Kinetic modelling of the active transport of copper(II) across liquid membranes using thiourea derivatives immobilized on microporous hydrophobic supports

被引:24
作者
El Aamrani, FZ [1 ]
Kumar, A [1 ]
Sastre, AM [1 ]
机构
[1] Univ Politecn Catalunya, ETSEIB, Dept Chem Engn, E-08028 Barcelona, Spain
关键词
D O I
10.1039/a901203f
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The facilitated transport of Cu-II from chloride media through a flat-sheet supported liquid membrane (FSSLM) is investigated, using thiourea derivatives as ionophores, as a function of hydrodynamic conditions, concentration of copper (1-3 x 10(-7) mol cm(-3)) and H+ (pH 0.1-2.5) in the feed solution, structure of carrier, carrier concentration (0.7-3 x 10(-5) mol cm(-3)) in the membrane, strippant in receiving phase and support characteristics. A model is presented that describes the transport mechanism, consisting of diffusion through a feed aqueous diffusion layer, a fast interfacial chemical reaction, and diffusion of carrier and its metal complex through the organic membrane. The organic membrane diffusional resistance (Delta(o)) and aqueous diffusional resistance (Delta(a)) were calculated from the proposed model, and their values were 107 x 10(2) s cm(-1) and 625 s cm(-1), respectively. It was observed that the Cu-II flux across the membrane tends to reach a plateau at a high concentration of Cu-II or a low concentration of H+ owing to carrier saturation within the membrane, leading to a diffusion-controlled process. The values of the apparent diffusion coefficient(D-o(a)) and limiting metal flux J(lim) were calculated from the limiting conditions and found to be 2.9 x 10(-6) cm(2) s(-1) and 1.4 x 10(-9) mol cm(-2) s(-1), respectively. The values of the bulk diffusion coefficient (D-o,D-b) and diffusion coefficient (D-o) calculated from the model were 2.6 x 10(-6) cm(2) s(-1) and 1.2 x 10(-6) cm(2) s(-1). The polymeric microporous solid support, Durapure, was selected throughout the study as it gave the best performance.
引用
收藏
页码:517 / 523
页数:7
相关论文
共 44 条
[1]   Modelling and simulation of integrated membrane processes for recovery of Cr(VI) with Aliquat 336 [J].
Alonso, AI ;
Pantelides, CC .
JOURNAL OF MEMBRANE SCIENCE, 1996, 110 (02) :151-167
[2]  
[Anonymous], 1975, J CHROMATOGRAPHY LIB
[3]  
[Anonymous], 1982, IUPAC CHEM DATA SERI
[4]   NEW SULFUR-CONTAINING REAGENTS AS CARRIERS FOR THE SEPARATION OF PALLADIUM BY SOLID SUPPORTED LIQUID MEMBRANES [J].
ANTICO, E ;
MASANA, A ;
HIDALGO, M ;
SALVADO, V ;
VALIENTE, M .
HYDROMETALLURGY, 1994, 35 (03) :343-352
[5]  
BAKER RW, 1977, J MEMBRANE SCI, V2, P213, DOI 10.1016/S0376-7388(00)83248-2
[6]   DIFFUSIONAL BOUNDARY-LAYER RESISTANCE FOR MEMBRANE-TRANSPORT [J].
BOHRER, MP .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (01) :72-78
[7]   MEMBRANE EXTRACTION OF SILVER BY DI(2-ETHYLHEXYL)DITHIOPHOSPHORIC ACID [J].
BROMBERG, L ;
LEWIN, I ;
WARSHAWSKY, A .
JOURNAL OF MEMBRANE SCIENCE, 1992, 70 (01) :31-39
[8]   A NOVEL TETRADENTATE HYDROXAMATE AS ION CARRIER IN LIQUID MEMBRANES [J].
BROMBERG, L ;
LEVIN, G ;
LIBMAN, J ;
SHANZER, A .
JOURNAL OF MEMBRANE SCIENCE, 1992, 69 (1-2) :143-153
[9]   MEMBRANES WHICH PUMP [J].
CUSSLER, EL .
AICHE JOURNAL, 1971, 17 (06) :1300-&
[10]   Efficiency of hollow fiber modules for nondispersive chemical extraction [J].
Daiminger, UA ;
Geist, AG ;
Nitsch, W ;
Plucinski, PK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (01) :184-191