Manganese extraction by sulfur-based reduction roasting–acid leaching from low-grade manganese oxide ores

2013 ◽  
Vol 133 ◽  
pp. 126-132 ◽  
Author(s):  
Yuanbo Zhang ◽  
Zhixiong You ◽  
Guanghui Li ◽  
Tao Jiang
2015 ◽  
Vol 25 (5) ◽  
pp. 1677-1684 ◽  
Author(s):  
Chang-xin LI ◽  
Hong ZHONG ◽  
Shuai WANG ◽  
Jian-rong XUE ◽  
Fang-fang WU ◽  
...  

Author(s):  
Yuanbo Zhang ◽  
Daoxian Duan ◽  
Zhixiong You ◽  
Guanghui Li ◽  
Xiaohui Fan ◽  
...  

2013 ◽  
Vol 49 (1) ◽  
pp. 97-106 ◽  
Author(s):  
D. Hariprasad ◽  
M. Mohapatra ◽  
S. Anand

Low and medium grade land as well sea based manganese ores were used for manganese extraction in H2SO4 - NH3NH2HSO4 (hydrazine sulphate) medium For land based Mn ores, only Mn recovery is important but for sea nodules which contain substantial amounts Co, Ni, and Cu, their recovery is equally important. In the present studies four samples used were: Indian ocean manganese nodules, medium and low grade Mn ores of Gujarat, and low grade Mn ore of Orissa, India. The Mn content of these ores varied from 15 to 39%. The objective of this work is to establish a reductant which can be used for leaching Mn from all types of ores. The optimum conditions established for nodules by varying parameters such as time, temperature, pulp density, H2SO4 and NH3NH2HSO4 concentrations were: pulp density 10%, time 0.5h, temperature 110?C, NH3NH2HSO4 3.25 g/10g, H2SO4 2.0% (v/v) for 96.9% Mn, 85.25% Cu, 92.58% Ni and 76.5% Co extractions. More than 92% Mn could be leached from different types of ores by varying amount of reductant and acid concentration at 35?C. Depending on Mn content 1.0 to 1.2 times stochiometric amount of reductant and 1.5 to 1.8 times sulphuric acid were required for >92% Mn extraction.


2010 ◽  
Vol 49 (3) ◽  
pp. 219-226 ◽  
Author(s):  
F. R. Carrillo-Pedroza ◽  
M. A. Sánchez-Castillo ◽  
M. J. Soria-Aguilar ◽  
A. Martínez-Luévanos ◽  
E. C. Gutiérrez

Author(s):  
Malaya Kumar Jena ◽  
Subhabrata Mishra ◽  
Shaswat Kumar Das ◽  
Syed Mohammed Mustakim ◽  
Adeyemi Adesina

2014 ◽  
pp. 105-109 ◽  
Author(s):  
Alexander G. Suss ◽  
Alexander A. Damaskin ◽  
Alexander S. Senyuta ◽  
Andrey V. Panov ◽  
Andrey A. Smirnov

2020 ◽  
Vol 989 ◽  
pp. 559-563
Author(s):  
Ashimkhan T. Kanayev ◽  
Khussain Valiyev ◽  
Aleksandr Bulaev

The goal of the present work was to perform bioleaching of uranium from low grade ore from Vostok deposit (Republic of Kazakhstan), which was previously subjected to long-term acid leaching. The ore initially contained from 0.15 to 0.20% of uranium in the form of uraninite, but ore samples used in the study contained about 0.05% of uranium, as it was exhausted during acid leaching, and uranium was partially leached. Representative samples of ore were processed in 1 m columns, leach solutions containing 5, 10, 20 g/L of sulfuric acid and bacterial cells (about 104) were percolated through the ore. Leaching was performed at ambient temperature for 70 days. In one of the percolators, the leaching was performed with leaching solution containing 10 g/L of H2SO4, cells of A. ferrooxidans, and 0.5 g/L of formaldehyde. Leaching with the solution containing 5, 10, and 20 g/L of sulfuric acid made it possible to extract 50, 53, and 58% of uranium. Addition of formaldehyde in leach solution led to the decrease in uranium extraction extent down to 37%. Thus, the results of the present work demonstrated that uranium ore exhausted during long-term acid leaching may be successfully subjected to bioleaching, that allows extracting residual quantities of uranium. Leaching rate of uranium from exhausted ore depended on both sulfuric acid concentration and microbial activity of bacteria isolated from acid mine drainage, formed on uranium deposit. In the same time, acid mine drainage may be used as a source of inoculate, to start bioleaching process.


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