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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received June 16, 2025
Revised August 27, 2025
Accepted September 28, 2025
Available online February 25, 2026
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Selenium Control in the Electrolyte of Electrowinning Nickel System: Speciation, Electrochemical Analysis and Removal Strategies

School of Materials Science and Engineering, Lanzhou University of Technology 1School of Petroleum and Chemical Engineering, Lanzhou University of Technology
lanzhouxuyt@163.com, xiatd@lut.edu.cn
Korean Journal of Chemical Engineering, February 2026, 43(3), 775-788(14)
https://doi.org/10.1007/s11814-025-00573-3

Abstract

Due to its high solubility and potential harm to metals, the speciation, electrochemical behavior, and removal mechanisms of

selenium in the electrowinning nickel system have garnered significant attention for the production of high-purity nickel. The

speciation of selenium in the electrolyte and nickel deposits was analyzed using high-performance liquid chromatographymass

spectrometry and X-ray photoelectron spectroscopy, respectively. The electrochemical behavior of selenium was investigated

using cyclic voltammetry and chronoamperometry in the electrolyte. The selenium removal process was optimized,

and the underlying mechanism of selenium removal was elucidated through a combination of inductively coupled plasma

atomic emission spectrometry, X-ray diffraction, and scanning electron microscopy. The chromatogram results indicate that

the primary speciation of selenium in the electrolyte is Se(VI). Selenium does not affect the nucleation and growth mechanism

of nickel but leads to cathodic polarization. The occurrence states of selenium in the nickel deposits are NiSe, NiSe2,

Ni3Se2,

and SeO2.

Furthermore, selenium removal experiments demonstrated that in nickel sulfate solutions containing 20 mg/L

of Se(IV)/Se(VI), under conditions of 25 °C and pH 2 with 1000 mg/L NaBH4,

the removal efficiency reached 98.77% for

tetravalent selenium (Se(IV)) and 83.60% for hexavalent selenium (Se(VI)). During the chemical reduction process, soluble

selenium was initially reduced to elemental selenium, which subsequently reacted with nickel to form NiSe and Ni3Se2.

This

study provides valuable guidance for the removal of selenium from highly acidic solutions.

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