Method for producing alumina through bauxite acid process

A technology of bauxite and alumina, applied in chemical instruments and methods, aluminum compounds, inorganic chemistry, etc., can solve the problems of low comprehensive utilization rate of resources, large amount of dissolved red mud, complicated process, etc., and increase ore processing capacity , high resource utilization and simple operation

Active Publication Date: 2010-09-08
DONGDA NONFERROUS SOLID WASTE TECH RES INST LIAOLING CO LTD
View PDF4 Cites 16 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the production of alumina by the Bayer process requires a higher grade of bauxite. When the grade of the ore is low, the aluminum in the mineral will combine with the silicon-containing mineral to form hydrated sodium aluminosilicate, which will lead to low extraction efficiency of aluminum and redness. The emergence of problems such as large amount of mud, taking bauxite with an aluminum-silicon ratio of 5 as an example, the theoretical dissolution rate of alumina in the ore during the production of alumina by the Bayer process is only about 80%, resulting in a sharp drop in aluminum yield , the comprehensive utilization rate of resources is low
A kind of stripping method of diaspore ore (CN101289205A) invented by Aluminum Corporation of China, but can not fundamentally solve the shortcomings such as large amount of red mud of middle and low grade bauxite, resource utilization rate, and a large amount of red mud Mud cannot be applied, takes up a lot of land, and causes serious soil pollution
[0003] In my country's bauxite resources, the total reserves of minerals with high iron content (>10%) exceed 800 mil

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for producing alumina through bauxite acid process
  • Method for producing alumina through bauxite acid process
  • Method for producing alumina through bauxite acid process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] The aluminum-silicon ratio in the bauxite used is 1.5. The bauxite is crushed and finely ground until the particle size is less than 150 μm, and then placed in a closed container and leached with hydrochloric acid. During the leaching process, hydrogen chloride gas is introduced into the device. The amount of hydrogen chloride gas added It is 0.6t / t bauxite; the weight concentration of hydrochloric acid used is 5%, the liquid-solid ratio of hydrochloric acid and bauxite is 20:1L / kg, the temperature of the material during leaching is 80°C, and the leaching time is 240min. The leaching rate of aluminum element was 91.58%, and the leaching rate of iron element was 95.42%. The ore slurry was separated by solid-liquid to obtain leaching liquid and leaching slag, and the mass content of silicon dioxide in the leaching slag was 88.13%.

[0035] Use tributyl phosphate as extractant and sulfonated kerosene as diluent to separate the iron and aluminum elements in the leaching solu...

Embodiment 2

[0040]The aluminum-silicon ratio in the bauxite used is 2.5. The bauxite is crushed and finely ground to a particle size of less than 150 μm, then placed in a closed container and leached with hydrochloric acid. During the leaching process, hydrogen chloride gas is introduced into the device. The amount of hydrogen chloride gas added It is 1.0t / t bauxite; the weight concentration of hydrochloric acid used is 20%, the liquid-solid ratio of hydrochloric acid and bauxite is 2:1L / kg, the temperature of the material during leaching is 110°C, and the leaching time is 60min. The leaching rate of aluminum element in the ore was 93.15%, and the leaching rate of iron element was 93.56%. The leachate and leaching slag were obtained through solid-liquid separation of the pulp, and the mass content of silicon dioxide in the leaching slag was 90.75%.

[0041] Use tributyl phosphate as extractant and sulfonated kerosene as diluent to separate iron and aluminum elements in the leaching solutio...

Embodiment 3

[0047] The aluminum-silicon ratio in the bauxite used is 5. The bauxite is crushed and finely ground to a particle size of less than 150 μm, then placed in a closed container and leached with hydrochloric acid. During the leaching process, hydrogen chloride gas is continuously injected into the device for injection. The amount of hydrogen chloride gas added is 0.8t / t bauxite; the initial weight concentration of hydrochloric acid is 20%, the liquid-solid ratio of hydrochloric acid and bauxite is 10:1L / kg, the temperature of the material during leaching is 170°C, and the leaching time is 30min . The leaching rate of aluminum element in the ore was 93.15%, and the leaching rate of iron element was 96.53%. The leachate and leaching slag were obtained through solid-liquid separation of the ore slurry, and the mass content of silicon dioxide in the leaching slag was 92.46%.

[0048] Use tributyl phosphate as extractant and sulfonated kerosene as diluent to separate iron and aluminum...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a method for producing alumina through a bauxite acid process, which comprises the following steps that: (1) alumyte with the Al-Si ratio of 1.5 to 5 or the ferric oxide content of 10 to 50 percent is selected as the raw material, crushed and put into a closed container to be leached, and hydrogen chloride gas is blown in during the leaching process; (2) TBP and sulfonated kerosene are added into leachate to be extracted, and extraction phase and the raffinate phase are obtained after extraction; (3) the aluminum chloride solution is separated from the extraction phase, and then the aluminum chloride solution is heated and decomposed, the pyrolysis temperature is 400 to 900DEG C, and the pyrolysis time is 5 to 60min, and alumina and hydrogen chloride gas are obtained. The extraction phase is back extracted to obtain ferric chloride solution and pyrolysed to obtain ferric oxide. The method for producing alumina through bauxite acid process realizes the effective treatment to low-grade and high-iron bauxite ore, has high resource utilization rate, realizes the integrated utilization of aluminum, iron, silicon and other valuable elements; and that the hydrogen chloride is added in through a continuous spraying and blowing method during the leaching process can improve the ore blending and provide the production capability.

Description

technical field [0001] The invention relates to a production method of alumina, in particular to a method for producing alumina by a bauxite acid method. technical background [0002] At present, almost all enterprises using bauxite resources to produce alumina use the alkaline method, of which the Bayer method is the most important method for producing alumina. However, the production of alumina by the Bayer process requires a higher grade of bauxite. When the grade of the ore is low, the aluminum in the mineral will combine with the silicon-containing mineral to form hydrated sodium aluminosilicate, which will lead to low extraction efficiency of aluminum and redness. The emergence of problems such as large amount of mud, taking bauxite with an aluminum-silicon ratio of 5 as an example, the theoretical dissolution rate of alumina in the ore during the production of alumina by the Bayer process is only about 80%, resulting in a sharp drop in aluminum yield , The comprehens...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C01F7/22
Inventor 张廷安豆志河吕国志刘燕鲍丽牛丽萍赵秋月蒋孝丽赫冀成
Owner DONGDA NONFERROUS SOLID WASTE TECH RES INST LIAOLING CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products