Lithium-ion battery recycling pre-processing with electrochemical discharge: Enhancing gas product analysis and pH monitoring

Efficient discharge of Lithium-ion Batteries (LIBs) ensures safe recycling. Electrochemical discharge commonly uses NaCl solutions, causing severe corrosion of battery casing and a release of hazardous gases. This work proposes a novel setup to explore a gaseous product formation during electrochemical discharge processes with low gas quantities, in non-corrosive carbonates solutions (Na 2 CO 3 and K 2 CO 3 ). Two discharge setups were tested over 120 h: a conventional setup with a single battery completely immersed in the electrolyte; and a novel half-cells setup with two batteries in series, connected through a platinum wire, and partially immersed in the electrolyte. The two setups showed consistent discharge curves and pH trends, without corrosion. After 70 h, the residual voltage of new LIBs (3.8 V) dropped below the safety threshold (2V, 45 ± 1 % of initial voltage for Na 2 CO 3 and 50 % ± 1 % for K 2 CO 3 ). H 2 production was observed during the first 11 h for Na 2 CO 3 (1722 ± 400 ppm/h) and 9 h for K 2 CO 3 (1519 ± 670 ppm/h), with peaks at 2000–2300 ppm/h after 3–5 h while O 2 and CO 2 production was below the detection limit of the detector (0.1 %-vol for O 2 , 50 ppm for CO 2 ). pH trends in the aqueous electrolytes (pH increased from 11.5 to 11.6 to 12.5 ± 0.48 pH units after 3 h in Na 2 CO 3 , and 12.06 ± 0.06 after 4 h in K 2 CO 3 ) matched H 2 production and the formulation of the hydroxyl ions. The half-cell setup confirmed that H 2 release at negative half-cell, increasing the pH of discharge solution. These results presented a safe method for LIBs discharge, avoiding corrosion and hazardous gases release. • Method to accurately quantify small gas evolution during electrochemical discharge. • H 2 release occurs at negative half-cell, matched by pH trend in discharge solutions. • pH can also work as an indicator of discharge rate and H 2 production. • CO 2 emission not observed at LIBs discharge in carbonate salt solutions.

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Publication Details

Journal
Cleaner Engineering and Technology
Published
2025-03-18
DOI
https://doi.org/10.1016/j.clet.2025.100938
Citations
1
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
0.71

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article

Lithium-ion battery recycling pre-processing with electrochemical discharge: Enhancing gas product analysis and pH monitoring

Martina Bruno, Silvia Fiore, Annukka Santasalo-Aarnio
1 citations
Cleaner Engineering and Technology
Extraction and Separation Processes
0.71
article

Lithium-ion battery recycling pre-processing with electrochemical discharge: Enhancing gas product analysis and pH monitoring

Martina Bruno, Silvia Fiore, Annukka Santasalo-Aarnio
article en
1 citations

Abstract

Efficient discharge of Lithium-ion Batteries (LIBs) ensures safe recycling. Electrochemical discharge commonly uses NaCl solutions, causing severe corrosion of battery casing and a release of hazardous gases. This work proposes a novel setup to explore a gaseous product formation during electrochemical discharge processes with low gas quantities, in non-corrosive carbonates solutions (Na 2 CO 3 and K 2 CO 3 ). Two discharge setups were tested over 120 h: a conventional setup with a single battery completely immersed in the electrolyte; and a novel half-cells setup with two batteries in series, connected through a platinum wire, and partially immersed in the electrolyte. The two setups showed consistent discharge curves and pH trends, without corrosion. After 70 h, the residual voltage of new LIBs (3.8 V) dropped below the safety threshold (2V, 45 ± 1 % of initial voltage for Na 2 CO 3 and 50 % ± 1 % for K 2 CO 3 ). H 2 production was observed during the first 11 h for Na 2 CO 3 (1722 ± 400 ppm/h) and 9 h for K 2 CO 3 (1519 ± 670 ppm/h), with peaks at 2000–2300 ppm/h after 3–5 h while O 2 and CO 2 production was below the detection limit of the detector (0.1 %-vol for O 2 , 50 ppm for CO 2 ). pH trends in the aqueous electrolytes (pH increased from 11.5 to 11.6 to 12.5 ± 0.48 pH units after 3 h in Na 2 CO 3 , and 12.06 ± 0.06 after 4 h in K 2 CO 3 ) matched H 2 production and the formulation of the hydroxyl ions. The half-cell setup confirmed that H 2 release at negative half-cell, increasing the pH of discharge solution. These results presented a safe method for LIBs discharge, avoiding corrosion and hazardous gases release. • Method to accurately quantify small gas evolution during electrochemical discharge. • H 2 release occurs at negative half-cell, matched by pH trend in discharge solutions. • pH can also work as an indicator of discharge rate and H 2 production. • CO 2 emission not observed at LIBs discharge in carbonate salt solutions.

Cleaner Engineering and TechnologyVol. 26
Politecnico di Torino (IT), Aalto University (FI)
Academy of Finland
Openalex Percentile: Top 35%
Extraction and Separation Processes
0.71
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