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Desalting and reusing method of high-salinity heavy ash mother liquor in combined-soda system

A technology of high-salt heavy ash mother liquor and heavy ash, which is applied to alkali metal carbonates, chemical instruments and methods, alkali metal compounds, etc., can solve the problems of mother liquor expansion in the system and affect product quality, so as to reduce the expansion of mother liquor and reduce the The effect of accumulating and reducing calcium content

Active Publication Date: 2015-04-22
TIANJIN BOHUA YONGLI CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the high-salt heavy ash mother liquor discharged from the combined alkali system is mainly used for brine refining or as a raw material for the production of baking soda, but with the recycling of the mother liquor, the system mother liquor will expand and affect the product quality

Method used

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  • Desalting and reusing method of high-salinity heavy ash mother liquor in combined-soda system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] The content of sodium chloride in the heavy ash mother liquor is 60g / L, and the effluent heavy ash mother liquor (sodium carbonate content is 310g / L) enters the evaporation device to evaporate, and the evaporation of the solution reaches carbonic acid when it is about 79% of the total solution mass. The co-saturation point of sodium and sodium chloride causes sodium carbonate monohydrate crystals to separate out, and liquid-solid separation is carried out. The obtained crystals are dissolved in desalinated water to obtain a solution with a sodium chloride content of about 7.8g / L, and the solution is returned to heavy The ash system is reused; the remaining high-salt heavy ash mother liquor after evaporation is used for the salt washing process in the vacuum salt production.

[0021] After testing, the content of sodium carbonate in the low-salt heavy ash mother liquor recycled to the heavy ash system after treatment is about 307g / L, and the content of sodium chloride is ...

Embodiment 2

[0023] Sodium chloride content is 80g / L in the heavy ash mother liquor, the heavy ash mother liquor (sodium carbonate content is 310g / L) of effluent liquid is sent into evaporating device and evaporates, and the evaporation of solution reaches when about 72% of total solution mass. The co-saturation point of sodium carbonate and sodium chloride causes sodium carbonate monohydrate crystals to separate out, and liquid-solid separation is carried out, and the crystal obtained is dissolved in desalinated water to obtain a solution with a sodium chloride content of about 8.3g / L, and the solution is returned to The heavy ash system is reused, and the remaining high-salt heavy ash mother liquor after evaporation is used for the salt washing process in the vacuum salt making process.

[0024] After testing, the content of sodium carbonate in the low-salt heavy ash mother liquor recycled to the heavy ash system after treatment is about 312g / L, and the content of sodium chloride is about...

Embodiment 3

[0026] The content of sodium chloride in the heavy ash mother liquor is 100g / L, and the heavy ash mother liquor (sodium carbonate content is 310g / L) of the effluent liquid is sent to the evaporator for evaporation, and the evaporation of the solution is about 66% of the total mass of the solution. The co-saturation point of sodium carbonate and sodium chloride causes sodium carbonate monohydrate crystals to separate out, and liquid-solid separation is carried out, and the crystal obtained is dissolved in demineralized water to obtain a solution with a sodium chloride content of about 8.9g / L, and the solution is returned to The heavy ash system is reused, and the remaining high-salt heavy ash mother liquor after evaporation is used for the salt washing process in the vacuum salt making process.

[0027] After testing, the content of sodium carbonate in the low-salt heavy ash mother liquor recycled to the heavy ash system after treatment is about 314g / L, and the content of sodium...

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Abstract

The invention discloses a desalting and reusing method of high-salinity heavy ash mother liquor in a combined-soda system, which comprises the following steps that (1) when the sodium chloride content of heavy ash mother liquor is higher than 60 g / L, a part of high-salinity heavy ash solution is required to be discharged, and the discharged solution is conveyed to an evaporator to evaporate; (2) the discharged high-salinity heavy ash solution is evaporated to the co-saturated point of sodium carbonate and sodium chloride, so that monohydrate sodium carbonate crystals are precipitated out, and the monohydrate sodium carbonate crystals are separated from residual mother liquor after evaporating; and (3) the separated crystals are dissolved, so that a solution with a sodium chloride content of less than 20 g / L is obtained, and the solution is returned to a heavy ash system to reuse; and the residual mother liquor is applied to a salt-leaching process of a vacuum salt manufacturing device. In a solution which can be reused in the system and obtained by using the method disclosed by the invention, the sodium chloride content of is less than 20 g / L, and the sodium carbonate content is about 310 g / L, so that the solution can meet the index requirements of the heavy ash system.

Description

technical field [0001] The present invention relates to a method for desalination and reuse of high-salt heavy ash mother liquor, and in particular to a method in which sodium carbonate in high-salt heavy ash mother liquor is reused in the heavy ash system, and the remaining solution after evaporation is used in the vacuum salt washing process . Background technique [0002] The use of liquid phase hydration for heavy ash production has the advantages of high hydration rate, uniform crystal particle size, and low salt content in the product, so it is widely used. But use this method to carry out heavy ash production process, along with the heavy ash product is separated out, and chloride ion is constantly accumulated in the heavy ash mother liquor, and the sodium chloride content in the mother liquor increases gradually, and when the sodium chloride content increases to a certain degree, it will affect Due to the salt content in the heavy ash product, it is necessary to dis...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D7/00
Inventor 王松晓庞栓林李治水谢智勇
Owner TIANJIN BOHUA YONGLI CHEM IND
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