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Cobalt-doped high-pressure cobalt-iron separation method for high-concentration cobalt-iron leaching solution

A separation method and leachate technology, applied in the field of hydrometallurgy, can solve the problems of increasing the pressure of subsequent wastewater treatment, reducing the iron grade of iron removal slag, high sulfur content, etc., reaching the limit of improvement and iron removal efficiency, increasing the gas-liquid contact area, The effect of improving stirring efficiency

Active Publication Date: 2022-07-08
취저우화여우코발트뉴머터리얼컴퍼니리미티드 +1
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  • Application Information

AI Technical Summary

Problems solved by technology

The method is divided into two stages, and the iron removal process is relatively cumbersome. In addition, the iron removal agent introduces impurity elements such as ammonia nitrogen and calcium, which reduces the iron grade (Fe content 25%) in the iron removal slag, and increases the subsequent wastewater treatment pressure.
[0005] In the field of cobalt hydrometallurgy, the separation of cobalt and iron in acid leaching solution itself is a relatively difficult task. Conventional and mature iron removal methods have certain problems when dealing with leaching solutions with high iron concentration.
The neutralization hydrolysis method will produce a large amount of ferric hydroxide colloid, which is not only difficult to achieve liquid-solid separation, but also easily causes the adsorption loss of cobalt ions
The treatment capacity of the goethite method is limited, and it is generally suitable for treating leachate with an iron ion concentration of about 5g / L. When the iron ion concentration is high, this process is difficult to implement
The jarosite method is suitable for treating leachate with high concentration of iron ions, but because the amount of slag produced by the jarosite method is large, and the sulfur content is high and the iron content is low, it is difficult to recycle, resulting in waste of resources and accumulation of waste slag

Method used

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  • Cobalt-doped high-pressure cobalt-iron separation method for high-concentration cobalt-iron leaching solution
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  • Cobalt-doped high-pressure cobalt-iron separation method for high-concentration cobalt-iron leaching solution

Examples

Experimental program
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Effect test

Embodiment 1

[0036] A cobalt-copper-iron alloy material was leached with sulfuric acid at 80°C to obtain a high-concentration leaching solution containing 103g / L of iron and 18g / L of cobalt. The solution was diluted to 1.6 times the volume after removing iron to obtain 65g / L of iron and 32g of cobalt. / L diluted solution, add Co(OH) at a concentration of 50g / L 2 Separation accelerator, the addition amount is 27.8g / L. The cobalt-iron pre-separation solution with a pH of 4.36 was obtained. It is continuously pumped into a closed high-pressure equipment, and the reaction is carried out under the environment of 180 ° C and 0.3MPa oxygen partial pressure, and the liquid flux rate is controlled to make the solution flow and react in the high-pressure equipment for about 2 hours. The pressure relief device relieves the pressure, and the generated steam heat resource is returned to the front end to maintain the liquid temperature before iron removal. After depressurization, the iron-removal liqu...

Embodiment 2

[0041] A cobalt-copper-iron alloy material was leached with sulfuric acid at 80°C to obtain a leaching solution containing 75g / L of iron and 15g / L of cobalt. The solution was diluted to 1.5 times the volume by separating the cobalt and iron to obtain 50.6g / L of iron and 21g of cobalt. / L diluted solution, add Co(OH) at a concentration of 30g / L 2 The iron removal accelerator was added in an amount of 11.2g / L. A solution before iron removal with pH of 3.5 was obtained. It is continuously pumped into a closed high-pressure equipment, and the reaction is carried out under the environment of 180 ° C and 0.3MPa oxygen partial pressure, and the liquid flux rate is controlled to make the solution flow and react in the high-pressure equipment for about 4 hours. The pressure of the device is relieved, and the generated steam heat resource is returned to the front end to maintain the liquid temperature before iron removal. The cobalt-iron separation liquid after pressure relief enters ...

Embodiment 3

[0043] A cobalt-copper-iron alloy material was leached with sulfuric acid at 80 °C to obtain a high-concentration leaching solution containing 103 g / L of iron and 18 g / L of cobalt. Cobalt 32.5g / L diluted solution, add CoCO at a concentration of 50g / L 3 The iron removal accelerator was added in an amount of 41.5g / L. A solution before iron removal with pH 4.0 was obtained. It is continuously pumped into a closed high-pressure equipment, and the reaction is carried out under the environment of 180 ° C and 0.3MPa oxygen partial pressure, and the liquid flux rate is controlled to make the solution flow and react in the high-pressure equipment for about 2 hours. The pressure of the device is relieved, and the generated steam heat resource is returned to the front end to maintain the liquid temperature before iron removal. The cobalt-iron separation liquid after pressure relief enters the thickener at 80°C. After flocculation and sedimentation, the supernatant liquid is separated f...

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Abstract

The invention discloses a cobalt-doped high-pressure cobalt-iron separation method for high-concentration cobalt-iron leaching solution. The technical scheme adopted in the present invention is as follows: the cobalt-containing copper-iron raw material is leached with sulfuric acid to obtain a high-concentration cobalt-iron leaching solution; after the high-concentration cobalt-iron leaching solution is diluted to a set concentration, a cobalt-containing compound is added, and the cobalt-iron separation is obtained by fully stirring. Pre-liquid; cobalt-iron pre-separation liquid is pumped into closed high-pressure equipment to create a high oxygen partial pressure environment with pure oxygen, and fully reacted under the comprehensive action of stirring, gas disturbance and liquid flow; the liquid after cobalt-iron separation adopts thickening + pressure filtration + centrifugation Liquid-solid separation is carried out, the obtained solid is iron oxide powder, and the obtained liquid is processed by SO 2 After reduction, it is returned to the front end as a diluent of high-concentration cobalt-iron leaching solution, or enters the extraction system as a cobalt-extracting stock solution. The method can realize the rapid separation of elements in the cobalt-iron leaching solution, the obtained iron oxide powder has low impurity content, can be sold as iron concentrate powder, and can realize the full and comprehensive utilization of resources while reducing the pressure of environmental protection.

Description

technical field [0001] The invention belongs to the technical field of hydrometallurgy, and relates to a cobalt-doped high-pressure cobalt-iron separation method for a high-concentration cobalt-iron leaching solution. Background technique [0002] Copper-cobalt-iron oxide mixture, hydroxide mixture or crude copper-cobalt-iron alloy are common leaching raw materials in cobalt hydrometallurgy industry. These raw materials have the advantages of high content of valuable elements and low content of impurities such as manganese and magnesium. However, some of these raw materials also have the problem of too high iron content. Due to the close properties of cobalt and iron, the two elements will enter the solution at the same time during leaching, thus producing a large amount of mixed leaching solution containing cobalt and iron. How to efficiently separate cobalt and iron It is one of the limiting factors restricting the increase of cobalt production capacity. [0003] Chinese...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/08C22B3/22C22B3/44C22B23/00
CPCY02P10/20
Inventor 王斌洪涛姜俊程琛邓永贵张涛
Owner 취저우화여우코발트뉴머터리얼컴퍼니리미티드
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