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Environmentally Physical Separation and Recycling for the Spent Automotive Lithium-Ion Batteries

机译:废旧汽车锂离子电池的环境物理分离和回收

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摘要

Nowadays, high power Lithium-ion batteries are used as power sources for automobiles in significant quantities. The environmental recycling and resources reuse of these spent automotive Lithium-ion batteries should be highly desired, after their useful lives end. An automotive Li-ion battery pack consists of hundreds of or more individual cells, which are connected and assembled into a pack with control circuitry, as well as thermal and battery management system. These components could be recycled intact from the battery pack, but the recycling process of these individual cells with different chemical compositions is more complicated. In this paper, an effective physical recycling process is put forward and applied to 60Ah prismatic Lithium-ion batteries with steel cove, which are used in electric vehicles produced by China's Beijing New Energy Automotive Corporation. The recycling process includes the first electrolyte extraction and harmless treatment, cell incision and components separation, and the recovery of active materials. The cleanly separated components such as current collectors, active materials and separator, are high-purity materials which could be reused directly as raw materials to produce another high-value product. Firstly, it is very important to ensure the safety and prevent explosion during the recycling processes, because Lithium-ion batteries contain toxic and flammable electrolyte. The pre-treatment of the individual cell includes the collection and concentration process of organic electrolyte: safe and non-toxic organic solvent was injected into the sealed cell to dissolve the electrolyte, then withdrew and distilled to reuse. The collection process was repeated, finally the sealed cell was vacuum extracted. The distilled residues contain some organic electrolyte solvents such as ethyl methyl carbonate, diethyl carbonate, and salt LiPF6. It was treated with alkali solution to reduce the toxicity of LiPF6, and the reaction product gas HF was absorbed by Ca(OH)2 to form CaF2. The harmless treatment of the LiPF6 in the electrolyte is helpful to carrying out the subsequence processes. Secondly, the individual cell without electrolyte was opened by cold cutting mode from the top, and jell roll of lithium-ion cell was withdrew from the steel can by clamp. Then jelly roll was reversely winded to part cathode electrode, anode electrode and separator. The segregation of cathode and anode electrodes is benefitial to respectively recycle high-purity different electrode materials (LiFeP04 with binder and conductive additive, graphite with binder) and Cu, Al foils, and avoid the cross contamination. It is quite different the chemical process, by which batteries are crushed, and leached the elements are leached by complicated chemical processes. High power ultrasonic system was used to exfoliate electrode materials from the current collectors. After comparing different solvents, it was verified that low concentration alkaline solution was most effective to exfoliate the cathode and anode electrode materials. Within about 10 minutes, the electrode could be separated into black electrode