Iron removal method of high-iron gibbsite bauxite

A gibbsite type, bauxite technology, applied in chemical instruments and methods, aluminate/alumina/aluminum hydroxide purification, alkali metal aluminate/alumina/aluminum hydroxide preparation, etc. Solve the problems of general beneficiation effect, high equipment specification requirements, high environmental protection pressure, etc., to achieve better magnetic separation effect, strong selectivity, and reduce alkali consumption.

Inactive Publication Date: 2021-01-08
GUIZHOU BRANCH CHINA ALUMINUM IND
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  • Summary
  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After the alumina is extracted from gibbsite ore, the iron-containing minerals enter the red mud and become a kind of industrial waste. Due to the influence of the alkali content in the red mud, the iron in it is difficult to recycle and has to be discharged together with the red mud. Environmental pollution and waste of resources
Chinese patent CN102583477B introduces a technical route of first extracting alumina from bauxite, and then smelting the dissolved red mud to extract iron. This technology still has the problems of high energy consumption and separation of iron and alkali in the ignition method.
Chinese patent CN102515223B uses hydrochloric acid to react with high-iron bauxite in a pressurized reactor to obtain aluminum chloride and ferric chloride solution and high-silicon slag; adding excess sodium hydroxide lye can obtain sodium aluminate solution and high-iron slag, Chlorine gas, hydrogen gas, sodium hydroxide solution and pure sodium aluminate solution are obtained by electrolysis; sodium aluminate solution can be used to produce metallurgical grade alumina. This technology has problems such as long process, high equipment specification requirements, and high environmental pressure.
Chinese patent CN101417260B has introduced a kind of bauxite flotation technology, after grinding bauxite finely, iron and aluminum minerals are separated by combined magnetic separation and flotation; "Experimental Research" and "Study on Raw Ore Slurry Iron Separation Technology of Pingguo Bauxite" also introduced the related technologies of magnetic separation and flotation to treat high-iron bauxite; in this kind of technology, it is difficult to remove iron, Embedded distribution and inclusion of aluminum minerals, general beneficiation effect, high magnetic component iron oxide content is not high
The biggest problem in the technology of selecting iron from red mud is that it is difficult to completely separate iron and alkali, which affects the effective utilization of the selected high-iron components

Method used

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  • Iron removal method of high-iron gibbsite bauxite

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] The high iron gibbsite type bauxite raw ore is crushed and ground to obtain a ground ore, and the mass percentage of the ore particles on the sieve after the ground ore passes through a sieve with an aperture of 150 μm is 20%. The mass percentage of the undersized ore particles after 250 μm sieve is 99%. The ground ore and water are mixed into an ore slurry with a solid content of 300g / L, and the ore slurry is put into a pressure reactor for hydrothermal reaction. The reaction temperature is 250°C and the reaction time is 30min. After the reaction, a mixed slurry is obtained. After the reaction is completed, the material is discharged. Adjust the mixed slurry to a slurry with a solid content of 200g / L for magnetic separation. The magnetic field strength of the magnetic separation is 15000GS. After magnetic separation, a strong magnetic component solid with a high iron oxide content and a gibbsite type with a low iron oxide content are obtained Bauxite slurry; strong ma...

Embodiment 2

[0028] The raw ore of high-iron gibbsite bauxite is crushed and ground to obtain ground ore, and the mass percentage of ore particles on the sieve after the ground ore passes through a sieve with an aperture of 150 μm is 5%. The mass percentage of the undersized ore particles after 250 μm sieve is 100%. The ground ore and water are mixed into an ore slurry with a solid content of 50g / L, and the ore slurry is put into a pressure reactor for hydrothermal reaction. The reaction temperature is 200°C and the reaction time is 180min. After the reaction, a mixed slurry is obtained. After the reaction is completed, the material is discharged. Adjust the mixed slurry to a slurry with a solid content of 50g / L for magnetic separation. The magnetic field strength of the magnetic separation is 6000GS. After magnetic separation, a strong magnetic component solid with a high iron oxide content and a gibbsite type with a low iron oxide content are obtained Bauxite slurry; strong magnetic com...

Embodiment 3

[0030] The high iron gibbsite type bauxite raw ore is crushed and ground to obtain the ground ore. The mass percentage of the ore particles on the sieve after the ground ore passes through a sieve with an aperture of 150 μm is 10%. The mass percentage of the undersized ore particles sieved to 250 μm is 99.5%. The ground ore and water are mixed into an ore slurry with a solid content of 150g / L, and the ore slurry is put into a pressure reactor for hydrothermal reaction. The reaction temperature is 230°C and the reaction time is 60min. After the reaction, a mixed slurry is obtained. After the reaction is completed, the material is discharged. Adjust the mixed slurry to a slurry with a solid content of 100g / L for magnetic separation. The magnetic field strength of the magnetic separation is 9000GS. After magnetic separation, the strong magnetic component solid with high iron oxide content and the gibbsite type with low iron oxide content are obtained Bauxite slurry; strong magne...

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Abstract

The invention discloses an iron removal method of high-iron gibbsite bauxite, which comprises the following steps of crushing and grinding high-iron gibbsite bauxite raw ore to obtain ground ore, wherein the mass percentage content of oversize ore particles obtained after the levigated ore passes through a sieve with the pore diameter of 150 microns is 5%-20%, and the mass percentage content of undersize ore particles obtained after the levigated ore passes through a sieve with the pore diameter of 250 microns is 99%-100%, preparing ore slurry from the levigated ore and water, and carrying outhydrothermal reaction to obtain mixed slurry, carrying out magnetic separation on the mixed slurry to obtain strong magnetic component solids with high iron oxide content and gibbsite bauxite slurrywith low iron oxide content, and carrying out solid-liquid separation on the gibbsite bauxite slurry with low iron oxide content, and enabling the obtained solid to enter an aluminum oxide productionprocess. According to the method, iron-containing minerals are separated out before bauxite enters the aluminum oxide production process, so that environmental protection is facilitated, and the aluminum oxide production cost is reduced.

Description

technical field [0001] The invention belongs to the field of alumina metallurgy, in particular to a method for removing iron from high-iron gibbsite type bauxite. Background technique [0002] Worldwide, gibbsite-type bauxite is the main raw material for alumina production. Usually, the impurity minerals with the highest content in gibbsite ore are iron-containing minerals. After the alumina is extracted from gibbsite ore, the iron-containing minerals enter the red mud and become a kind of industrial waste. Due to the influence of the alkali content in the red mud, the iron in it is difficult to recycle and has to be discharged together with the red mud. Bringing environmental pollution and waste of resources. Therefore, along with the development of alumina industry, the selection of iron from bauxite and iron from red mud has always been a research hotspot. [0003] The main difficulty in iron selection in bauxite is how to break the inclusion and intercalation relations...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/06C01F7/46
CPCC01F7/0613C01F7/46
Inventor 杨会宾李亚广康少杰
Owner GUIZHOU BRANCH CHINA ALUMINUM IND
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