首页 | 官方网站   微博 | 高级检索  
     

某金矿热压氧化后氰化浸金氰化钠消耗实验研究
引用本文:罗 星,李尽善,周卫宁,冯吉福,马荣锴.某金矿热压氧化后氰化浸金氰化钠消耗实验研究[J].贵金属,2015,36(4):51-55, 62.
作者姓名:罗 星  李尽善  周卫宁  冯吉福  马荣锴
作者单位:中国有色桂林矿产地质研究院有限公司,广西 桂林 541004,中国有色桂林矿产地质研究院有限公司,广西 桂林 541004,中国有色桂林矿产地质研究院有限公司,广西 桂林 541004,中国有色桂林矿产地质研究院有限公司,广西 桂林 541004,中国有色桂林矿产地质研究院有限公司,广西 桂林 541004
基金项目:中国有色集团科技计划项目(2014KJJH02)、广西科学研究与技术开发计划项目(桂科攻14122006-25)。
摘    要:简要介绍了我国难处理金矿资源现状、难选冶原因、预处理方法,详细分析了该类资源中有害元素热压氧化过程的化学过程。针对某金矿热压氧化渣进行了炭浸氰化实验,考察了p H、调浆时间、底炭浓度、浸出时间对氰化钠消耗量的影响。实验证明,经过热压氧化,能够降低炭浸氰化过程中的氰化钠消耗量及氰化时间。针对实验样,氰化钠消耗量仅为0.27~0.29 kg/t,浸出时间为2~4 h,浸出率为95.34%。

关 键 词:有色金属冶金  难处理金矿  热压氧化  氰化钠  炭浸法
收稿时间:2015/3/27 0:00:00

Research on the Dosage of Sodium Cyanide Used for Leaching Refractory Gold Ore after Pressure Oxidation Procedure
LUO Xing,LI Jinshan,ZHOU Weining,FENG Jifu and MA Rongkai.Research on the Dosage of Sodium Cyanide Used for Leaching Refractory Gold Ore after Pressure Oxidation Procedure[J].Precious Metals,2015,36(4):51-55, 62.
Authors:LUO Xing  LI Jinshan  ZHOU Weining  FENG Jifu and MA Rongkai
Affiliation:China Nonferrous Metal Guilin Geology and mining Co. Ltd., Guilin 541004, Guangxi, China,China Nonferrous Metal Guilin Geology and mining Co. Ltd., Guilin 541004, Guangxi, China,China Nonferrous Metal Guilin Geology and mining Co. Ltd., Guilin 541004, Guangxi, China,China Nonferrous Metal Guilin Geology and mining Co. Ltd., Guilin 541004, Guangxi, China and China Nonferrous Metal Guilin Geology and mining Co. Ltd., Guilin 541004, Guangxi, China
Abstract:The current situation of resource of refractory gold ore in China is briefly described, the reasons for difficulty in leaching and mineral processing, and pretreatment methods. The chemical process of harmful elements in the hot pressure oxidation is also discussed. Cyanide leaching tests of the refractory gold ore after the pressure oxidation were carried out, and the effects of the consumption of sodium cyanide, pH, pulping time, bottom carbon concentration and leaching time were investigated. The results show the pressure oxidation can reduce consumption of sodium cyanide and save the time in carbon leaching process. The leaching percentage of gold increased to 95.34% even when sodium cyanide consumption was 0.27~0.29 kg/t and the leaching time was 2~4 h.
Keywords:nonferrous metallurgy  refractory gold ore  pressure oxidation  sodium cyanide  carbon in leaching
本文献已被 CNKI 等数据库收录!
点击此处可从《贵金属》浏览原始摘要信息
点击此处可从《贵金属》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司    京ICP备09084417号-23

京公网安备 11010802026262号