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Split regeneration of chelating resins for the selective recovery of nickel and copper

机译:螯合树脂的分裂再生,用于镍和铜的选择性恢复

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The management of spent acids containing heavy metals has been traditionally carried out by neutralization-precipitation technologies that often fail to provide the required selectivity for metal recovery. This work proposed a split elution process using H2SO4 and NH4OH solutions to regenerate bispicolylamine-based chelating resins (Puromet (TM) MTS9600) employed in a previous work to separate nickel and copper from spent sulfuric acid effluents. Operation variables namely S/L ratio, concentration of the regeneration agents and process configuration were analysed to select the best conditions to optimize the metal unloading and their selective recovery in independent solutions. It was found that 43% of nickel was eluted from the resin by H2SO4 2.0 M and recovered with purities of 98% while 47% of copper was desorbed with NH4OH 2.0 M and recovered with purities of 97%. The long-term assessment evidenced that copper removal and metal recovery were not affected after 10 adsorption-regeneration cycles, while the nickel adsorption efficacy decreased about 10%.
机译:含有重金属的废酸的管理传统上通过中和沉淀技术进行,这些技术经常未能为金属回收率提供所需的选择性。这项工作提出了使用H2SO4和NH 4 OH溶液的分裂洗脱方法,以再生在先前的工作中使用的双吡啶啉基胺基螯合树脂(PURMOM(TM)MTS9600),以将镍和铜与废硫酸流出物分离。操作变量即S / L比,分析再生剂的浓度和工艺配置,选择优化金属卸载及其在独立解决方案中的选择性恢复的最佳条件。发现43%的镍通过H 2 SO 4 2.0m从树脂中洗脱并用纯度回收98%,而47%的铜用NH 4 OH 2.0m解吸并用纯度回收97%。长期评估证明,在10个吸附 - 再生循环后,铜去除和金属恢复不受影响,而镍吸附效能降低约10%。

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