Abstract
水热浸出-浮选综合回收铅银渣中金银实验研究
Experimental Research on Comprehensive Recovery of Gold and Silver from Lead-Silver Residue by Hydrothermal Leaching-Floatation
Received:May 15, 2015  
DOI:
中文关键词: 有色金属冶金  铅银渣  水浸  浮选  T19  硫酸铜  酯-30
英文关键词: nonferrous metallurgy  lead-silver residue  hydrothermal leaching  flotation  T19  copper sulfate  Ester-30
基金项目:
Author NameAffiliationE-mail
GUO Yanhua Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China gyh19861109@163.com 
SUN Yunli Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China  
GUO Haining Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China  
YANG Junlong Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China  
LIAO Xuezhen Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China  
PENG Jiancheng Northwest Institute of Mining and Metallurgy, Baiyin 730900, Gansu, China  
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中文摘要:
      为了提高资源利用效率,实现二次资源综合利用,对铅银渣进行了实验研究。铅银渣中银品位为245 g/t,金品位为1.52 g/t,金、银含量均较高。银的赋存状态研究表明,银主要以再造矿物铜蓝、硫化银混合相存在。结合银的赋存状态进行流程探索,确定采用水热浸出-浮选工艺流程。条件实验研究表明,液固比为2:1,浸出温度为70℃,浸出时间为2 h进行水热浸出,金、银在渣中富集率较高。当磨矿细度-0.044 mm占85%,粗选T19用量为4000 g/t,硫酸铜用量为600 g/t,酯-30用量为500 g/t时,经过一次粗选、两次精选、一次扫选的闭路实验流程,可获得银品位为3805 g/t,银回收率为86.82%的银精矿,银精矿中金的品位为25.8 g/t,金回收率为94.96%的较好指标,实现了铅银渣的综合回收。
英文摘要:
      In order to improve the efficiency of resource utilization and realize the comprehensive utilization of secondary resources, the present tests were carried out to recover gold and silver effectively from lead-silver residue as a secondary resource. The content of gold and silver in the lead-silver residue was high, with the silver being at 245 g/t in the form of copper blue and silver sulfide minerals,and gold being at 1.52 g/t. Based on the state of silver, a hydrothermal leaching-flotation process was used. The involved condition experiments showed that a great enrichment rate of gold and silver in the slag was achieved when the liquid-solid ratio was 2:1 at 70℃ for 2 h in hydrothermal leaching procedure. The flotation included grinding, one roughing, two cleaning, one scavenging of aclosed-circuit process. The chemicals used in flotation procedure were T19 at a dose of 4000 g/t, copper sulfate at a dose of 600 g/t, ester-30 at a dose of 500 g/t. After leaching-flotation, silver was concentrated to a content of 3805 g/t with a recovery rate of 86.82% while gold to a content of 25.8 g/t with the recovery being up to 94.96%.
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