Recovery of germanium and other valuable metals from zinc plant residues

2008 ◽  
Vol 92 (3-4) ◽  
pp. 87-94 ◽  
Author(s):  
M. Kul ◽  
Y. Topkaya
2011 ◽  
Vol 396-398 ◽  
pp. 552-555 ◽  
Author(s):  
Cun Xiong Li ◽  
Chang Wei ◽  
Hong Sheng Xu ◽  
Zhi Gan Deng ◽  
Ji Qiang Liao ◽  
...  

A hydrometallurgical process was used for selectively extraction of valuable metals from zinc plant residues. The process includes the following two steps. (1) The zinc plant residue is treated by sulfuric acid atmospheric leaching process with KMnO4 as oxidatant to selectively dissolve zinc while leaving most (above 98 pct) of indium and germandium in the iron residues. (2) The iron residues are treated by acidic atmospheric leaching process with NaClO3 as oxidant to dissolve indium and germanium. The valuable metals of indium and germanium in the second leaching solution can be reclaimed by further treatment. The optimum operating parameters of the first stage and the second stage were established by conditional tests. The experimental data indicated that under the conditions employed the zinc extraction in the first stage was above 95%, and the leaching percentage of indium and germanium in the second stage reached 91.6% and 90.7%, respectively.


2012 ◽  
Vol 51 (10) ◽  
pp. 3887-3894 ◽  
Author(s):  
Bahram Behnajady ◽  
Javad Moghaddam ◽  
Mohammad A. Behnajady ◽  
Fereshteh Rashchi

1991 ◽  
Vol 8 (1) ◽  
pp. 43-47
Author(s):  
J. Y. Kim ◽  
L. Rosato ◽  
R. W. Stanley

2010 ◽  
Vol 23 (1) ◽  
pp. 51-53 ◽  
Author(s):  
S.M. Javad Koleini ◽  
Hossein Mehrpouya ◽  
Kamal Saberyan ◽  
Mahmoud Abdolahi
Keyword(s):  

2012 ◽  
Vol 38 (3) ◽  
pp. 29-40
Author(s):  
Mahdi Gharabaghi ◽  
Mehdi Irannajad ◽  
Amir Reza Azadmehr ◽  
Majid Ejtemaei

Abstract Zinc plant residue is a hazardous waste which contains high quantity of nickel and other valuable metals. Process parameters such as reaction time, acid concentration, solid-liquid ratio, particle size, stirring speed and temperature for nickel extraction from this waste were optimized using factorial design. Main effects and their interactions were obtained by the analysis of variance ANOVA. Empirical regression model was obtained and used to predict nickel extraction with satisfactory results and to describe the relationship between the predicted results and the experiment results. The important parameters for maximizing nickel extraction were identifi ed to be a leaching time solid-liquid ratio and acid concentration. It was found that above 90% of nickel could be extracted in optimum conditions.


2017 ◽  
Vol 65 ◽  
pp. 128-138 ◽  
Author(s):  
Meng Li ◽  
Shili Zheng ◽  
Biao Liu ◽  
Hao Du ◽  
David Bruce Dreisinger ◽  
...  

Metals ◽  
2020 ◽  
Vol 10 (5) ◽  
pp. 655
Author(s):  
Sushanta Kumar Sahu ◽  
Maryam Kargar Razi ◽  
Mathieu Beuscher ◽  
Alexandre Chagnes

This paper concerns the development of an environment-friendly hydrometallurgical flowsheet dedicated to the recovery of zinc and nickel from a waste residue collected from an Iranian zinc plant. In particular, valuable metals from Ni-Cd cake waste generated at this plant were recovered by a simple hydrometallurgical process using minimum acid for leaching, and solvent extraction step was designed such that addition of sodium hydroxide was not required and the effluent generated is safe to dispose off. The waste was leached with a mixture of hydrochloric acid and sulfuric acid in the presence of hydrogen peroxide in order to achieve a good selectivity towards iron and calcium. Afterwards, cementation was performed at pH 5 in order to remove cadmium. Liquid–liquid extraction was then implemented to produce high-purity solutions of zinc and nickel. Zinc-nickel separation was obtained at pH 2 by using a mixture of bis-(2-ehtyl-hexyl)-phosphoric acid (HDEHP) and tris-2-ethylhexyl amine (TEHA) diluted in an aliphatic kerosene. TEHA did not directly participate but helped in the extraction of zinc by scavenging the protons released by HDEHP. Therefore, no alkaline solution was necessary for maintaining the equilibrium pH during liquid–liquid extraction. Finally, this flowsheet allowed to recover more than 95% of zinc and nickel from the residue with more than 99% purity.


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