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Selective transport of copper(II) ions across polymer inclusion membrane with aromatic β–diketones as carriers

Radzymińska-Lenarcik E., Witt K., Bożejewicz D.

Physicochemical Problems of Mineral Processing

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2018

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Vol. 54, iss. 3

741--750

EN

The transport of Cu(II) ions from an equimolar mixture of Co(II), Ni(II), and Cu(II) ions as well as from solutions containing only Cu(II) ions in the feed phase through polymer inclusion membranes (PIMs) with aromatic β–diketones as carriers has been investigated. The polymer membranes consisted of polyvinylchloride (PVC) as the support, bis(2-ethylhexyl)adipate (ADO) as plasticizer, and aromatic β–diketones (benzoylacetone (1) and dibenzoylmethane (2)) as ion carriers. The transport selectivity of PIMs with 1 and 2 was: Cu(II) > Co(II) > Ni(II). The highest recovery factors of Cu(II) ions were observed for 1 (94.0%), whereas for Co(II) and Ni(II) the factors were 21.4 and 7.3%, respectively. The Cu(II)/Co(II) and Cu(II)/Ni(II) selectivity coefficients were equal to 8.9 and 33.7 (for 1), 6.4 and 28.3 (for 2), respectively.

2

Application of polymer inclusion membranes doped with 1-hexyl-4-methylimidazole for pertraction of zinc(II) and other transition metal ions

Ulewicz M., Radzyminska-Lenarcik E.

Physicochemical Problems of Mineral Processing

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2015

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Vol. 51, iss. 2

447--460

EN

Transport of Zn(II) from unary aqueous chloride solutions and from solutions which contain mixtures of Cd(II), Co(II) and Ni(II) ions in source phases (cMe = 0.001 mol/dm3, pH = 6.0) across polymer inclusion membranes (PIMs) doped with 1-hexyl-4-methylimidazole as ion carrier was studied. The use of 1-hexyl-4-methylimidazole enables the separation of 98.5% Zn(II) from a unary solution and 96.9% from a quaternary solution of Zn(II)-Cd(II)-Co(II)-Ni(II) after running the process for 24 hours. Using that ion carrier, the metals are transported in the following order: Zn(II) > Cd(II) > Ni(II) > Co(II), and the selectivity coefficients of Zn(II)/Cd(II), Zn(II)/Ni(II), and Zn(II)/Co(II) are 12.9, 23.4 and 40.8, respectively. Findings of atomic force microscopy (AFM) examinations as well as thermograms of a polymer inclusion membrane containing 1-hexyl-4-methylimidazole are also presented. A membrane with 1.0 mol/dm3 of carrier has a porosity of 15.8%, and roughness of 6.6 nm. The membranes remain thermally stable at temperatures up to 200oC. The findings were compared with earlier-reported results for 1-hexylimidazole.

3

Zastosowanie ciekłych membran im mobilizowanych i emulsyjnych w procesie separacji jonów Zn(II), Cu(II), Co(II) i Ni(II)

Gęga J.

Hutnik, Wiadomości Hutnicze

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2007

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Vol. 74, nr 6

333-337

PL

Przedstawiono próbę zastosowania ciekłych membran emulsyjnych i immobilizowanych do rozdzielenia mieszaniny kationów: Zn(II), Cu(II), Co(II) i Ni(II). Stwierdzono, że najważniejszym czynnikiem decydującym o efektywności separacji jest kwasowość roztworu wyjściowego. Wykazano, że przez zastosowanie D2EHPA w roli przenośnika jonów możliwe jest rozdzielenie wyjściowej mieszaniny w procesie składającym się z trzech etapów.

EN

An application of supported and emulsion liquid membranes for separation of mixture of Zn(II), Cu(II), Co(II) and Ni(II) cations is presented. It is shown that the most important factor influencing on separation efficiency is acidity of an initial solution. There is possible a satisfactory separation of investigated metal ions in three-stage process using D2EHPA as an ion carrier.