Recovering Battery-Grade LiOH·H2O from Spent Lithium-Containing Sagger Crucible by Thermal Dehydration and BaSO4-Driven Double Decomposition

This study develops and validates an integrated hydrometallurgical process to recover battery-grade lithium hydroxide monohydrate from spent aluminosilicate sagger crucibles. Lithium was first leached as Li2SO4 from the crucibles using sulfuric acid; the Li2SO4·H2O present in the leachate was then thermally decomposed at 300 °C to Li2SO4 + H2O, as confirmed by TGA-guided selection and XRD. Subsequent conversion to LiOH proceeded via double decomposition with Ba(OH)2. Guided by HSC-based equilibrium simulations and an Eh–pH analysis of the Li–Ba–S–H2O system, reaction conditions were optimized over 60–80 °C and [OH−]/[Li+] = 1–3. The optimum was identified at 70 °C and [OH−]/[Li+] = 1, delivering a conversion efficiency of 98.78% and a Li recovery of 98.86%. Two-end-point acid titration indicated a LiOH content of 90.29 wt.% in solution with minimal Li2CO3 formation, consistent with processing under vacuum–Ar to suppress CO2 uptake. The crystallized product obtained by evaporation at ≥90 °C for 24 h was confirmed as LiOH·H2O (with LiOH) by XRD, while the solid by-product was single-phase BaSO4. ICP-OES measured a final LiOH·H2O purity of 99.8%.

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Publication Details

Journal
Metals
Published
2025-11-25
DOI
https://doi.org/10.3390/met15121293
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
0.00

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article

Recovering Battery-Grade LiOH·H2O from Spent Lithium-Containing Sagger Crucible by Thermal Dehydration and BaSO4-Driven Double Decomposition

Jei‐Pil Wang, S.J. Heo
Metals
Extraction and Separation Processes
article

Recovering Battery-Grade LiOH·H2O from Spent Lithium-Containing Sagger Crucible by Thermal Dehydration and BaSO4-Driven Double Decomposition

Jei‐Pil Wang, S.J. Heo
article en

Abstract

This study develops and validates an integrated hydrometallurgical process to recover battery-grade lithium hydroxide monohydrate from spent aluminosilicate sagger crucibles. Lithium was first leached as Li2SO4 from the crucibles using sulfuric acid; the Li2SO4·H2O present in the leachate was then thermally decomposed at 300 °C to Li2SO4 + H2O, as confirmed by TGA-guided selection and XRD. Subsequent conversion to LiOH proceeded via double decomposition with Ba(OH)2. Guided by HSC-based equilibrium simulations and an Eh–pH analysis of the Li–Ba–S–H2O system, reaction conditions were optimized over 60–80 °C and [OH−]/[Li+] = 1–3. The optimum was identified at 70 °C and [OH−]/[Li+] = 1, delivering a conversion efficiency of 98.78% and a Li recovery of 98.86%. Two-end-point acid titration indicated a LiOH content of 90.29 wt.% in solution with minimal Li2CO3 formation, consistent with processing under vacuum–Ar to suppress CO2 uptake. The crystallized product obtained by evaporation at ≥90 °C for 24 h was confirmed as LiOH·H2O (with LiOH) by XRD, while the solid by-product was single-phase BaSO4. ICP-OES measured a final LiOH·H2O purity of 99.8%.

MetalsVol. 15(12)
Hanyang University (KR), Pukyong National University (KR)
Ministry of Trade, Industry and Energy
Openalex Percentile: Top 62%
Extraction and Separation Processes
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Recovering Battery-Grade LiOH·H2O from Spent Lithium-Containing Sagger Crucible by Thermal Dehydration and BaSO4-Driven Double Decomposition — Jei‐Pil Wang, S.J. Heo · Metals (2025) | TGRS Research Map | TGRS