Modeling of facilitated transport of Cr(III) using (RNH3+HSO4-) ionic liquid and pseudo-emulsion hollow fiber strip dispersion (PEHFSD) technology

被引:10
作者
Alguacil, F. J. [1 ]
Garcia-Diaz, I. [1 ]
Lopez, F. A. [1 ]
机构
[1] Ctr Nacl Invest Met CSIC, Madrid 28040, Spain
关键词
Chromium(III); Amine PJMT; Liquid membranes; Ionic liquids; Wastewater treatment; SOLVENT-EXTRACTION; AQUEOUS-SOLUTION; METALS REMOVAL; MEMBRANE; CHROMIUM; RECOVERY; PERTRACTION; SEPARATION; CR(VI); ZINC;
D O I
10.1016/j.jiec.2012.12.003
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The permeation of chromium (III) using PEHFSD technology and the ionic liquid (RNH3+HSO4-), formed by reaction of the primary amine PRIMENE JMT and sulphuric acid, dissolved in n-decane as mobile carrier has been investigated. The alkaline feed solution containing Cr(III) was passed through the tube side, and pseudo-emulsions of the ionic liquid + n-decane + n-decanol and sulphuric acid were passed through the shell side in counter-current mode and using a single hollow fiber module for extraction and stripping. In this advanced membrane technology, the aqueous acidic strip solution is dispersed in the organic membrane solution in a tank with an impeller stirrer to form a strip dispersion. The pseudo-emulsion phase is circulated from the tank to the membrane module to provide a constant supply of the organic solution to the membrane micropores. Factors affecting chromium permeability, such as hydrodynamic conditions, carrier concentration in the organic phase, metal and NaOH concentrations in the feed phase, have been analyzed. A model is reported describing the transport mechanism, whereas the experimental data are quantitatively explained by mathematical equations describing the rate of transport. Different rate-controlling processes take place as long as the metal transport occurs. (c) 2013 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1086 / 1091
页数:6
相关论文
共 40 条
[1]   Extractive removal of chromium (VI) from industrial waste solution [J].
Agrawal, Archana ;
Pal, Chandana ;
Sahu, K. K. .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 159 (2-3) :458-464
[2]   Copper removal from acidic wastewaters using 2-hydroxy-5-nonylbenzaldehyde oxime as ionophore in pseudo-emulsion membrane with strip dispersion (PEMSD) technology [J].
Alguacil, F. J. ;
Lopez, F. A. ;
Garcia-Diaz, I. .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2012, 18 (01) :255-259
[3]   Liquid membranes and the treatment of metal-bearing wastewaters [J].
Alguacil, FJ ;
Villegas, MA .
REVISTA DE METALURGIA, 2002, 38 (01) :45-55
[4]   Study of the structure of H2SO4-amine Primene 81R and Fe(III)-amine Primene 81R sulphate compounds by infrared spectroscopy [J].
Alguacil, FJ .
REVISTA DE METALURGIA, 1999, 35 (04) :249-254
[5]   Uphill permeation of Cr(VI) using Hostarex A327 as ionophore by membrane-solvent extraction processing [J].
Alguacil, Francisco Jose ;
Alonso, Manuel ;
Lopez, Felix ;
Lopez-Delgado, Aurora .
CHEMOSPHERE, 2008, 72 (04) :684-689
[6]  
Belay Alebel Abebe, 2010, Journal of Environmental Protection, V1, P53, DOI 10.4236/jep.2010.11007
[7]   Supported liquid membranes technologies in metals removal from liquid effluents [J].
de Agreda, D. ;
Garcia-Diaz, I. ;
Lopez, F. A. ;
Alguacil, F. J. .
REVISTA DE METALURGIA, 2011, 47 (02) :146-168
[8]   Removal of Metal Ions from Aqueous Solutions by Extraction with Ionic Liquids [J].
de los Rios, A. P. ;
Hernandez-Fernandez, F. J. ;
Lozano, L. J. ;
Sanchez, S. ;
Moreno, J. I. ;
Godinez, C. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (02) :605-608
[9]   Task-specific ionic liquid trioctylmethylammonium salicylate as extraction solvent for transition metal ions [J].
Egorov, Vladimir M. ;
Djigailo, Dmitry I. ;
Momotenko, Dmitry S. ;
Chernyshov, Denis V. ;
Torocheshnikova, Irina I. ;
Smirnova, Svetlana V. ;
Pletnev, Igor V. .
TALANTA, 2010, 80 (03) :1177-1182
[10]  
Feng R., 2010, J. Environm. Protection, V1, P95