Tie line data for the (water plus butyric acid plus n-butyl alcohol or amyl alcohol) at T = ( 298.2, 308.2, and 318.2) K and ( water plus butyric acid plus isoamyl alcohol) at T=298.2

被引:13
|
作者
Gilani, A. Ghanadzadeh [1 ]
Gilani, H. Ghanadzadeh [2 ]
Amouzadeh, F. [1 ]
机构
[1] Univ Guilan, Dept Chem, Rasht, Iran
[2] Univ Guilan, Dept Chem Engn, Rasht, Iran
来源
关键词
Butyric acid; LLE data; Ternary mixture; NRTL model; UNIQUAC model; LIQUID-LIQUID EQUILIBRIA; TERNARY-SYSTEM; AQUEOUS-SOLUTIONS; PHASE-EQUILIBRIA; ACETIC-ACID; FERMENTATION; CYCLOHEXANE; EXTRACTION; TOLUENE; TEMPERATURE;
D O I
10.1016/j.jct.2013.11.028
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this study, solubility and tie-line data of the (water + butyric acid + n-butyl alcohol or amyl alcohol) ternary systems were determined at T = (298.2, 308.2, and 318.2) K and p = 101.3 kPa for the first time. Due to the structural similarity, the tie-line data for (water + butyric acid + isoamyl alcohol) system were also measured and correlated at T = 298.2 K. The ternary systems investigated display type-1 behaviour of LLE. The cloud point method was used to measure the solubility data and the Karl-Fischer, acidimetric titration, and refractive index methods were used to determine the tie-line data. For each system, the experimental tie-line data were correlated using the UNIQUAC and NRTL models. The Othmer-Tobias and Hand correlations equations were used to establish the quality of the LLE data. Experimental distribution coefficients and separation factors were evaluated over the immiscibility regions. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:103 / 111
页数:9
相关论文
共 50 条
  • [31] Phase equilibria of water plus 1-propanol plus solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T=298.2 K
    Ozmen, Dilek
    Cehreli, Suheyla
    FLUID PHASE EQUILIBRIA, 2007, 253 (01) : 61 - 66
  • [32] Phase equilibria for ternary liquid systems of (water plus levulinic acid plus cyclic solvent) at T=298.2 K:: Thermodynamic modeling
    Senol, A
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2005, 37 (10): : 1104 - 1110
  • [33] Phase equilibria of (water plus propionic acid or butyric acid+2-methoxy-2-methylpropane) ternary systems at 298.2 K and 323.2 K
    Luo, Liejin
    Liu, Dong
    Li, Libo
    Chen, Yun
    FLUID PHASE EQUILIBRIA, 2015, 403 : 30 - 35
  • [34] Phase equilibria of (water plus butyric acid plus butyl acetate) ternary systems at different temperatures
    Bayazit, Kayhan
    Gok, Asli
    Uslu, Hasan
    Kirbaslar, S. Ismail
    FLUID PHASE EQUILIBRIA, 2014, 379 : 185 - 190
  • [35] (Liquid plus liquid) equilibria of (water plus lactic acid plus alcohol) ternary systems
    Sahin, Selin
    Kirbaslar, S. Ismail
    Bilgin, Mehmet
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2009, 41 (01): : 97 - 102
  • [36] (Liquid plus liquid) equilibria of (water plus propionic acid plus alcohol) ternary systems
    Kirbaslar, S. Ismail
    Sahin, Selin
    Bilgin, Mehmet
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (12): : 1503 - 1509
  • [37] Determination and correlation of liquid-liquid equilibria for the (water plus carboxylic acid plus dimethyl maleate) ternary systems at T=298.2 K
    Oezmen, Dilek
    FLUID PHASE EQUILIBRIA, 2008, 269 (1-2) : 12 - 18
  • [38] Liquid-liquid equilibrium study for ternary systems of (water plus furfuryl alcohol plus solvents) at 298.2 K: Measurement and thermodynamic modelling
    Dong, Shihua
    Sun, Weizhen
    Jiang, Yueyang
    Jia, Bing
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2020, 148
  • [39] Liquid plus liquid equilibria for the quaternary systems of (water plus acetic acid plus mixed solvent) at 298.2 K and atmospheric pressure
    Ozmen, Dilek
    Senoymak, M. Imge
    FLUID PHASE EQUILIBRIA, 2010, 298 (02) : 293 - 297
  • [40] Vapour-liquid equilibrium of carboxylic acid-alcohol binary systems: 2-Propanol plus butyric acid, 2-butanol plus butyric acid and 2-methyl-1-propanol plus butyric acid
    Iwarere, Samuel A.
    Raal, J. David
    Naidoo, Paramespri
    Ramjugernath, Deresh
    FLUID PHASE EQUILIBRIA, 2014, 380 : 18 - 27