materials and clean metal foils with metal luster. There is no Al element detected in the solution by ICP, except the alkaline concentration is higher than 2 mol/L. This process has the advantage that almost cathode and anode components are segregated without contaminants, therefore, it is very favorable to recover the active materials by simple heat-treatment with Li salt supplement. Moreover, the recycled steel cans, clean Cu and Al foils can be reused directly. The recycled components corresponding to the separation and recycling steps are shown in Figure 1. It is difficult to recover Li element from recycled cathode material LiFeP04 by chemical precipitation. Because Fe element is very easy to form colloidal precipitation to adsorb a mass of Li+, which greatly decreases the Li recovery efficiency to 52.4%. Considering the recovery cost, it is an effective route to recover the active material LiFeP04 using the recycled materials. Although the recovery efficiency is 95.8% using the amount of cathode electrode in the spent battery as reference, the electrochemical performance of the recovered active material needs to be improved. Their discharge capacities of 120-130mAh/g are lower than original 150mAh/g. Perhaps it is reasonable that recovered materials could possibly be used in less-stringent capacity requirements. Based on our environmentally friendly separation and recycling processes, the pilot recycling demonstration line of automotive Lithium-ion batteries had been established in China's Beijing Pride Power System Technology Corporation, providing Lithium-ion battery packs for China's Beijing New Energy Automotive Corporation. The simple recycling technologies are helpful to solve the environmental and resources problems caused by the retirement of mass automotive batteries in the future, and it also needs time to improve the equipment and enact regulations to achieve the recycling goal of harmlessness,standardization and automatization and commercialization.
机译:如今,大功率锂离子电池已大量用作汽车的电源。这些用完的汽车用锂离子电池在使用寿命到期后,应该对环境进行回收和资源再利用。汽车锂离子电池组由数百个或更多个单独的电池组成,这些电池通过控制电路以及热量和电池管理系统连接并组装成一个电池组。这些组件可以从电池组中完整地回收,但是具有不同化学成分的这些单个电池的回收过程更加复杂。本文提出了一种有效的物理回收方法,并将其应用于60Ah钢制方形棱柱形锂离子电池,该电池用于中国北京新能源汽车公司生产的电动汽车。回收过程包括第一次电解质提取和无害处理,细胞切口和成分分离以及活性物质的回收。干净分离的组件(例如集电器,活性材料和隔板)是高纯度材料,可以直接作为原材料重复使用以生产另一种高价值产品。首先,在回收过程中确保安全并防止爆炸非常重要,因为锂离子电池包含有毒和易燃的电解质。单个电池的预处理包括有机电解质的收集和浓缩过程:将安全且无毒的有机溶剂注入密封的电池中以溶解电解质,然后取出并蒸馏以重复使用。重复收集过程,最后将真空室抽真空。蒸馏的残留物包含一些有机电解质溶剂,例如碳酸乙基甲基酯,碳酸二乙酯和LiPF6盐。用碱溶液处理可降低LiPF6的毒性,反应产物气体HF被Ca(OH)2吸收形成CaF2。电解液中LiPF6的无害处理有助于进行后续过程。其次,通过冷切割方式从顶部打开没有电解质的单个电池,并通过夹具将锂离子电池的胶卷从钢罐中抽出。然后将果冻卷反向卷绕成一部分阴极,阳极和隔板。阴极和阳极的隔离有利于分别回收高纯度的不同电极材料(带粘合剂和导电添加剂的LiFePO4,带粘合剂的石墨)和铜,铝箔,并避免交叉污染。化学过程与之完全不同,化学粉碎过程是将电池压碎,然后通过复杂的化学过程浸出元素。高功率超声系统用于从集电器上剥落电极材料。比较了不同的溶剂后,证实低浓度的碱性溶液最有效地剥落阴极和阳极电极材料。在大约10分钟内,电极可被分离成黑色电极材料和干净的具有金属光泽的金属箔。 ICP溶液中没有检测到Al元素,只是碱浓度高于2 mol / L。该方法的优点是几乎将正极和负极组分分离而没有污染物,因此,通过用锂盐补充剂进行简单的热处理来回收活性材料是非常有利的。此外,回收的钢罐,干净的铜箔和铝箔可以直接重复使用。对应于分离和再循环步骤的再循环组分示于图1。难以通过化学沉淀从再循环阴极材料LiFePO 4中回收Li元素。由于Fe元素很容易形成胶体沉淀物以吸附大量的Li +,因此将Li的回收率大大降低至52.4%。考虑到回收成本,这是使用回收材料回收活性材料LiFePO4的有效途径。尽管以废电池中的阴极电极的量为基准,回收效率为95.8%,但是需要提高回收的活性材料的电化学性能。它们的放电容量为120-130mAh / g,低于原来的150mAh / g。回收的材料可以用于不太严格的容量要求,这也许是合理的。基于我们环保的分离和回收流程,汽车锂离子电池先导性回收示范线已在中国北京骄傲动力系统技术公司成立,为中国北京新能源汽车公司提供锂离子电池组。简单的回收技术有助于解决将来因大量汽车电池报废而造成的环境和资源问题而且,还需要时间改进设备并颁布法规,以实现无害化,标准化,自动化和商业化的回收目标。

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