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Cobalt and magnesium separation method in cobalt nickel wet metallurgy process

A technology of hydrometallurgy and separation method, applied in the direction of magnesium hydroxide, process efficiency improvement, etc., can solve the problems of process cost increase, low recovery efficiency, waste of cobalt and nickel, etc., achieve simple and easy to control operation, and increase adsorption capacity , The effect of low process cost

Inactive Publication Date: 2018-06-19
MEISHAN SHUNYING POWER BATTERY MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, because magnesium fluoride itself is a strong base and weak acid salt, on the one hand, the liquid needs to have a higher pH during the magnesium fluoride precipitation process, which will cause a large amount of cobalt or nickel to precipitate into the filter residue, thereby causing cobalt, nickel waste and low recovery efficiency; on the other hand, it is necessary to add an excessive amount of sodium fluoride to completely precipitate the magnesium in the solution, which will cause a large amount of fluoride ions in the final waste liquid. If the standard is less than 5mg / L, the wastewater needs to be treated again, resulting in an increase in process costs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] This embodiment provides a cobalt-magnesium metal separation method in the cobalt-nickel hydrometallurgy process, and the specific operations are as follows:

[0042] The cobalt-containing magnesium solution extracted and removed from the cobalt-nickel hydrometallurgy process was tested. The cobalt content in the cobalt-containing magnesium solution was 14.6g / L and the magnesium content was 3.4g / L. Then adjust the pH of the cobalt-containing magnesium solution to 2.1, and at a temperature of 27° C., control the cobalt-containing magnesium solution to 6 m 3 / h flow rate over special resin CH-90. After the cobalt metal content in the outlet liquid of the special resin CH-90 resin column reaches 0.01g / L, use 5% sulfuric acid solution as the analysis solution to wash the resin column, and the analysis solution is 15m 3 Rinse the resin at a flow rate of / h for 1 hour, and control the volume ratio of the analysis solution to the special resin to be 3:1. After repeated analys...

Embodiment 2

[0045] The cobalt-containing magnesium solution extracted and removed from the cobalt-nickel hydrometallurgy process was tested. The cobalt content in the cobalt-containing magnesium solution was 18.2g / L and the magnesium content was 5.3g / L. Then the pH of the cobalt-containing magnesium solution is adjusted to 2.4, and at a temperature of 32°C, the cobalt-containing magnesium solution is controlled to 4 m 3 / h flow rate over special resin CH-90. After the cobalt content reaches 0.008g / L in the outlet liquid of the special resin column, use 7% sulfuric acid solution as the analysis solution, and control the analysis solution at 15m 3 Rinse the resin at a flow rate of / h for 1 hour to obtain a cobalt content of 16.2g / L in the solution after analysis, and then return to the extraction section for impurity removal to produce cobalt sulfate crystals or battery-grade ternary precursors.

[0046] Then the solution after the selective adsorption of cobalt metal is adjusted to 8.4 wi...

Embodiment 3

[0048] Take the cobalt-containing magnesium solution after extraction and removal of impurities during the cobalt-nickel hydrometallurgy process. After testing, the cobalt content in the cobalt-containing magnesium solution is 26.7g / L, and the magnesium content is 7.6g / L. Then adjust the pH of the cobalt-containing magnesium solution to 2.7. At a temperature of 38°C, control the cobalt-containing magnesium solution to 3m 3 / h flow rate over special resin CH-90. After the outlet liquid of the special resin column reaches 0.007g / L, use 8% hydrochloric acid solution as the analysis solution to rinse the resin column, and the analysis solution is 15m 3 Rinse the resin at a flow rate of / h for 1 hour, and the cobalt content in the resolved solution is 21.8g / L, and then return to the extraction section to remove impurities to produce cobalt sulfate crystals or battery-grade ternary precursors.

[0049] Then adjust the pH of the solution after selective adsorption of cobalt metal t...

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Abstract

The invention discloses a cobalt and magnesium separation method in the cobalt nickel wet metallurgy process, and relates to the technical field of metal separation and purification in the cobalt nickel wet metallurgy process. The method comprises the steps that cobalt metal ions in a cobalt containing magnesium solution obtained after extraction impurity removal in the cobalt nickel wet metallurgy process are selectively absorbed through polyvalent metal adsorbent resin, and therefore cobalt and magnesium in the solution are separated. The method further comprises the steps that adsorption saturation polyvalent metal adsorbent resin is subject to reverse analysis treatment to obtain high-concentration cobaltates solution; a magnesium containing solution obtained after cobalt absorbing issubject to alkali blending, precipitation and filtering, and high-purity magnesium hydrate crystals are obtained. Compared with a cobalt and magnesium separation method in the traditional cobalt nickel wet metallurgy process, the method is easy to operate and easy to control, separation of cobalt and magnesium in an acid leaching solution after extraction and impurity removal and high-purity sufficient recycling of cobalt and magnesium can be effectively achieved, the method is environment-friendly, efficient, low in process cost and high in industrial practical value.

Description

technical field [0001] The invention relates to a metal separation and purification method in the cobalt-nickel hydrometallurgy process, in particular to a separation method for magnesium impurity metal and cobalt metal in the cobalt-nickel hydrometallurgy process. Background technique [0002] The cobalt-nickel hydrometallurgy process is the process of separating and purifying cobalt and nickel metals from cobalt-nickel ores or various metal wastes containing cobalt and nickel. It usually consists of three major steps: acid leaching and dissolution-extraction and impurity removal-cobalt and nickel separation composition. With the widespread use of various cobalt-magnesium alloys, most of the acid leaching solutions contain relatively high magnesium metal ion impurities in the process of recycling metal waste for cobalt-nickel hydrometallurgy. Moreover, since the extraction curve of metal magnesium is very close to the extraction curve of cobalt-nickel metal in the process ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/24C22B3/44C22B23/00C01F5/14
CPCC01F5/14C01P2006/80C22B3/24C22B3/44C22B23/0453C22B23/0461Y02P10/20
Inventor 赵澎赵林但勇陈雪风
Owner MEISHAN SHUNYING POWER BATTERY MATERIALS CO LTD
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