In Situ Production of Carbonate Anions from Water Electrolysis and CO<sub>2</sub> Absorption for Li<sub>2</sub>CO<sub>3</sub> Crystallization from Preconcentrated Brines

Lithium carbonate (Li2CO3) is normally crystallized from concentrated brines via the addition of sodium carbonate (Na2CO3, soda ash). While this is a methodology largely proved and in implementation in almost all facilities in operation today, it is a chemical intensive procedure. Both the associated costs of sodium carbonate and the logistic issues of bringing large amounts of chemicals to the remote locations where lithium mining from brines takes place should be considered. Here a new prospective technology is proposed for the in situ production of carbonate anions via water reduction and direct CO2 absorption on alkaline media. Experiments were performed on a real concentrated brine sample obtained from an operating facility in the Lithium Triangle. In the first electrolysis, traces of divalent cations were removed with only 1.3% of the total Li+ content in the original brine being trapped in the obtained solid. The second electrolysis produced removal from the brine from 67.2% of the originally contained Li+. Studies were conducted to improve the purification of the solid, since in the highly saline brine (total dissolved solids of 412 g L–1) the as obtained solid was only 70.5% pure. Upon 2 purification steps, a solid 99.1% pure could be obtained. A third electrolysis step could crystallize further 11.8% extra of the original Li+ content, albeit at a much higher energy cost. Upon brine treatment, 88.0 g CO2 per liter of brine fed to the first electrolysis could be absorbed; 63.2 g of which remain in the Li+ depleted brine, and only 24.8 g in the obtained solids.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2024-09-13
DOI
https://doi.org/10.1021/acs.iecr.4c02193
Citations
1
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
0.21

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article

In Situ Production of Carbonate Anions from Water Electrolysis and CO2 Absorption for Li2CO3 Crystallization from Preconcentrated Brines

César H. Díaz Nieto, Victoria Flexer, Nadia Carla Zeballos, Walter R. Torres
1 citations
Industrial & Engineering Chemistry Research
Extraction and Separation Processes
0.21
article

In Situ Production of Carbonate Anions from Water Electrolysis and CO2 Absorption for Li2CO3 Crystallization from Preconcentrated Brines

César H. Díaz Nieto, Victoria Flexer, Nadia Carla Zeballos, Walter R. Torres
article en
1 citations

Abstract

Lithium carbonate (Li2CO3) is normally crystallized from concentrated brines via the addition of sodium carbonate (Na2CO3, soda ash). While this is a methodology largely proved and in implementation in almost all facilities in operation today, it is a chemical intensive procedure. Both the associated costs of sodium carbonate and the logistic issues of bringing large amounts of chemicals to the remote locations where lithium mining from brines takes place should be considered. Here a new prospective technology is proposed for the in situ production of carbonate anions via water reduction and direct CO2 absorption on alkaline media. Experiments were performed on a real concentrated brine sample obtained from an operating facility in the Lithium Triangle. In the first electrolysis, traces of divalent cations were removed with only 1.3% of the total Li+ content in the original brine being trapped in the obtained solid. The second electrolysis produced removal from the brine from 67.2% of the originally contained Li+. Studies were conducted to improve the purification of the solid, since in the highly saline brine (total dissolved solids of 412 g L–1) the as obtained solid was only 70.5% pure. Upon 2 purification steps, a solid 99.1% pure could be obtained. A third electrolysis step could crystallize further 11.8% extra of the original Li+ content, albeit at a much higher energy cost. Upon brine treatment, 88.0 g CO2 per liter of brine fed to the first electrolysis could be absorbed; 63.2 g of which remain in the Li+ depleted brine, and only 24.8 g in the obtained solids.

Industrial & Engineering Chemistry ResearchVol. 63(38)
Consejo Nacional de Investigaciones Científicas y Técnicas (AR), National University of Jujuy (AR), National Institute of Industrial Technology (AR)
Fondo para la Investigación Científica y Tecnológica
Clean water and sanitation
Openalex Percentile: Top 52%
Extraction and Separation Processes
0.21
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