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Synchronized production method of reducing leaching and oxidizing deironing of cobalt-copper ore

A technology for oxidative iron removal and production method, applied in the field of chemical industry, can solve the problems of high cost, large consumption, time consumption, etc., and achieve the effects of reducing direct production cost, improving production efficiency, and improving metal recovery rate

Active Publication Date: 2014-06-25
江苏雄风科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The leaching of existing cobalt-copper ores generally adopts a two-stage leaching method. Firstly, the metal cobalt-copper is leached from the ore into the solution with a reducing agent, and then an oxidant is added to oxidize and remove impurities such as iron. The qualified solution is sent for extraction. This method cobalt-copper During the leaching process of ore, the consumption of various auxiliary materials is relatively large, and the metal recovery rate is not high
[0003] Its main disadvantages are: long process flow, high cost, low efficiency, time-consuming

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0014] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:

[0015] The cobalt-copper ore is crushed and slurried into cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6mol / l. The volume ratio of cobalt-copper slurry to sulfuric acid is 20:1, and the temperature is controlled at 75°C, while stirring, add 4% of the total amount of cobalt-copper ore sodium sulfite for reductive leaching, control the mass percentage of cobalt in the wet slag to 0.13%, and the mass percentage of copper to 0.2%. Iron, control the reaction temperature at 90℃, the reaction time is 1 hour, slowly add calcium carbonate to adjust the pH value of the solution to 2.0, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is added at 50kg, the dry ore ratio is 1g / L iron, and the electrode pot...

Embodiment 2

[0017] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:

[0018] The cobalt-copper ore is crushed and slurried into a cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6mol / l. The volume ratio of the cobalt-copper slurry and sulfuric acid is 50:3, and the temperature is controlled at 80℃, under the condition of stirring, add 5% of the total amount of cobalt copper ore sodium metabisulfite for reductive leaching, control the mass percentage of cobalt in the wet slag to 0.17%, and the percentage of copper to 0.22%, while directly heating up In addition to iron, control the reaction temperature at 92℃, the reaction time is 2.5 hours, slowly add sodium carbonate to adjust the pH value of the solution to 2.8, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is ...

Embodiment 3

[0020] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:

[0021] The cobalt-copper ore is crushed and slurried into a cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6 mol / l. The volume ratio of the cobalt-copper slurry to sulfuric acid is 100:7, and the temperature is controlled at At 85°C, while stirring, add 6% of the total amount of cobalt-copper ore sulfur dioxide for reduction leaching, control the mass percentage of cobalt in the wet slag to 0.18%, and the mass percentage of copper to 0.25%, and directly increase the temperature to remove Iron, control the reaction temperature to 95℃, the reaction time is 4 hours, slowly add sodium hydroxide to adjust the pH value of the solution to 3.5, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is added in...

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PUM

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Abstract

The present invention discloses a synchronized production method of reducing leaching and oxidizing deironing of cobalt-copper ore, including the following steps: crushing and mixing the cobalt-copper ore into cobalt copper slurry, then adding sulfuric acid into the cobalt-copper slurry for leaching with a temperature controlled at 75-85 DEG C, stirring while adding a reducing agent for reducing leaching with an amount of 4-6% of the total cobalt-copper ore, controlling cobalt content in wet residue to be less than 0.2% and copper content less than 0.3%, controlling of the reaction temperature to be 90-95 DEG C and reaction time being 1 to 4 hours, slowly adding alkali to adjust the PH value of the solution to 2.0-3.5, at the same time slowly supplementarily adding cobalt copper slurry for oxidizing deironing according to the content of Fe2+ in solution to make Co3+ and Fe2+ to reach a equilibrium state, and finally performing the solid-liquid separation to obtain qualified leachate. According to the invention, by controlling the electrode potential of the solution, synchronized performance of the reducing leaching process - the oxidizing deironing process is ensured, so direct production cost is significantly reduced, the metal recovery is significantly improved, thus improving production efficiency.

Description

Technical field [0001] The invention relates to a production method for simultaneous reduction, leaching, oxidation and iron removal of cobalt-copper ore, and belongs to the field of chemical engineering. Background technique [0002] The existing cobalt-copper ore generally adopts a two-stage leaching method. First, the metal cobalt and copper are leached from the ore into the solution with a reducing agent, and then an oxidant is added to oxidize and remove impurities such as iron. The qualified solution is sent for extraction. During the leaching process of ore, various auxiliary materials are consumed, and the metal recovery rate is not high. [0003] The main disadvantages are: long process flow, high cost, low efficiency and time-consuming. Summary of the invention [0004] The purpose of the present invention is to provide a production method with simple process flow, high metal recovery rate, low production cost and low environmental pollution by cobalt copper ore reduction...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/08C22B3/04C22B3/44C22B15/00C22B23/00
CPCY02P10/20
Inventor 沈哲昊施东峰王松辉
Owner 江苏雄风科技有限公司
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