A method for reducing cobalt content in mixed slag in nickel sulfate production
A technology of nickel sulfate and cobalt content, applied in the direction of improving process efficiency, can solve the problems of affecting the yield of cobalt metal, failing to be separated and utilized, and containing cobalt in leaching slag, so as to reduce the content of cobalt metal, simple operation, Yield-enhancing effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0030] Flush the mixed slag weighing about 5 tons into 10m with hot water 3 Stir the slurry in the reactor, and then pump the slurry into 30m 3 The reaction kettle was filled with hot water, heated to about 80°C with steam, slowly added 350g / l dilute sulfuric acid to adjust the pH to 2.2, and kept the reaction temperature for 1.0h. Concentrated hydrochloric acid was slowly added to the slurry to adjust the pH to 1.3, and the reaction temperature was maintained to continue the reaction for 1.0 h. Then the slurry is pumped into the filter press for solid-liquid separation. After the filter press is stopped, hot water with a temperature of 80°C to 90°C is pumped into the filter press to wash the filter cake until the filter press filtrate is colorless. Then pass the high-pressure air into the filter press and blow for more than 30 minutes, until the filter cake is dried, stop the high-pressure air, and unload the filter cake.
[0031] After treatment, the mixed residue Co: 0.36%, mo...
Embodiment 2
[0033] Wash the mixed slag weighing about 4 tons into 10m with hot water 3 Stir the slurry in the reactor, and then pump the slurry into 30m 3 The reaction kettle was filled with hot water, heated to about 80°C with steam, slowly added dilute sulfuric acid with a concentration of 290g / l to adjust the pH to 2.5, and kept the reaction temperature to react for 1.0h. Concentrated hydrochloric acid was slowly added to the slurry to adjust the pH to 1.0, and the reaction temperature was maintained for 1.0 h. Then the slurry is pumped into the filter press for solid-liquid separation. After the filter press is stopped, hot water with a temperature of 80°C to 90°C is pumped into the filter press to wash the filter cake until the filter press filtrate is colorless. Then pass the high-pressure air into the filter press and blow for more than 20 minutes, until the filter cake is dried, stop the high-pressure air, and unload the filter cake.
[0034] After treatment, the mixed residue Co: 0....
Embodiment 3
[0036] The mixed slag weighing about 5 tons is flushed into 10m with hot water 3 Stir the slurry in the reactor, and then pump the slurry into 30 m 3 The reaction kettle is filled with hot water, heated to about 80°C with steam, slowly added with dilute sulfuric acid with a concentration of 400g / l to adjust the pH to 2.0, and the reaction temperature is maintained for 1.0h. Concentrated hydrochloric acid was slowly added to the slurry to adjust the pH to 1.5, and the reaction temperature was maintained for 1.0 h. Then the slurry is pumped into the filter press for solid-liquid separation. After the filter press is stopped, hot water with a temperature of 80°C to 90°C is pumped into the filter press to wash the filter cake until the filter press filtrate is colorless. Then pass the high-pressure air into the filter press and blow for 40 minutes until the filter cake is dried, stop the high-pressure air, and unload the filter cake.
[0037] After treatment, the mixed residue Co: 0....
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More