Method for producing aluminum oxide based on calcification-carbonization transformation

A low-grade bauxite, carbonization transformation technology, applied in the preparation of alkali metal aluminate/alumina/aluminum hydroxide, alumina/aluminum hydroxide, alkaline earth metal silicate, etc. The increase in lime consumption and the increase in unit consumption of bauxite have achieved the effect of solving land occupation and polluting the environment, reducing the amount of CO2 gas, and improving environmental protection standards

Active Publication Date: 2014-06-18
DONGDA NONFERROUS SOLID WASTE TECH RES INST LIAOLING CO LTD
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  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] (1) After adding lime, the A / S in red mud dissolved by Bayer method is higher than that dissolved by conventional Bayer method, and the unit consumption of aluminum ore increases under the same dissolution conditions. Although the increase of lime helps to reduce the alkali consumption, But it reduces the comprehensive utilization efficiency of ore
[0010] (2) The consumption of lime increases, so the consumption of limestone and coke also increases
[0011] In summary, although the alkali consumption is reduced with the increase of lime addition, it will also increase the aluminum content in red mud, which will lead to a decrease in the comprehensive utilization rate of valuable elements in bauxite.
Therefore, in the alumina production process using the lime Bayer process, the amount of slaked lime usually used is 10% to 15% of the mineral amount. Under this condition, the mass ratio of alumina to silica in the residue generated during the production process is still 1.3 ~1.4, which is very unfavorable for processing low-grade bauxite, and the content of sodium oxide in red mud is more than 4%, so it is difficult to use

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  • Method for producing aluminum oxide based on calcification-carbonization transformation

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Crush the low-grade bauxite to -500μm, then mix the burned slaked lime and bauxite at a mass ratio of 0.5:1, and put them in 260g / L caustic soda under the conditions of transformation temperature of 130℃ and transformation time of 15min Calcification transformation in the solution, the liquid-solid mass ratio is 7:1, part of the alumina in the mineral enters the eluate (the eluate can be recycled during the transformation process), and the other alumina and slaked lime and all the silicon in the mineral are converted into hydration Garnet enters the slag phase and obtains a transformation slag;

[0047] After mixing the primary transformation slag and clean water in a closed container under the condition of liquid-solid ratio (15:1) mL / g, in CO 2 The partial pressure of the gas is 1.8MPa, and the carbonization temperature is 150°C for 10 minutes, and the hydrated garnet of the primary transformation slag is transformed into the secondary transformation slag whose main c...

Embodiment 2

[0050] Crush the low-grade bauxite to -500μm, then mix the burned slaked lime and bauxite at a mass ratio of 0.5:1, and put in 140g / L caustic soda under the conditions of transformation temperature of 260℃ and transformation time of 60min Medium calcification transformation, the liquid-solid mass ratio is 2.5:1, part of the alumina in the mineral enters the eluate (the eluate can be recycled during the transformation process), and other alumina, slaked lime and all the silicon in the mineral are transformed into hydrated pomegranate The stone enters the slag phase and obtains a transformation slag;

[0051] After mixing the primary transformation slag and clean water in a closed container under the condition of a liquid-solid ratio of 3:1, the CO 2 The partial pressure of the gas is 0.8MPa, and the carbonization temperature is 90°C for 30 minutes, and the hydrated garnet of the primary transformation slag is transformed into the secondary transformation slag whose main compone...

Embodiment 3

[0054] Crush the low-grade bauxite to -500μm, then mix the burned slaked lime and bauxite at a mass ratio of 0.3:1. The transformation temperature is 180°C, the transformation time is 40min, the concentration of sodium hydroxide is 200g / L, hydrogen Calcification transformation in sodium aluminate solution with a molar ratio of sodium oxide to alumina of 3.5:1, the mass ratio of liquid to solid is 4:1, part of the alumina in the mineral enters the eluate (the eluate can be recycled), and the other alumina and slaked lime And all the silicon in the mineral is converted into hydrated garnet and enters the slag phase to obtain a transformation slag;

[0055] After mixing the primary transformation slag and the low-concentration sodium aluminate solution with a sodium hydroxide mass content of 30g / L in a closed container under the condition of liquid-solid ratio (4:1) mL / g, the CO 2 The partial pressure of the gas is 1.2MPa, and the carbonization temperature is 120°C for 20 minutes...

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Abstract

The invention belongs to the field of production of aluminum oxide, and particularly relates to a method for producing aluminum oxidizing based on calcification-carbonization transformation. The method comprises the following steps of: performing a calcification transformation reaction on white lime and middle and low-grade alumyte serving as a raw material in a caustic alkali solution of 1400-260g / L to obtain primarily-transformed slag; intruding CO2 into the primarily-transformed slag in clear water or a low-concentration sodium aluminum solution under an enclosed condition for carbonating obtain the secondarily-transformed slag; and dissolving the secondarily-transformed slag out by adopting a sodium hydroxide solution of 30-120g / L or a sodium aluminate solution of a corresponding concentration at the temperature of 40-100 DEG C to obtain novel structure slag which takes calcium silicate and calcium carbonate as main components and of which the aluminum to silicon ratio is 0.0-0.4, wherein the soda content can be lowered below 0.5 percent, and the comprehensive yield of aluminum oxide in a mineral raw material can be up to 90-100 percent. Due to the adoption of the method, the novel structural slag can be completely taken as a raw material in the cement industry, the problem of environmental pollution such as red mud space occupation and the like is solved completely, and a large amount of CO2 can be absorbed simultaneously in a production process; and the method is an environment-friendly and economical aluminum oxide production method.

Description

technical field [0001] The invention belongs to the field of alumina production, and in particular relates to a method for producing alumina based on calcification-carbonization transformation. technical background [0002] Most of the bauxite resources in China are diaspore bauxite, and most of them are low-grade aluminum resources with high aluminum and high silicon. At present, there are many methods of producing alumina in China with low- and medium-grade bauxite as raw materials. Among them, "a combined desiliconization method for low-grade bauxite invented by Chen Xiangqing et al. of Aluminum Corporation of China, China Patent Application No.: 200810115455" discloses the combined process of selective desliming and positive flotation for desiliconization Si, so as to increase the A / S ratio of raw ore, to achieve the purpose of reducing production costs; "A method for the joint production of aluminum hydroxide by lime sintering and Bayer process invented by Ma Wuquan and...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/02C01F7/04C01B33/24C01F11/18
Inventor 张廷安吕国志刘燕豆志河赵秋月牛丽萍赫冀成
Owner DONGDA NONFERROUS SOLID WASTE TECH RES INST LIAOLING CO LTD
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