Abstract
An electrolytic process is applied to the de-metalization of rinse waters emerging from nickel-plating baths. Optimum conditions of nickel recovery from this type of solution have been investigated through a series of experiments carried out in a rotating packed cell (Rollschichtzelle®). The effects of temperature and pH of electrolyte, current density, cell rotation speed, and diameter of the cathode granules were examined. Ninety percent of the nickel was recovered from a solution of 450 mL volume, with a pH of 5.5 ± 0.05, 2 g/L initial nickel concentration, and by using cathode granules of 5 mm in diameter. At 50 °C electrolyte temperature and 325 A/m2 current density, 74% current efficiency was attained with 4.2 kWh/kg Ni energy consumption.
Original language | English |
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Pages (from-to) | 1-8 |
Number of pages | 8 |
Journal | Hydrometallurgy |
Volume | 65 |
Issue number | 1 |
DOIs | |
Publication status | Published - Jul 2002 |
Keywords
- Nickel recovery
- Plating industry
- Reduction electrolysis
- Rinse waters
- Rollschichtzelle
- Rotating cathode