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Method for reinforcing leaching of bornite through high-iron sphalerite

A technology of sphalerite and bornite, applied in the direction of improving process efficiency, etc., can solve the problems of long leaching cycle, slow microbial growth, slow leaching rate, etc., achieve shortening leaching cycle, less process flow, and shorten lag period Effect

Active Publication Date: 2018-12-18
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with the acidic leaching system, the alkaline leaching system has some disadvantages: 1. The reagent for alkaline leaching is ammonia water. In order to reduce the volatility of ammonia water, it needs to be mixed with ammonium salt as the leaching agent during the leaching process, which increases the cost of leaching.
3. When the copper ore is leached in the alkaline leaching system, other metal elements in the mineral, such as iron, will be converted into insoluble oxygen or hydroxyl compounds and filtered out, resulting in a certain waste of resources
4. Under the conditions of oxygen as oxidant, low temperature and alkaline leaching, the oxidative leaching rate of copper ore is relatively slow, so alkaline leaching is often carried out at high temperature and high pressure. On the one hand, high temperature and high pressure conditions have higher requirements on leaching equipment, so the acid leaching system is easier to promote and apply
[0005] At present, acidophilic microorganisms are used to leaching bornite, which can promote the leaching of bornite to a certain extent, but there are still problems such as slow leaching rate, low leaching rate, long leaching period (several months), high acid consumption, Problems such as slower growth of microorganisms in it
[0006] The current status of the existing wet leaching bornite is: when the leaching time is short, the leaching rate is low; and when the leaching rate is high, the leaching time is too long, so how to shorten the leaching cycle and realize efficient leaching of bornite , become the current technical problem

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The high-iron sphalerite and bornite are ground separately to -0.074mm, and the ore powder content of this particle size reaches more than 85%. The ferric sphalerite powder and bornite powder were intermittently sterilized, and the sterilized ferric sphalerite powder and bornite powder were mixed in a mixing ratio of 3:1, and then sterilized The 9K basal medium of the bacteria is obtained to obtain the ore pulp, and by regulating the chemical conditions of the leaching solution, 0.1-0.5mol / L H 2 SO 4 Adjust the pH of the pulp to 1.5-2.0, then stir and leaching the mixed pulp, the leaching temperature is 30°C, the stirring speed is 100-300rpm, the leaching potential is 180-610mV, leaching for 15 days, measure and calculate the leaching of copper Compared with the single leaching of bornite in the prior art, the leaching rate has increased by 3.9%.

Embodiment 2

[0030] The high-iron sphalerite and bornite are ground separately to -0.074mm, and the ore powder content of this particle size reaches more than 85%. Intermittently sterilize the sphalerite powder and bornite powder, mix the sterilized sphalerite powder and bornite powder in a mixing ratio of 1:1, and then add the sterilized The 9K basal medium of the bacteria is obtained to obtain the ore pulp, and by regulating the chemical conditions of the leaching solution, 0.1-0.5mol / L H 2 SO 4 Adjust the pH of the pulp to 1.5-2.0, then stir and leaching the mixed pulp, the leaching temperature is 30°C, the stirring speed is 100-300rpm, the leaching potential is 180-610mV, leaching for 15 days, measure and calculate the leaching of copper Compared with the single leaching bornite in the prior art, the leaching rate has increased by 2.5%.

Embodiment 3

[0032] The high-iron sphalerite and bornite are ground separately to -0.074mm, and the ore powder content of this particle size reaches more than 85%. The ferric sphalerite powder and bornite powder are intermittently sterilized, and the sterilized ferric sphalerite powder and bornite powder are mixed in a mixing ratio of 1:3, and then sterilized The 9K basal medium of the bacteria is obtained to obtain the ore pulp, and by regulating the chemical conditions of the leaching solution, 0.1-0.5mol / L H 2 SO 4 Adjust the pH of the pulp to 1.5-2.0, then stir and leaching the mixed pulp, the leaching temperature is 30°C, the stirring speed is 100-300rpm, the leaching potential is 180-610mV, leaching for 15 days, measure and calculate the leaching of copper Compared with the existing technology for leaching bornite alone, the leaching rate has increased by 1.8%.

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PUM

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Abstract

The invention provides a method for reinforcing leaching of bornite through high-iron sphalerite. The method includes the following steps that the high-iron sphalerite and the bornite are ground, andhigh-iron sphalerite powder and bornite powder are obtained; a 9K basic culture medium is subjected to high-temperature high-pressure steam sterilization, and the high-iron sphalerite powder and the bornite powder are intermittently sterilized; the sterilized high-iron sphalerite powder and the sterilized bornite powder are mixed, then the sterilized 9K basic culture medium is added, ore pulp is obtained, and then the pH value of the ore pulp is adjusted to 1.5-2.0; and the ore pulp is subjected to agitation leaching, and chemical conditions of a leaching solution are adjusted and controlled.The whole leaching period is shortened, meanwhile, the leaching rate and the leaching speed are greatly increased, and the method is clean and environmentally friendly, low in cost and suitable for large-scale application and popularization.

Description

technical field [0001] The invention relates to the fields of hydrometallurgy and mineral processing, in particular to a method for strengthening bornite leaching by using ferric sphalerite. Background technique [0002] Copper is an indispensable non-ferrous metal in human production and life. Copper smelting technology is mainly divided into pyrometallurgy and hydrometallurgy. Pyro-smelting requires a higher copper grade, and a large amount of sulfur dioxide fumes will be produced during the smelting process, causing environmental pollution; pyro-smelting consumes a lot of energy; pyro-smelting will make the iron in the copper concentrate adhere to the slag In the process, a large amount of solid waste is produced, which to a certain extent causes the waste of iron resources and environmental pollution. As the world's largest copper consumer, my country has a huge demand for copper. However, there are few 10,000-ton-level copper mines in my country, and the copper grade ...

Claims

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Application Information

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IPC IPC(8): C22B3/18C22B15/00
CPCC22B3/18C22B15/0065Y02P10/20
Inventor 赵红波张艳军张伊升
Owner CENT SOUTH UNIV
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