发明名称
摘要 <p>The ore is crushed and leached in a Cl ion contg. acid medium. The resultant Zn chloride contg. soln. is purified by adsorption on an anionic or neutral ion exchanger followed by elution of this ion exchanger. The Zn chloride contg. eluate is then subjected to electrolysis using a Hg cathode, the electrolysis being repeated using a Hg anode. Zn is extracted from the amalgam in known manner. The Zn-free soln. after the ion exchange treatment is recycled. The Cl2 gas produced during the electrolysis is combined with H2S produced in the leaching process, and the resulting HCl recycled for leaching the ore.</p>
申请公布号 JPS4839322(A) 申请公布日期 1973.06.09
申请号 JP19720000051 申请日期 1972.01.05
申请人 发明人
分类号 C22B19/20;C22B19/00;C22B19/02;C25C1/16;(IPC1-7):C22B19/26 主分类号 C22B19/20
代理机构 代理人
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