An Ecofriendly and Cost-Effective Method for Producing LiOH from Li <sub>2</sub> SO <sub>4</sub> Using Indigenously Engineered Bipolar Membrane Electrodialysis

Lithium hydroxide, which is utilized in lithium-ion battery applications, is produced as an intermediary from lithium sulfate (Li<sub>2</sub>SO<sub>4</sub>) in the conventional lithium extraction process. This work represents a more convenient way for the production of LiOH from lithium sulfate using the bipolar membrane electrodialysis (BMED) process at various applied potentials. Here, we have prepared the bipolar membrane (BPM) using the solution casting technique, having an interfacial layer (IL) of sulfonated molybdenum sulfide (S-MoS<sub>2</sub>) to boost the water splitting rate. Sulfonated poly(ether sulfone) and quaternized poly(phenylene oxide) were used as the cation exchange layer (CEL) and the anion exchange layer (AEL) in the bipolar membrane (BPM), respectively. Various characterization techniques, such as NMR, FE-SEM, UTM, and XRD, were carried out for the membranes and the S-MoS<sub>2</sub> catalyst. The current-voltage curves (CVCs) for the prepared BPMs were recorded in 0.1 M LiCl to evaluate the various operational parameters for the BMED process. The feed solution of 0.4 M Li<sub>2</sub>SO<sub>4</sub> produced 0.62 M of LiOH. To produce high-purity LiOH, dilute H<sub>2</sub>SO<sub>4</sub> was circulated in the acid compartment (Acid mode), which reduced the migration of sulfate ions from the acid to the base compartment. This reduced the average sulfate flux from 0.034 × 10<sup>-4</sup> mol m<sup>-2</sup> s<sup>-1</sup> to 0.021 × 10<sup>-4</sup> mol m<sup>-2</sup> s<sup>-1</sup> for the dissociation of 0.2 M Li<sub>2</sub>SO<sub>4</sub> at 6 V/pair. All Acid-mode experiments showed more than 90% lithium recovery and higher product purity with an energy consumption of 1.77 kWh kg<sup>-1</sup>. After further reducing the sulfate content, battery-grade LiOH could be obtained. This work illustrates that the BMED process can effectively produce LiOH from Li<sub>2</sub>SO<sub>4</sub> and replace the conventional solvent extraction and chemical precipitation process by excluding the large amounts of bases, related precipitation, and solid-liquid separation steps.

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Journal
Langmuir
Published
2026-01-12
DOI
https://doi.org/10.1021/acs.langmuir.5c04466
Primary Topic
Membrane-based Ion Separation Techniques
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article
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article

An Ecofriendly and Cost-Effective Method for Producing LiOH from Li 2 SO 4 Using Indigenously Engineered Bipolar Membrane Electrodialysis

Nehal H. Rathod, Sarthak Mishra, Vartika Sharma, Vaibhav Kulshrestha
Langmuir
Membrane-based Ion Separation Techniques
article

An Ecofriendly and Cost-Effective Method for Producing LiOH from Li 2 SO 4 Using Indigenously Engineered Bipolar Membrane Electrodialysis

Nehal H. Rathod, Sarthak Mishra, Vartika Sharma, Vaibhav Kulshrestha
article en

Abstract

Lithium hydroxide, which is utilized in lithium-ion battery applications, is produced as an intermediary from lithium sulfate (Li<sub>2</sub>SO<sub>4</sub>) in the conventional lithium extraction process. This work represents a more convenient way for the production of LiOH from lithium sulfate using the bipolar membrane electrodialysis (BMED) process at various applied potentials. Here, we have prepared the bipolar membrane (BPM) using the solution casting technique, having an interfacial layer (IL) of sulfonated molybdenum sulfide (S-MoS<sub>2</sub>) to boost the water splitting rate. Sulfonated poly(ether sulfone) and quaternized poly(phenylene oxide) were used as the cation exchange layer (CEL) and the anion exchange layer (AEL) in the bipolar membrane (BPM), respectively. Various characterization techniques, such as NMR, FE-SEM, UTM, and XRD, were carried out for the membranes and the S-MoS<sub>2</sub> catalyst. The current-voltage curves (CVCs) for the prepared BPMs were recorded in 0.1 M LiCl to evaluate the various operational parameters for the BMED process. The feed solution of 0.4 M Li<sub>2</sub>SO<sub>4</sub> produced 0.62 M of LiOH. To produce high-purity LiOH, dilute H<sub>2</sub>SO<sub>4</sub> was circulated in the acid compartment (Acid mode), which reduced the migration of sulfate ions from the acid to the base compartment. This reduced the average sulfate flux from 0.034 × 10<sup>-4</sup> mol m<sup>-2</sup> s<sup>-1</sup> to 0.021 × 10<sup>-4</sup> mol m<sup>-2</sup> s<sup>-1</sup> for the dissociation of 0.2 M Li<sub>2</sub>SO<sub>4</sub> at 6 V/pair. All Acid-mode experiments showed more than 90% lithium recovery and higher product purity with an energy consumption of 1.77 kWh kg<sup>-1</sup>. After further reducing the sulfate content, battery-grade LiOH could be obtained. This work illustrates that the BMED process can effectively produce LiOH from Li<sub>2</sub>SO<sub>4</sub> and replace the conventional solvent extraction and chemical precipitation process by excluding the large amounts of bases, related precipitation, and solid-liquid separation steps.

LangmuirVol. 42(3)
Central Salt and Marine Chemicals Research Institute (IN), Academy of Scientific and Innovative Research (IN)
Clean water and sanitation
Openalex Percentile: Top 90%
Membrane-based Ion Separation Techniques
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