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Method for preparing silicon dioxide and aluminum oxide from coal ash

A silica and fly ash technology, applied in the direction of silica, silica, alumina/aluminum hydroxide, etc., can solve the problem of unsatisfactory solid raw material uniformity, high metal ion content of sodium silicate liquid, equipment and Operators have high requirements to achieve the effect of high added value of products, reducing production costs and simplifying the impurity removal process

Active Publication Date: 2012-11-21
CHINACOAL PINGSHUO GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional process characterizes the chemical composition of fly coal, and extracts Al in fly ash by strong acid or strong alkali 2 o 3 or SiO 2 , the process is limited by the chemical composition of fly ash, so it cannot be popularized, and at the same time, it will cause secondary pollution
CN101049935A discloses desiliconization with high-concentration NaOH liquid alkali-soluble fly ash, and desiliconization fly ash prepares CaO and CaCO 3 The method of preparing alumina by Bayer roasting, the high-concentration NaOH solution of this method is highly corrosive, and has high requirements for equipment and operators. The desiliconization rate of the normal temperature and pressure reaction system is low, and the prepared sodium silicate solution has a high metal ion content. , the impurity removal process increases the production cost, and at the same time the desilication fly ash is prepared into CaO and CaCO 3 When the uniformity of solid raw materials cannot be satisfied, the high alkali content of desiliconized fume not only increases the cost of dekalization but also causes waste of caustic alkali

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0028] Put a certain proportion of fly ash, sodium carbonate, calcium oxide and water into a closed reaction vessel, wherein 500g of fly ash, the molar ratio of sodium carbonate and calcium oxide is 3, the mass ratio of fly ash and calcium oxide is 2, the liquid The solid ratio is 4. After 30 minutes of alkali dissolution at 180°C and 0.9MPa pressure, filter and separate the sodium silicate liquid, desiliconized fly ash and calcium carbonate solid mixture, wash the solid mixture, and dry the desiliconized ash;

[0029] Sodium silicate solution into CO 2 Carbon content, prepared silica, partially desiliconized fly ash and calcium carbonate solid mixture, cement, foaming agent and water to prepare foamed concrete.

[0030] Partially desiliconized fly ash and calcium carbonate solid mixture is prepared by soda lime sintering method to prepare alumina, and the waste residue after preparing alumina by soda lime sintering method is used to prepare cement.

Embodiment approach 2

[0032] Put a certain proportion of fly ash, sodium carbonate, calcium oxide and water into a closed reaction vessel, wherein 500g of fly ash, the molar ratio of sodium carbonate and calcium oxide is 3, the mass ratio of fly ash and calcium oxide is 2, the liquid The solid ratio is 4. After 30 minutes of alkali dissolution at 240°C and 1.2MPa pressure, filter and separate the sodium silicate liquid, desiliconized fly ash and calcium carbonate solid mixture, wash the solid mixture, and dry the desiliconized ash;

[0033] Sodium silicate solution into CO 2 Carbon is prepared to obtain silica, and the mixture of desiliconized fly ash and calcium carbonate solid is prepared by soda lime sintering method to prepare alumina, and the waste residue after preparing alumina by soda lime sintering method is used to prepare foamed concrete blocks.

Embodiment approach 3

[0035] Put a certain proportion of fly ash, sodium carbonate, calcium oxide and water into a closed reaction vessel, wherein 500g of fly ash, the molar ratio of sodium carbonate and calcium oxide is 1, the mass ratio of fly ash and calcium oxide is 4, the liquid The solid ratio is 6, and at 300°C and 7.2MPa pressure, after 50 minutes of alkali dissolution, filter and separate the sodium silicate liquid, desiliconized fly ash and calcium carbonate solid mixture, wash the solid mixture, and dry the desiliconized ash;

[0036] Sodium silicate solution into CO 2 Carbon content, prepared silica, desiliconized fly ash and calcium carbonate solid mixture prepared by soda lime sintering method to prepare alumina, and the waste residue after preparing alumina by soda lime sintering method was used for purification of coal-fired boiler tail gas after beating.

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Abstract

The invention relates to a method for preparing silicon dioxide and aluminum oxide, in particular to a method for preparing silicon dioxide and aluminum oxide from coal ash. In the method, the coal ash, sodium carbonate and calcium oxide are used as raw materials, the sodium carbonate is causticized in situ by the calcium oxide, and is dissolved with alkali in a high-temperature high-pressure reaction system to form sodium silicate, calcium carbonate and desiliconized coal ash solid, wherein the sodium silicate solution is carbonated by CO2 to form silicon dioxide; and aluminum oxide and foamconcrete can be prepared from the calcium carbonate and the desiliconized coal ash by a soda lime sintering method. Residues after aluminum oxide preparation can be used as a raw material for preparing a tail gas purification absorbent in cement and chemical plants and coal burning boilers, and the foam concrete. Compared with the prior art, the method has the advantages of weak reacting solutioncorrosion, high desiliconization rate, low metal content of prepared sodium carbonate and high white carbon black quality, high aluminum oxide extraction rate and the like; meanwhile, the raw material source is wide, the process is simple, the production cost is low, and the product additional value is high.

Description

technical field [0001] The invention relates to a method for preparing silica and alumina, in particular to a method for preparing silica and alumina from fly ash. Background technique [0002] Fly ash is the fine particle dispersed residue after pulverized coal combustion. The total accumulation stock of fly ash in my country has exceeded billions of tons, and it is increasing at a rate of 100 million tons per year. The continuous generation of a large amount of solid waste has brought enormous pressure to the normal operation of coal enterprises and the ecological environment, and will also have an important impact on the implementation of the national sustainable development strategy. Therefore, the development and research of comprehensive and effective utilization of fly ash has important economic and social significance for resource utilization and environmental protection. [0003] The main chemical composition of fly ash is Al 2 o 3 and SiO 2 , Al 2 o 3 About 1...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B33/12C01F7/02B09B3/00
Inventor 商兆会杜雄伟杨露王中杰贾丽君
Owner CHINACOAL PINGSHUO GRP
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