ANALYSIS OF PARTITION COEFFICIENTS OF TERNARY LIQUID-LIQUID EQUILIBRIUM SYSTEMS AND FINDING CONSISTENCY USING UNIQUAC MODEL

被引:5
|
作者
Islam, Akand W. [1 ]
Zavvadi, Anand [1 ]
Kabadi, Vinayak N. [1 ]
机构
[1] N Carolina Agr & Tech State Univ, Dept Chem Engn, Greensboro, NC 27411 USA
来源
CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA | 2012年 / 33卷 / 02期
关键词
partition coefficients; UNIQUAC model; consistent systems; inconsistent systems; cross behavior; MIXTURES; EQUATION;
D O I
10.2478/v10176-012-0022-1
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The objective of this study is to investigate the change in partition coefficient with a change in the concentration of the solute in a liquid system consisting of two relatively immiscible solvents. To investigate the changes in the partition coefficients, the data of the partition coefficients at infinite dilution and the ternary Liquid-Liquid Equilibrium (LLE) data at finite concentrations of the solute should be consistent. In this study, 29 ternary systems that are found in literature and for which the partition coefficients at infinite dilution and the ternary LLE data cannot be predicted accurately by the universal quasi-chemical (UNIQUAC) model are identified. On the basis of this model, some consistent and inconsistent ternary systems are introduced. Three inconsistent systems, namely hexane-butanol-water, CCl4 (carbon tetrachloride)-PA (propanoic acid)-water, and hexane-PA-water, are chosen for detailed analysis in this study. The UNIQUAC activity coefficient model is used to represent these data over a range of concentrations. The results show large errors, exhibiting the inability of this model to correlate the data. Furthermore, some ternary systems in which cross behavior of solutes between two phases observed are identified.
引用
收藏
页码:243 / 253
页数:11
相关论文
共 50 条
  • [1] Ternary liquid-liquid phase behavior by decorated-UNIQUAC
    Kim, YC
    Kim, JD
    Kim, H
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 1996, 13 (05) : 439 - 447
  • [2] Identification of UNIQUAC binary interaction parameters in liquid-liquid equilibrium
    Tomassetti, Sebastiano
    Di Nicola, Giovanni
    Santori, Giulio
    FLUID PHASE EQUILIBRIA, 2020, 510
  • [3] Computation of liquid-liquid equilibrium of organic-ionic liquid systems using NRTL, UNIQUAC and NRTL-NRF models
    Haghtalab, Ali
    Paraj, Aliakbar
    JOURNAL OF MOLECULAR LIQUIDS, 2012, 171 : 43 - 49
  • [4] Experimental Determination of Liquid-Liquid Equilibrium Data on Ternary Water Systems
    Simic, Zoran
    Radovic, Ivona
    Kijevcanin, Mirjana
    EXPERIMENTAL RESEARCH AND NUMERICAL SIMULATION IN APPLIED SCIENCES, CNNTECH 2022, 2023, 564 : 183 - 197
  • [5] Determination of liquid-liquid partition coefficients by separation methods
    Berthod, A
    Carda-Broch, S
    JOURNAL OF CHROMATOGRAPHY A, 2004, 1037 (1-2) : 3 - 14
  • [6] UNIQUAC correlation of liquid-liquid equilibrium in systems involving ionic liquids: The DFT-PCM approach
    Santiago, Rilvia S.
    Santos, Geormenny R.
    Aznar, Martin
    FLUID PHASE EQUILIBRIA, 2009, 278 (1-2) : 54 - 61
  • [7] A Convenient Hybrid Method for Obtaining Liquid-Liquid Equilibrium Data in Ternary Systems
    Racovita, Radu C.
    Crisciu, Adrian Victor
    Sima, Sergiu
    Secuianu, Catinca
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (07) : 3384 - 3392
  • [8] Mathematical model of liquid-liquid equilibrium for a ternary system using the GMDH-type neural network and genetic algorithm
    Ghanadzadeh, H.
    Ganji, M.
    Fallahi, S.
    APPLIED MATHEMATICAL MODELLING, 2012, 36 (09) : 4096 - 4105
  • [9] Prediction of liquid-liquid equilibrium for ternary systems containing ionic liquids with the tetrafluoroborate anion using ASOG
    Robles, Pedro A.
    Graber, Teofilo A.
    Aznar, Martin
    FLUID PHASE EQUILIBRIA, 2010, 296 (02) : 154 - 158
  • [10] Experimental and Computational Study on Liquid-Liquid Equilibrium in Ternary Systems of γ-Valerolactone, Toluene, and Hydrocarbons
    Klajmon, Martin
    Rehak, Karel
    Matousova, Maja
    Moravek, Pavel
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (01) : 391 - 397