Transport and separation of iron(III) from nickel(II) with the ionic liquid trihexyl(tetradecyl)phosphonium chloride

被引:80
作者
Kogelnig, Daniel [1 ]
Stojanovic, Anja [1 ]
Jirsa, Franz [1 ]
Koerner, Wilfried [2 ]
Krachler, Regina [1 ]
Keppler, Bernhard K. [1 ]
机构
[1] Univ Vienna, Inst Inorgan Chem, A-1090 Vienna, Austria
[2] Univ Vienna, Dept Environm Geosci, A-1090 Vienna, Austria
关键词
Liquid-liquid extraction; Bulk liquid membrane; Cyphos IL101; Iron(III)tetrachloroferrate; Transport kinetic; QUATERNARY AMMONIUM HALIDES; EXTRACTION; CARRIER; COBALT(II); COPPER; HG2+;
D O I
10.1016/j.seppur.2009.12.028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Iron(III) was efficiently extracted from a 6 M hydrochloride solution with the ionic liquid trihexyl(tetradecyl)phosphonium chloride, Cyphos (R), dissolved in chloroform. Spectroscopical data revealed that iron exists as tetrachloroferrate species in the organic phase. In contrast, nickel(II) was not extracted under experimental conditions. Satisfying back extraction of Fe(III) was achieved with a 0.5 M HCl solution. Consequent time-dependent transport studies with Cyphos IL101 as ionic liquid carrier in chloroform (0.01 M), showed a successful quantitative transport of 0.1 M Fe(III) from a 6 M hydrochloride source phase to a 0.5 M hydrochloride receiving phase and a favorable separation from Ni(II). The transport of Fe(III) through the bulk liquid membrane (BLM) was assumed to follow a nonsteady kinetic regime with two consecutive and irreversible first-order reactions. With an initial Fe(III)/Cyphos IL101 concentration ratio of 10, an apparent rate constant k(s) of 31.4 x 10(-3) min(-1) was obtained for the Fe(III) transport from the membrane- to the receiving phase, whereas the rate constant k(f) for the Fe(III) transport from the source- to the membrane phase was 11.8 x 10(-3) min(-1). (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:56 / 60
页数:5
相关论文
共 19 条
[1]   Transport of Hg2+ through bulk liquid membrane using a bis-calix[4]arene nitrile derivative as carrier:: kinetic analysis [J].
Alpoguz, HK ;
Memon, S ;
Ersoz, M ;
Yilmaz, M .
NEW JOURNAL OF CHEMISTRY, 2002, 26 (04) :477-480
[2]   THE IRON(III) CHLORIDE SYSTEM - A STUDY OF THE STABILITY-CONSTANTS AND OF THE DISTRIBUTION OF THE TETRACHLORO SPECIES BETWEEN ORGANIC-SOLVENTS AND AQUEOUS CHLORIDE SOLUTIONS [J].
BJERRUM, J ;
LUKES, I .
ACTA CHEMICA SCANDINAVICA SERIES A-PHYSICAL AND INORGANIC CHEMISTRY, 1986, 40 (01) :31-40
[3]  
Cieszynska A., 2007, Pol. J. Chem. Technol, V9, P99, DOI DOI 10.2478/V10026-007-0037-4
[4]   Structure and magnetic behavior of transition metal based ionic liquids [J].
Del Sesto, Rico E. ;
McCleskey, T. Mark ;
Burrell, Anthony K. ;
Baker, Gary A. ;
Thompson, Joe D. ;
Scott, Brian L. ;
Wilkes, John S. ;
Williams, Peg .
CHEMICAL COMMUNICATIONS, 2008, (04) :447-449
[5]  
ELWAKIL AM, 1982, FRESEN Z ANAL CHEM, V311, P522
[6]   STUDIES ON EXTRACTION OF IRON(III) AND COBALT(II) CHLORIDES BY QUATERNARY AMMONIUM HALIDES [J].
ELYAMANI, IS ;
SHABANA, EI .
TRANSITION METAL CHEMISTRY, 1984, 9 (05) :199-202
[7]   LIQUID-LIQUID EXTRACTION WITH LONG-CHAIN QUATERNARY AMMONIUM HALIDES [J].
GOOD, ML ;
HOLLAND, FF ;
SRIVASTAVA, SC .
ANALYTICA CHIMICA ACTA, 1964, 31 (06) :534-&
[8]   Immobilization of extractants in biopolymer capsules for the synthesis of new resins: a focus on the encapsulation of tetraalkyl phosphonium ionic liquids [J].
Guibal, Eric ;
Vincent, Thierry ;
Jouannin, Claire .
JOURNAL OF MATERIALS CHEMISTRY, 2009, 19 (45) :8515-8527
[9]  
Holleman A.F., 1995, LEHRBUCH ANORGANISCH
[10]   Separation of iron and nickel from a spent FeCl3 etching solution by solvent extraction [J].
Lee, MS ;
Lee, KJ .
HYDROMETALLURGY, 2005, 80 (03) :163-169