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A method for preparing aluminum-silicon alloy by mixing aluminum-containing minerals and fly ash by chlorination and low-temperature electrolysis

An aluminum-silicon alloy and fly ash technology, applied in the field of electrochemical metallurgy, can solve the problems of high production cost, complex process flow, large energy consumption, etc., and achieve the effects of reducing moisture absorption and other processes, improving reaction efficiency, and improving current efficiency.

Active Publication Date: 2015-09-30
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, fly ash is an aluminum-containing silicate calcined at high temperature. There are two obvious defects in the preparation of anhydrous aluminum chloride by chlorination of fly ash as raw material: first, the crystal phase of aluminum, silicon and other substances is relatively stable, and the chlorination temperature is relatively stable. It is 50-100°C higher than industrial alumina or bauxite, that is, fly ash can be chlorinated better at 800-900°C. At this time, calcium and magnesium chloride produced in the system are in a molten state, which directly leads to the bonding of reaction materials. , fluidized bed loss; secondly, the alumina content in fly ash is 20-35% lower, and the silicon oxide content is 40-56% higher. The material flow in the chlorination process aimed at producing anhydrous aluminum chloride is larger, and the process Longer and costs significantly more
However, this method has high requirements on the taste of aluminum ore resources, the process is very complicated, energy consumption is large, and production costs are high. These factors have restricted the development of my country's aluminum industry to a certain extent.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] After crushing bauxite and fly ash into powders, sieving, select 160-200 mesh raw material particles, and mix them in a mass ratio of 1:9; add 20% mass fraction of 140-180 mesh calcined to the mixed raw materials Petroleum coke, the mixture is added to the boiling chlorination furnace, Cl 2 Carbothermal boiling chlorination is carried out in an atmosphere, the gas flow rate is 0.0015m / s, and the chlorination temperature is 650°C. The chlorinated product is filtered and purified and quickly condensed and collected. The gaseous product is cooled at a cooling temperature of 10°C. The mixed chlorinated product is dissolved in BmimCl (1-butyl-3-methylimidazole chloride) ionic liquid to obtain a clear and transparent electrolysis liquid. The mass fraction of aluminum chloride in the chlorination product is 65%, the mass fraction of ferric chloride is 28%, the mass fraction of silicon chloride is 5%, the total content of calcium chloride and magnesium chloride is 2%, the total ...

Embodiment 2

[0021] After crushing coal gangue and fly ash into powder, sieving, select raw material particles of 140-180 mesh, and mix according to the mass ratio of 2:8, and add 25% mass fraction of 120-160 mesh calcined petroleum into the mixed raw material Coke, the mixture is added to the boiling chlorination furnace, in the COCl 2 Carbothermal boiling chlorination is carried out in an atmosphere, the gas flow rate is 0.0018m / s, and the chlorination temperature is 700°C. The chlorinated product is filtered and purified and quickly condensed and collected. The cooling temperature of the gaseous product is 20°C. The mixed chlorinated product is dissolved in N-butylpyridinium bromide ionic liquid to obtain a clear and transparent electrolyte. The mass fraction of aluminum chloride in the chlorination product is 72%, the mass fraction of ferric chloride is 23%, the mass fraction of silicon chloride is 7%, and the ratio of the total amount of chloride to the amount of ionic liquid is 1.3. ...

Embodiment 3

[0023] After the kaolinite and fly ash are crushed into powder, they are sieved to select the raw material particles of 160-200 mesh and mix them in a mass ratio of 3:7. Add 30% mass fraction of 140-180 mesh calcined petroleum to the mixed raw materials Coke, the mixture is added to the boiling chlorination furnace, in the Cl 2 And COCl 2 Carbothermal boiling chlorination is carried out under a mixed atmosphere of, the gas flow rate is 0.002m / s, and the chlorination temperature is 750°C. The chlorinated product is filtered and purified and quickly condensed and collected. The cooling temperature of the gaseous product is 30°C. The mixed chlorinated product is dissolved in N-methyl, butylpyrrolidine bistrifluoromethanesulfonimide salt ionic liquid to obtain clarification Transparent electrolyte. The mass fraction of aluminum chloride in the chlorination product is 78%, the mass fraction of silicon chloride is 8%, the total content of calcium and magnesium chloride is 2%, and the...

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PUM

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Abstract

The invention provides a method for preparing aluminum silicon alloy through mixed chlorination and low-temperature electrolysis of aluminum-containing mineral and fly ash. According to the method, a mixture of bauxite and fly ash with different reaction activities is used as a raw material, the catalytic effect of a chlorination product of the bauxite on the chlorination process of the fly ash enables that the chlorination temperature of the fly ash is reduced, the reaction can be continuously performed in a fluidized state, and the reaction efficiency is improved. Meanwhile, since the aluminum-containing mineral and the fly ash have different chemical compositions, the adjustment and control on the composition of the chlorination product can be realized by adjusting the proportion of the mixed materials, the processes such as moisture absorption can be effectively reduced, and the cost is saved. The method can be used for realizing effective separation of iron impurity in the chlorination product in low-temperature ironic liquid, and meanwhile also obtaining an elementary substance iron byproduct. Electrolysis is performed in the ionic liquid within the temperature range of 40-100 DEG C to prepare aluminum silicon alloy with certain composition after purification, so that the heat loss is obviously reduced and the current efficiency is improved.

Description

Technical field [0001] The invention relates to a method for preparing aluminum-silicon alloy by mixed chlorination of aluminum-containing minerals and fly ash and low-temperature electrolysis, and belongs to the technical field of electrochemical metallurgy. Background technique [0002] Anhydrous aluminum trichloride is currently mainly used as a catalyst for organic synthesis, and the market demand is not large. Therefore, most anhydrous aluminum trichloride manufacturers use metallic aluminum as raw materials to preheat the processed high-purity aluminum After that, it is added into a closed chlorination reaction furnace, and chlorine gas reacts with metallic aluminum at 800-900°C to produce anhydrous aluminum trichloride. It is precisely because this method uses high-purity aluminum as the raw material to produce anhydrous aluminum chloride at a relatively high cost, which greatly limits the application of anhydrous aluminum chloride. The proposal of ionic liquid system low...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C1/24C22B7/00C22B21/00
CPCY02P10/20
Inventor 张军玲陈仕谋何宏艳高洁康艳红石朝辉郎海燕张锁江
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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