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Method for producing alumina by using high-alumina fly ash

A high-alumina fly ash and alumina technology, applied in the direction of alumina/aluminum hydroxide, can solve the problems of large slag phase flow in the ammonium sulfate sintering method, difficult industrial production of metallurgical-grade alumina, and low recovery rate, and achieve Reduce equipment cost and operation difficulty, good industrialization scalability, and save production cost

Active Publication Date: 2015-03-18
DATANG INT HIGH ALUMINA COAL R & D CENT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In recent years, various colleges and universities and research institutes in my country have actively carried out research on new processes for extracting alumina from high-alumina fly ash. Bayer method, limestone sintering-low temperature Bayer method, etc. Among them, the acid method is difficult to realize large-scale industrial production due to serious corrosion of equipment materials and high impurity content in the product, and it is difficult to produce metallurgical grade alumina. Ammonium sulfate sintering method has slag phase flow There are no industrial examples for the disadvantages of large size and difficulty in recycling ammonia gas. The limestone sintering method is similar to the soda-limestone sintering method, but the amount of slag is larger, the energy consumption is higher, and the recovery rate is slightly lower than that of the soda-limestone sintering method. The desiliconization-soda lime sintering method is currently the only process method that realizes industrial production and has achieved success. Patent CN201110117710 discloses the technical characteristics of this process
[0004] However, CN201110117710 adopts a lengthy one-stage and two-stage desiliconization process, which requires difficult-to-operate equipment such as high-pressure desiliconization tanks and deep desiliconization tanks, and the equipment costs are high and the operation is complicated.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] 1) Pre-desiliconization, after heating the mixed solution composed of high-aluminum fly ash and 20% sodium hydroxide solution (the mass ratio of sodium hydroxide to high-alumina fly ash is 0.5:1) to 110°C, Import into a pressure vessel for desiliconization reaction for 2 hours, and then carry out liquid-solid separation to obtain liquid-phase desiliconization liquid and solid-phase fly ash filter cake. The aluminum-silicon ratio in the fly ash filter cake is higher than that before the desilication reaction. High fly ash; the mass content of alumina in high aluminum fly ash is higher than 40%;

[0042] 2) Preparation of raw slurry: add fly ash filter cake to the slurry made of limestone and sodium carbonate to obtain mixed slurry, grind the mixed slurry in a ball mill and prepare raw slurry; before mixing quicklime and sodium carbonate, After grinding, the calcium ratio of the raw slurry is 2, the alkali ratio is 1, and the moisture content is 30wt%;

[0043] 3) Clinke...

Embodiment 2

[0055] 1) Pre-desilication, heating the mixed solution composed of high alumina fly ash and 10% sodium hydroxide solution (the mass ratio of sodium hydroxide solution to high alumina fly ash is 0.6:1) to 130°C , introduced into the insulation retention tank for desiliconization reaction for 2.5h, and then liquid-solid separation was carried out after the evaporator was decompressed to obtain the desiliconization liquid in the liquid phase and the desiliconization fly ash filter cake in the solid phase, wherein the aluminum of the original fly ash The silicon ratio is 1.15, which rises to 2.12 after desiliconization, and the SiO in the desiliconization solution 2 The concentration is 62g / l;

[0056] 2) Preparation of raw slurry, adding fly ash filter cake to a slurry made of limestone (quicklime) and sodium carbonate to obtain a mixed slurry, grinding the mixed slurry in a ball mill and blending into a raw slurry; limestone and sodium carbonate Grinding is required before mixi...

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Abstract

The invention provides a method for producing alumina by using high-alumina fly ash. The method comprises adopting the high-alumina fly ash to be reacted with a sodium hydroxide solution to conduct desilicication in advance to obtain coal ash filter cakes and desilicication liquid firstly; and adding the desilicication coal ash filter cakes in slurry of the limestone and sodium carbonate to mix to form raw material slurry, then roasting the raw material slurry to form ripe materials, considering a liquid phase dissolved from the ripe materials as sodium aluminate coarse liquid, conducting carbon separation on the obtained sodium aluminate coarse liquid, and then conducting Bayer process dissolving, dilution desilicication, kind separation and roasting. Tedious desilicication processes of a first section and a second section are removed, equipment, such as high-pressure desilicication groove and deep desilicication groove which are difficult to operate is reduced, equipment cost and operation difficulties are reduced, and high-purity alumina products can be obtained simultaneously.

Description

technical field [0001] The invention relates to a method for utilizing fly ash, in particular to a method for producing alumina from high-aluminum fly ash. Background technique [0002] Alumina is the main raw material for the production of aluminum ingots. More than 95% of the world's alumina is produced through bauxite. my country is the world's largest producer of alumina, and currently produces more than 30 million tons of alumina per year. But at the same time, my country's bauxite resources are relatively scarce, and bauxite reserves only account for about 7% of the world's total reserves, and most of them are difficult-to-handle diaspore mines. Due to insufficient bauxite resources, currently about 60% of bauxite mines are dependent on imports from abroad. [0003] However, the reserves of high-aluminum fly ash produced by coal power generation in central and western Inner Mongolia and northern Shanxi in my country are abundant. The potential reserves of high-alumin...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/02
Inventor 张生苏杰孙俊民公彦兵
Owner DATANG INT HIGH ALUMINA COAL R & D CENT