出版日期: 2021-08-11

Study on thermodynamic model of vapor-liquid equilibrium of electrolyte system

  • Zhiguo Liu ,
  • Na Zhang ,
  • Chuan Chen ,
  • Xianzhen Xu
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  • 1. Navel Aeronautical University,Qingdao Branch,Qingdao 266000,China
    2. College of Chemistry and Chemical Engineering,Qingdao University

Received date: 2020-10-19

  Online published: 2021-08-11

摘要

水盐体系的相平衡性质是化工单元操作的基础,在化学化工、海洋、地质等领域有着重要的研究价值。国内外许多学者对水盐体系汽液平衡进行了实验和理论的研究,构筑了各具特色的经验和半经验的模型。针对水盐体系,在NRTL理论的基础上,基于水化作用和混合盐假设建立了能够预测混合体系汽液平衡的活度系数扩展模型。通过对21组二元水盐体系和14组混合体系的关联计算,验证了该模型的可行性;同时,该模型可以采用二元体系参数直接预测计算混合水盐体系汽液平衡。

本文引用格式

刘治国 , 张娜 , 陈川 , 徐显朕 . 水盐体系汽液平衡的热力学模型研究[J]. 无机盐工业, 2021 , 53(8) : 55 -59 . DOI: 10.19964/j.issn.1006-4990.2020-0562

Abstract

The phase equilibrium of electrolyte solution systems is the basis of chemical unit operation,and has important research value in in the fields of chemistry and chemical engineering,oceanography,geology and so on.Scholars at home and abroad have studied the experiment and theory on the vapor-liquid equilibrium for electrolyte solution system,and developed the empirical and semi-empirical models with their own characteristics.The extended activity coefficient model with prediction was established in this article,and the model was based on the NRTL theory and the hypothesis of hydration and mixed salt.The feasibility of the model was verified by the correlation calculation of 21 binary electrolyte systems and 14 mixed systems.In addition,the binary system parameters could be used to directly predict the vapor-liquid equilibrium of the mixed electrolyte solution system.

