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Method for acid-free leaching of cobalt intermediate product from sulfate

A technology of acid leaching and sulfate, applied in the direction of improving process efficiency, etc., can solve the problems of ammonia nitrogen or sodium pollutants, large consumption of auxiliary materials, large consumption of acid and alkali, etc., achieve good filtration performance, high-efficiency leaching, avoid The effect of alkali consumption

Active Publication Date: 2021-07-23
赣州逸豪优美科实业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In view of the deficiencies in the prior art, the purpose of the present invention is to provide a method for leaching cobalt intermediates without acid with sulfate. Pollution is generated, and the acidic leaching solution needs to be neutralized and adjusted to pH later, resulting in a large amount of acid and alkali consumption, and will produce ammonia nitrogen or sodium pollutants. At the same time, it is difficult to filter, low in operating efficiency, and high in production costs. Technical problems such as large consumption of auxiliary materials in iron cobalt leaching solution in the process of iron removal

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:

[0037] Step 1, batching; Thick cobalt hydroxide and the cobalt leaching solution containing ferrous sulfate (Fe in its solution 2+ The concentration is 30g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio is 0.8:1 to carry out proportioning and mixing, it is added in the leaching tank;

[0038]Step 2, acid-free leaching; blow oxygen into the mixed materials in step 1, and carry out leaching at a temperature of 90°C for 2 hours, and control the liquid-solid ratio during the leaching process to 10; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the leaching ...

Embodiment 2

[0041] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:

[0042] Step 1, batching; Thick cobalt carbonate and ferrous sulfate solution (Fe in its solution 2+ The concentration is 32g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio 1:1, mix it, and add it into the leaching tank;

[0043] Step 2, acid-free leaching; blow oxygen into the mixed materials in step 1, and carry out leaching at a temperature of 85°C for 5 hours, and control the liquid-solid ratio during the leaching process to be 7; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the leaching is complete;

[0044] Step 3: Filtration; solid-liquid separa...

Embodiment 3

[0046] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:

[0047] Step 1, batching; Thick cobalt hydroxide and the cobalt leaching solution containing ferrous sulfate (Fe in its solution 2+ The concentration is 35g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio is 1.05:1 carry out proportioning mixing, it is added in the leaching tank;

[0048] Step 2, acid-free leaching; air is blown into the mixed materials in step 1, and leaching is carried out at a temperature of 90°C for 6 hours, and the liquid-solid ratio during the leaching process is controlled to be 6; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the ...

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Abstract

The invention discloses a method for acid-free leaching of a cobalt intermediate product from sulfate, and aims to solve the technical problems that inorganic acid and a reducing agent need to be added in the leaching process of the cobalt intermediate product, gas pollution is easy to generate, acid leaching liquid needs to be neutralized subsequently to adjust the pH value, the acid and alkali consumption is large, pollutants of ammonia nitrogen or sodium are generated, meanwhile, filtration is difficult, operation efficiency is low, production cost is high, and auxiliary material consumption in the iron removal process of the cobalt leaching solution containing ferrous sulfate is large. According to the method, a solution containing ferrous sulfate is used for leaching the cobalt intermediate product, then solid-liquid separation is carried out, valuable elements such as cobalt and copper are left in filtrate, and impurity elements such as iron and silicon are left in filter residues. According to the method, the cobalt intermediate product can be leached without using inorganic acid such as sulfuric acid and a reducing agent, so that the situation that sulfur dioxide pollutes the environment is thoroughly eliminated, and meanwhile, the cobalt leaching liquid containing ferrous sulfate is used for leaching, so that consumption of alkali is avoided, leaching of the cobalt intermediate product is achieved, and two purposes are achieved.

Description

technical field [0001] The invention belongs to the technical field of nickel-cobalt hydrometallurgy and cobalt resource recovery, and specifically belongs to a method for leaching cobalt intermediates without acid with sulfate. Background technique [0002] my country's cobalt resources are scarce, so most of the raw materials of domestic cobalt smelting enterprises need to rely on imports; at the same time, with the rapid development of batteries, hard alloys, industrial catalysis and other industries, my country's cobalt consumption is increasing year by year. Nowadays, for the import of cobalt resources, it is generally first to enrich foreign low-grade cobalt ores into higher-grade crude cobalt intermediates, the main components of which are cobalt hydroxide or cobalt carbonate, and then transport them back to China to process. [0003] At present, the traditional treatment method for crude cobalt intermediates is to use an acid method for leaching. This method needs t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/04C22B3/22C22B15/00C22B23/00
CPCC22B3/04C22B3/08C22B3/22C22B23/043C22B15/0071Y02P10/20
Inventor 熊以俊许用华钟轩谢欣旭
Owner 赣州逸豪优美科实业有限公司
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