Preprint Article Version 1 Preserved in Portico This version is not peer-reviewed

Simultaneously Recovery of Thorium and Tungsten by Hybrid Electrolysis–Nanofiltration Processes

Version 1 : Received: 17 December 2023 / Approved: 18 December 2023 / Online: 19 December 2023 (09:44:08 CET)

A peer-reviewed article of this Preprint also exists.

Man, G.T.; Albu, P.C.; Nechifor, A.C.; Grosu, A.R.; Popescu (Stegarus), D.I.; Grosu, V.-A.; Marinescu, V.E.; Nechifor, G. Simultaneously Recovery of Thorium and Tungsten through Hybrid Electrolysis–Nanofiltration Processes. Toxics 2024, 12, 103. Man, G.T.; Albu, P.C.; Nechifor, A.C.; Grosu, A.R.; Popescu (Stegarus), D.I.; Grosu, V.-A.; Marinescu, V.E.; Nechifor, G. Simultaneously Recovery of Thorium and Tungsten through Hybrid Electrolysis–Nanofiltration Processes. Toxics 2024, 12, 103.

Abstract

The recovery and recycling of metals that generate toxic ions in the environment is of particular importance, especially when these are tungsten and, in particular, thorium. The radioactive element thorium has unexpectedly accessible domestic applications (filaments of light bulbs and electronic tubes, welding electrodes, working alloys containing aluminum and magnesium), which lead to its appearance in electrical and electronic waste from municipal waste management platforms. The current paper proposes the simultaneous recovery of waste containing tungsten and thorium from welding electrodes. The simultaneous recovery is done by applying a hybrid membrane electrolysis technology coupled with nanofiltration. An electrolysis cell with sulphonated polyether–ether–ketone membranes (sPEEK) and a nanofiltration module with chitosan-polypropylene membranes (C–PHF–M) are used to carry out the hybrid process. The analysis of welding electrodes led to a composition of: W (tungsten) 89.4%; Th 7.1%; O2 2.5% and Al 1.1%. Thus, the parameters of the electrolysis process were chosen according to the speciation of the three metals suggested by the superimposed Pourbaix diagrams. At a constant potential of 20.0 V and an electrolysis current of 1.0 A, the pH is varied and the possible composition of the solution in the anodic workspace is analyzed. Favorable conditions for both electrolysis and nanofiltration were obtained at pH from 6 to 9, when the soluble tungstate ion, the aluminum hydroxide and solid thorium dioxide were formed. Through a first nanofiltration, the tungstate ion is obtained in the permeate, and thorium dioxide and aluminum hydroxide in the concentrate. By adding a pH 13 solution over the two precipitates, the aluminum is solubilized as sodium aluminate which will be found after the second nanofiltration in permeate, the thorium dioxide remaining integrally (within an error of ±0.1ppm) on the C–PHF–M membrane.

Keywords

thorium recovery; wolfram recovery; membrane processes; membrane electrolysis; nanofiltration; thorium recycling; wolfram recycling; Pourbaix diagrams

Subject

Chemistry and Materials Science, Applied Chemistry

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