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Harmless treatment method for aluminum ash

A technology for harmless treatment of aluminum ash, applied in chemical instruments and methods, inorganic chemistry, aluminum compounds, etc., can solve problems such as incompleteness, slow reaction speed, catalyst residue, etc., to improve the safety factor, the method is simple, and the guarantee safe effect

Inactive Publication Date: 2020-01-24
湖南绿脉环保科技股份有限公司
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, none of the above-mentioned wet treatment processes for producing water purifiers mentions the problem that aluminum ash releases flammable and explosive hydrogen and ammonia when it encounters acid, and the ammonium chloride residue produced by the neutralization of ammonia and acid will cause water purifiers to The ammonia nitrogen in it is unqualified, the reaction equation is: 2Al+6HCl→2AlCl 3 +3H 2 ↑, AlN+3H 2 O→Al(OH) 3 +NH 3 ↑, NH 3 +HCl→NH 4 Cl
[0007] CN105271327A discloses a method for harmless treatment and recycling of aluminum ash, and discloses a method for deammonization by water immersion. However, since the product formed by the hydrolysis of aluminum nitride on the surface of aluminum ash particles is aluminum hydroxide, the aluminum ash particles The tight package prevents the continuous penetration of water, which leads to a very long hydrolysis process of aluminum ash under natural conditions. Aluminum hydroxide is an amphoteric compound. Therefore, there is a problem of slow reaction speed in deamination by water immersion. Aluminum oxide is dissolved to accelerate the decomposition of aluminum nitride
[0008] CN105347361A discloses a treatment method for comprehensive utilization of aluminum ash, which uses a catalyst that can accelerate deamination, but there will be catalyst residues in the regenerated product, and it is necessary to increase the washing process
Although the hydrolysis reaction of aluminum nitride can be accelerated in the initial stage, because the inclusions produced by hydrolysis will prevent the penetration of water, the reaction rate will decrease in the later stage, and aluminum nitride still cannot be completely decomposed.
[0010] CN108893615A discloses a method for recovering metal aluminum from aluminum ash, which is to use a ball mill to add water and wet mill to carry out deep aluminum extraction. However, it has not been noticed that wet milling will produce flammable and explosive ammonia and hydrogen (hydrogen explosion limit is 4.0-75.6%, ammonia 15.7-27.4%), and issues derived from gas collection and gas treatment
However, there are also the problems of long and incomplete deamination time

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] (1) Mix 310kg of aluminum ash 1 and 300kg of water, stir the slurry at 85℃ for 100min, and then at 50℃, settle and classify for 80min, to obtain fine particle slurry with ≤325 mesh and elemental aluminum content ≤1% ( 230kg on dry basis);

[0052] (2) In step (1), the fine particle slurry (230kg on dry basis) with 325 meshes or less and elemental aluminum content ≤1% is added, and a mixture of 2kg ferric chloride and 7kg 10% ammonia water by mass concentration is added. , After 0.2h of leaching reaction, a non-metallic slurry is obtained;

[0053] (3) Put the non-metal slurry obtained in step (2) in a MQY1245 closed ball mill at a temperature of 50°C and a rotation speed of 30r / min for a stage of ball milling for 2h, until the total concentration of ammonia and hydrogen in the released gas is less than 10ppm , The deaminated slurry is washed (the volume ratio of deaminated slurry to washing water is 1:1), filtered, washed (the volume ratio of deaminated slurry to washing wa...

