Liquid-liquid equilibrium and critical states for the quaternary system propionic acid-n-butanol-n-butyl propionate-water at 303.15 K

被引:15
|
作者
Toikka, Maria [1 ]
Trofimova, Dariya [1 ]
Samarov, Artemiy [1 ]
机构
[1] St Petersburg State Univ, Dept Chem Thermodynam & Kinet, Univ Skiy Prospect 26, St Petersburg 198504, Russia
基金
俄罗斯科学基金会;
关键词
Liquid-liquid equilibrium; n-butyl propionate; Critical states; Cloud-point technique; ACETIC-ACID; ESTERIFICATION; MIXTURES; OIL; SOLUBILITY; 1-BUTANOL; CATALYST; ETHANOL; ESTERS;
D O I
10.1016/j.fluid.2017.12.023
中图分类号
O414.1 [热力学];
学科分类号
摘要
New experimental data on liquid-liquid equilibrium (LLE) and critical phases for the propionic acid nbutanol n-butyl propionate water system at 303.15 K and atmospheric pressure are presented. The LLE compositions were determined by gas chromatography, correlated and predicted by NRTL and UNIFAC models respectively. The results of NRTL and UNIFAC modelling are in sufficient agreement with experimental data. Standard deviations for binary and ternary subsystems do not exceed 0.79% (NRTL) and 5.1% (UNIFAC). In case of quaternary system investigated sigma(NRTL) = 0.56% and sigma(UNIFAC) = 2.2%. The study of critical states was carried out by "cloud-point technique" method. The run of critical curve in quaternary system was studied. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:17 / 22
页数:6
相关论文
共 50 条
  • [41] Liquid-liquid equilibrium for the quaternary system toluene plus water plus propionic acid plus ethyl acetate at 25 °C and atmospheric pressure
    Kim, JK
    Park, DW
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (02): : 625 - 629
  • [42] Liquid-liquid equilibrium of glycerol - acetone - solketal - water quaternary system at 303.2 K, 308.2 K and 313.2 K
    Zhang, Qing
    Xu, Danru
    Hao, Miaoli
    Wu, Zhiqiang
    Yi, Chunhai
    Liu, Jingjun
    FLUID PHASE EQUILIBRIA, 2024, 576
  • [43] Liquid-liquid equilibrium for the quaternary system water plus tetrahydrofuran plus n-heptane plus butyl acetate mixture at 25 °C and atmospheric pressure
    Kim, Young-Kyu
    Park, Dong-Won
    JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2008, 14 (05) : 602 - 607
  • [44] Chemical equilibrium for the reactive system acetic acid + n-butanol + n-butyl acetate + water at 308.15 K
    Samarov, Artemiy
    Naumkin, Pavel
    Toikka, Alexander
    FLUID PHASE EQUILIBRIA, 2015, 403 : 10 - 13
  • [45] Salt Effect on the Liquid-Liquid Equilibrium of (Water plus Propionic Acid plus Cyclohexanol) System at T=(298.2, 303.2, and 308.2) K
    Ghalami-Choobar, Bahram
    Ghanadzadeh, Ali
    Kousarimehr, Shahram
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2011, 19 (04) : 565 - 569
  • [46] Liquid-Liquid Equilibrium for the Ternary Systems Water+1-Butanol+1-Hexanol or 1-Octanol at 303.15, 313.15, and 323.15 K
    Zhang, Lili
    Yu, Yingmin
    Liao, Zhaohui
    Xu, Xiaosheng
    Huang, Xin
    Jia, Bing
    Li, Qingsong
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (02): : 477 - 486
  • [47] DETERMINATION, CORRELATION AND PREDICTION OF LIQUID-LIQUID EQUILIBRIUM DATA OF n- BUTYL ALCOHOL-WATER-BUTYL ACETATE TERNARY SYSTEM.
    Lin, Jiaqi
    Zhang, Jianhou
    J Chem Ind Eng (China) (Engl Ed), 1988, 3 (01): : 111 - 123
  • [48] Liquid-liquid equilibrium of the water plus citric acid plus 2-butanol plus sodium chloride system at 298.15 K
    Lintomen, L
    Pinto, RTP
    Batista, E
    Meirelles, AJA
    Maciel, MRW
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2000, 45 (06): : 1211 - 1214
  • [49] LIQUID-LIQUID EQUILIBRIUM FOR TERNARY-SYSTEM N-HEXANE-WATER-ACETONE
    RAGAINI, V
    RAVERDIN.V
    SANTI, R
    QUADERNI DELL INGEGNERE CHIMICO ITALIANO, 1974, 10 (02): : 19 - 22
  • [50] Liquid-liquid equilibrium measurements and interaction explorations for separation of azeotrope n-butyl acetate and n-butanol using three ionic liquids
    Wang, Dan
    Wei, Feng
    Reyes-Labarta, Juan A.
    Wang, Zhaojie
    Xu, Dongmei
    Gao, Jun
    Zhang, Lianzheng
    Wang, Yinglong
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2021, 155