直接回收电动汽车生产废料 NMC532 阴极材料

Emily C. Giles, Abbey Jarvis, Alexander T. Sargent, Paul A. Anderson, Phoebe K. Allan and Peter R. Slater
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摘要

随着电动汽车(EV)的普及,全球锂离子电池产量急剧增加。据预测,随着产量的增加,不仅需要回收的报废电池会大量增加,而且还会产生大量的生产废料,尤其是在千兆工厂建立的早期阶段。此类电池电极材料的回收利用有许多挑战需要考虑,特别是从电流收集器分层和去除粘合剂,例如阴极材料主要是聚偏二氟乙烯(PVDF)。传统的火法冶金或湿法冶金方法需要经过多个分离步骤才能获得纯金属盐,然后才能重新合成阴极活性材料,因此是一种高成本、高二氧化碳排放量和高废料的工艺。然而,生产废料为采用成本较低、对环境影响较小的直接回收工艺提供了可能性,从而保留了电极材料的制造价值。为了说明这种方法的潜力,我们在此展示了一种直接回收电动汽车生产废料阴极材料的方法,即利用低温热处理分解粘合剂,使阴极材料与铝集流器分层。结果表明,只需添加少量的锂就能提高电化学性能(第一周期放电容量(2.5-4.2 V)分别为 129(2) mA h g-1 和 146(4) mA h g-1,锂的添加量分别为 0 wt% 和 10 wt%)。通过将上限电压窗口提高到 4.3 V,可进一步提高电化学性能(在 2.5-4.2 V 和 2.5-4.3 V 下,第一周期放电容量分别为 146(4) mA h g-1 和 164(2) mA h g-1)。
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Direct recycling of EV production scrap NMC532 cathode materials†

The transition to widespread adoption of electric vehicles (EVs) is leading to a steep increase in lithium ion battery production around the world. With this increase it is predicted there will not only be a large increase in end of life batteries needing to be recycled, but also a substantial amount of production scrap, particularly in the early stages of gigafactory set-up. The recycling of such battery electrode materials has a number of challenges which need to be considered, in particular the delamination from the current collector and removal of the binder, e.g. mainly polyvinylidene fluoride (PVDF) for cathode materials. Traditional pyrometallurgy or hydrometallurgy approaches require multiple separation steps to obtain pure metal salts before resynthesising the cathode active material, and so can be high cost, high CO2 and high waste processes. Production scrap in particular, however, offers the potential for lower cost and lower environmental impact direct recycling processes to be employed, which preserves the manufactured value of the electrode material. To illustrate the potential of such an approach, here we demonstrate a direct recycling approach on EV production scrap cathode materials which utilises a low temperature heat treatment to decompose the binder and allow delamination of the cathode material from the Al current collector. A further higher temperature heat treatment is then employed to ensure complete binder removal and regenerate the cathode, with the results showing that the addition of a small amount of Li is required to improve electrochemical performance (first cycle discharge capacity (2.5–4.2 V) of 129(2) mA h g−1 and 146(4) mA h g−1 with 0 wt% and 10 wt% added lithium, respectively). Electrochemical performance can be further improved by increasing the upper voltage window to 4.3 V (first cycle discharge capacity of 146(4) mA h g−1 and 164(2) mA h g−1 at 2.5–4.2 V and 2.5–4.3 V, respectively).

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