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A method for producing xonotlite and alumina by hydrothermal method of fly ash alkali leaching and sintering

A technology of tobermorite and fly ash is applied in the field of comprehensive utilization of fly ash, which can solve the problems of scarcity, large resource and environmental impact, high production energy consumption and cost, and achieve engineering stability, land saving, etc. The effect of resources

Active Publication Date: 2016-05-25
NORTHEASTERN UNIV ENG & RES INST CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

However, my country's bauxite resources are quite scarce, and bauxite reserves only account for about 5% of the world's total reserves, and most of them are low-grade diaspore-type bauxite that is difficult to handle. Purchasing restriction policy, bauxite resource problem has become the biggest bottleneck for the sustainable development of my country's alumina and aluminum industry
[0005] The traditional process produces xonotlite and its products, and its siliceous raw materials are generally produced by using diatomite or quartz sand and alkali under melting conditions to generate industrial water glass. In the preparation process of raw materials, it is necessary to use a large amount of high-quality silicon ore such as quartz sand and diatomaceous earth to co-melt with soda ash or sodium sulfate in a melting kiln, and then cool, pulverize and dissolve to make it; this makes the selection of silicon raw materials require mining and Consume a large amount of non-renewable silicon mineral resources such as quartz and diatomaceous earth; at the same time, calcareous raw materials generally need to use high-quality fuels such as coke or white coal to separately burn lime and refined milk of lime, which consumes a lot of energy and costs, and is harmful to resources and the environment. Great impact
[0006] Existing various processes for producing aluminum hydroxide or aluminum oxide with high alumina fly ash all produce a large amount of silicon-calcium slag or silicon slag, a large amount of silicon-calcium slag or The large-scale rational utilization of silicon slag has become a huge bottleneck in various processes

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  • A method for producing xonotlite and alumina by hydrothermal method of fly ash alkali leaching and sintering

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] 1. Chemical beneficiation: Put the fly ash into the batching tank with chemical beneficiation solvent for batching. The chemical beneficiation solvent contains Na 2 O30g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 3 according to the weight ratio of chemical beneficiation solvent and fly ash; and then undergo chemical beneficiation treatment with a reaction temperature of 70°C and a reaction time of 600 minutes; the obtained chemical beneficiation slurry is continuously separated and separated by a horizontal belt filter. Washing to obtain the washed filter residue and crude sodium silicate solution; washing the washed filter residue again to make a fly ash concentrate with a water weight content of 30%;

[0040] Na in the obtained crude sodium silicate solution 2 O concentration is 30g / L, SiO 2 The concentration is 15g / L; the crude sodium silicate solution is refined by leaf filtration to obtain a refined sodium silicate solution with solid floating ma...

Embodiment 2

[0053] Method is with embodiment 1, and difference is:

[0054] (1) The chemical beneficiation solvent contains Na 2 O80g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 6 according to the weight ratio of chemical beneficiation solvent and fly ash; the reaction temperature of chemical beneficiation treatment is 90°C, and the reaction time is 100min; the washed filter residue is washed again to make fly ash with a water weight content of 40% Concentrate;

[0055] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 40g / L;

[0056] (2) Na in sodium aluminate solution 2 o k The concentration is 210g / L, Na 2 O+K 2 O and Al 2 o 3 The molar ratio is 2.8, the mixing ratio of fly ash concentrate and sodium aluminate solution is based on the Na in all materials 2 O+K 2 O and Al 2 o 3 The molar ratio is 1.58, the leaching temperature is 270°C, and the reaction time is 60min; 2 o k The concentration is contro...

Embodiment 3

[0065] Method is with embodiment 1, and difference is:

[0066] (1) The chemical beneficiation solvent contains Na 2 O120g / L; the proportion of ingredients is 9 according to the weight ratio of chemical beneficiation solvent to fly ash; then chemical beneficiation treatment, the reaction temperature is 120°C, and the reaction time is 30min; the washed filter residue is washed again to make a powder with a water weight content of 45%. coal ash concentrate;

[0067] Na in the obtained crude sodium silicate solution 2 O concentration is 120g / L, SiO 2 The concentration is 60g / L;

[0068] (2) Na in sodium aluminate solution 2 o k The concentration is 245g / L, Na 2 O+K 2 O and Al 2 o 3 The molar ratio is 3.2, the mixing ratio of fly ash concentrate and sodium aluminate solution is based on the Na in all materials 2 O+K 2 O and Al 2 o 3 The molar ratio is 1.6, the leaching temperature is 280°C, and the reaction time is 30min; 2 o k The concentration is controlled at 165...

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Abstract

A method for producing xonotlite and alumina by fly ash alkali leaching and sintering hydrothermal method, comprising the following steps: (1) chemical beneficiation; (2) alkali leaching to produce alumina; (3) preparing raw slurry; 4) Preparation of clinker by sintering; (5) Dissolution of clinker and separation and washing; (6) Preparation of xonotlite precursor original slurry; (7) Preparation of xonotlite precursor by hydrothermal synthesis; (8) Hydrothermal synthesis Synthetic preparation of xonotlite filter cake. The invention effectively solves the problems and defects of large limestone consumption, large energy consumption and large slag volume in the prior art; the comprehensive utilization of fly ash can produce xonotlite and alumina, which not only realizes the replacement of silicon minerals Resources, and achieved the replacement of bauxite resources, but also save resources such as land, and can also achieve large-scale economic production.

Description

technical field [0001] The invention relates to a comprehensive utilization method of fly ash, in particular to a method for producing xonotlite and alumina by a hydrothermal method of alkali leaching and sintering of fly ash. Background technique [0002] Some coal fields in central and western Inner Mongolia and northern Shanxi are rich in high-alumina coal resources, with prospective reserves of nearly 100 billion tons, equivalent to about 15 billion tons of high-alumina fly ash, which is equivalent to the current reserves of bauxite in my country More than 8 times of that, and the alumina content in some fly ash can reach 40~50%. This kind of fly ash is generally called high aluminum fly ash. Fly ash is the main solid waste from the perspective of power generation in power plants, but the alumina content in the high-alumina fly ash produced by the combustion of high-alumina coal can reach 35-45%, some even as high as 50%, and the silicon content is generally 35%. %above....

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B33/24C01F7/14
CPCY02P20/129
Inventor 李光柱于海燕崔德成潘晓林毕诗文涂赣峰黎娜
Owner NORTHEASTERN UNIV ENG & RES INST CO LTD
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