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有色金属(冶炼部分):2019,(7):36-41
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锌加压酸浸渣中硫磺的回收方法研究
常军1, 王子阳1, 张泽彪2
(1.铜仁学院材料与化学工程学院;2.昆明理工大学冶金与能源工程学院)
Recovery of Elemental Sulfur from Zinc Pressure Acid Leaching Residue
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本文已被:浏览 2185次   下载 1940次
投稿时间:2019-04-11     修订日期:2019-04-16     录用日期:2019-04-17     网络发布日期:2019-06-17
中文摘要: 对比分析了浮选法、热过滤法和硫化铵法回收锌加压酸浸渣中硫磺的优缺点。考察了硫化铵溶液浸出浮选硫精矿、硫化物滤饼和多硫化铵母液热分解过程的影响因素。结果表明,液固比和硫化铵浓度对硫磺浸出效果影响较为明显,在最佳试验条件下硫化物滤饼中硫的浸出率约为95%,浮选硫精矿中硫的浸出率和回收率均达到98%,多硫化铵母液热分解后获得的硫磺产品纯度高达99.57%。硫化铵浸出渣中有价金属富集倍数较高,有利于锌加压酸浸渣的综合利用。
中文关键词: 锌加压酸浸渣  浮选  热过滤  硫化铵  硫磺
Abstract:Advantages and disadvantages to recover elemental sulfur from zinc pressure acid leaching residue by flotation method, melting and filtration method, ammonium sulfide method is contrastively analyzed. Effects of different factors on leaching process of flotation sulfur concentrate and sulfide filter cake with ammonium sulfide, and on thermal decomposition process of polysulfide solution were analyzed. The results indicate that ratio of liquid to solid and concentration of ammonium sulfide have significant impact on sulfur leaching rate. Sulfur leaching rate from sulfide filter cake is about 95% under optimal conditions. Sulfur leaching rate and recovery from flotation sulfur concentrate is 98%. Purity of sulfur obtained by thermal decomposition of ammonium polysulfide solution is 99.57%. Content of valuable metals in residue after sulfur extraction is enriched by remarkable times, which is favorable for comprehensive utilization of zinc pressure acid leaching residue.
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基金项目:国家自然科学基金资助项目(51804220)
引用文本:
常军,王子阳,张泽彪.锌加压酸浸渣中硫磺的回收方法研究[J].有色金属(冶炼部分),2019(7):36-41.
CHANG Jun,WANG Zi-yang,ZHANG Ze-biao.Recovery of Elemental Sulfur from Zinc Pressure Acid Leaching Residue[J].Nonferrous Metals (Extractive Metallurgy),2019(7):36-41.

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