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Method for directly preparing copper sulfate and cathode copper from copper ore concentrate

A technology of copper concentrate and copper sulfate, applied in the direction of rotary drum furnace, crucible furnace, furnace, etc., can solve the problems of high operating cost, accumulation of impurities, and large one-time investment, so as to simplify the copper washing process, ensure the leaching effect, Overcome the effect of large investment

Active Publication Date: 2010-06-02
ZIJIN MINING GROUP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The first method is pyrometallurgy to produce cathode copper and by-product copper sulfate, generally including roasting, smelting, blowing, refining and other processes, suitable for the application of copper concentrate with a grade of 20-30%, and this method has a large one-time investment , long process flow, high technical requirements, high energy consumption and waste gas pollution in the pyrolysis process, and with the large-scale mining of copper mines, there are fewer and fewer rich ores, which can meet the requirements of high-grade pyrometallurgy. The source of ore is less and less, which hinders the development of pyrometallurgy
[0004] The second method is hydrometallurgy to produce cathode copper, mainly including copper concentrate sulfate roasting-atmospheric acid leaching-clean liquid-electrowinning process, roasting-ammonia leaching-extraction-electrowinning process, catalytic pre-oxidation leaching-extraction -Electrowinning processes, etc. are generally suitable for lower-grade copper concentrates, and these processes have a low recovery rate of copper, generally about 90%, and the highest is 94%. The productivity and metal recovery rate are low, resulting in relatively high production costs. high
Among them, scientific researchers have done a lot of experimental research work, and have continuously improved the copper leaching process and purification process, but there are still some problems: 1. Whether it is pre-roasting leaching method or direct leaching method, dilute sulfuric acid is basically used Leaching, the acidity and impurity content of the leaching solution are high, and it is difficult to obtain qualified products by direct crystallization. If the neutralization process is used to purify and remove impurities such as iron, the cost is high, the lost copper is difficult to wash and recover, and the process is complicated.
2. Due to the high concentration of copper in the leaching solution, the washing process of the leaching slag is longer, and the copper in this part of the washing water is returned to the leaching process, which greatly reduces the copper concentration in the leaching solution, which makes the equipment for evaporating and crystallizing copper sulfate a large investment and high energy consumption. High labor intensity and high operating costs
3. Due to the long-term circulation of the copper sulfate mother liquor prepared by concentrated crystallization, the accumulation of impurities is serious. In order to solve this problem, electrowinning copper removal is used to produce black copper or iron powder replacement method is used to produce sponge copper. Since these products are semi-finished products, resulting in product additional Problems such as low value and slow capital turnover also restrict the development of enterprises
[0006] In short, comparing the different processes of producing copper products from copper concentrates, the scope of application of the first two processes has limitations: pyrometallurgy is not suitable for small-scale production and low-grade copper concentrates; hydrometallurgy produces cathode copper, and the recovery rate of copper Low, not suitable for higher grade copper concentrate
Although the last type of bile copper method is suitable for higher-grade copper concentrates, there are many problems such as high equipment investment and labor intensity, high operating costs, and low added value of products.

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  • Method for directly preparing copper sulfate and cathode copper from copper ore concentrate
  • Method for directly preparing copper sulfate and cathode copper from copper ore concentrate

Examples

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Effect test

Embodiment 1

[0028] Embodiment one: if figure 1 Shown, a kind of method for directly producing copper sulfate and cathode copper with copper concentrate, the method comprises following sequential processing steps:

[0029] (a) Sulfation roasting, slurry copper concentrate with 28% sulfur content, 78%-0.074mm particle size, and 13% grade with water and stir evenly, and send it to the boiling furnace at a temperature of 400-900°C and -30-0Pa Sulphate roasting within the range of 1 ~ 5h, and then the dusty SO produced by roasting 2 After the flue gas is collected by the dust removal equipment, acid is produced to produce sulfuric acid as a by-product;

[0030] (b) water immersion, send the calcined sand produced by roasting and the dust collected by dust collection to the water immersion tank together for 0.2-4 hours in the temperature range of 40-95 °C;

[0031] (c) filtering, filtering the water leaching pulp, and then performing iron removal, concentrated crystallization, and centrifugat...

Embodiment 2

[0037] Embodiment two: refer to figure 1 , the method further comprises the following sequential process steps:

[0038] (a) Sulfation roasting, slurry copper concentrate with 28% sulfur content, 78%-0.074mm particle size, and 13% grade with water and stir evenly, and send it to the fluidized bed furnace at a temperature of 500-700°C and -20-0Pa Sulphate roasting within a certain range for 1 to 3 hours, and then the dust-containing SO produced by roasting 2 After the flue gas is collected by the dust removal equipment, acid is produced to produce sulfuric acid as a by-product;

[0039] (b) water immersion, the calcine produced by roasting and the dust collected by dust collection are sent to the water immersion tank together for 0.5-2.5 hours in the temperature range of 60-90 °C;

[0040] (c) filtering, filtering the water leaching pulp, and then performing iron removal, concentrated crystallization, and centrifugation on the filtered high-copper leachate to obtain the produ...

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Abstract

The invention relates to a method for directly preparing bluestone and cathode copper from copper concentrate. The method orderly comprises the following technological steps: sulphating roasting, water immersion, filtration, acid dipping, filtration washing, extraction, back extraction, electrodeposition and the circular utilization of local working procedures; and when products of bluestone and electrolytic copper with high purity are obtained, side products such as sulphuric acid, iron oxide red and waste residues are simultaneously generated. The method of the invention has the characteristics of low production cost, strong material adaptability, high working efficiency, low investment, simple operation, high utilization rate of copper, diversified products and easy industrialized production, etc., so that the method is suitable to exploit and apply low-grade copper ores.

Description

1. Technical field [0001] The invention relates to a method for directly producing copper sulfate and cathode copper from copper concentrate, which is suitable for mining low-grade copper ore. 2. Background technology [0002] There are three main ways to produce copper products using copper concentrate as raw material: [0003] The first method is pyrometallurgy to produce cathode copper and by-product copper sulfate, generally including roasting, smelting, blowing, refining and other processes, suitable for the application of copper concentrate with a grade of 20-30%, and this method has a large one-time investment , long process flow, high technical requirements, high energy consumption and waste gas pollution in the pyrolysis process, and with the large-scale mining of copper mines, there are fewer and fewer rich ores, which can meet the requirements of high-grade pyrometallurgy. There are fewer and fewer ore sources, which hinders the development of pyrometallurgy. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B15/00
Inventor 陈景河邹来昌梁春来罗吉束陈淑萍张建峰张毓芳
Owner ZIJIN MINING GROUP
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