Peroxodisulphuric acid synthesis in a flow electrolyser and its potential utilisation for black mass leaching

This study demonstrates the electrochemical synthesis of peroxodisulfuric acid (H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>) in a coaxial flow-type electrolyser. It evaluates its potential as a leaching agent for the black mass from spent lithium-ion batteries. The optimised synthesis (conditions: flow rate, current density) achieved high concentrations of (H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>) (≈180 g dm<sup>-3</sup>) at a specific energy consumption of nearly 1.5 Wh g<sup>-1</sup>. The leaching performance of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> was compared with that of conventional systems, including aqua regia and 2 M H<sub>2</sub>SO<sub>4</sub> + H<sub>2</sub>O<sub>2</sub>. While aqua regia completely dissolved the NMC phase, and the H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> mixture ensured nearly full transition metal leaching, H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> leaching resulted in only partial dissolution of Ni (≈61%), Co (≈61%), and Mn (≈5%). However, lithium was fully extracted (≈99.6%) due to dual dissolution from residual electrolyte salts and chemical deintercalation from the cathode lattice. Mechanistic analysis using XRD, AAS, and Pourbaix diagrams revealed that the poor transition metal recovery originates from the extreme oxidising environment of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>, which stabilises insoluble high-valent oxides and prevents reductive dissolution pathways. The results highlight that direct application of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> is less practical than H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> for transition metal extraction but could be exploited for selective Li recovery or integrated into a three-step process: (i) <i>in situ</i> H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> generation, (ii) controlled hydrolysis to H<sub>2</sub>SO<sub>4</sub> + H<sub>2</sub>O<sub>2</sub>, and (iii) reductive leaching. This approach offers industrial advantages, including on-site oxidant production and the elimination of H<sub>2</sub>O<sub>2</sub> transport hazards.

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Journal
RSC Advances
Published
2025-01-01
DOI
https://doi.org/10.1039/d5ra06474k
Primary Topic
Advanced Battery Materials and Technologies
Type
article
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article

Peroxodisulphuric acid synthesis in a flow electrolyser and its potential utilisation for black mass leaching

Fyodor Malchik, Saken Abdimomyn, Sergey Nechipurenko, Yaroslav Zhigalenok et al.
RSC Advances
Advanced Battery Materials and Technologies
article

Peroxodisulphuric acid synthesis in a flow electrolyser and its potential utilisation for black mass leaching

Fyodor Malchik, Saken Abdimomyn, Sergey Nechipurenko, Yaroslav Zhigalenok, Aigerim Tazhibayeva, S.K. Malik, Kaiyrgali Zhumadil, Altynai Tanash
article en

Abstract

This study demonstrates the electrochemical synthesis of peroxodisulfuric acid (H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>) in a coaxial flow-type electrolyser. It evaluates its potential as a leaching agent for the black mass from spent lithium-ion batteries. The optimised synthesis (conditions: flow rate, current density) achieved high concentrations of (H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>) (≈180 g dm<sup>-3</sup>) at a specific energy consumption of nearly 1.5 Wh g<sup>-1</sup>. The leaching performance of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> was compared with that of conventional systems, including aqua regia and 2 M H<sub>2</sub>SO<sub>4</sub> + H<sub>2</sub>O<sub>2</sub>. While aqua regia completely dissolved the NMC phase, and the H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> mixture ensured nearly full transition metal leaching, H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> leaching resulted in only partial dissolution of Ni (≈61%), Co (≈61%), and Mn (≈5%). However, lithium was fully extracted (≈99.6%) due to dual dissolution from residual electrolyte salts and chemical deintercalation from the cathode lattice. Mechanistic analysis using XRD, AAS, and Pourbaix diagrams revealed that the poor transition metal recovery originates from the extreme oxidising environment of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub>, which stabilises insoluble high-valent oxides and prevents reductive dissolution pathways. The results highlight that direct application of H<sub>2</sub>S<sub>2</sub>O<sub>8</sub> is less practical than H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> for transition metal extraction but could be exploited for selective Li recovery or integrated into a three-step process: (i) <i>in situ</i> H<sub>2</sub>SO<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> generation, (ii) controlled hydrolysis to H<sub>2</sub>SO<sub>4</sub> + H<sub>2</sub>O<sub>2</sub>, and (iii) reductive leaching. This approach offers industrial advantages, including on-site oxidant production and the elimination of H<sub>2</sub>O<sub>2</sub> transport hazards.

RSC AdvancesVol. 15(50)
Al-Farabi Kazakh National University (KZ)
Nazarbayev University
Openalex Percentile: Top 68%
Advanced Battery Materials and Technologies
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