首页> 外文期刊>Journal of Hazardous Materials >A promising selective recovery process of valuable metals from spent lithium ion batteries via reduction roasting and ammonia leaching
【24h】

A promising selective recovery process of valuable metals from spent lithium ion batteries via reduction roasting and ammonia leaching

机译:通过减少焙烧和氨浸出,从锂离子电池中获得有价值金属的有望的选择性恢复过程

获取原文
获取原文并翻译 | 示例
       

摘要

In this study, a promising process has been developed for selective recovery of valuable metals from spent lithium ion batteries (LIBs). First, reduction roasting which used spent anode powder as reduction agent and water immersion are applied to preferentially recover lithium. Subsequently, an ammonia leaching method is adopted to eff ;ectively separate nickel and cobalt from water immersion residue. Results indicate that Li2CO3, (NiO)m(MnO)n, Ni, Co are the ultimate reduction products at 650 degrees C for 1 h with 5% anode powder. 82.2 % Li is preferentially leached via water immersion after reduction roasting and Li2CO3 products are obtained by eva-poration crystallization. Thermodynamics shows that reducing ammonia leaching is feasible for water immersion residue. Amounts of 97.7 % Ni and 99.1 % Co can be selectively leached by NH3H2O and (NH4)(2)SO3 while Mn remain in the residue as (NH4)(2)Mn(SO3)(2)H2O, (NH4)(2)Mn(SO4)(2)6H(2)O and (NH4)(2)Mn-2(SO3)(3) under the optimized conditions. Ammonia leaching kinetic show the activation energy of Ni and Co is 84.44 kJ/mol and 91.73 kJ/mol, which indicate the controlling steps are the chemical reaction. Summarily, the whole process achieves the maximum degree of selective recovery and reduces the environmental pollution caused by the multistep purification.
机译:在这项研究中,已经开发了有希望的过程,用于选择性地回收来自锂离子电池(LIBS)的有价值金属。首先,将使用废阳极粉末作为还原剂和水浸的还原焙烧以优先回收锂。随后,采用氨浸出方法来效果;从水浸渍残留物中渗透地分离镍和钴。结果表明,Li 2 CO 3,(NiO)M(MNO)N,Ni,Co是650℃的最终降低产物,其具有5%阳极粉末。通过浸渍焙烧和Li 2 CO 3产物通过EVA-POTION结晶获得82.2%LI通过水浸渍优先浸出。热力学表明,降低氨浸出对于水浸渍残留物是可行的。 NH 3 H 2 O和(NH 4)(2)SO 3可以选择性地浸出97.7%Ni和99.1%CO的量,而MN保留在残余物中(NH 4)(2)Mn(SO 3)(2)H 2 O,(NH4)(2在优化条件下,Mn(SO4)(2)6H(2)o和(NH4)(2)MN-2(SO 3)(3)。氨浸出动力学显示Ni和Co的活化能是84.44kJ / mol和91.73kJ / mol,表明控制步骤是化学反应。总而言之,整个过程实现了最大程度的选择性恢复程度,并降低了多次间隔净化引起的环境污染。

著录项

  • 来源
    《Journal of Hazardous Materials》 |2021年第1期|123491.1-123491.11|共11页
  • 作者单位

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

    Cent South Univ Sch Met & Environm Changsha 410083 Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Spent LIBs; Selective recovery; Reduction roasting; Water immersion; Ammonia leaching;

    机译:花了libs;选择性恢复;减少烘烤;水浸;氨浸出;

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号