Process method for producing aluminum hydroxide by seed decomposition of supersaturated sodium aluminate solution

A technology of aluminum hydroxide and sodium aluminate, which is applied in the field of metallurgy, can solve the problems of reducing the supersaturation of sodium aluminate solution, the volume of the decomposition tank is large, and the cost of manufacturing and installation is expensive, so as to improve the output rate and product quality, change the Dynamic conditions, the effect of reducing maintenance costs

Active Publication Date: 2014-08-27
GUIZHOU R & D CENT ON MODERN MATERIALS
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  • Application Information

AI Technical Summary

Problems solved by technology

The seed separation tank adopting the air full-mixing method has simple structure, low manufacturing cost and low maintenance cost. However, this method also has some shortcomings: a) Large power consumption
Although this kind of strong stirring can prevent the crystals from depositing and accumulating at the bottom of the decomposition tank, the shear force generated in the flow field of the sodium aluminate solution will destroy the crystal growth process of aluminum hydroxide on the one hand, resulting in the crystallized and grown hydrogen Alumina particles are crushed, eroded, and refined, which reduces product quality and is not conducive to the output of sandy alumina products
In addition, due to the large volume of the decomposition tank, the mechanical stirring device is tens of meters long, and the stirring load is relatively large, not only the manufacturing requirements for the stirring shaft, stirring blades and other components of the stirring system are relatively high, but also the energy consumption is relatively large. Expensive manufacturing and installation costs, high operation and maintenance costs
A seed tank with a diameter of 14 meters and a height of 35 meters needs to be equipped with a 75-kilowatt stirring motor and gearbox, which is relatively expensive; and the motor runs continuously without stopping production or stopping, which consumes a lot of power
Years of production practice has proved that whether it is air full mixing or mechanical full mixing, it will cause the upper and lower liquids to mix with each other (commonly known as "short circuit"), reducing the supersaturation of the sodium aluminate solution delivered to the seed tank. degree, the reaction efficiency is reduced; at the same time, the strong full mixed flow agitation also causes the particle size of the product to decrease
In 1985, the French Piccini Aluminum Company invented the "method and equipment for producing alumina by decomposing sodium aluminate solution without stirring" (CN85108251A or US4666687). phenomenon, but the invention is only applicable to cylindrical-conical small-scale seeding tanks (1500M 3 left and right), cannot be used in large flat-bottomed, arc-shaped bottom or other types of tanks, and the solid content of sodium aluminate solution is also limited within 600-700g / l, and the slurry flow rate also has special requirements, so its The scope of application is greatly limited, and it cannot meet the requirements of the current development of seed crystal decomposition technology for large capacity (4000M 3 above), high solid content (800-1000g / l) decomposition equipment requirements, and because the invention completely cancels the stirring, it is easy to produce a large amount of accumulated material at the bottom of the seed separation tank, causing sinking accidents and interrupting the production process

Method used

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  • Process method for producing aluminum hydroxide by seed decomposition of supersaturated sodium aluminate solution

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Example 1. The cylindrical-flat bottom structure is used to mechanically stir the seed tanks, each seed tank has a diameter of 14m, a height of 35m, and a tank volume of 4500m 3 . A layer of rotating paddles is used for local agitation at the bottom area (or discharge end) of each seed sub-trough. The agitation intensity is determined by the fact that the aluminum hydroxide particles at the bottom of the seed crystal decomposition tank can remain suspended and not generated at the bottom of the seed crystal decomposition tank. The deposition shall prevail, and the rest shall be carried out according to the requirements of the daily production operation procedures of the alumina plant. The feeding speed at the discharge end of the sub-groove is greater than the final speed of the interference settling of solid particles in the solution. The way of material lifting can be but not limited to compressed air, mechanical pump or manufacturing liquid level difference and oth...

Embodiment 2

[0034] Example 2. The air-stirred seed tank with cylindrical-conical bottom structure is adopted. The diameter of each seed tank is 8.2m, the height is 29.7m, and the tank volume is 1300m 3 . Blow compressed air into the bottom area (or discharge end) of each seed sub-tank for local agitation. The agitation intensity is based on the fact that the aluminum hydroxide particles at the bottom of the seed crystal decomposition tank can maintain a suspended state and no deposition occurs at the bottom of the seed crystal decomposition tank. The rest shall be carried out according to the requirements of the daily production operation procedures of the alumina plant. The feeding speed at the discharge end of the sub-groove is greater than the final speed of the interference settling of solid particles in the solution. The way of material lifting can be but not limited to compressed air, mechanical pump or manufacturing liquid level difference and other ways.

Embodiment 3

[0035] Example 3. Adopt cylinder-multi-cone bottom combined air stirring seed tank, each seed tank has a diameter of 15m, a height of 35m, and a tank volume of 5500m 3 ;Blow compressed air into each cone bottom (or discharge end) of the bottom area of ​​each seed sub-trough for partial agitation. The agitation intensity is such that the aluminum hydroxide particles at the bottom of the seed crystal decomposition tank can maintain a suspended state and not decompose in the seed crystal The deposition at the bottom of the tank shall prevail, and the rest shall be carried out in accordance with the requirements of the daily production operation procedures of the alumina plant. The feeding speed at the discharge end of the sub-groove is greater than the final speed of the interference settling of solid particles in the solution. The way of material lifting can be but not limited to compressed air, mechanical pump or manufacturing liquid level difference and other ways.

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Abstract

The invention discloses a process method for producing aluminum hydroxide by decomposing supersaturated sodium aluminate solution seed crystals. The method only performs partial agitation at the bottom of the seed crystal decomposition tank, and the agitation intensity is determined by the aluminum hydroxide particles at the bottom of the seed crystal decomposition tank. The suspension state shall prevail, so as to promote the diffusion and mass transfer of the sodium aluminate solution with high solid content and high molecular ratio at the bottom of the seed crystal decomposition tank, and prevent the aluminum hydroxide particles at the bottom of the seed crystal decomposition tank from depositing. The present invention breaks the previous traditional technological route that requires full mixed-flow stirring in the decomposition process of seed crystals, and proposes a new technological method of "partial stirring + flat push flow", which has good energy-saving and consumption-reducing effects, high decomposition output rate, and high product quality. Good quality and other characteristics.

Description

technical field [0001] The invention relates to a process for producing alumina, in particular to a process for producing aluminum hydroxide by decomposing supersaturated sodium aluminate solution seed crystals, and belongs to the field of metallurgy technology. Background technique [0002] The production of alumina by Bayer method has the characteristics of simple process, convenient operation and high product quality. At present, more than 90% of the alumina produced in the world is produced by the Bayer process. In the process of producing alumina by the Bayer process, adding seeds to supersaturated sodium aluminate solution for decomposition reaction is one of the important processes, usually called "seed decomposition process", referred to as "seed separation process". Add a large amount of aluminum hydroxide as a seed crystal to the sodium aluminate solution to induce crystallization and growth of aluminum hydroxide crystals, decompose the supersaturated sodium alumi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/14C01F7/144
CPCB01D9/0036C01F7/144
Inventor 苏向东胡大乔何力丁元法李丹宁薛涛金开胜李勇黄健罗宏刘洪波熊永昇李刚谭春生
Owner GUIZHOU R & D CENT ON MODERN MATERIALS
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