Abstract
Copper, cadmium and lead were extracted through a hollow fiber supported liquid membrane with Lix 84-i as copper extractant and Alamine 304-i as extractant for cadmium and lead. The mass transfer rate, expressed as permeability P, was limited by the diffusion through the aqueous stagnant films in the module for copper extraction. A characteristic permeability of 6.9 x 10-6 m s-1 was measured at a flow rate of 0.076 m s-1 through the fibers. The measured permeabilities were compared to generally accepted mass transfer correlations. For a feed flowing on the tube side, these correlations predicted a three times higher permeability than was measured, while at the shell side, the permeabilities predicted from these accepted correlations were up to a factor of 8 lower than the measured ones. The extraction rate of cadmium from chloride solutions was limited by membrane diffusion. At 0.2 M Alamine 304-i, a permeability of 4·10-6 m s-1 was measured. Higher extraction rates were found when cadmium was extracted from chloride-containing mixtures of phosphoric and sulfuric acid. The extraction rate of lead was a factor of 20 lower than that of cadmium. This was due to the fact that the extractant had a lower affinity for lead.
Original language | English (US) |
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Pages (from-to) | 185-195 |
Number of pages | 11 |
Journal | Journal of Membrane Science |
Volume | 146 |
Issue number | 2 |
DOIs | |
State | Published - Aug 5 1998 |
Externally published | Yes |
Keywords
- Cadmium
- Copper
- Extraction
- Hollow fiber
- Supported liquid membrane
ASJC Scopus subject areas
- Biochemistry
- General Materials Science
- Physical and Theoretical Chemistry
- Filtration and Separation