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Selective removal of transition metal ions in transport through polymer inclusion membranes with organophosphorus acids

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Separation of transition metal ions from aqueous chloride solutions by transport through polymer inclusion membrane (PIM) process is presented. The competitive transport of equimolar mixtures of Zn(II) and Cd(II) as well as Zn(II), Cu(II), Co(II), Cd(II), and Ni(II) was investigated. The selective transport of metal ions from aqueous chloride source phase through PIM-containing cellulose triacetate (support), o?nitrophenyl pentyl ether (plasticizer) and organophosphorus acidic compounds, i.e. di(2-ethylhexyl)phosphoric acid (D2EHPA), di(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272), di(2,4,4-trimethylpentyl)dithiophosphinic acid (Cyanex 301) and bis(2,4,4-trimethylpentyl)monothiophosphinic acid (Cyanex 302) as ion carriers, is shown. The influence of extractant nature on the selectvity and efficiency of cation transport has been examined. Zn(II) can be effectively removed from dilute aqueous chloride solutions containing equilmolar mixture of Zn(II) and Cd(II) ions in transport through PIMs with di(2,4,4-trimethylpentyl)phosphinic acids, bis(2,4,4-trimethylpentyl)monothiophosphinic acid or di(2-ethylhexyl)phosphoric acid as the ionic carriers into 1.0 M HCl as the receiving phase. The per cent removal of Zn(II) and Cd(II) ions increases with an increase in pH, but more efficient separation of Zn(II) than Cd(II) ions decreases with pH increase in the source phase. Zn(II) can be also effectively removed from dilute aqueous chloride solutions containing equimolar mixture of Zn(II), Cd(II), Cu(II), Co(II) and Ni(II) ions by its transport through PIMs with D2EHPA, Cyanex 272 and Cyanex 302. All ions investi-gated are effectively removed with di(2,4,4-trimethylpentyl)dithio-phosphinic acids (Cyanex 301) as the ionic carrier into 1.0 M HCl as the receiving phase. The per cent removal of all metal ions investigated increases with an increase in pH of solution in the source phase. The initial transport fluxes of all metal ions through PIM with Cyanex 272 increase with an increase in an initial chloride acid concentration in the receiving phase.
Rocznik
Strony
73--82
Opis fizyczny
Bibliogr. 14 poz., tab., rys.
Twórcy
autor
  • Department of Metal Extraction and Recirculation, Częstochowa University of Technology, 42-200 Częstochowa, ul. Armii Krajowej 19, Poland
autor
  • Institute of Inorganic Chemistry and Metallurgy of Rare Elements, Wrocław University of Technology, 50-370 Wrocław, Wybrzeże Wyspiańskiego 27, Poland
Bibliografia
  • [1] SASTRE A.M., KUMAR A., SHUKLA J.P, SINGH R.K., Improved Techniques in Liquid Membrane Separations: An Overview, Separation and Purification Methods, 1998, 27, 213–298.
  • [2] WODZKI R., SIONKOWSKI G., Hybrid: polymer-liquid-polymer membrane system for removal of heavy metal ions from waste waters, [in:] Howell J.A., Noworyta A. (Eds.), Towards Hybrid Membrane and Biotechnology Solutions for Polish Environmental Problems, Wrocław Technical University Press, Wrocław, 1995, 235–239.
  • [3] BARTSCH R.A., WAY J. (Eds.), Chemical Separation with Liquid Membranes, ACS Symposium Series 642, Amer. Chem. Soc., 1996, Washington, DC.
  • [4] SUGIURA M., KIKKAWA M., URITA S., Sep. Sci. Technol., 1987, 22, 2263–2271.
  • [5] SOLE K.C., HISKEY J.B., Solvent extraction characteristic of thiosubstituted organophosphinic acid extractants, Hydrometallurgy, 1992, 30, 345–365.
  • [6] BINGHUA Y., NAGAOSA M., SATAKE A., NOMURA K., HORITA K., Solvent Ext. Ion Exch., 1996, 14, 849–870.
  • [7] WALKOWIAK W., GEGA J., Transition metal cation separation by organophosphorous compounds in liquid membrane processes, [in:] Chemical separations with liquid membranes, Bartsch R.A. (Ed.), Kluwer Academic Pub., 1996, Washington.
  • [8] GĘGA J., WALKOWIAK W., GAJDA B., Separation of Co(II) and Ni(II) ions by supported and hybrid liquid membranes, Sep. Purification Technol., 2001, 22–23, 551–558.
  • [9] WODZKI R., SIONKOWSKI G., POZNIAK G., Sep. Sci. Technol., 1999, 34, 627–649.
  • [10] ATA O.N., BESE A.V., DÖNMEZ B., CAKICI A., Effect of parameters on the transport of zinc ion through supported liquid membrane, Chemical Engineering and Processing, 2004, 43, 895–903.
  • [11] ULEWICZ M., WALKOWIAK W., Separation of zinc(II) and cadmium(II) ions from sulfate solutions by ion flotation and transport through liquid membranes, Physicochemical Problems of Mineral Processing, 2003, 37, 77–86.
  • [12] ULEWICZ M., WALKOWIAK W., GĘGA J., POŚPIECH B., Zinc(II) selective removal from other transition metal ions by solvent extraction and transport through polymer inclusion membranes with D2EHPA, Ars Separatoria Acta, 2003, 2, 47–55.
  • [13] ULEWICZ M., GĘGA J., WALKOWIAK W., Selektywne wydzielanie jonów Zn(II) w procesie transportu przez polimerowe membrany inkluzyjne zawierające Cyanex 272, Monografie Komitetu Inżynierii Środowiska PAN, 2004, 22, 305–312.
  • [14] ALGUACIL F.J., NAVARRO P., Permeation of cadmium through a supported liquid membrane impregnated with Cyanex 923, Hydrometallurgy, 2001, 61, 137–142.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPG5-0011-0028
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