Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
9632571 | Hydrometallurgy | 2005 | 16 Pages |
Abstract
The extraction and stripping characteristics of CYANEX 301® binary extractant systems were investigated for the recovery of cobalt and nickel from sulphate solutions. The selectivity properties of these systems against calcium, manganese and magnesium were also studied. These binary extractant systems consisted of mixtures of CYANEX 301 with basic extractants (Primene® JMT, Amberlite® LA-2, Alamine® 336 and Aliquat® 336). Based on criteria such as extraction and stripping characteristics (efficiency and rates) and selectivity against calcium, manganese and magnesium, screening experiments were performed to select the most appropriate binary extractant systems. From this screening work, the CYANEX 301/amine systems all demonstrated that cobalt and nickel could be selectively extracted from calcium, manganese and magnesium. A large synergistic effect on the stripping kinetics and efficiencies of cobalt and nickel was also observed when any amine extractant was added to CYANEX 301. Among the amine extractant systems, CYANEX 301/Aliquat 336 was shown to be the most promising binary extractant system. McCabe-Thiele extraction and stripping isotherms with this system were then constructed to determine the number of stages required. Complete extraction of cobalt and nickel could be achieved in 2-3 stages while still maintaining a high selectivity against calcium, manganese and magnesium. Complete stripping of cobalt could also be achieved in 2-3 stages while complete nickel stripping was shown to still be difficult. The loading capacity of the binary system for cobalt and nickel was determined and found to be lower than the loading capacity of CYANEX 301.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
C. Bourget, B. Jakovljevic, D. Nucciarone,