摘要
采用添加剂焙烧-氰化浸出中试处理锰银矿。回转窑连续运转80 h,物料焙烧时间30±5 min,所得焙砂产率85.54%,焙砂中银含量237.73 g/t、锰含量24.68%,银回收率99.19%,锰回收率98.70%;焙砂经500 L反应釜直接氰化浸出,浸出液固比2:1~2.2:1,时间6~15 h,氰化钠用量700 g/t原矿,所得银浸出率86.5%,氰化尾渣满足冶金用锰矿石标准。
Additive roasting-cyanide leaching process was adopted for treating manganese-silver ore. The rotary kiln was continuously operated for 80 hours, and the ore was roasted for 30±5 minutes. The results showed that the content of silver and manganese was 237.73 g/t and 24.68% in the calcine, and that the recovery of silver and manganese was 99.19% and 98.70%, respectively. The resulted calcine was leached in 500 L reactor with a solid liquid ratio of 2:1~2.2:1, 6~15 h of leaching time, and 700 g/t of NaCN. Leaching results showed that the leaching ratio of silver was up to 86.5%, and that the residue met the standards of manganese ore for metallurgy.
作者
王明
齐建云
宁新霞
王祥
WANG Ming;QI Jianyun;NING Xinxia;WANG Xiang(Engineering & Technology Center for Comprehensive Utilization of Mineral Resource of Shaanxi Province,Xi’an Northwest Geological Institute of Nonferrous Metals Co. Ltd.,Xi’an 710054)
出处
《贵金属》
CAS
CSCD
北大核心
2019年第1期47-50,共4页
Precious Metals
关键词
有色金属冶金
银
焙烧-氰化
中试
锰银矿
nonferrous metals metallurgy
silver
roasting-cyanide leaching
pilot test
manganese-silver ore