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Method for recycling alumina and sodium oxide from bayer process red mud

A Bayer process red mud and alumina technology, applied in the direction of alumina/aluminum hydroxide, alkali metal oxides, etc., can solve problems such as excessive requirements, difficulty in meeting high-efficiency circulation of media, and thermodynamic limitations

Active Publication Date: 2014-11-05
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At the same time, the resources faced by my country's alumina industry are characterized by the fact that 98% of the bauxite is hard and difficult to dissolve diaspore type bauxite, and the A / S (aluminum-silicon ratio) is 4-7. Low-grade ores are mainly low-grade ores, and the internationally accepted Bayer method is used to treat ores in my country, which requires high temperature and high pressure dissolution conditions; The alkali content is high, and the red mud stockpiled in large quantities in the industry not only wastes resources such as alkali aluminum, but also has potential environmental hazards
Comalco first proposed a hydrothermal method with relatively mild operation in the patent. The recovery rate of alkali reaches 80-90%, but the recovery rate of alumina is low, and the A / S in red mud is still greater than 1. Even if the operating temperature is as high as 300 ° C, oxidation Improvements in aluminum recycling rates are still very limited
In 1982, Cresswell used the hydrothermal method to recover alumina and sodium oxide from the red mud of the Bayer process. The dissolution process was high temperature and high pressure, and the medium circulation was realized by evaporating a large amount of water, which required high energy consumption.
[0006] Patent CN101607725B provides a method for recovering alumina and sodium oxide from Bayer process red mud under low temperature and low pressure conditions. The process has too high requirements for the crystallization process of sodium aluminate, and it is difficult to meet the premise of efficient medium circulation, and then it is difficult to realize Economical and efficient recovery process of sodium oxide from red mud
Patent CN101538058B discloses a method for recovering alumina and sodium oxide in red mud by low-temperature and low-pressure hydrochemical method, but this method cannot solve the problem of equipment scarring in the process of extracting aluminum from red mud, and consumes much energy during the recovery process of sodium oxide higher

Method used

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  • Method for recycling alumina and sodium oxide from bayer process red mud

Examples

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Effect test

Embodiment 1

[0066] With the method for recovering alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan is used as raw material to recover alumina and sodium oxide. The red mud composition of the alumina plant (mass percentage, wt%, the same below) as described in Table 1:

[0067] Table 1

[0068]

[0069] Its production process is as figure 1 The methods shown include:

[0070] (1) Mix the red mud of an alumina factory in Henan with concentrated sodium hydroxide solution to prepare a slurry with a liquid NaOH mass fraction of 40% and a ratio of liquid NaOH mass to dry red mud mass of 2.5:1. And add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.4:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 210 ° C, and the stripping time is 0.3 hours. The stripping solution containing sodiu...

Embodiment 2

[0076] With the method for reclaiming alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan as described in Table 1 is still used as raw material to reclaim alumina and sodium oxide, and the production process is as follows Said:

[0077] (1) Mix the crystallization mother liquor of Example 1 with the prepared concentrated NaOH solution and the Bayer process red mud evenly, and adjust the liquid phase NaOH mass fraction to 50%, and the ratio of the liquid phase NaOH mass to the dry basis red mud mass is 3:1 slurry, and add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.6:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 240 ° C, and the stripping time is 0.2 hours, and the stripping solution containing sodium aluminate and slag are obtained. The solid-liquid mixture, the rel...

Embodiment 3

[0083] With the method for reclaiming alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan as described in Table 1 is still used as raw material to reclaim alumina and sodium oxide, and the production process is as follows Said:

[0084] (1) Mix the red mud of an alumina plant in Henan with concentrated sodium hydroxide solution to prepare a slurry with a liquid NaOH mass fraction of 55% and a ratio of liquid NaOH mass to dry red mud mass of 4:1. And add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.3:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 270 ° C, and the stripping time is 0.5 hours, and the stripping solution containing sodium aluminate and slag are obtained. The solid-liquid mixture, the relative dissolution rate of alumina entering the solution is 88.4%;

...

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Abstract

The invention relates to a method for recycling alumina and sodium oxide from bayer process red mud. In the method, by adopting a high molecular ratio and high alkali concentration sodium aluminate solution, aluminum extracting reaction can be rapidly carried out under mild operating conditions, so that the recovery rate of alumina in the red mud reaches more than 85%, and the defects, such as equipment scabbing and the like can be effectively prevented and even eliminated; by implementing an efficient crystallization process of an intermediate product of hydrated sodium aluminate, the cycle efficiency of a dissolution medium is greatly improved; due to complete transformation of a phase in the aluminum extracting reaction, a reaction process of recycling sodium oxide can be performed at low temperature and normal pressure; and after secondary sodium removal reaction, the sodium oxide content in final red mud is not more than 1% and is far less than 6-8% of the bayer process red mud. Therefore, the red mud can be doped in large proportion for preparing cement, brick and roadbed materials, concrete additives, environmental remediation materials and other fillers, and the problems such as resource utilization of the red mud, potential environment hazard and the like are hopefully solved.

Description

technical field [0001] The invention relates to the field of resource recovery, in particular, the invention relates to a method for cleanly and efficiently recovering aluminum, alkali and other components from the red mud waste residue of a Bayer process alumina plant. Background technique [0002] The metal aluminum and alumina industry is an important basic raw material industry for the development of the national economy. More than 90% of the total output of industrial alumina is used for electrolytic production of metal aluminum, and the rest is used in the fields of electronics, refractory materials, petroleum, chemical industry, ceramics, environmental protection and pharmaceuticals. [0003] At present, the industrial production method of alumina is basically alkali method, mainly including Bayer method, sintering method and Bayer-sintering combined method. At the same time, the resources faced by my country's alumina industry are characterized by the fact that 98% ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/02C01D1/02
Inventor 曹绍涛郭涛张亦飞张懿
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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