Method for deeply removing copper in hydrochloric acid leaching solution of cobalt nickel hydroxide
A technology of nickel-cobalt hydroxide hydrochloride and nickel-cobalt hydroxide, which is applied in the field of non-ferrous hydrometallurgy, can solve the problems of inability to achieve deep copper removal, limit the scope of application, and fail to meet the requirements of subsequent processes, and achieve obvious copper removal effect and easy operation The effect of simplicity and ease of industrial production
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0018] (1) After the nickel cobalt hydroxide is leached with hydrochloric acid, the hydrochloric acid leaching solution is obtained. After analysis, the sulfate content in the nickel cobalt hydroxide hydrochloric acid leaching solution is 15g / L, and the nickel ion concentration is 155g / L. After adjustment, the solution sulfate radical content 35g / L forms pre-extraction solution, and after analysis, its copper content is 0.23g / L;
[0019] (2) Add nickel-cobalt hydroxide to the pre-extraction solution to adjust the pH value. After adjustment, the pH value of the solution is 4.0;
[0020] (3) Press-filter the pH-adjusted solution and saponify the P 507 The extraction agent is subjected to countercurrent extraction, the extraction ratio is 5:1, and the copper content of the raffinate is analyzed after extraction, which is 0.0018g / L.
Embodiment 2
[0022] (1) After the nickel cobalt hydroxide is leached with hydrochloric acid, the hydrochloric acid leaching solution is obtained. After analysis, the sulfate content in the nickel cobalt hydroxide hydrochloric acid leaching solution is 18g / L, and the nickel ion concentration is 162g / L. Adjustment, after adjustment, solution sulfate radical content 28g / L, forms the pre-extraction liquid, analyzes its copper content to be 0.19g / L;
[0023] (2) Add nickel-cobalt hydroxide to the pre-extraction solution to adjust the pH value. After adjustment, the pH value of the solution is 4.5;
[0024] (3) Press-filter the pH-adjusted solution and saponify the P 507 The extraction agent is subjected to countercurrent extraction, the extraction ratio is 4:1, and the copper content of the raffinate is analyzed after extraction, which is 0.0023g / L.
Embodiment 3
[0026] (1) After the nickel cobalt hydroxide is leached with hydrochloric acid, the hydrochloric acid leaching solution is obtained. After analysis, the sulfate content in the nickel cobalt hydroxide hydrochloric acid leaching solution is 21g / L, and the nickel ion concentration is 170g / L. Adjustment, after adjustment, solution sulfate content 25g / L, forms pre-extraction solution, analyzes its copper content to be 0.26g / L;
[0027] (2) Add nickel-cobalt hydroxide to the pre-extraction solution to adjust the pH value. After adjustment, the pH value of the solution is 4.2;
[0028] (3) Press-filter the pH-adjusted solution and saponify the P 507 The extraction agent is subjected to countercurrent extraction, the extraction ratio is 3:1, and the copper content of the raffinate is analyzed after extraction, which is 0.0035g / L.
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com