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Hydrometallurgical recovery of lead from spent lead-acid battery paste via leaching and electrowinning in chloride solution

机译:通过浸出和氯化物溶液中的铅酸电池糊的铅液回收铅铅

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摘要

Recycling spent lead-acid batteries has always been a research hotspot. Although traditional pyrometallurgical smelting is still the dominant process, it has serious environmental drawbacks, such as the emission of lead dust and SO2, and high energy consumption. This study presents a clean process for recycling spent lead-acid battery paste. The lead in paste was recovered via hydrometallurgical leaching and electrowinning in chloride solution. The leaching ratio of lead was > 99% under optimum conditions: temperature of 90 degrees C, CaCl2 concentration of 400 g/L, Fe2+ concentration of 5 g/L, pH 1.0, and leaching time of 2 h. The appropriate minimum Pb concentration and optimum current density for electrowinning were determined to be 10 g/L and 200 A/m(2), respectively. Cathode lead powders with a purity of 99.6% were obtained via electrowinning. The current efficiency and the power consumption at 200 A/m(2) were 96.3% and 85.9 kWh per ton of lead produced, respectively. Due to the use of soluble anode (iron), the energy consumption of the electrowinning process was considerably reduced and the chlorine evolution was avoided. The electrowinning has obvious economic advantages over cementation, and the metallic lead with high purity can be obtained using this method. Furthermore, as the spent electrolyte containing ferrous ions is recyclable, the consumption of reagents and the liquid effluent are minimised. The final leaching residue is a mixture of harmless akaganeite and calcium sulphate. The experimental results show that the proposed process is promising for the recovery of lead from spent lead-acid battery paste.
机译:回收废酸电池一直是研究热点。虽然传统的火数冶金冶炼仍是主要的过程,但它具有严重的环境缺点,例如铅粉尘和SO2的排放,以及高能耗。本研究提出了一种循环回收铅酸电池浆料的清洁方法。通过液压型浸出和在氯化物溶液中电催化回收糊状物的铅。铅的浸出比在最佳条件下> 99%:温度为90℃,CaCl 2浓度为400g / L,Fe2 +浓度为5g / L,pH 1.0,浸出时间为2小时。将电氢化的适当最小Pb浓度和最佳电流密度分别测定为10g / L和200a / m(2)。通过电环宁获得纯度为99.6%的阴极铅粉末。目前的效率和200A / m(2)的功耗分别为每吨铅96.3%和85.9千瓦时。由于使用可溶性阳极(铁),电催化过程的能量消耗显着降低,避免了氯进化。电环宁在胶结上具有明显的经济优势,并且可以使用该方法获得具有高纯度的金属铅。此外,由于含有含有铁离子的金属电解质是可回收的,因此最小化试剂和液体流出物的消耗。最终的浸出残留物是无害的αkaganeite和硫酸钙的混合物。实验结果表明,该过程是对废酸电池浆料的铅回收的承诺。

著录项

  • 来源
    《Hydrometallurgy》 |2019年第2019期|共7页
  • 作者单位

    Univ Sci &

    Technol Beijing Sch Met &

    Ecol Engn Beijing 100083 Peoples R China;

    Univ Sci &

    Technol Beijing Sch Met &

    Ecol Engn Beijing 100083 Peoples R China;

    Univ Sci &

    Technol Beijing Sch Met &

    Ecol Engn Beijing 100083 Peoples R China;

    Univ Sci &

    Technol Beijing Sch Met &

    Ecol Engn Beijing 100083 Peoples R China;

    Univ Sci &

    Technol Beijing Sch Met &

    Ecol Engn Beijing 100083 Peoples R China;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 冶金技术;
  • 关键词

    Lead-acid battery; Lead paste; Lead; Leaching; Electrowinning;

    机译:铅酸电池;铅膏;铅;浸出;electwinning;
  • 入库时间 2022-08-20 08:10:46

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