(Liquid plus liquid) equilibria measurements for ternary systems (sulfolane plus a carboxylic acid plus n-heptane) at T=303.15 K and at 0.1 MPa

被引:7
|
作者
Cele, N. P. [1 ]
Bahadur, I. [2 ,3 ]
Redhi, G. G. [1 ]
Ebenso, E. E. [3 ]
机构
[1] Durban Univ Technol, Dept Chem, POB 1334, ZA-4000 Durban, South Africa
[2] North West Univ, Dept Chem, Mafikeng Campus,Private Bag X2046, ZA-2735 Mmabatho, South Africa
[3] North West Univ, Fac Agr Sci & Technol, Mat Sci Innovat & Modelling MaSIM Res Focus Area, Mafikeng Campus,Private Bag X2046, ZA-2735 Mmabatho, South Africa
来源
基金
新加坡国家研究基金会;
关键词
(Liquid plus liquid) equilibrium; Sulfolane; n-Heptane; Carboxylic acid; NRTL; UNIQUAC; BINARY-SYSTEMS; WATER PLUS; M-XYLENE; MIXTURES; BENZENE; TOLUENE; HEXANE; TEMPERATURE; SOUND;
D O I
10.1016/j.jct.2015.12.019
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present work, new (liquid + liquid) equilibrium (LLE) values are reported for ternary systems {sulfolane(1) + acetic acid, or propanoic acid, or butanoic acid, or 2-methylpropanoic acid, or pentanoic acid, or 3-methylbutanoic acid (2) + n-heptane (3)} at T = 303.15 K and at p = 0.1 MPa. The mutual solubility of carboxylic acid in sulfolane is dependent on the length and structure of the alkyl chain of the carboxylic acid; it progressively increases with an increase in the alkyl chain of the carboxylic acid. The single phase homogenous region increases as the alkyl chain of the carboxylic acid increases. The n-heptane is most soluble in the carboxylic acid mixtures with long alkyl chain, that is, (3-methylbutanoic acid + sulfolane) and (pentanoic acid + sulfolane) systems and least soluble in the carboxylic acid with short alkyl chain (acetic acid + sulfolane) system. Carboxylic acid together with many other oxygenates and hydrocarbons are produced by SASOL Company in South Africa using the Fischer-Tropsch process. The details about this process are given in introduction section. The NRTL and UNIQUAC models were used to correlate the experimental tie-lines and to calculate the phase compositions of the ternary systems. It was found that the NRTL model fits the experimental values significantly better than the UNIQUAC model. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:169 / 174
页数:6
相关论文
共 50 条
  • [41] (Liquid plus liquid) equilibria for water plus etbanol plus citral multicomponent system at 303.15 K
    de Doz, Monica B. Gramajo
    Cases, Alicia M.
    Diaz, Pablo A.
    Solimo, Horacio N.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (05): : 1710 - 1714
  • [42] Ternary (liquid plus liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) plus benzene plus an alkane at T=298.2 K and p=0.1 MPa
    Letcher, TM
    Reddy, P
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2005, 37 (05): : 415 - 421
  • [43] Liquid-Liquid Equilibria of the Methanol plus Hexane plus Methylcyclohexane plus Toluene Quaternary System at T=303.15 K
    Gramajo, Monica B.
    Cases, Alicia M.
    JOURNAL OF SOLUTION CHEMISTRY, 2015, 44 (02) : 171 - 180
  • [44] High-pressure (vapor plus liquid) equilibria in the (nitrogen plus n-heptane) system
    Garcia-Sanchez, Fernando
    Eliosa-Jimenez, Gaudencio
    Silva-Oliver, Guadalupe
    Godinez-Silva, Armando
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2007, 39 (06): : 893 - 905
  • [45] Vapor-liquid equilibria for the ternary system benzene plus n-heptane plus N,N-dimethylformamide at 101.33 kPa
    Blanco, B
    Sanz, MT
    Beltrán, S
    Cabezas, JL
    Coca, J
    FLUID PHASE EQUILIBRIA, 2000, 175 (1-2) : 117 - 124
  • [46] Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) plus Phenols plus Water
    Martin, Antje
    Klauck, Mandy
    Grenner, Andreas
    Meinhardt, Rene
    Martin, Diana
    Schmelzer, Juergen
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (04): : 741 - 749
  • [47] Liquid-liquid equilibria for ternary mixtures (an ionic liquid plus benzene plus heptane or hexadecane) at T=298.2 K and atmospheric pressure
    Deenadayalu, Nirmala
    Ngcongo, Khulekani C.
    Letcher, Trevor M.
    Ramjugernath, Deresh
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (03): : 988 - 991
  • [48] Thermophysical Properties and Liquid-Liquid Equilibria of Pseudoternary Systems {Toluene plus n-Heptane plus Deep Eutectic Solvents Based on Levulinic Acid}
    Jung, Myeongjin
    Park, YoonKook
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2022, 67 (02): : 416 - 427
  • [49] Liquid-Liquid Equilibria of Ternary Systems cis-1,2-Dimethylcyclohexane plus Toluene plus Sulfolane
    Sun, Xiaoyan
    Xiang, Shuguang
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2014, 22 (11-12) : 1298 - 1301
  • [50] Vapor-liquid equilibria of the ternary system benzene plus n-heptane plus N-methylpyrrolidone (NMP) at 101.33 kPa
    Blanco, B
    Sanz, MT
    Beltrán, S
    Cabezas, JL
    Coca, J
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (05): : 1167 - 1170