Liquid-Liquid Equilibria for the Ternary Systems Dodecane plus Toluene or Thiophene or Pyridine+1-Ethyl-3-methylimidazolium Methyl Sulfate

被引:16
|
作者
Baelhadj, Abdelaziz Chikh [1 ,2 ]
Mutelet, Fabrice [2 ]
机构
[1] USTHB, Fac Chim, Lab Thermodynam & Modelisat Mol, BP 32 El Alia, Bab Ezzouar 16111, Alger, Algeria
[2] Univ Lorraine, Ecole Natl Super Ind Chim, Lab React & Genie Procedes, UMR 7274,CNRS, 1 Rue Grandville, F-54000 Nancy, France
来源
关键词
IONIC LIQUIDS; ACTIVITY-COEFFICIENTS; INFINITE DILUTION; ORGANIC-COMPOUNDS; EXTRACTIVE DESULFURIZATION; ALIPHATIC-HYDROCARBONS; THERMODYNAMIC PROPERTIES; PHASE-DIAGRAMS; BINARY-SYSTEMS; FUEL OILS;
D O I
10.1021/acs.jced.6b00437
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid liquid equilibria for the three ternary systems (dodecane + toluene + 1-ethyl-3-methylimidazolium methyl sulfate ([EMIM][MeSQ(4)])), (dodecane + thiophene + [EMIM][MeSO4]) and (dodecane + pyridine + [EMIM][MeSO4]) were measured at 298.15 K and at atmospheric pressure. Experimental data were used to calculate the distribution coefficient and selectivity values. Results indicate that [EMIM] [MeSO4] is a potential solvent for the extraction of pyridine from n-dodecane. It was found that NTRL and UNIQUAC models can used to represent with good accuracy ternary systems containing [EMIM][MeSO4]. Then, we have shown that [EMIM] [MeSO4] can be used as solvent for the extraction of pyridine from a synthetic mixture.
引用
收藏
页码:1749 / 1755
页数:7
相关论文
共 50 条
  • [41] Liquid-Liquid Equilibria for the Ternary Systems of Perfluamine plus Hydrofluoroether plus Benzene, Toluene, or Xylene at 298.15 K or 313.15 K
    Lee, Tae Gyu
    Song, Kwang Ho
    Choe, Jaehoon
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2013, 58 (11): : 3130 - 3136
  • [42] Liquid-liquid equilibria for the ternary systems water+1-propanol plus methyl methacrylate, plus butyl methacrylate, and plus isobutyl methacrylate
    Chen, Jui-Tang
    Lin, Yi-Min
    FLUID PHASE EQUILIBRIA, 2007, 258 (01) : 1 - 6
  • [43] Liquid-liquid(-liquid) equilibria in ternary systems of water plus cyclohexylamine plus aromatic hydrocarbon (toluene or propylbenzene) or aliphatic hydrocarbon (heptane or octane)
    Klauck, Mandy
    Grenner, Andreas
    Schmelzer, Juergen
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (03): : 1043 - 1050
  • [44] LIQUID-LIQUID EQUILIBRIA OF THE TERNARY MIXTURES WATER PLUS PROPANOIC ACID PLUS METHYL ETHYL KETONE AND WATER PLUS PROPANOIC ACID PLUS METHYL PROPYL KETONE
    ARCE, A
    BLANCO, A
    SOUZA, P
    VIDAL, I
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1995, 40 (01): : 225 - 229
  • [45] (Liquid plus liquid) equilibria for ternary mixtures of (methanol or ethanol plus toluene or m-xylene plus n-dodecane)
    Mohsen-Nia, M
    Modarress, H
    Doulabi, F
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (02): : 158 - 164
  • [46] Liquid-liquid equilibria for the acetic acid plus water plus amyl acetate and acetic acid plus water plus 2-methyl ethyl acetate ternary systems
    Wang, Lijun
    Cheng, Youwei
    Li, Xi
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (06): : 2171 - 2173
  • [47] Liquid-liquid equilibria for ternary system water plus toluene plus benzaldehyde at (303.2-343.2) K
    Wang, Hui
    Wang, Qinbo
    Xiong, Zhenhua
    Chen, Chuxiong
    FLUID PHASE EQUILIBRIA, 2014, 383 : 43 - 48
  • [48] Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
    Kumar, U. K. Arun
    Mohan, Ratan
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (03): : 485 - 490
  • [49] Liquid-liquid equilibria for pseudo-ternary systems: (Sulfolane+2-ethoxyethanol) plus octane plus toluene at 293.15 K
    Awwad, Akl M.
    Al-Dujaili, Amar H.
    Al-Haideri, Abdul-Muhsin A.
    Essa, Hatim M.
    FLUID PHASE EQUILIBRIA, 2008, 270 (1-2) : 10 - 14
  • [50] The analysis of liquid-liquid equilibria (LLE) of toluene plus heptane plus ionic liquid ternary mixture using intelligent models
    Shaahmadi, Fariborz
    Anbaz, Mohammad Amin
    Bazooyar, Bahamin
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2018, 130 : 184 - 198