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Dealkalization method of fly ash Al-extraction residues

A technology for extracting aluminum from fly ash and extracting aluminum residues is applied in sustainable waste treatment, solid waste management, cement production, etc. The effect of synergistic utilization and simple process method

Inactive Publication Date: 2012-02-15
INNER MONGOLIA DATANG INT RENEWABLE RESOURCES DEV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the treatment methods of the above two patents are relatively simple and the cost is relatively low, after the two methods are processed, the R in the red mud of the former 2 O (R stands for alkali metal elements, mainly Na and K) content is still as high as 0.9-1.1%, the latter is higher, which cannot meet the technical requirements of the building materials industry for alkali content
[0006] Although the chemical properties and composition of the aluminum extraction residue from fly ash soda-lime sintering are similar to those of red mud, its phase composition and the occurrence state of alkali metal elements are still quite different from those of pure red mud. There should also be some differences in the alkali mechanism and process methods. At present, there is no report on the dealkalization of similar aluminum extraction residues.

Method used

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  • Dealkalization method of fly ash Al-extraction residues
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Examples

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Effect test

Embodiment 1

[0026] figure 1 It is a flow chart of the dealkalization method for the aluminum extraction residue from fly ash provided in Example 1 of the present invention. As shown in the figure, the step of the dealkalization method of the fly ash aluminum extraction residue is: first, the aluminum extraction residue (wherein the mass percentage content of sodium oxide is 2.0%, and the mass percentage content of water is 35%) through three times of washing is extracted. The main phase in the aluminum residue is C2S (dicalcium silicate), which accounts for 70-80% of the entire aluminum extraction residue. Scanning electron microscopy studies have shown that most of the non-free Na in the aluminum extraction residue 2 O to Na 2 O CaO SiO 3 (Basic calcium silicate) in the form of occurrence, which is the difference in the occurrence of alkali metal elements in aluminum extraction residues and red mud. In addition, it contains 5-10% 3CaO·Al 2 o 3 ·6H 2 O nSiO 2 (Garnet Hydrate), 1-2%...

Embodiment 2

[0031] The steps of the dealkalization method of the fly ash aluminum extraction residue provided by embodiment two are: first, the aluminum extraction residue (wherein the mass percentage content of sodium oxide is 1.4%, water The mass percentage content is 45%), and new water is added according to the mass ratio of water to aluminum extraction residue on a dry basis of 1.5, and the mixture is evenly stirred to obtain an aluminum extraction residue slurry. Then, under the condition of stirring, slowly add calcium carbide slag to the aluminum extraction residue slurry to carry out dealkalization reaction. Calculated on the dry basis of the aluminum extraction residue, the mass ratio of the dry basis of the aluminum extraction residue to the calcium carbide slag is 12:1, and the reaction temperature is 85°C. , The reaction time is 0.5h. Finally, filter the aluminum extraction residue slurry after the above dealkalization reaction, and wash once with new water to obtain the deal...

Embodiment 3

[0036] The steps of the dealkalization method of the fly ash aluminum extraction residue provided in Example 3 are as follows: first, the aluminum extraction residue of the fly ash soda-lime sintering method washed three times (wherein the mass percentage content of sodium oxide is 1.73%), according to The mass ratio of the water to the aluminum extraction residue on a dry basis is 2.0, adding fresh water and stirring evenly to prepare the aluminum extraction residue slurry. Then, under the condition of stirring, slowly add calcium carbide slag to the aluminum extraction residue slurry to carry out dealkalization reaction. Calculated on the dry basis of the aluminum extraction residue, the mass ratio of the dry basis of the aluminum extraction residue to the calcium carbide slag is 10:1, and the reaction temperature is 90°C. , The reaction time is 0.5h. Finally, filter the aluminum extraction residue slurry after the above dealkalization reaction, and wash once with new water ...

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Abstract

The invention discloses a dealkalization method of fly ash Al-extraction residues, comprising the following steps of: (1) adding water into the Al-extraction residues with stirring to prepare an Al-extraction residue slurry; (2) slowly adding calcium carbide slag into the Al-extraction residue slurry with stirring for a dealkalization reaction; (3) filtering the Al-extraction residue slurry which has undergone the dealkalization reaction, followed by washing to obtain the dealkalized Al-extraction residues. The invention is suitable for dealkalization of the Al-extraction residues by the fly ash alkali lime sintering method. After the dealkalization processing, the content of sodium oxide in the Al-extraction residues by the fly ash alkali lime sintering method is reduced from 1.3-2.0% to 0.4-0.6%, which can satisfy the requirement of mixing material addition material and cement clinker raw materials on the alkali content in the building material industry. The method provided by the invention has advantages of simple process, low energy consumption, less material consumption amount and low treatment cost, and is suitable for industrial popularization.

Description

technical field [0001] The invention relates to a comprehensive utilization technology of industrial solid waste, in particular to a dealkalization method of fly ash aluminum extraction residue Background technique [0002] With the increasing shortage of bauxite resources in our country, the use of fly ash, coal gangue and other industrial solid wastes to extract alumina has attracted more and more attention. For example, the Late Paleozoic coal seams and gangue in the Ordos Basin are rich in boehmite and kaolinite and other minerals, and the alumina content in the fly ash produced after combustion is as high as about 50%, which is comparable to that in medium-grade bauxite. The content is equivalent, and it is a very valuable raw material for alumina production. According to statistics, the potential reserves of high-aluminum fly ash in the central and western regions of Inner Mongolia are as high as 15 billion tons. With the increasing shortage of bauxite resources in o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B18/08C04B7/28
CPCY02P40/10Y02W30/91
Inventor 孙俊民陈刚张战军张晓云武利成张靖峰张先奇高峰
Owner INNER MONGOLIA DATANG INT RENEWABLE RESOURCES DEV
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