Liquid-liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite plus water aqueous two phase systems

被引:29
|
作者
Nemati-Kande, Ebrahim [2 ]
Shekaari, Hemayat [1 ]
Jafari, Safar A. [1 ]
机构
[1] Univ Tabriz, Dept Phys Chem, Fac Chem, Tabriz 51664, Iran
[2] Islamic Azad Univ, Dept Chem, Fac Sci, Parsabad Mogan Branch, Parsabad, Iran
关键词
Liquid-liquid equilibria; Alcohol; Sodium sulfite; Cloud point; Wilson equation; EXCESS GIBBS ENERGY; AQUEOUS-SOLUTIONS; PLUS WATER; PHASE-EQUILIBRIA; ELECTROLYTE SYSTEMS; WILSON MODEL; SOLVENT; THERMODYNAMICS; POTASSIUM; MIXTURES;
D O I
10.1016/j.fluid.2012.05.012
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water ternary systems was studied at T = 298.15 K. Both binodal curves and tie-line compositions for the studied systems at T = 298.15 K were also reported. Furthermore, cloud-point data as a function of alcohol mole fraction at the temperature range of T = 293.15-323.15 K was measured to study the effect of temperature. Effect of different alcohols and different anions were also studied considering the intermolecular interaction. Also, the use of the Setschenow-type equations to study the slating-out effect of the mentioned ATPSs was discussed. Additionally, the segment based Wilson equation was generalized to represent the mixed organic-aqueous solvent electrolyte systems and successfully used for the correlation of binary and ternary data. The restricted binary interaction parameters were also reported. The result of the generalized Wilson model in the correlation of the tie-line compositions was compared with the e-NRTL model. The obtained results show that the simpler generalized Wilson equation can represent the tie-line compositions better than the e-NRTL model. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 54
页数:13
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