Pressure acid leaching of black shale for extraction of vanadium

被引:25
作者
Li Min-ting [1 ]
Wei Chang [1 ]
Fan Gang [1 ]
Li Cun-Xiong [1 ]
Deng Zhi-gan [1 ]
Li Xin-bin [1 ]
机构
[1] Kunming Univ Sci & Technol, Fac Met & Energy Engn, Kunming 650093, Peoples R China
来源
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA | 2010年 / 20卷
关键词
pressure acid leaching; black shale; vanadium; catalyst; SANDS FLY-ASH; OIL; CATALYSTS; RECOVERY; SULFUR;
D O I
10.1016/S1003-6326(10)60023-4
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Extraction of vanadium from black shale was attempted in pressure acid leaching. The chemical components of the sample obtained from Guizhou Province of China show that it contains 3.258% V2O5, 52.880% SiO2 and 16.140% Al2O3. Phase analyses of vanadium indicates vanadium mainly exists in the free oxide and mica. Vanadium contents in the two phases are 18% and 53%, respectively. The contents of V3+, V4+ and V5+ are almost equal. Under the optimum parameters of one-step leaching (reaction time of 3 h, sulfuric addition of 25%, temperature of 150 degrees C, liquid to solid ratio of 1.2 mL/g, catalyst (FeSO4) addition of 5% and size of 85% particle 0.074 mm), about 77% of vanadium is recovered. After two-step countercurrent leaching, the leach recovery of vanadium can reach above 90%. Air replacing oxygen is completely feasible. The impurity metals can dissolve into solution in different degrees.
引用
收藏
页码:S112 / S117
页数:6
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