Comparative Study of Different Ion-Exchange Membrane Types in Diffusion Dialysis for the Separation of Sulfuric Acid and Nickel Sulfate

Сравнительное исследование различных типов ионообменных мембран в диффузионном диализе для разделения серной кислоты и сульфата никеля
S. A. Loza, N. V. Loza, Nikita Kovalchuk, N. A. Romanyuk, Julia Loza
2023-03-30

anion-exchange membranecation-exchange membranediffusion dialysisheterogeneous membraneion-exchange membranesmembrane thicknessquaternary ammoniumsulfuric acid and nickel sulfate separation
The possibility of using various types of ion-exchange membranes in diffusion dialysis for the separation of sulfuric acid and nickel sulfate has been evaluated. The process of the dialysis separation of a real waste solution from an electroplating facility containing 252.3 g/L of sulfuric acid, 20.9 g/L of nickel ions and small amounts of zinc, iron, copper ions, etc. has been studied. Heterogeneous cation-exchange membrane containing sulfonic groups and heterogeneous anion-exchange membranes with different thicknesses (from 145 μm to 550 μm) and types of fixed groups (four samples with quaternary ammonium base and one sample with secondary and tertiary amines) have been used. The diffusion fluxes of sulfuric acid, nickel sulfate, and the total and osmotic fluxes of the solvent have been determined. The use of a cation-exchange membrane does not allow the separation of the components, since the fluxes of both components are low and comparable in magnitude. The use of anion-exchange membranes makes it possible to efficiently separate sulfuric acid and nickel sulfate. Anion-exchange membranes with quaternary ammonium groups are more effective in the diffusion dialysis process, while the thin membrane turns out to be the most effective.
1
Anion-exchange membranes bearing quaternary ammonium fixed groups perform better in diffusion dialysis than membranes with secondary/tertiary amines.
2
Anion-exchange membranes enable efficient separation of sulfuric acid and nickel sulfate in diffusion dialysis.
3
Diffusion dialysis can be applied to separate sulfuric acid (252.3 g/L) and nickel sulfate (20.9 g/L) from real electroplating waste solution containing minor other metal ions.
4
Heterogeneous cation-exchange membrane with sulfonic groups fails to separate sulfuric acid and nickel sulfate because both component fluxes are low and comparable.
5
Thinner anion-exchange membranes (as thin as 145 μm tested) are more effective for diffusion dialysis separation than thicker ones (up to 550 μm).

Diffusion dialysis separation of sulfuric acid and nickel sulfate from an electroplating waste solution using various ion-exchange membranes

Effectiveness of different ion-exchange membrane types (heterogeneous cation-exchange with sulfonic groups and heterogeneous anion-exchange with quaternary ammonium or secondary/tertiary amine groups, varying thicknesses) on diffusion fluxes of sulfuric acid and nickel sulfate and on solvent total/osmotic fluxes to achieve component separation

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Publication Date
2023-03-30
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S. A. Loza
N. V. Loza
Nikita Kovalchuk
N. A. Romanyuk
Julia Loza
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