Sulfuric acid leaching of a complex zinc sulfide concentrate with high copper and lead concentrations under oxygen pressure

被引:1
作者
Sun, Pu [1 ,2 ]
Li, Xingbin [1 ,2 ]
Wei, Chang [1 ,2 ]
Dai, Xingzheng [3 ]
Chen, Guomu [3 ]
Deng, Zhigan [1 ,2 ]
Wang, Jibo [1 ,2 ]
Gang, Fan [1 ,2 ]
Li, Minting [1 ,2 ]
机构
[1] Kunming Univ Sci & Technol, Fac Met & Energy Engn, Kunming, Peoples R China
[2] Kunming Univ Sci & Technol, State Key Lab Complex Nonferrous Met Resources Cle, Kunming, Peoples R China
[3] Yunnan Chihong Zinc & Germanium Co Ltd, Qujing, Peoples R China
基金
中国国家自然科学基金;
关键词
Zinc sulfide concentrate; pressure acid leaching; zinc and copper extraction; iron removal; lead jarosite; DISSOLUTION RATES; RECOVERY; METALS; PYRITE; ORE;
D O I
10.1080/00084433.2024.2340228
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
This paper presents the use of an oxygen pressure-based acid leaching process for the selective extraction of basic metals from a complex zinc ore containing high concentrations of lead (6.00%) and copper (2.47%). The effects of leaching temperature, ore particle size distribution, leaching time, liquid-to-solid ratio, and oxygen partial pressure on the leaching efficiencies of zinc and copper were investigated, and the phase transformation behaviour of lead compounds was studied. Under the optimal conditions that is, a particle size of -48/+40 mu m, initial sulfuric acid concentration of 150 g/L, liquid-to-solid ratio of 6:1, leaching time of 150 min, leaching temperature of 150 degrees C, and oxygen partial pressure of 0.8 MPa - the leaching efficiencies of zinc, copper, and iron were 98.85%, 82.69%, and 33%, respectively. The leaching residue showed that almost all of the zinc sulfide was dissolved as ZnSO4, and most of the negatively charged bivalent sulfur was converted to zero-valent element sulfur. Through the pressure leaching reaction, galena in the concentrate was converted to lead jarosite (PbFe6(SO4)4(OH)12) and elemental sulfur. The formation of lead jarosite facilitated the removal of a significant portion of iron during leaching, reducing the subsequent purification burden.
引用
收藏
页码:260 / 273
页数:14
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