Lithium recovery from battery waste leachate by nanofiltration:
This study focuses on the hydrometallurgical recovery of Li from spent LIBs leachate using nanofiltration (NF) processes. Two key aspects were evaluated, the type of leaching acid (H 2
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This study focuses on the hydrometallurgical recovery of Li from spent LIBs leachate using nanofiltration (NF) processes. Two key aspects were evaluated, the type of leaching acid (H 2
A new type of deep-eutectic solvents (DESs), consisting of ethylene glycol (EG) and sulfosalicylic acid dihydrate (SAD), were designed for efficient leaching valuable metals
Leaching of active cathode materials of Li-ion batteries (LIB) is a hotly contested topic. In the published literature, the best processes utilize concentrated acid (e.g. 2–3 M H 2
Recycling cathodic materials from spent lithium-ion batteries (LIBs) is crucial not just for the environmental aspects but also for the supply of precious raw materials such as
It usually involves two steps: (1) acid leaching, where acid solutions, such as sulfuric acid and hydrochloric acid, are used with reducing agents, such as hydrogen peroxide
The most prevalent method for recycling lithium-ion batteries is acid leaching. However, it has unavoidable disadvantages such as hazardous gas emissions, equipment
Therefore, the use of organic acids to leach lithium-ion batteries has some research significance. 2.2. Ammonia leaching. In recent years, Citric acid exhibits strong
This study collected citric acid leaching and nitric acid leaching inventory data from the published literature and compared them with DES leaching. With leaching 1 kg of
The word lithium-ion battery is commonly used for a battery containing lithium metal, (acid/alkaline leaching, etc.), purification, and recovery process (extraction,
Here, we first reported a direct electro-oxidation method for lithium leaching from spent T-LIBs (Li 0.8 Ni 0.6 Co 0.2 Mn 0.2 O 2); 95.02% of Li in the spent T-LIBs was leached
A process of leaching recovery for cobalt and lithium from spent lithium-ion batteries by citric acid and salicylic acid. Meiling Xu a, Shumei Kang * a, Feng Jiang b, Xinyong Yan a, Zhongbo Zhu
The necessity to preserve the environment and accomplish the rising demand for precious metals has made recycling of spent lithium-ion batteries (LIBs) crucial for
The amount of spent lithium-ion batteries has grown dramatically in recent years, and the development of a recycling process for spent lithium-ion batteries is necessary and
The leaching experiments were conducted using actual LLZO production waste in 1 M of acid at 1:20 S/L ratio at 25 °C for 24 h. The results showed that strong acids, such as H2SO4, almost completely dissolved LLZO.
Lithium-ion batteries with an LFP cell chemistry are experiencing strong growth in the global battery market. Consequently, a process concept has been developed to recycle
Traditional hydrometallurgical methods for recovering spent lithium-ion batteries (LIBs) involve acid leaching to simultaneously extract all valuable metals into the leachate. These methods usually are followed by a
Consequently, researchers explored the use of organic acids and bioleaching to reduce environmental impact (Jiang et al., 2023). Nevertheless, each approach presents
The more environment-friendly acids, so far reported, include formic acid, 19 lactic acid, 14 acetic acid, 20 and citric acid. 21 In the absence of ultrasound, these weaker organic acids would
Chen & Ho (2018) studied the leaching of NMC 111 battery with sulfuric acid as the leaching agent and hydrogen peroxide as the reducing agent. At 70 °C, Ultrasound
ANOVA and F-test of mixed-organic-acid leaching test show that the leaching efficiencies of lithium and manganese were significantly affected by the ratio of citric acid to
Likewise, hydrometallurgy utilizes strong acid/alkali as leaching reagents, requiring multiple intricate stages and complex procedures to obtain high-purity products,
Lithium-ion battery recycling includes discharging and processing exhausted batteries to recover valuable metals for reuse in new battery production. The improper disposal of e-waste draws attention to the possibility
Organic acids, such as gluconic acid, have been widely studied for their potential in the hydrometallurgical recycling of lithium-ion batteries. These organic alternative
Rapid development of energy storage system causes a burst demand of lithium-ion batteries (LIBs), and large number of spent LIBs with high valuable metals are produced. Here we propose a novel application of oxalic
The extraction of valuable metals from spent Ni–Co–Mn oxide (NCM) cathodes typically encounters the use of strong acids or alkalis, often leading to secondary pollution.
