Separation of Heavy Metal Ions from the Solution Obtained by Leaching Low-Grade Pyrolusite with Pyrite and H2SO4

Article Preview

Abstract:

The manganese sulfate solution leached from low-grade pyrolusite with pyrite and H2SO4 contains heavy metal ions of high concentration, influencing the quality of the final products of manganese compounds and causing manganese ions not to be electrolyzed. The present study was focused on the separation of Co, Ni and Zn ions from the leached solution with BaS. By controlling the pH value at 5.0-6.5, temperature at 50-60°C, reaction time at 15 min and mixing velocity at 78 rpm, the heavy metal ions could be separated effectively. Under the above optimized conditions, the ion concentration of Co, Ni, and Zn in the solution was reduced to 0.06 mg.L-1, 0.27mg.L-1 and 0.01mg.L-1, and the separation efficiency was 99.72%, 99.18% and 99.9% respectively. The obtained pure solution meets the demands of manganese electrowinning.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

283-288

Citation:

Online since:

September 2013

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2013 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] Zhou, C., Zhu, G.C., Zhao, Y. Study in reduction-roast leaching manganese from low-grade manganese dioxide ores using cornstalk as reluctant. Hydrometallurgy, 2009, 96: 175-179.

DOI: 10.1016/j.hydromet.2008.08.004

Google Scholar

[2] Zhang, W.S., Chu, Y.C. Manganese metallurgy review. Part Ⅰ: Leaching of ores/secondary materials and recovery of electrolytic/chemical manganese dioxide. Hydrometallurgy, 2007, 89: 137-159.

DOI: 10.1016/j.hydromet.2007.08.010

Google Scholar

[3] Zhang, W.S., Chu, Y.C. Manganese metallurgy review. Part Ⅱ: Manganese control in zinc and copper electrolytes. Hydrometallurgy, 2007, 89: 160-177.

DOI: 10.1016/j.hydromet.2007.08.011

Google Scholar

[4] Zhang, W.S., Chu, Y.C. Manganese metallurgy review. Part Ⅲ: Manganese control in zinc and copper electrolytes . Hydrometallurgy, 2007, 89: 178-188.

DOI: 10.1016/j.hydromet.2007.08.011

Google Scholar

[5] Ma, Z., Ek, C. Engineering application of the acid leaching kinetics of a manganese carbonate ore. Hydrometallurgy, 1992, 28: 223-235.

DOI: 10.1016/0304-386x(92)90132-j

Google Scholar

[6] Ma, Z., Ek, C. Rate processes and mathematical modeling of the acid leaching of a manganese carbonate ore. Hydrometallurgy, 1991, 27: 125-139.

DOI: 10.1016/0304-386x(91)90061-p

Google Scholar

[7] YANG, J., ZENG ,Z.M. The Situation Analysis of EMM of China Market in 2010, China's Manganese Ind, 2011, 29(02): 6-10.

Google Scholar

[8] Zhuo, C., Zhu, G.C., Zhao, Y.N. Study in reduction-roast leaching manganese from low-grade manganese dioxide ores using cornstalk as reductant. Hydrometallurgy, 2009, 96: 175-179.

DOI: 10.1016/j.hydromet.2008.08.004

Google Scholar

[9] Mishra, D., Srivastava, R.R., Sahu, K.K. Leaching of roast-reduced manganese nodules in NH3–(NH4)2CO3 medium. Hydrometallurgy, 2011, 109: 215-220.

DOI: 10.1016/j.hydromet.2011.07.006

Google Scholar

[10] Alison. L. Review of metal sulphide precipitation. Hydrometallurgy, 2010, 104: 222-234.

Google Scholar

[11] Shea, D., Helz G R. The solubility of copper in sulfidic waters: Sulfide and polysulfide complexes in equilibrium with covellite. Geochimica et Cosmochimica Acta, 1988, 52(7): 1815–1825.

DOI: 10.1016/0016-7037(88)90005-1

Google Scholar