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Method of leaching copper, cobalt and nickel from smelting alloy

An alloy, copper-cobalt technology, applied in the fields of hydrometallurgy and chemical production, can solve the problems of increasing the burden of iron removal, affecting the recovery rate of cobalt, and high price of sodium chlorate, achieving low requirements for anti-corrosion and high gas utilization rate , the effect of high reaction efficiency

Active Publication Date: 2015-11-18
CHANGSHA RES INST OF MINING & METALLURGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 3. The leaching method with sulfuric acid and sodium chlorate is a fast and easy-to-implement method, but the price of sodium chlorate is high and the production cost is high
[0009] The above-mentioned methods are difficult to process such high-temperature smelting alloys with complex components and stable structures, and generally have disadvantages such as low leaching of copper, cobalt and nickel, long process flow, and high production costs.
In addition, at the same time as the copper, cobalt and nickel in the alloy are leached, a large amount of iron is leached into the leach solution, which brings difficulties to the subsequent iron removal, increases the burden of subsequent iron removal operations, and leads to the loss of cobalt and copper, affecting the recovery of cobalt, copper and nickel Rate

Method used

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  • Method of leaching copper, cobalt and nickel from smelting alloy
  • Method of leaching copper, cobalt and nickel from smelting alloy
  • Method of leaching copper, cobalt and nickel from smelting alloy

Examples

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Embodiment 1

[0052] A method for leaching copper-cobalt-nickel from molten alloy of the present invention comprises the following steps:

[0053] The waste lithium-ion battery reduction smelting alloy containing three metals of copper, cobalt, nickel and iron impurities is melted, and the melting temperature is 1400°C, and then atomized into alloy powder by high-pressure water; the alloy powder is passed through a 100-mesh sieve, and the The particle size distribution is as shown in the following table 1, and the composition of the alloy powder is as shown in the following table 2:

[0054] Table 1: Particle size distribution of alloy powder in Example 1

[0055] Particle size / mm

Distribution rate / %

Cumulative distribution rate / %

-0.043 (-325 mesh)

73.22

73.22

-0.074~+0.043 (200~325 mesh)

16.46

89.68

-0.098~+0.074(150~200 mesh)

6.28

95.96

-0.150~+0.098(100~150 mesh)

4.04

100

[0056] Table 2: The particle ...

Embodiment 2

[0062] A method for leaching copper-cobalt-nickel from molten alloy of the present invention comprises the following steps:

[0063] The waste lithium-ion battery reduction smelting alloy containing three metals of copper, cobalt, nickel and iron impurities is melted, and the melting temperature is 1400°C, and then atomized into alloy powder by high-pressure water; the alloy powder is passed through a 100-mesh sieve, and the The particle size distribution is as shown in the above table 1 and table 2;

[0064] Take 250 g of the atomized 150-200 mesh alloy powder and add it to a stirring and aerating reaction device. In this stirring and aerating reaction device, 98% concentrated sulfuric acid is used as the leaching medium. The theoretical amount of the sum of the elements is 1.7 times, so that air or oxygen is evenly blown into the stirring shaft system of the stirring and aerating reaction device, and the shearing action of the stirring shaft system makes the blown gas evenly...

Embodiment 3

[0068] A method for leaching copper-cobalt-nickel from molten alloy of the present invention comprises the following steps:

[0069] The waste lithium-ion battery reduction smelting alloy containing three metals of copper, cobalt, nickel and iron impurities is melted, and the melting temperature is 1400°C, and then atomized into alloy powder by high-pressure water; the alloy powder is passed through a 100-mesh sieve, and the The particle size distribution is as shown in the above table 1 and table 2;

[0070] Take 250g of the atomized 200-325 mesh alloy powder and add it into a stirring and aerating reaction device. In this stirring and aerating reaction device, 98% concentrated sulfuric acid is used as the leaching medium, and the amount of acid is 2.0 times the theoretical amount of the sum of the elements, so that air or oxygen is evenly blown into the stirring shaft system of the stirring and aerating reaction device, and the shearing action of the stirring shaft system ma...

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Abstract

A method of leaching copper, cobalt and nickel from smelting alloy comprises the following steps: the smelting alloy containing at least two of copper, cobalt and nickel and iron impurities is molten, and then the molten smelting alloy is atomized into alloy powder by high-pressure gas or high-pressure water; the atomized alloy powder is added into a stir aeration reaction device, a sulfuric acid solution is used as a leaching medium in the stir aeration reaction device, air or oxygen is uniformly brought from a stirring shaft system of the stir aeration reaction device, the brought gas is uniformly dispersed under the shear action of stirring blades in high-speed rotation at the bottom of the stirring shaft system, and under the effects of an oxidizing agent and a catalyst, the alloy powder is subjected to corrosion oxidizing leaching reaction in the stir aeration reaction device; after reaction is completed, most iron impurities enter a leaching residue, and solid-liquid separation is finally carried out to collect and obtain a leaching liquid containing at least two of copper, cobalt and nickel. The method of leaching copper, cobalt and nickel from the smelting alloy has the advantages that the process cost is low; the technology is convenient to control; the production is stable and reliable; the environment pollution is low and the like.

Description

technical field [0001] The invention relates to the technical fields of hydrometallurgy and chemical production, in particular to a method for separating copper, cobalt, nickel and iron in smelted alloys. Background technique [0002] Waste lithium-ion battery smelting alloy is obtained by high-temperature reduction smelting of waste lithium-ion batteries. The alloy raw material is an iron alloy containing copper, cobalt and nickel, containing 10%-40% of cobalt, 10-50% of copper, and 10%-50% of nickel. 0.1% to 5%, the iron content is 10% to 80%, and the manganese content is 0.1% to 5%. [0003] At present, the methods for leaching valuable metals from copper-cobalt-nickel alloy mainly include: [0004] 1. High-temperature and high-pressure leaching method: use sulfuric acid or hydrochloric acid to leach cobalt, copper, and nickel in the cobalt-copper alloy into the solution through high-pressure leaching or combined normal pressure leaching. This method has complicated equ...

Claims

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Application Information

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IPC IPC(8): C22B3/04C22B7/00C22B15/00C22B23/00
CPCY02P10/20
Inventor 肖松文任国兴潘炳王鹏
Owner CHANGSHA RES INST OF MINING & METALLURGY
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