Highly Efficient p-Toluenesulfonic Acid-Based Deep-Eutectic Solvents for Cathode Recycling of Li-Ion Batteries

溶解 背景(考古学) 共晶体系 材料科学 化学工程 燃烧 无机化学 锂(药物) 化学 有机化学 冶金 微观结构 工程类 内分泌学 古生物学 生物 医学
作者
María J. Roldán‐Ruiz,M. Luisa Ferrer,Marı́a C. Gutiérrez,Francisco del Monte
出处
期刊:ACS Sustainable Chemistry & Engineering [American Chemical Society]
卷期号:8 (14): 5437-5445 被引量:187
标识
DOI:10.1021/acssuschemeng.0c00892
摘要

The common use of Li-ion batteries (LIBs) in portable devices and electric vehicles is promoting an exponential growth of the rechargeable batteries market. Their use in electric vehicles while not yet so common will be favored in the near future by government incentives aiming to mitigate global warming effects coming from combustion engines. Despite the remote risk of cobalt (Co) and lithium (Li) supplies running low, metals recovery from “postconsumer” scrap is a rapidly expanding topic in the political agenda within the context of the circular economy. Among other recycling technologies, processes using mild conditions and providing high recycling efficiencies are gaining increased interest. For instance, organic acids are particularly interesting for LiCoO2 dissolution even though they typically need the additional use of reducing agents. Herein, we explore the Co (and Li) recovery from spent LIBs using deep eutectic solvents (DESs) at temperatures as low as 90 °C, at times of dissolution as short as 15 min and without the use of any additional reducing agent. In particular, we used the eutectic mixture composed of p-toluenesulfonic acid (PTSA) monohydrate and choline chloride (ChCl) (e.g., PTSA·H2O·ChClDES with a 1:1:1 molar ratio) and aqueous dilutions thereof (e.g., PTSA·2H2O·ChClDES and PTSA·3H2O·ChClDES with 1:2:1 and 1:3:1 molar ratios, respectively). Compared to organic acids, PTSAChCl-based DESs offered a significant reduction of the solute to solvent ratio (in g/L) needed for full Co dissolution. This brings benefits both in economic and sustainable terms that handling low solvent volumes has in industrial processes. Interestingly, Co recovery efficiencies from spent LIBs reached figures of up to 94% over the whole process relating to the extraction from spent LIBs using PTSAChCl-based DESs, the precipitation with either Na2CO3 or (NH4)2CO3, and the final calcination to obtain Co3O4.
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