Method for extracting alumina from bauxite

A technology of bauxite and alumina, applied in chemical instruments and methods, aluminum compounds, inorganic chemistry, etc., can solve the problems of decreased extraction rate, long and complicated process, and large amount of slag discharge, and achieve energy consumption and production The effect of cost reduction, simple process, and lower grade requirements

Active Publication Date: 2011-09-14
北京蔚然欣科技有限公司
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Problems solved by technology

In the above-mentioned existing various methods, except the Bayer method, there are serious defects: either the energy consumption is too high, and it is difficult to obtain benefits (techniques such as soda lime sintering method, lime sintering method and microwave aiding dissolution method); If the extraction rate is too low, it is also difficult to obtain benefits (non-high temperature method); or the amount of slag discharge is too large, resulting in excessive solid waste discharge, which seriously pollutes the environment, and fundamentally, it is still difficult to obtain benefits; or the process is long and complicated , a large number of equipment, a lot of operating processes are mutually restrained, and there are problems such as high energy consumption and high cost (combined method, etc.); or the additives used are too corrosive to the equipment, and the recovery of the auxiliary acid is difficult and it is easy to cause pollution to the environment. A series of fatal shortcomings have seriously affected the promotion of its industrialization (acid leaching method, ammonium fluoride aiding method, ammonium sulfate sintering method, etc.)
[0004] Compared with other existing methods, although the Bayer process is relatively simple, the investment and energy consumption are relatively low, more than 90% of alumina is produced by the Bayer process, but the serious disadvantage of this method is that it is only suitable for high Processing of gibbsite-type bauxite with aluminum-silicon ratio
Among all kinds of bauxite resources in my country, diaspore accounts for more than 98% of the total reserves, especially most of them have high SiO 2 The outstanding characteristics of the content, the use of the Bayer method is greatly restricted
[0005] In addition to the above, Alkali fusion of soda ash and bauxite raw materials was first invented by the French chemist Satri in 1858 to extract Al 2 o 3 The technology - soda ash sintering method, due to the alkali fusion process, SiO 2 and Al 2 o 3 with Na 2 CO 3 The reaction produces a large amount of insoluble sodium aluminosilicate (Na 2 O·Al 2 o 3 2SiO2 2 ) solid, not only makes Al 2 o 3 The extraction rate has dropped significantly, the quality of the extracted alumina is poor, and a large amount of raw material soda ash Na 2 CO 3 to Na 2 O·Al 2 o 3 2SiO2 2 Na in solid 2 O, cannot be released for recycling, so Al 2 o 3 Extraction costs have risen substantially

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  • Method for extracting alumina from bauxite
  • Method for extracting alumina from bauxite

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] (1) Mix the crushed bauxite with solid sodium carbonate at a ratio of 1:0.6 and grind it into a 100-mesh mixed material.

[0034] (2) Calcining the mixed material obtained in step (1) at a temperature of 620° C. for 60 minutes to obtain roasted clinker. The roasted clinker is divided into several equal parts with the same quality for later use; during roasting, the roasting equipment is connected to the gas output pipe and connected to the carbon separation tank, and the recovered carbon dioxide gas is directly used for carbon separation.

[0035] (3) Add an appropriate amount of water to the first portion of roasted clinker, and make the solid-liquid mass ratio 1:6, and leaching for 50 minutes at a temperature of 10°C. After leaching, filter to obtain filter residue and filtrate respectively. After determination, the leaching rate of alumina in the filtrate was 76%, and the leaching rates of other components such as silicon dioxide and iron oxide were all zero.

[00...

Embodiment 2

[0043] (1) Mix the crushed bauxite with solid sodium carbonate at a ratio of 1:2.5 and grind it into a 250-mesh mixed material.

[0044] (2) Calcining the mixed material obtained in step (1) at a temperature of 990° C. for 10 minutes to obtain roasted clinker. The roasted clinker is divided into several equal parts with the same quality for later use; during roasting, the roasting equipment is connected to the gas output pipe and connected to the carbon separation tank, and the recovered carbon dioxide gas is directly used for carbon separation.

[0045] (3) Add an appropriate amount of water to the first portion of roasted clinker, and make the solid-to-liquid mass ratio 1:120, and leaching at 85° C. for 5 minutes. After leaching, filter to obtain filter residue and filtrate respectively. After determination, the leaching rate of alumina in the filtrate is 80%, and the leaching rates of other components such as silicon dioxide and iron oxide are all zero.

[0046] Put the s...

Embodiment 3

[0053] (1) Mix the crushed bauxite with solid sodium carbonate at a ratio of 1:2.3 and grind it into a 150-mesh mixed material.

[0054] (2) Calcining the mixed material obtained in step (1) at a temperature of 720° C. for 50 minutes to obtain calcined clinker. The roasted clinker is divided into several equal parts with the same quality for later use; during roasting, the roasting equipment is connected to the gas output pipe and connected to the carbon separation tank, and the recovered carbon dioxide gas is directly used for carbon separation.

[0055] (3) Add appropriate amount of water to the first batch of roasted clinker, and make the solid-liquid mass ratio 1:15, and leaching for 40 minutes under the temperature condition of 20°C. After leaching, filter to obtain filter residue and filtrate respectively. After determination, the leaching rate of alumina in the filtrate was 79%, and the leaching rates of other components such as silicon dioxide and iron oxide were all ...

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Abstract

The invention discloses a method for extracting alumina from bauxite, which is suitable for extracting the alumina from various and different ore mineral types of bauxites. The method comprises the following steps: mixing and grinding the crushed bauxite and sodium carbonate according to a certain proportion, and then obtaining high-purity alumina through roasting, circular leaching, sedimentation-filtration, carbonization, additive recycling, washing, calcinations and the like. In the whole production process, the generated carbon dioxide and the used additive can be recovered and reused. Compared with the Bayer process and other methods for producing the alumina, the method has the advantages of low requirement on the grade of the alumina from the bauxite, low requirement on the aluminum-silicate (A/S) ratio, no limitation to the type of minerals, high extraction rate of the alumina, low energy consumption, more succinct process, no special requirements on the equipment, lower cost and the like, thereby easily realizing industrialization.

Description

Technical field: [0001] The invention belongs to the field of metallurgy and chemical comprehensive production, in particular to a method for extracting alumina from bauxite. technical background: [0002] With the continuous development of human society, the demand for aluminum resources is also increasing. At present, with the development of the alumina industry, there has been a serious shortage of bauxite resources, especially high-quality bauxite resources. At present, the contradiction between the supply and demand of bauxite is very prominent, especially in my country, most of the mines are seriously depleted in ore grade to varying degrees, and the high-grade or high-aluminum-silicon ratio bauxite in most major mining areas is even on the verge of depletion. Facing the current situation that high-grade or high-quality bauxite resources with high aluminum-silicon ratio are increasingly scarce, the existing alumina production technology is facing serious challenges. H...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/20
Inventor 潘爱芳马昱昭马润勇
Owner 北京蔚然欣科技有限公司
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