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A method for producing tobermorite 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, and can solve the problems of large production energy consumption and cost, large resource and environmental impact, consumption and the like

Active Publication Date: 2016-05-25
NORTHEASTERN UNIV ENG & RES INST CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

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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] 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 kiln, and then cool, pulverize and dissolve to make it; this makes the selection of silicon raw materials require mining and A large amount of non-renewable silicon mineral resources such as quartz and diatomaceous earth are consumed; at the same time, in addition to calcium carbide slag, limestone generally needs to be burned separately with high-quality fuels such as coke or white coal to burn lime and refined lime milk. The production energy consumption and High cost, great impact on resources and environment
Existing various processes for producing aluminum hydroxide or aluminum oxide with high alumina fly ash produce a large amount of silicon-calcium slag or silicon slag, and the large-scale and rational utilization of a large amount of silicon-calcium slag or silicon slag has become a huge bottleneck for various processes

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

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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 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%;

[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 ma...

Embodiment 2

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

[0055] (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 to fly ash; then chemical beneficiation treatment, the reaction temperature is 90°C, and the reaction time is 200min; the washed filter residue is washed again to make water with a weight content of 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 con...

Embodiment 3

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

[0067] (1) The chemical beneficiation solvent contains Na 2 O120g / 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 concentration ...

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Abstract

A method for producing tobermorite and alumina by a 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 the original slurry of tobermorite precursor; (7) Preparation of tobermorite precursor by hydrothermal synthesis; (8) Hydrothermal synthesis Synthetic preparation of tobermortite slurry. The invention effectively solves the problems and defects of large limestone consumption, large energy consumption and large slag volume in the prior art; it can not only produce tobermorite, but also produce alumina, which not only realizes the replacement of silicon mineral resources, but also realizes In addition to replacing bauxite resources, it also saves land and other resources, 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 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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Patent Type & Authority Patents(China)
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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