Modeling and experimental evaluation of enantioselective liquid-liquid extraction of (D, L)-4-chlorophenylglycine in a biphasic system

被引:19
|
作者
Tang, Kewen [1 ,2 ]
Fu, Tao [2 ]
Zhang, Panliang [1 ]
Yang, Changan [1 ]
Zhou, Congshan [1 ]
Liang, Enxiang [1 ]
机构
[1] Hunan Inst Sci & Technol, Dept Chem & Chem Engn, Yueyang 414006, Hunan, Peoples R China
[2] Xiangtan Univ, Coll Chem Engn, Xiangtan 411105, Hunan, Peoples R China
基金
美国国家科学基金会;
关键词
Extraction; 4-Chlorophenylglycine; BINAP-metal complexes; Interfacial reaction; Simulation; REACTIVE EXTRACTION; CHIRAL SEPARATION; AMINO-ACIDS; CROWN-ETHER; ENANTIOMERS; RESOLUTION; ALCOHOLS; CHROMATOGRAPHY; INHIBITORS; MEMBRANES;
D O I
10.1016/j.cherd.2014.08.002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Enantioselective Liquid-Liquid Extraction (ELLE) is a potentially attractive technology for the production of enantiopure compounds. The purpose of this research is to investigate ELLE of 4-chlorophenylglycine (CPG) enantiomers with metal-BINAP complexes as enantioselective extractants. The metal complexes were synthesized by the complexation of (S)-2,2'-bis(diphenylphosphino)-1,1'- binaphthalene (BINAP) with different central ions, among which, palladium complex allowed the separation of the CPG enantiomers with the highest operational selectivity. Efficiency of the extraction depends, often strongly, on a number of process variables, including types of organic solvents, pH of the aqueous phase, concentration of host and substrate, and temperature. In order to better understand the extraction process, equilibrium of the system was modeled by an interfacial reaction model. Important parameters required by the modeling, such as complexation equilibrium constant, were determined experimentally. When coupled with the parameters, extraction performance can be predicted by the model. By modeling and experiment, an optimal extraction condition concerning pH of 7 and the host concentration of 1.10(-3) mol/L was obtained with high enantioselective (a) of 1.862 and performance factor (pf) of 0.056. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:290 / 300
页数:11
相关论文
共 24 条
  • [21] Experimental Data and Thermodynamic Modeling of the Liquid-Liquid Equilibrium Ternary System (Water plus Acetic Acid+1-Octanol) at Several Temperatures
    Ebrahimkhani, Mohammad Javad
    Azadian, Meysam
    Gilani, Hossein Ghanadzadeh
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2022, 67 (02) : 404 - 415
  • [22] Experimental Data and Modeling of Salt Effect on Liquid-Liquid Equilibrium of the Ternary (Water+1-Propanol+Hexane) System at 298K
    Regabe, Slimane
    Merzougui, Abdelkarim
    Hasseine, Abdelmalek
    Laiadi, Djemoui
    Bouredji, Hamza
    IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION, 2020, 39 (06): : 199 - 210
  • [23] Preparation of sulfobutylether-beta-cyclodextrin bonded Fe3O4/SiO2 core-shell nanoparticles and its application in enantioselective liquid-liquid extraction
    Chen, Ben
    Lin, Tingting
    You, Haibo
    Fang, Liqun
    Chu, Chu
    Yang, Jintao
    Tong, Shengqiang
    COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2022, 652
  • [24] Extraction, Preconcentration and Isolation of Flavonoids from Apocynum venetum L. Leaves Using Ionic Liquid-Based Ultrasonic-Assisted Extraction Coupled with an Aqueous Biphasic System
    Tan, Zhijian
    Yi, Yongjian
    Wang, Hongying
    Zhou, Wanlai
    Wang, Chaoyun
    MOLECULES, 2016, 21 (03)