scholarly journals The Iron Removal in Marmatite Concentrate Pressure Leaching Process

Author(s):  
LUO Wen-bo ◽  
WANG Ji-kun ◽  
GAN Yin
2018 ◽  
Vol 51 (21) ◽  
pp. 117-122
Author(s):  
Adriaan Haasbroek ◽  
Johannes J. Strydom ◽  
John T. McCoy ◽  
Lidia Auret

1989 ◽  
Vol 25 (3-4) ◽  
pp. 241-260 ◽  
Author(s):  
Fiona M. Doyle ◽  
Hernando Arauco ◽  
Lucia M. Feng

Rare Metals ◽  
2011 ◽  
Vol 30 (6) ◽  
pp. 688-694 ◽  
Author(s):  
Zhanliang Yu ◽  
Keqiang Xie ◽  
Wenhui Ma ◽  
Yang Zhou ◽  
Gang Xie ◽  
...  

Metals ◽  
2020 ◽  
Vol 10 (7) ◽  
pp. 893
Author(s):  
Shenyong Li ◽  
Penghui Bo ◽  
Lianwei Kang ◽  
Haigang Guo ◽  
Wenyue Gao ◽  
...  

Experiments were conducted to investigate the process of aluminum and lithium extraction from high-alumina coal fly ash (HCFA) generated from coal-fired power plants located in northern China. The presence of mullite and other aluminosilicates lead to low reactivity of coal fly ash. An activation pretreatment that destroys an inert composition of coal is necessary. The activation roasting of coal fly ash using sodium chloride and a subsequent leaching process were performed in this research. The results showed that almost no aluminum and lithium were dissolved under direct water leaching, while about 7% and 10% of those were leached into the acid solution respectively. Adding NaCl enhanced the atmospheric pressure leaching of aluminum and lithium with a leaching rate around 50%. Phase analysis and equilibrium calculations results showed that the roasting reaction between the HCFA and NaCl occurred, which led to generation of main new phase NaAlSi3O8. The pressure extraction efficiencies of aluminum and lithium were increased to about 93% and 98%, respectively. The implications of the findings provide an alternative process for recovering aluminum and lithium from readily available high-alumina coal fly ash.


Minerals ◽  
2020 ◽  
Vol 10 (3) ◽  
pp. 224
Author(s):  
Shu-Chen Qin ◽  
Kai-Xi Jiang ◽  
Hai-Bei Wang ◽  
Bang-Sheng Zhang ◽  
Yu-Fang Wang ◽  
...  

Dissolved iron exerts significant effects on mineral leaching, impurity removal, and solution purification in the zinc hydrometallurgy process. To date, iron oxidation and migration behaviors are yet to be fully understood and further research on effective regulation mechanisms of iron is required. In this paper, zinc sulfide concentrate was used as the research object. The behaviors of both Zn and Fe during pressure leaching were investigated for varying temperature, acid addition, and leaching time. At temperature of 100~160 °C, H2SO4/Zn ratio of 0.9:1–1.25:1, and leaching time of 0.5–2.5 h, the zinc extraction increased with temperature, acidity and leaching time. The iron extraction, however, varied differently with increasing temperature, acidity and leaching time: (A) it increased with temperature to 150 °C and then decreased at higher temperature, and (B) displayed an initial increase followed by a decrease with respect to the leaching time. Based on the characteristics of the residue phase, chemical phase analysis was used to analyze the residue in detail. The extent of dissolution of iron-containing minerals and the extent of precipitation of ferric ions during the leaching process were quantitatively calculated.


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