The most often used organic leaching agents include ascorbic acid, citric acid, succinic acid, tartaric acid, acetic acid, and formic acid . Under optimal circumstances, the Li-leaching rate of
In the present work, HCl was employed to leach lithium from the anode electrode materials of spent lithium-ion batteries, with H 2 O 2 as the reducing agent. The chemical
The recycling of valuable metals from spent lithium-ion batteries (LIBs) is becoming increasingly important due to the depletion of natural resources and potential pollution from the spent batteries. In this work, different types of
In this investigation, alkaline and reductive acid leaching processes were evaluated and compared in order to determine the effect of parameters such as pH,
from spent lithium-ion battery by nitric acid leaching was controlled by diffusion through product reached when using strong acid as leaching agent . In principle, lithium-ion battery cathode
In the hydrometallurgical process for recycling LIBs, after leaching lithium-ion batteries with inorganic acids , , , organic acids , , , or DESP , , , either the
Focusing on hydrometallurgy, acids have proven to be effective with LIB metal recoveries of over 90% being achieved , organic acids such as sulfuric acid (H 2 SO
On the other hand, reductive acid leaching, with acid sulfuric and hydrazine sulfate (H 2 SO 4 + N 2 H 6 SO 4) solutions resulted in an efficient system, extracting ≥90 %
The recycling of Li from secondary sources was one of the important means to alleviate the imbalance between supply and demand of Li resources [, ,
Citric acid has shown good leaching performance due to its strong chelating properties, which enables good leaching capabilities as a weak organic acid Selective
The use of organic acids (i.e., citric acid, aspartic acid, malic acid, oxalic acid, ascorbic acid, and glycine) as leachants provides an alternative approach to solve the
The Conventional hydrometallurgical processes primarily employ inorganic acids, including hydrochloric acid, 10-12 sulfuric acid, 13-18 nitric acid, 11 and phosphoric
The leaching and recovery of spent lithium batteries (SLiB) using deep eutectic solvents (DESs) have received widespread attention. This review summarizes the latest
Furthermore, SLFP batteries have a high lithium resource level of 1 %, which is far higher than the 0.002 % lithium content in the earth''s crust (Li et al., 2020). SLFP batteries
Rapid development of energy storage system causes a burst demand of lithium-ion batteries (LIBs), and large number of spent LIBs with high valuable metals are produced. Here we propose a novel application of oxalic acid leaching to regenerate Li (Ni 1/3 Co 1/3 Mn 1/3)O 2 (NCM) cathodes from spent LIBs.
ANOVA and F-test of mixed-organic-acid leaching test show that the leaching efficiencies of lithium and manganese were significantly affected by the ratio of citric acid to maleic acid, but not by temperature, whereas cobalt and nickel were both affected by temperature and ratio of acid mixture.
A broad spectrum of organic acids is currently being researched to achieve maximum leaching efficiencies when applied to different cathode materials or spent lithium-ion batteries. Citric acid, a three-protonic carboxylic acid, is one of the most widely studied forms [33, 40, 41, 42, 43, 44, 45].
Under optimal leaching conditions (leaching time of 1.5 h, leaching temperature of 70°C, liquid-solid ratio of 4 mL/g, oxalic acid ratio of 1.3, and sulfuric acid ratio of 1.3), the lithium leaching efficiency reached 89.6%, and the leaching efficiencies of Ni, Co, and Mn were 12.8%, 6.5%, and 21.7%.
Accordingly, the highest leaching rates resulted from a low-level addition of black mass to the leach. Additionally, the highest metal contents of lithium required 0.9 mol/L of acid and 1 vol % of oxidizing agent.
The leaching step is aimed at dissolving the metal components from spent lithium-ion batteries and further processing them in a wet chemical process, as seen in conventional hydrometallurgy [56, 57].