scholarly journals High Pressure Acid Leaching of Co Matte Converted from Co Concentrate

2016 ◽  
Vol 57 (10) ◽  
pp. 1753-1758
Author(s):  
Gunha Kim ◽  
Ga-hee Kang ◽  
Sangjun Kim ◽  
Sookyung Kim ◽  
Jeongsoo Sohn ◽  
...  
Author(s):  
Dmitry Zinoveev ◽  
Pavel Grudinsky ◽  
Ekaterina Zhiltsova ◽  
Darya Grigoreva ◽  
Anton Volkov ◽  
...  

Red mud is a hazardous waste of alumina industry that contains high amounts of iron, aluminum, titanium and REEs. One of the promising methods for the extraction of iron from red mud is car-bothermic reduction with the addition of sodium salts. This research focuses on the process of hy-drochloric high-pressure acid leaching using 10–20% HCl of two samples of non-magnetic tailings obtained by 60-minute carbothermic roasting of red mud at 1300 °C and the mixture of 84.6 wt. % of red mud and 15.4 wt. % Na2SO4 at 1150 °C, respectively, with subsequent magnetic separation of metallic iron. An influence of temperature, leaching duration, solid-to-liquid-ratio and acid con-centration on dissolution behavior of Al, Ti, Mg, Ca, Si, Fe, Na, La, Ce, Pr, Nd, Sc, Zr were studied. Based on the investigation of the obtained residues, mechanism of passing of valuable elements into the solution was proposed. It has shown that 90% Al, 91% Sc and above 80% of other REEs can be dissolved under optimal conditions; Ti can be extracted into the solution or the residue depending on the leaching temperature and acid concentration. Based on the research results, novel flowsheets for red mud treatment were developed.


Metals ◽  
2021 ◽  
Vol 11 (3) ◽  
pp. 469
Author(s):  
Dmitry Zinoveev ◽  
Pavel Grudinsky ◽  
Ekaterina Zhiltsova ◽  
Darya Grigoreva ◽  
Anton Volkov ◽  
...  

Red mud is a hazardous waste of the alumina industry that contains high amounts of iron, aluminum, titanium and rare-earth elements (REEs). One of the promising methods for the extraction of iron from red mud is carbothermic reduction with the addition of sodium salts. This research focuses on the process of hydrochloric high-pressure acid leaching using 10 to 20% HCl of two samples of non-magnetic tailings obtained by 60 min carbothermic roasting of red mud at 1300 °C and the mixture of 84.6 wt.% of red mud and 15.4 wt.% Na2SO4 at 1150 °C, respectively, with subsequent magnetic separation of metallic iron. The influence of temperature, leaching duration, solid-to-liquid-ratio and acid concentration on the dissolution behavior of Al, Ti, Mg, Ca, Si, Fe, Na, La, Ce, Pr, Nd, Sc, Zr was studied. Based on the investigation of the obtained residues, a mechanism for passing valuable elements into the solution was proposed. It has shown that 90% Al, 91% Sc and above 80% of other REEs can be dissolved under optimal conditions; Ti can be extracted into the solution or the residue depending on the leaching temperature and acid concentration. Based on the research results, novel flowsheets for red mud treatment were developed.


2019 ◽  
Vol 184 ◽  
pp. 162-174 ◽  
Author(s):  
Rodolfo Marin Rivera ◽  
Buhle Xakalashe ◽  
Ghania Ounoughene ◽  
Koen Binnemans ◽  
Bernd Friedrich ◽  
...  

2016 ◽  
Vol 52 (2) ◽  
pp. 127-134 ◽  
Author(s):  
Y. Chang ◽  
K. Zhao ◽  
B. Pesic

High pressure acid leaching (HPAL) is the primary method for extraction of nickel from limonitic laterite. The severe operating conditions, the complexity of facilities, and several technical problems, such as scale formation, have always accompanied the HPAL, however. In this paper, the selective acid leaching of nickel from the pre-reduced limonitic laterite under moderate HPAL conditions was studied. For the calcine with reduction degree of 93.4%, about 88.2% nickel could be selectively extracted at 100?C with an acid/ore ratio of 0.164, leaving less then 5.0g/L iron in the solution. Further increase of leaching temperature, and the ensuing dehydration, transformed goethite in the leaching residue to hematite. When the temperatures were as high as 180?C, the recovery of nickel increased to 95.2%, within one hour, depressing the residual soluble iron to below 1.0g/L (pO2= 1.0 MPa, acid/ore= 0.287).


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