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Eco-friendly and economical gold extraction by nickel catalyzed ammoniacal thiosulfate leaching-resin adsorption recovery

机译:镍催化氨代硫代硫酸盐浸出树脂吸附回收的环保,经济提取金

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摘要

Nickel catalyzed ammoniacal thiosulfate leaching-resin adsorption recovery, an environmentally friendly and cost-effective process, was developed to extract gold from a gold concentrate calcine. The catalytic mechanism was presented based on thermodynamic analysis that NH3 catalyzed the anodic dissolution of gold, and Ni3O4 catalyzed the cathodic reduction of O-2. The leaching result indicates that thiosulfate consumption reduced considerably under nickel-ammonia catalysis, whilst gold leaching percentage was comparable with that under conventional copper-ammonia catalysis. The kinetics study demonstrates that the reaction orders of initial nickel (II), ammonia and thiosulfate concentrations were separately 0.21, 0.37 and 0.28. The apparent activation energy calculation shows that the catalytic efficiencies of nickel-ammonia and copper-ammonia were close, and gold leaching with nickel-ammonia catalysis was possibly diffusion controlled that was supported by the XPS analysis result. For the gold recovery from its actual leach solution by ion-exchange resin, the resin and desorbent dosages were less, and loaded gold could be desorbed by a simple one-step desorption process because nickel did not co-adsorb with gold on resin surface. Besides, gold leaching percentage only declined 1.8% after the leach solution was recycled five times, and thiosulfate consumption decreased 5.8 kg/t-calcine. (C) 2019 Elsevier Ltd. All rights reserved.
机译:镍催化硫代硫酸盐浸出树脂的吸附回收是一种环境友好且具有成本效益的工艺,已开发出从金精矿煅烧物中提取金的方法。基于热力学分析,提出了NH3催化金的阳极溶解,Ni3O4催化O-2的阴极还原的催化机理。浸出结果表明,镍-氨催化下硫代硫酸盐的消耗量大大降低,而金的浸出率与常规铜氨催化下的相当。动力学研究表明,初始镍(II),氨和硫代硫酸盐浓度的反应顺序分别为0.21、0.37和0.28。表观活化能的计算表明,镍氨和铜氨的催化效率相近,而XPS分析结果支持了镍氨催化的金浸出的扩散控制。对于通过离子交换树脂从其实际浸出溶液中回收金,树脂和解吸剂的用量较少,并且负载的金可以通过简单的一步解吸过程解吸,因为镍不会与金在树脂表面上共吸附。此外,浸出液循环使用五次后,金的浸出率仅下降了1.8%,硫代硫酸盐的消耗量减少了5.8千克/吨分解钙。 (C)2019 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Journal of Cleaner Production》 |2019年第1期|1475-1485|共11页
  • 作者单位

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

    Cent S Univ, Sch Minerals Proc & Bioengn, Changsha 410083, Hunan, Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Gold; Thiosulfate; Nickel-ammonia catalysis; Kinetics; Resin adsorption;

    机译:金;硫代硫酸盐;镍氨催化;动力学;树脂吸附;

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