Method for producing tobermorite and aluminum oxide by using coal ash alkaline leaching sintering hydrothermal method

A technology of tobermorite and fly ash, which is applied in the field of comprehensive utilization of fly ash, and can solve problems such as large impact on resources and the environment, consumption, and shortage

Active Publication Date: 2015-04-01
NORTHEASTERN UNIV ENG & RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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] Tobermorite and its products are produced by traditional techniques, 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 kil

Method used

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  • Method for producing tobermorite and aluminum oxide by using coal ash alkaline leaching sintering hydrothermal method
  • Method for producing tobermorite and aluminum oxide by using coal ash alkaline leaching sintering hydrothermal method

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Embodiment 1

[0040] 1. Chemical beneficiation: Put the fly ash into the batching tank with chemical beneficiation solvent for batching. The chemical beneficiation solvent contains Na 2 O 30g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 3 according to the weight ratio of chemical beneficiation solvent and fly ash; then chemical beneficiation treatment, the reaction temperature is 70°C, and the reaction time is 600 min; the obtained chemical beneficiation slurry is continuously separated through a horizontal belt filter and washing to obtain the washing filter residue and crude sodium silicate solution; the washing filter residue is washed again to make a fly ash concentrate with a water weight content of 30%;

[0041] 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 matter less than ...

Embodiment 2

[0054] Method is with embodiment 1, and difference is:

[0055] (1) The chemical beneficiation solvent contains Na 2 O 80g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 6 according to the weight ratio of chemical beneficiation solvent and fly ash; then chemical beneficiation treatment, the reaction temperature is 90°C, and the reaction time is 200 min; the washed filter residue is washed again to make the water weight content 40% fly ash concentrate;

[0056] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 40g / L;

[0057] (2) Na in sodium aluminate solution 2 o k The concentration is 220g / 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

[0066] Method is with embodiment 1, and difference is:

[0067] (1) The chemical beneficiation solvent contains Na 2 O 120g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 9 according to the weight ratio of chemical beneficiation solvent and fly ash; then chemical beneficiation treatment, the reaction temperature is 120°C, and the reaction time is 30 minutes; the washed filter residue is washed again to make water with a weight content of 45%. fly ash concentrate;

[0068] Na in the obtained crude sodium silicate solution 2 O concentration is 120g / L, SiO 2 The concentration is 60g / L;

[0069] (2) Na in sodium aluminate solution 2 o k The concentration is 45g / 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 concentratio...

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Abstract

The invention discloses a method for producing tobermorite and aluminum oxide by using a coal ash alkaline leaching sintering hydrothermal method. The method comprises the following steps: (1) performing chemical ore separation; (2) producing aluminum oxide through alkaline leaching; (3) preparing raw material slurry; (4) sintering to prepare clinker; (5) dissolving, separating and washing the clinker; (6) preparing tobermorite precursor raw material slurry; (7) performing hydro-thermal synthesis to prepare a tobermorite precursor; (8) performing hydro-thermal synthesis to prepare tobermorite slurry. By adopting the method, the problems and the defects that in the prior art a great deal of limestone is consumed, the energy consumption is large and a great deal of slag is generated are effectively solved, both tobermorite and aluminum oxide can be produced, a silicon mineral resource is saved, a monohydrallite resource is replaced, sources such as soil are also saved, and large-scale economic production is achieved.

Description

technical field [0001] The invention relates to a comprehensive utilization method of fly ash, in particular to a method for producing tobermorite 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%. %abov...

Claims

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Application Information

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IPC IPC(8): C01B33/24C01F7/02B09B3/00
CPCY02P20/129Y02W30/20Y02W30/78
Inventor 李光柱崔德成于海燕涂赣峰潘晓林毕诗文黎娜
Owner NORTHEASTERN UNIV ENG & RES INST CO LTD
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