期刊文献+

复杂硫化铜精矿微波活化预处理-加压浸出工艺 被引量:15

Microwave Activation Pretreatment and Pressure Leaching of Complex Copper Sulfide Concentrate
下载PDF
导出
摘要 研究了以黝铜矿为主的复杂硫化铜精矿微波活化预处理-加压浸出工艺.结果表明,该精矿在微波功率82W、每批处理量95g及辐照时间120s条件下预处理后,矿石浸出性能显著改善.预处理过程中未见铅、锌、硫、砷等元素挥发损失.实验确定了微波活化铜精矿加压浸出工艺条件为:浸出温度453K,氧分压0.6MPa,初始硫酸浓度1.23mol/L,液固比5mL/g,浸出时间2.0h,木质素磺酸钙用量为精矿质量的1.25%,搅拌速度500r/min.在此条件下,铜、锌、铁浸出率分别达到86.36%,92.33%和27.64%.加压浸出渣经高温煤油溶解单质硫后返回作浸出配矿使用,可保障有价金属铜锌收率. The microwave activation-pressure leaching technique of complex copper sulfide concentrate with tetrahedrite as the main mineral is studied.The results show that the leaching of complex copper sulfide concentrate is greatly improved after the microwave activation pretreatment under the following conditions:microwave power of 82 W,batch concentrate weight of 95 g,and handling time of 120 s.No loss of lead,zinc,sulfur and arsenic in the concentrate occurs during the pretreatment.The pressure leaching conditions of activated copper concentrate are further determined as follows:temperature of 453 K,oxygen partial pressure of 0.6 MPa,initial sulfuric acid concentration of 1.23 mol/L,ratio of liquid to solid of 5 mL/g,calcium lignosulphonate dosage of 1.25%(ω) of the concentrate,leaching time of 2.0 h,and agitation speed of 500 r/min.Under these conditions,the extraction rate of copper,zinc and iron is achieved at 86.36%,92.33% and 27.64% respectively.The leaching residues may return to the rationing of leaching materials for high recovery of copper and zinc after the residues are processed by high-temperature kerosene for deprivation of elemental sulfur.
出处 《过程工程学报》 CAS CSCD 北大核心 2010年第2期256-262,共7页 The Chinese Journal of Process Engineering
基金 江西省自然科学基金资助项目(编号:2007GQC0656) 国家重点基础研究发展规划(973)基金资助项目(编号:2007CB613505)
关键词 复杂铜精矿 黝铜矿 微波活化 预处理 加压浸出 complex copper concentrate tetrahedrite microwave activation pretreatment pressure leaching
  • 相关文献

参考文献27

  • 1王海北,蒋开喜,邱定蕃,卢惠民.国内外硫化铜矿湿法冶金发展现状[J].有色金属,2003,55(4):101-104. 被引量:28
  • 2刘大星.湿法炼铜的发展与前景[J].有色金属再生与利用,2005(7):34-36. 被引量:19
  • 3Hackl R P,Dreisinger D B,Peters E,et al.Passivation of Chalcopyrite during Oxidative Leaching in Sulfate Media[J].Hydrometallurgy,1995,39(1/3):25-48.
  • 4Davies D S,Leueders R E,Spitz R A,et al.Nitric-Sulfuric Leaching Process Improvements[J].Miner.Eng.,1981,33(8):1252-1259.
  • 5王永慧.铜矿石和精矿氮类物催化加压浸出的应用与经济估算[J].中国有色冶金,2009,38(1):6-11. 被引量:3
  • 6Skrobian M,Havlik T,Ukasik M.Effect of NaCl Concentration and Particle Size on Chalcopyrite Leaching in Cupric Chloride Solution[J].Hydrometallurgy,2005,77(1/2):109-114.
  • 7Lu Z Y,Jeffrey M I,Lawson F.Effect of Chloride Ions on the Dissolution of Chalcopyrite in Acidic Solutions[J].Hydrometallurgy,2000,56(2):189-202.
  • 8Vracar R Z,Parezanovic I S,Cerovic K P.Leaching of Copper(I) in Calcium Chloride Solution[J].Hydrometallurgy,2000,58(3):261-267.
  • 9Corrans I J,Angove J E.Ultrafine Milling for the Recovery of Refractory Gold[J].Miner.Eng.,1991,4(7/11):763-776.
  • 10Welham N J.Mechanochemical Processing of Enargite (Cu3AsS4)[J].Hydrometallurgy,2001,62(3):165-173.

二级参考文献62

共引文献157

同被引文献184

引证文献15

二级引证文献74

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部