参考文献

[1] Robinson R A, Stokes R H. Electrolyte Solutions[M].2nd ed. London: Courier Dover Publications, 2002.
[2] Patil K R, Tripathi A D, Pathak G, Katti S S. Thermodynamic proper-ties of aqueous electrolyte solutions,vapor pressure of aqueous so-lutions of sodium bromide,sodium iodide,potassium chloride,pota-ssium bromide,potassium iodide,rubidium chloride,cesium chlo-ride,cesium bromide,cesium iodide,magnesium chloride,calcium chloride,calcium bromide,calcium iodide,strontium chloride,st-rontium bromide,strontium iodide,barium chloride,and barium bromide[J]. Journal of Chemical and Engineering Data, 1991, 36:225-230.
[3] Dinane A, Guendouzi M E, Mounir A. Hygrometric determination of water activities,osmotic and activity coefficients of (NaCl+KCl)(aq) at T=298.15 K[J]. Journal of Chemical Thermodynamics, 2002, 34:423-441.
[4] Kolár P, Nakata H, Tsuboi A, et al. Measurement and modeling of vapor-liquid equilibria at high salt concentrations[J]. Fluid Phase Equilibria, 2005, 228:493-497.
[5] Apelblat A, Korin E. Temperature dependence of vapor pressures over saturated aqueous solutions at invariant points of the NaCl+KCl+H2O,NaCl+NaNO3+H2O,KCl+KBr+H2O,KCl+KI+H2O,KCl+KNO3+H2O,and KCl+K2SO4+H2O systems[J]. Journal of Chemical and Engineering Data, 2009, 54:1619-1624.
[6] Chen C C, Britt H I, Boston J F. Extension and application of the pi-tzer equation for vapor-liquid equilibrium of aqueous electrolyte systems with molecular solutes[J]. AIChE Journal, 1979, 25(5):820-831.
[7] Pitzer K S. Thermodynamics of electrolytes,I.Theoretical basis and general equations[J]. Journal of Physical Chemistry, 1973, 77(2):268-277.
[8] Clegg S L, Pitzer K S. Thermodynamics of multicomponent,miscible,ionic solutions:Generalize equations for symmetrical electrolytes[J]. Journal of Physical Chemistry, 1992, 96(8):3513-3520.
[9] Chen C C, Britt H I, Boston J F, et al. Local composition model for excess Gibbs energy of electrolyte systems; part Ⅰ:Single solvent,single completely dissociated electrolyte systems[J]. AIChE Journal, 1982, 28(4):588-596.
[10] Chen C C, Evans L B. A local composition model for the excess gi-bbs energy of aqueous electrolyte systems[J]. AIChE Journal, 1986, 32(3):444-454.
[11] Lu X H, Maurer G. Model for describing activity coefficients in mi-xed electrolyte aqueous solutions[J]. AIChE Journal, 1993, 39(9):1527-1538.
[12] Lu X, Zhang L, Wang Y, et al. Prediction of activity coefficients of electrolytes in aqueous solutions at high temperatures[J]. Indus-trial & Engineering Chemistry Research, 1996, 35(5):1777-1784.
[13] Wang P, Anderko A, Young R D. A speciation-based model for mi-xed-solvent electrolyte systems[J]. Fluid Phase Equilibria, 2002, 203(1/2):141-176.
[14] Thomsen K, Rasmussen P. Modeling of vaporliquid-solid equilibri-um in gas-aqueous electrolyte systems[J]. Chemical Engineering Science, 1999, 54(12):1787-1802.
[15] Renon H, Prausnitz J M. Local compositions in thermodynamic ex-cess functions for liquid mixtures[J]. AIChE Journal, 1968, 14(1),135-144.
[16] Xu X, Wang Y, Sun X, et al. Vapor-liquid equilibria study of LiCl+CaCl2+H2O system[J]. ACS Omega, 2019(4):4390-4396.
[17] Platford R F. Osmotic coefficients of aqueous solutions of seven co-mpounds at 0 deg[J]. Journal of Chemical and Engineering Data, 1973, 18(2):215-217.
[18] Xu X, Hu Y, Wu L, et al. Experimental and modeling of vapor-liquid equilibria for electrolyte solution systems[J]. Journal of Chemical and Engineering Data, 2014, 59(11):3741-3748.
[19] Xu X, Hu Y, Wang X, et al. Experimental and modeling of vapor-liquid equilibria for mixed electrolyte solution systems[J]. Journal of Chemical and Engineering Data, 2016, 61(7):2311-2320.
[20] Wu Y C, Rush R M, Scatchard G. Osmotic and activity coefficients for binary mixtures of sodium chloride,sodium sulfate,magnesium sulfate,and magnesium chloride in water at 25 deg.I.Isopiestic mea-surements on the four systems with common ions[J]. Journal of Phy-sical Chemistry, 1968, 72:4048-4053.
[21] Wu Y C, Rush R M, Scatchard G. Osmotic and activity coefficients for binary mixtures of sodium chloride,sodium sulfate,magnesium sulfate,and magnesium chloride in water at 25 deg.Ⅱ.Isopiestic and electromotive force measurements on the two systems without common ions[J]. Journal of Physical Chemistry, 1969, 73:2047-2053.
[22] Saad D, Padova J, Marcus Y. Thermodynamics of mixed electrolyte solutions.Ⅵ.An isopiestic study of a pseudo-ternary system:NaCl-KCl-MgCl2·H2O at 25 ℃[J]. Journal of Solution Chemistry, 1975(4):983-993.
[23] Padova J, Saad D, Rosenzweig D. Thermodynamics of mixed elec-trolyte solutions.X.An isopiestic study of the uaternary system NaCl-KCl-MgCl2·H2O at 25 ℃[J]. Journal of Solution Chemistry, 1977(6):309-325.
[24] Saad D, Padova J. Thermodynamics of mixed electrolyte solutions.Ⅸ.Calculation of the osmotic and activity coefficients in a pseudo-ternary system(NaCl-nKCl)-MgCl2-H2O at 298.15 K[J]. Journal of Solution Chemistry, 1977(6):191-201.
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