Recovery of lithium, nickel and cobalt from mixed lithium-ion batteries in ammonia media

This study investigates the recovery of valuable metals from a mixture of lithium iron phosphate (LFP) and nickel‑manganese‑cobalt (NMC) in an ammoniacal medium. A factorial design of experiments was applied to assess the effects of NH 3 , (NH 4 ) 2 SO 4 , and Na 2 SO 3 concentrations on the leaching behavior of Ni, Mn, Co, and Li. Ammonia enhanced metal dissolution through complexation, (NH 4 ) 2 SO 4 stabilized the pH via buffering, and Na 2 SO 3 acted as a reducing agent improving the dissolution of Ni, Co, and Li. Optimal conditions (6 mol L −1 NH 3 , 3 mol L −1 (NH 4 ) 2 SO 4 , 1 mol L −1 Na 2 SO 3 , 60 °C, S/L = 50 g L −1 ) yielded recoveries of 68.1% Ni, 25.9% Mn, 79.4% Co, 55.6% Li, and 99.7% Cu. An empirical model accurately predicted these dissolution yields. Subsequent solvent extraction enabled selective recovery of Ni, Mn, and Cu using Acorga® M5640, and Li using Cyanex® 936P diluted in kerosene. The proposed flowsheet demonstrates the efficiency and selectivity of ammoniacal leaching as a sustainable alternative to conventional acid-based recycling of lithium-ion batteries. • Factorial design reveals key effects of NH 3 , (NH 4 ) 2 SO 4 and Na 2 SO 3 on leaching. • Ammoniacal leaching achieves high Ni, Co, Li and near-complete Cu recovery. • Na 2 SO 3 improves dissolution via reduction of transition-metal species. • Empirical model accurately predicts multi-metal dissolution yields. • Flowsheet enables selective Ni, Mn, Cu and Li recovery via solvent extraction.

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Publication Details

Journal
Hydrometallurgy
Published
2026-03-24
DOI
https://doi.org/10.1016/j.hydromet.2026.106703
Primary Topic
Extraction and Separation Processes
Type
article
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article

Recovery of lithium, nickel and cobalt from mixed lithium-ion batteries in ammonia media

Hydrometallurgy
Extraction and Separation Processes
article

Recovery of lithium, nickel and cobalt from mixed lithium-ion batteries in ammonia media

article en

Abstract

This study investigates the recovery of valuable metals from a mixture of lithium iron phosphate (LFP) and nickel‑manganese‑cobalt (NMC) in an ammoniacal medium. A factorial design of experiments was applied to assess the effects of NH 3 , (NH 4 ) 2 SO 4 , and Na 2 SO 3 concentrations on the leaching behavior of Ni, Mn, Co, and Li. Ammonia enhanced metal dissolution through complexation, (NH 4 ) 2 SO 4 stabilized the pH via buffering, and Na 2 SO 3 acted as a reducing agent improving the dissolution of Ni, Co, and Li. Optimal conditions (6 mol L −1 NH 3 , 3 mol L −1 (NH 4 ) 2 SO 4 , 1 mol L −1 Na 2 SO 3 , 60 °C, S/L = 50 g L −1 ) yielded recoveries of 68.1% Ni, 25.9% Mn, 79.4% Co, 55.6% Li, and 99.7% Cu. An empirical model accurately predicted these dissolution yields. Subsequent solvent extraction enabled selective recovery of Ni, Mn, and Cu using Acorga® M5640, and Li using Cyanex® 936P diluted in kerosene. The proposed flowsheet demonstrates the efficiency and selectivity of ammoniacal leaching as a sustainable alternative to conventional acid-based recycling of lithium-ion batteries. • Factorial design reveals key effects of NH 3 , (NH 4 ) 2 SO 4 and Na 2 SO 3 on leaching. • Ammoniacal leaching achieves high Ni, Co, Li and near-complete Cu recovery. • Na 2 SO 3 improves dissolution via reduction of transition-metal species. • Empirical model accurately predicts multi-metal dissolution yields. • Flowsheet enables selective Ni, Mn, Cu and Li recovery via solvent extraction.

HydrometallurgyVol. 242
Centre National de la Recherche Scientifique (FR), Université de Technologie de Troyes (FR), Systématique, adaptation, évolution (FR), GeoRessources (FR), Université de Lorraine (FR)
Responsible consumption and production
Openalex Percentile: Top 11%
Extraction and Separation Processes
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