Method for recycling crystalline alkali in unrefined solution full confluence production by sintering process

A technology of sintering method and crystallization alkali, applied in the direction of alumina/aluminum hydroxide, etc., can solve the problems of increased energy consumption and increased labor intensity

Inactive Publication Date: 2010-11-10
GUIZHOU BRANCH CHINA ALUMINUM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the sodium carbonate in the crude liquid of the sintering method enters the Bayer process and then crystallizes out, and then goes to the sintering method for batching, the aluminum oxide and caustic alkali in the crystallization alkali attachment liquid circulate ineffectively, and the energy consumption increases
Simultaneously, because of the allocation of no carbon fraction mother liquor, the sintering method stripping process adopts artificial alkali to ensure the concentration of sodium carbonate (see figure 1 Shown original process flow chart), increased labor intensity

Method used

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  • Method for recycling crystalline alkali in unrefined solution full confluence production by sintering process
  • Method for recycling crystalline alkali in unrefined solution full confluence production by sintering process
  • Method for recycling crystalline alkali in unrefined solution full confluence production by sintering process

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Experimental program
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Effect test

Embodiment 1

[0011] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 10:1m 3 / t, once washing liquid dissolves the crystallization alkali temperature 50 ℃, decrystallization alkali time, 10min solution composition Na 2 o C 25.50g / l;

Embodiment 2

[0013] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 10:1m 3 / t, the temperature of the crystallization alkali dissolved in the primary wash solution is 70°C, the time of the crystallization alkali solution, and the solution component Na is 10min 2 o C 32.6g / l;

Embodiment 3

[0015] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 2:1m 3 / t, once washing liquid dissolves the crystallization alkali temperature 50 ℃, decrystallization alkali time, 10min solution composition Na 2 o C 106.1g / l;

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Abstract

The invention provides a method for recycling a crystalline alkali in unrefined solution full combination production by a sintering process. In the method, the crystalline alkali of a Bayer process system is dissolved by using sintering process red mud primary cleansing solution; and the primary cleansing solution in which the crystalline alkali is dissolved is used as correction liquor for the dissolution of clinker. The method has the advantages of not only avoiding futile cycle of aluminum oxide and caustic alkali in crystalline alkali adhesion solution when ingredients are sintered, but also contributing to the transportation of alkaline red mud and the relief of labor intensity of manually dissolving alkalis.

Description

technical field [0001] The invention relates to a method for recovering and utilizing crystallized alkali in the full confluence production of crude liquid in sintering method. Background technique [0002] The global financial crisis has greatly reduced the price of alumina. In order to control losses and increase profits, Shanxi Branch decisively implemented the low-aluminum-silicon ratio clinker sintering technology, and the sintering method coarse liquid full confluence production technology—that is, the sintering method coarse liquid does not Then use the traditional coarse liquid medium-pressure desiliconization technology, but all merge with the high-pressure dissolution red mud slurry of the Bayer process to desilicate in the diluted tank of the Bayer process, thus canceling the carbon decomposition process in the traditional sintering process. It not only shortens the production process, but also saves electricity and new steam, and greatly reduces production costs....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/02
Inventor 李光柱王素刚张占明杨金妮郭庆山王军候炳毅于斌唐海红钱杰
Owner GUIZHOU BRANCH CHINA ALUMINUM IND
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