Phase equilibrium of (water plus formic or acetic acid plus ethyl heptanoate) ternary liquid systems at different temperatures

被引:16
|
作者
Demirel, Cagla [1 ]
Cehreli, Suheyla [2 ]
机构
[1] DirectComm, TR-34718 Istanbul, Turkey
[2] Istanbul Univ, Fac Engn, Dept Chem Engn, TR-34320 Istanbul, Turkey
关键词
Liquid-liquid equilibrium; Formic acid; Acetic acid; UNIFAC; UNIQUAC; 298.15; K; ATMOSPHERIC-PRESSURE; FUEL-CELLS; MIXTURES; TOLUENE; ACID+1-HEPTANOL; PREDICTION; ACETATE; T=298.2;
D O I
10.1016/j.fluid.2013.07.015
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-liquid equilibrium (LLE) data for the ternary systems of (water + formic acid + ethyl heptanoate) and (water + acetic acid + ethyl heptanoate) were investigated at 288.15, 298.15, and 308.15 K and atmospheric pressure. The tie-line data was determined experimentally for each temperature. The experimental data was compared with the results predicted by the UNIFAC method, and correlated by means of UNIQUAC model. The reliability of the experimental tie-line data was confirmed by using the Othmer-Tobias correlation. Distribution coefficients and separation factor values were evaluated for the immiscibility region. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:71 / 77
页数:7
相关论文
共 50 条
  • [21] Liquid-Liquid Equilibrium for (water plus palm oil biodiesel plus methanol) ternary system at Different Temperatures
    Yan, Xingyue
    Chen, Yongchun
    Hu, Xiaoping
    2011 INTERNATIONAL CONFERENCE ON FUZZY SYSTEMS AND NEURAL COMPUTING (FSNC 2011), VOL III, 2011, : 379 - 382
  • [22] Liquid-Liquid Equilibrium for (Water plus Palm Oil Biodiesel plus Methanol) Ternary System at Different Temperatures
    Yan, Xingyue
    Chen, Yongchun
    Hu, Xiaoping
    FUTURE MATERIAL RESEARCH AND INDUSTRY APPLICATION, PTS 1 AND 2, 2012, 455-456 : 867 - 871
  • [23] Liquid-liquid equilibrium for the ternary systems of water plus acetyl acetone plus propyl acetate at several temperatures
    Yang, Zhidong
    Zhu, Jiawen
    Wu, Bin
    Chen, Kui
    Ye, Xiaohe
    FLUID PHASE EQUILIBRIA, 2011, 304 (1-2) : 7 - 11
  • [24] Ternary and Quaternary Liquid-Liquid Equilibria for Systems of Water plus Methanol plus Methylanthranilate plus Toluene at Different Temperatures
    Wang, Baohe
    Ran, Weili
    Li, Yanan
    Xiong, Jianping
    Li, Shaoyuan
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2012, 57 (12): : 3309 - 3314
  • [25] Investigation on isobaric vapor-liquid equilibrium for acetic acid plus water plus methyl ethyl ketone plus isopropyl acetate
    Xie, Qiang
    Wan, Hui
    Han, MingJuan
    Guan, GuoFeng
    FLUID PHASE EQUILIBRIA, 2009, 280 (1-2) : 120 - 128
  • [26] High-pressure phase equilibrium of the ternary system carbon dioxide plus water plus acetic acid at temperatures from 313 to 353 K
    Bamberger, A
    Sieder, G
    Maurer, G
    JOURNAL OF SUPERCRITICAL FLUIDS, 2004, 32 (1-3): : 15 - 25
  • [27] Liquid phase equilibrium of the ternary systems, water plus propionic or butyric acid plus mesityl oxide, at (298.2 and 323.2) K
    Chen, Yun
    Wang, Youchang
    Zhou, Shaoming
    Chen, Huang
    Liu, Dong
    Li, Libo
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2017, 111 : 72 - 79
  • [28] Phase equilibrium for ternary liquid systems of water plus carboxylic acid plus chlorinated hydrocarbon: Thermodynamic modeling through SERLAS
    Senol, A
    CHEMICAL ENGINEERING COMMUNICATIONS, 2006, 193 (03) : 402 - 416
  • [29] Investigation of Ternary Phase Diagrams of (Water plus Butyric Acid plus Phenyl Acetate) at Different Temperatures
    Bayazit, Kayhan
    Uslu, Hasan
    Gok, Ash
    Kirbaslar, S. Ismail
    Santos, Dheiver
    Bamufleh, Hisham S.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (03): : 1313 - 1320
  • [30] (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