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金属矿山 ›› 2016, Vol. 45 ›› Issue (02): 91-95.

• 矿物工程 • 上一篇    下一篇

广东某含硫铁低品位铜矿石选矿工艺研究

喻连香1,2,3,邱冠周1,王海东1,邱显扬2,3,陈淼4,周吉奎2,3   

  1. 1.中南大学资源加工与生物工程学院,湖南 长沙 410083;2.广州有色金属研究院,广东 广州 510651;3.稀有金属分离与综合利用国家重点实验室,广东 广州 510651;4.澳大利亚联邦科学与工业研究组织,维多利亚州 墨尔本 999029
  • 出版日期:2016-02-15 发布日期:2016-03-11
  • 基金资助:

    * 广东省部产学研企业创新平台项目(编号:2013B090800016) ,广东省教育部科技部企业科技特派员行动计划专项(编号:2009B090600062)。

New Beneficiation Technology on a Low Grade Copper Ore Containing Sulfur and Iron from Guangdong Province

Yu Lianxiang1,2,3,Qiu Guanzhuo1,Wang Haidong1,Qiu Xianyang2,3,Chen Miao4,Zhou Jikui2,3   

  1. 1.School of Minerals Processing and Bioengineering,Central South University,Changsha 410083,China;2.Guangzhou Research Institute of Non-ferrous Metals,Guangzhou 510651,China;3.State Key Laboratory of Rare Metal Separation and Comprehensive Utilization,Guangzhou 510651,China;4.Australia's Commonwealth Scientific and Industrial Research Organization,Melbourne 999029,Australia
  • Online:2016-02-15 Published:2016-03-11

摘要: 广东某含硫铁低品位铜矿石主要有用元素铜、硫、铁品位分别为0.51%、27.68%、34.07%。铜赋存状态复杂,以次生硫化铜形式存在的铜占总铜的54.91%,水溶性铜占总铜的26.39%,采用常规浮选方法选别铜回收率低。为探索该矿石中铜、硫、铁的高效分选工艺,对其进行了选冶工艺研究。结果表明:原矿磨细至-0.074 mm占72%时,采用pH=3的硫酸溶液为浸出剂,在液固比为4 mL/g、搅拌转速为1 400 r/min、浸出时间为24 h条件下浸铜,可以获得铜浸出率为93.33%的指标;铜浸渣经自来水搅拌洗涤至pH=6以后,以丁黄药为捕收剂、2号油为起泡剂,经1粗1扫硫浮选,可获得硫品位为48.44%、对铜浸渣回收率为95.57%的高品质硫精矿;浮硫尾矿在磁介质为Φ2 mm棒介质、脉动冲程为16 mm、冲次为280次/min、背景磁感应强度为0.6 T条件下,经1次高梯度强磁选选铁,可获得铁品位为51.42%、对铜浸渣回收率为17.02%的铁精矿。以上试验结果说明,采用铜浸出—硫浮选—铁磁选的工艺流程可以实现矿石中铜硫铁的有效分离。

关键词: 低品位铜硫矿石, 水溶性铜, 酸浸, 选冶联合流程, 浮选, 磁选

Abstract: Main valuable elements copper,sulfur,iron grade is 0.51%,27.68% and 34.07% in a low-grade copper ore from Guangdong province.Copper occurrence state is complex,secondary copper sulfide copper accounted for 54.91% of total copper,water soluble copper accounted for 26.39% of total copper,high copper recovery cannot obtained by conventional flotation method.To explore high efficient separation technology for copper,sulfur,iron,metallurgy process research was conducted.Results show that at the grinding fineness of 72% passing 0.074 mm,using sulfuric acid solution with pH=3 as leaching agent,the liquid-solid ratio of 4 mL/g,stirring speed of 1 400 r/min,leaching time of 24 h,copper leaching rate of 93.33% can be obtained;Copper leaching slag being lavated to pH=6 via one roughing one scavenging sulfur flotation process using butyl xanthate as collector,2# oil as frother,the sulfur concentrate was obtained with sulfur grade of 48.44% and recovery to copper leaching slag is 95.57%;Sulfur flotation tailings via one stage high gradient high intensity magnetic separation operation using Ф2 mm rods medium as magnetic medium,pulsating stroke is 16 mm,pulsating frequency is 280 times/min,background magnetic field intensity is 0.6 T,the iron concentrate was obtained with iron grade of 51.42%,recovery to copper leaching slag is 17.02%.The abrove test results indicated that effective separation of copper,sulfur and iron can be realized via copper leaching-sulfur flotation-magnetic separation technological process.

Key words: Low grade copper-sulfur ore, Water-soluble copper, Acid leaching, Beneficiation-metallurgy combined process, Flotation, Magnetic separation