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
相关论文
共 50 条
  • [1] vapor-liquid equilibrium for the systems trans-2-butene plus methanol, plus 1-propanol,plus 2-propanol, plus 2-butanol, and plus 2-methyl-2-propanol at 364.5 K
    Roininen, Jonas
    Uusi-Kyyny, Petri
    Pokki, Juha-Pekka
    Pakkanen, Minna
    Alopaeus, Ville
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (02): : 607 - 612
  • [2] Isothermal vapor liquid equilibrium for 2-methylpropene plus methanol, plus 1-propanol, plus 2-propanol, plus 2-butanol, and plus 2-methyl-2-propanol binary systems at 364.5 K
    Hynynen, K
    Uusi-Kyyny, P
    Pokki, JP
    Pakkanen, M
    Aittamaa, J
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (02): : 562 - 568
  • [3] Vapor-liquid equilibrium for 1-butene plus methanol, plus 1-propanol, plus 2-propanol, plus 2-butanol, and 2-methyl-2-propanol (TBA) at 364.5 K
    Visuri, Olli
    Uusi-Kyyny, Petri
    Pokki, Juha-Pekka
    Pakkanen, Minna
    Alopaeus, Ville
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (08): : 1829 - 1835
  • [4] Vapour-liquid equilibrium for the systems butane plus methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5 K
    Dell'Era, Claudia
    Zaytseva, Anna
    Uusi-Kyyny, Petri
    Pokki, Juha-Pekka
    Pakkanen, Minna
    Aittamaa, Juhani
    FLUID PHASE EQUILIBRIA, 2007, 254 (1-2) : 49 - 59
  • [5] Vapor-liquid equilibrium for the systems 2-methylpropane plus methanol,plus 2-propanol,plus 2-butanol, and plus 2-methyl-2-propanol at 364.5 K
    Laavi, Helena
    Uusi-Kyyny, Petri
    Pokki, Juha-Pekka
    Pakkanen, Minna
    Alopaeus, Ville
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (04): : 913 - 918
  • [6] Mixing properties of the liquid systems methanol plus 2-propanol and 1-propanol plus 2-propanol
    Haase, R
    Tillmann, W
    ZEITSCHRIFT FUR PHYSIKALISCHE CHEMIE-INTERNATIONAL JOURNAL OF RESEARCH IN PHYSICAL CHEMISTRY & CHEMICAL PHYSICS, 1995, 192 : 121 - 131
  • [7] Vapour-liquid equilibrium for the 2-methylpropane plus methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15 K
    Ouni, T
    Zaytseva, A
    Uusi-Kyyny, P
    Pokki, JP
    Aittamaa, J
    FLUID PHASE EQUILIBRIA, 2005, 232 (1-2) : 90 - 99
  • [8] The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T=298.15 K
    Zafarani-Moattar, Mohammed Taghi
    Hosseinpour-Hashemi, Vahid
    Banisaeid, Sepideh
    Beirami, Mohammad Ali Shamsi
    FLUID PHASE EQUILIBRIA, 2013, 338 : 37 - 45
  • [9] Vapor-liquid Equilibrium for the cis-2-butene plus methanol, plus 2-propanol, plus 2-butanol, plus 2-Methyl-2-propanol systems at 364.5 K
    Wierink, Gijsbert
    Roininen, Jonas
    Uusi-Kyyny, Petri
    Pokki, Juha-Pekka
    Pakkanen, Minna
    Alopaeus, Ville
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (07): : 1539 - 1544
  • [10] Vapour-liquid equilibrium for the 1-butene plus methanol, plus ethanol, plus 2-propanol, plus 2-butanol and plus 2-methyl-2-propanol systems at 326 K
    Laakkonen, M
    Pokki, JP
    Uusi-Kyyny, P
    Aittamaa, J
    FLUID PHASE EQUILIBRIA, 2003, 206 (1-2) : 237 - 252