Recovery of metals from chloride leach solutions of anode slimes by solvent extraction. Part II: Recovery of silver and copper with LIX 63 and Alamine 336

2018 ◽  
Vol 180 ◽  
pp. 49-57 ◽  
Author(s):  
Wei Dong Xing ◽  
Man Seung Lee ◽  
Gamini Senanayake
2012 ◽  
Vol 44 ◽  
pp. 1514
Author(s):  
S. Porhel ◽  
J. Duhamet ◽  
G. Borda ◽  
R. Denoyel ◽  
A.P. Serond

1978 ◽  
Vol 13 (5) ◽  
pp. 429-437 ◽  
Author(s):  
Curtis McDonald ◽  
Mohamed M. Mahayni ◽  
Marwan Kanjo

2013 ◽  
Vol 34 (1) ◽  
pp. 153-163 ◽  
Author(s):  
Raju Banda ◽  
Thi Hong Nguyen ◽  
Man Seung Lee

Abstract In the present work, amine based extractant and its mixture with cationic and solvating extractants were tested for the extraction of HCl from chloride solution containing Al(III). The chloride feed solution resulted from the leaching of spent HDS (hydro-desulfurization) catalysts. For this purpose, amine extractants, such as TOA (trioctyl amine), Alamine 336 (a mixture of tri-octyl/decyl amine), Alamine 308 (tri-isooctyl amine), and TEHA (tri 2-ethylhexyl amine) were used and the extraction and stripping behavior of HCl was compared. The extracted HCl was easily stripped from loaded TEHA phase, when compared with the other tested tertiary amine system. Solvent extraction reaction of HCl by TEHA was determined from the extraction data. Unlike TOA and Alamine 336, adding cationic extractant to TEHA had negligible effect on the extraction and stripping of HCl. In our experimental ranges, no Al was extracted by amines and pure HCl was recovered. MaCabe- Thiele diagrams for the extraction and stripping of HCl by TEHA were constructed.


2012 ◽  
Vol 113-114 ◽  
pp. 25-30 ◽  
Author(s):  
Jinshan Li ◽  
M. Sadegh Safarzadeh ◽  
Michael S. Moats ◽  
Jan D. Miller ◽  
K. Marc LeVier ◽  
...  

2017 ◽  
Vol 34 (1) ◽  
pp. 355-362 ◽  
Author(s):  
É. C. Avelar ◽  
C. L. G. Alvarenga ◽  
G. P. S. Resende ◽  
C. A. Morais ◽  
M. B. Mansur

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