Embodiment 2

[0059] (1) Use a high-frequency vibrating sieve with 350kg aluminum ash 2 at 20°C and a vibration frequency of 4000r / min, sieving and grading for 20min to obtain fine particles ≤325 mesh and elemental aluminum content ≤0.8% (290kg on a dry basis). The weight of coarse particles >325 mesh is 60kg, and the aluminum content is 70%;

[0060] Mix fine particles ≤325 mesh and elemental aluminum content ≤0.8% (290kg on a dry basis) with 700kg of water, and stir the slurry at 60°C for 40 minutes to obtain a fine particle slurry of 325 mesh and elemental aluminum content ≤0.8% (290kg on dry basis);

[0061] (2) In step (1) the fine particle slurry (290kg on dry basis) with 325 mesh ≤325 mesh and elemental aluminum content ≤0.8% is added, and a mixture of 3kg copper sulfate and 3kg 15% ammonia water by mass concentration is added. After 0.5h of leaching reaction, a non-metallic slurry is obtained;

[0062] (3) The non-metallic slurry obtained in step (2) is subjected to two-stage ball mill d...

Embodiment 3

[0068] (1) Mix 130kg of aluminum ash 3 with 200kg of water, stir the slurry at 35°C for 20min, then at 45°C, swirl classification for 90min, obtain fine particle slurry with ≤325 mesh and elemental aluminum content ≤0.5% (110kg on dry basis);

[0069] (2) In step (1), the fine particle slurry (110kg on dry basis) with 325 mesh ≤325 mesh and elemental aluminum content ≤0.5% is added, and a mixture of 3kg ferric nitrate and 1kg mass concentration 20% ammonia water is added. After 1h of leaching reaction, a non-metallic slurry is obtained;

[0070] (3) The non-metallic slurry obtained in step (2) is subjected to two-stage ball mill deamination in an MQY1245 closed ball mill. The first stage of ball mill deamination is carried out at a temperature of 45°C and a rotation speed of 22r / min for 1.5h. The slurry after ball milling was subjected to swirl classification at 30°C for 40 minutes, and the fine particle slurry with ≤325 mesh was subjected to the second stage of ball milling to re...

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PUM

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Abstract

A harmless treatment method for aluminum ash comprises the following steps: (1) mixing the aluminum ash with water, performing stirring to form a slurry, and grading the slurry to obtain a fine particle slurry; or mixing the graded aluminum ash with water, and performing stirring for forming a slurry to obtain the fine particle slurry; (2) adding a leaching agent, and carrying out a leaching reaction to obtain a nonmetal slurry; and (3) carrying out ball-milling deamination on the oxidized slurry, and washing, filtering, washing and drying the deaminated slurry to obtain harmless aluminum ash.The method has the advantages of high safety coefficient in the production process, simplicity, low cost, and suitableness for industrial production; and the obtained harmless aluminum contains, by mass, 95% of Al2O3, 0.02% or below of aluminum nitride, 0.01% or less of metallic aluminum and 0.2% or less of salt, meets the bauxite ore standard of GB / T 24483-2009, and can be used as a raw materialof a water purifying agent, ceramic, glass, a refractory material, a building material or electrolytic aluminum.

Description

Technical field [0001] The invention relates to a method for treating aluminum ash, in particular to a method for harmless treatment of aluminum ash. Background technique [0002] Aluminum ash is the product of cooling and processing of smelting slag produced in the production process of electrolytic aluminum or aluminum casting. It contains aluminum and a variety of valuable elements, mainly composed of metal aluminum, aluminum nitride, aluminum oxide, other metal oxides and salt fluxes. For example, the composition of 6 series alloy aluminum ash of a certain aluminum factory is: Al 2 O 3 54.71%, AlN 20%, MgO 6.21%, Fe 2 O 3 2.67%, KCl 3.69%, NaCl 4.28%, SiO 2 6.64%, CaO 1.8%. [0003] The high content of metallic aluminum and alumina in aluminum ash is a valuable renewable resource, while the deliquescent of metallic aluminum and aluminum nitride in aluminum ash will produce and release hydrogen and ammonia gas, which is a malodorous The gas is flammable and explosive, and th...

Claims

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Application Information

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IPC IPC(8): C01F7/06C22B7/04C22B21/00
CPCC01F7/0693C01P2006/80C22B7/008C22B7/04C22B21/0023Y02P10/20
Inventor 陈湘清唐剑陈小松陈黎军彭助贵
Owner 湖南绿脉环保科技股份有限公司
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