Method used for producing alumina from fly ash

A technology of alumina and fly ash, applied in chemical instruments and methods, preparation of alkali metal aluminate/alumina/aluminum hydroxide, inorganic chemistry, etc., can solve the problem of difficult guarantee of alumina quality and consumption of bauxite resources , resource shortage and other issues, to achieve the effect of alleviating resource shortage, low energy consumption and high product quality

Inactive Publication Date: 2019-11-01
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] With the rapid development of my country's aluminum industry, a large amount of bauxite resources are consumed. At present, high-grade bauxite is scarce, and a large number of low-grade bauxite has been mined and used. However, the development of my country's aluminum industry still faces the problem of resource shortage. At this stage, the import of bauxite resources has exceeded 50%, and the import ratio is still expanding. my country's aluminum industry may face the problem of "stuck neck" at any time
At the same time, we produce a large amount of fly ash solid waste every year. The treatment of these fly ash solid wastes is also a problem that needs to be solved urgently. Therefore, using fly ash as an aluminum source and extracting the aluminum element for production can effectively solve the problem. For the above problems, there are currently some industrial methods for producing alumina from fly ash, but there are a series of problems to be solved in these methods, such as: for the alkali method, it is necessary to improve the technology to achieve solid waste reduction treatment; for the acid method Generally speaking, the cost of removing impurities in acidic solution is too high, and the quality of alumina is difficult to guarantee. To solve the above problems, a new method for producing alumina by using fly ash is needed

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Take the above AlCl 3 .6H 2 1 kg of O crystals was hydrolyzed at 300° C. for 2 hours under a water vapor atmosphere to obtain 205.0 grams of alumina-containing intermediate product with a chlorine content of 9.7%; the intermediate product was stripped out with 615 g of sodium aluminate solution, and in the sodium aluminate solution used: Al 2 o 3 130g / L, molecular ratio 3.40 (caustic Na in sodium aluminate solution 2 O and Al 2 o 3 The molar ratio is called the molecular ratio of the sodium aluminate solution, the same below), and the dissolution temperature is 90° C. to obtain the sodium aluminate solution. In the prepared sodium aluminate solution: Al2 o 3 267g / L, molecular ratio 1.65, after filtration, 10g of filter residue was obtained, 306g of aluminum hydroxide was obtained by decomposing by seed fraction, and calcined to obtain Al 2 o 3 200 g.

Embodiment 2

[0033] Take the above AlCl 3 .6H 2 2 kilograms of O crystals were hydrolyzed for 3 hours at 400° C. under a water vapor atmosphere to obtain 408 grams of an intermediate product containing alumina and a chlorine content of 6.2%; the intermediate product was stripped out with 3260 g of sodium aluminate solution, and in the sodium aluminate solution used: Al 2 o 3 135g / L, molecular ratio 3.40, dissolution temperature 80°C to obtain sodium aluminate solution, in the obtained sodium aluminate solution: Al 2 o 3 278g / L, molecular ratio 1.65, 18g of filter residue was obtained after filtration, 613g of aluminum hydroxide was obtained by decomposing by seed fraction, and Al was obtained by calcining 2 o 3 401 grams.

Embodiment 3

[0035] Take the above AlCl 3 .6H 2 5 kilograms of O crystals were hydrolyzed for 3 hours at 600° C. under a water vapor atmosphere to obtain 1020 grams of an intermediate product containing alumina and a chlorine content of 1.5%; the intermediate product was dissolved with 13250 g of sodium aluminate solution, and in the sodium aluminate solution used: Al 2 o 3 140g / L, molecular ratio 3.40, dissolution temperature 150°C to obtain sodium aluminate solution, in the obtained sodium aluminate solution: Al 2 o 3 288g / L, molecular ratio 1.65, after filtration, 45g of filter residue was obtained, and 1545g of aluminum hydroxide was obtained by decomposing by seed fraction, and calcined to obtain Al 2 o 3 1010 grams.

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PUM

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Abstract

The invention provides a method used for producing alumina from fly ash. The method comprises following steps: high aluminum fly ash is subjected to dissolving out with hydrochloric acid at a high temperature, obtained aluminium chloride dissolving out solution and white clay are separated, and evaporation is carried out to obtain impurity containing AlCl<3>*6H<2>O crystal; the impurity containingAlCl<3>*6H<2>O crystal is subjected to hydrolysis at water vapour atmosphere at a hydrolysis temperature is controlled to be 200 to 850 DEG C to obtain an amorphous substance taking alumina as the main component; the amorphous substance is subjected to dissolving out with an alkali solution at normal pressure at a dissolving out temperature of 70 to 100 DEG C, or is subjected to dissolving out with an alkali solution at an increased pressure at a dissolving out temperature of 100 to 300 DEG C, a slag phase is removed through filtering, and a sodium aluminate solution is obtained at last; thesodium aluminate solution is filtered, diluted, and cooled for seed precipitation to obtain aluminium hydroxide. The methd is capable of reducing production cost of alumina from fly ash effectively, improving alumina quality, realizing utilization of large amount of solid waste, alleviating the shortage problem of bauxite resource of our state, and is suitable for application popularization in industrial production.

Description

technical field [0001] The invention relates to the technical field of industrial alumina extraction, in particular to a new method for producing alumina by using fly ash. Background technique [0002] With the rapid development of my country's aluminum industry, a large amount of bauxite resources are consumed. At present, high-grade bauxite is scarce, and a large number of low-grade bauxite has been mined and used. However, the development of my country's aluminum industry still faces the problem of resource shortage. At this stage, the import of bauxite resources has exceeded 50%, and the import ratio is still expanding. my country's aluminum industry may face the problem of "stuck neck" at any time. At the same time, we produce a large amount of fly ash solid waste every year. The treatment of these fly ash solid wastes is also a problem that needs to be solved urgently. Therefore, using fly ash as an aluminum source and extracting the aluminum element for production can ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/22C01F7/14B09B3/00
CPCC01F7/14C01F7/22B09B3/00B09B3/40
Inventor 王兆文陶文举杨酉坚石忠宁高炳亮胡宪伟刘风国于江玉刘爱民潘晓林
Owner NORTHEASTERN UNIV
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