Experimental investigation and thermodynamic modeling of amino acids partitioning in a water/ionic liquid system

被引:17
作者
Nazem, Hadi [1 ]
Ghotbi, Cyrus [1 ]
Zare, Masoud Habibi [2 ]
Shirazian, Saeed [3 ,4 ]
机构
[1] Sherif Univ Technol, Dept Chem & Petr Engn, Tehran, Iran
[2] Isfahan Univ Technol, Dept Chem Engn, Esfahan, Iran
[3] Ton Duc Thang Univ, Dept Management Sci & Technol Dev, Ho Chi Minh City, Vietnam
[4] Ton Duc Thang Univ, Fac Appl Sci, Ho Chi Minh City, Vietnam
关键词
Amino acids; Bio-separation; Ionic liquids; SAFT; NRTL; Liquid-liquid equilibrium; EQUATION-OF-STATE; IONIC LIQUIDS; ASSOCIATING MOLECULES; GAS-MIXTURES; SIMULATION; EXTRACTION; SEPARATION; POLYDISPERSE; EQUILIBRIUM; CONTACTORS;
D O I
10.1016/j.molliq.2018.03.108
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Amino acids partitioning including phenylalanine, glutamic acid, and tryptophan in aqueous and ionic liquid phases at temperature of 298.15 K and atmospheric pressure were measured. 1-Butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide used in this work can produce two phases with water immediately. The effect of aqueous solution pH on amino acids partitioning was studied and revealed that amino acid partitioning coefficient was decreased with increasing pH. This phenomenon pertains to the electrostatic interaction between cations of amino acid and the anions of ionic liquid which is decreased when pH increases. Considering the effect of pH, liquid-liquid equilibrium data of amino acids were obtained in a pH owning maximum partitioning coefficient. It was observed that chemical structure of amino acid has an important effect on partitioning of amino acids between two phases. Experimental data indicated that glutamic acid is mostly transferred to aqueous phase while tryptophan moves to the ionic liquid phase. In the modeling section, equilibrium behavior of water, amino acid and ionic liquid system were predicted by SAFT equation of state. Necessary parameters of water and pure ionic liquid for equation of state were measured and amino acid parameters were obtained from literature. Binary interactions of components were optimized by equilibrium data. NRTL model was used in order to analyze cabapility of SAFT EoS to predict the behavior of system. The results indicate that SAFF model anticipates liquid-liquid equilibrium of the system better than NRTL model. The percentage of average absolute deviation for SAFT equiation is <1.2% while for NRTL model is >1.9%. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:386 / 390
页数:5
相关论文
共 24 条
[1]   NEW REFERENCE EQUATION OF STATE FOR ASSOCIATING LIQUIDS [J].
CHAPMAN, WG ;
GUBBINS, KE ;
JACKSON, G ;
RADOSZ, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (08) :1709-1721
[2]   Extraction of vanillin using ionic-liquid-based aqueous two-phase systems [J].
Cláudio A.F.M. ;
Freire M.G. ;
Freire C.S.R. ;
Silvestre A.J.D. ;
Coutinho J.A.P. .
Separation and Purification Technology, 2010, 75 (01) :39-47
[3]   Thermophysical and thermodynamic properties of ionic liquids over an extended pressure range:: [bmim][NTf2] and [hmim][NTf2] [J].
de Azevedo, RG ;
Esperança, JMSS ;
Szydlowski, J ;
Visak, ZP ;
Pires, PF ;
Guedes, HJR ;
Rebelo, LPN .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2005, 37 (09) :888-899
[4]   (Liquid plus Liquid) Equilibrium for Ternary Systems Containing of an Ionic Liquid, n-Hexane and an Organic Compound Involved in the Kinetic Resolution of rac-2-Pentanol [J].
de los Rios, A. P. ;
Hernandez Fernandez, F. J. ;
Gomez, D. ;
Rubio, M. ;
Villora, G. .
SEPARATION SCIENCE AND TECHNOLOGY, 2012, 47 (02) :300-311
[5]   Ternary Liquid-Liquid Equilibria for Mixtures of {Ionic Liquid plus Thiophene or Benzothiophene plus Heptane} at T=308.15 K [J].
Domanska, Urszula ;
Walczak, Klaudia .
JOURNAL OF SOLUTION CHEMISTRY, 2015, 44 (3-4) :382-394
[6]   (Extraction of biomolecules using) aqueous biphasic systems formed by ionic liquids and aminoacids [J].
Dominguez-Perez, Montserrat ;
Tome, Luciana I. N. ;
Freire, Mara G. ;
Marrucho, Isabel M. ;
Cabeza, Oscar ;
Coutinho, Joao A. P. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2010, 72 (01) :85-91
[7]   Extraction of proteins from biological fluids by use of an ionic liquid/aqueous two-phase system [J].
Du, Zhuo ;
Yu, Yong-Liang ;
Wang, Jian-Hua .
CHEMISTRY-A EUROPEAN JOURNAL, 2007, 13 (07) :2130-2137
[8]   Computational fluid dynamics simulation of transport phenomena in ceramic membranes for SO2 separation [J].
Fasihi, Mojtaba ;
Shirazian, Saeed ;
Marjani, Azam ;
Rezakazemi, Mashallah .
MATHEMATICAL AND COMPUTER MODELLING, 2012, 56 (11-12) :278-286
[9]   Mathematical modeling and simulation of CO2 stripping from monoethanolamine solution using nano porous membrane contactors [J].
Ghadiri, Mehdi ;
Marjani, Azam ;
Shirazian, Saeed .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2013, 13 :1-8
[10]   Recent Applications of Ionic Liquids in Separation Technology [J].
Han, Dandan ;
Row, Kyung Ho .
MOLECULES, 2010, 15 (04) :2405-2426