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A hydrometallurgical process for recovering total metal values from waste monolithic ceramic capacitors

机译:一种湿法冶金工艺,用于从废弃的整体式陶瓷电容器中回收金属总量

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摘要

A hydrometallurgical process for recovering the total metal values from waste monolithic ceramic capacitors was investigated. The process parameters such as time, temperature, acid concentration, hydrogen peroxide concentration and other reagents (amount of zinc dust and sodium formate) were optimized. Base metals such as Ba, Ti, Sn, Cu and Ni are leached out in two stages using HC1 in stage 1 and HC1 with H_2O_2 in stage 2. More than 99% of leaching efficiency for base metals (Cu, Ni, Ba, Ti and Sn) was achieved. Precious metals such as Au and Pd are leached out using aquaregia and nitric acid was used for the leaching of Ag. Base metals (Ba, Ti, Sn, Cu and Ni) are recovered by selective precipitation using H_2SO_4 and NaOH solution. In case of precious metals, Au and Pd from the leach solution were precipitated out using sodium metabisulphite and sodium formate, respectively. Sodium chloride was used for the precipitation of Ag from leach solution. Overall recovery for base metals and precious metals are 95% and 92%, respectively. Based on the results of the present study, a process flow diagram was proposed for commercial application.
机译:研究了一种湿法冶金工艺,用于从废弃的整体式陶瓷电容器中回收总金属值。优化了工艺参数,例如时间,温度,酸浓度,过氧化氢浓度和其他试剂(锌粉和甲酸钠的量)。在第1阶段使用HC1在第2阶段使用H1和HC1在第2阶段用H_2O_2分两阶段浸出贱金属,例如Ba,Ti,Sn,Cu和Ni。99%以上的贱金属(Cu,Ni,Ba,Ti浸出效率) (Sn)。稀有金属(例如Au和Pd)使用氧化锆浸出,硝酸用于Ag的浸出。通过使用H_2SO_4和NaOH溶液进行选择性沉淀来回收贱金属(Ba,Ti,Sn,Cu和Ni)。如果是贵金属,则分别使用焦亚硫酸钠和甲酸钠从浸出溶液中沉淀出Au和Pd。氯化钠用于从浸出溶液中沉淀出银。贱金属和贵金属的总体回收率分别为95%和92%。基于本研究的结果,提出了用于商业应用的工艺流程图。

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