Method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction

A metathesis reaction and potassium nitrate technology, applied in the direction of ammonium halide, alkali metal nitrate preparation, etc., can solve the problems of high equipment requirements, high evaporation cost, high price of sodium nitrate, etc., achieve high degree of automation, compact equipment structure, improve transmission Effect of Thermal Coefficient

Inactive Publication Date: 2010-01-20
湖南丹化农资有限公司
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Problems solved by technology

Domestic potassium nitrate production methods mainly include: sodium nitrate-potassium chloride conversion method, mixing sodium nitrate and potassium chloride to an appropriate concentration, reacting at 80-90°C, and then evaporating while separating out sodium chloride and separating out Sodium chloride: properly dilute the mother liquor to prevent the precipitation of sodium salt, and then cool to about 5°C to precipitate the product potassium nitrate. After the crude product is centrifugally filtered and washed, potassium nitrate can be obtained. The product can be recrystallized to obtain industrial grade potassium nitrate. Disadvantages The price of sodium nitrate is high and resources are tight, and the use value and economic value of the by-product sodium chloride are low. In addition, due to the accumulation of impurities in the mother liquor, the mother liquor needs to be discharged regularly, which also affects the yield of potassium nitrate.
The ammonium nitrate-potassium chloride conversion method was first successfully developed by the French Auby company. The reaction of ammonium nitrate and potassium chloride produces potassium nitrate and by-product ammonium chloride. After the reaction, the solution is composed of potassium chloride, ammonium nitrate, and potassium nitrate. , ammonium chloride composition, from the analysis of the phase diagram, it can be seen that the isothermal diagram is divided into four phase crystallization regions. When the temperature is lowered, the content of potassium nitrate in the mixed solution is large, and the crystallization region incr

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  • Method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction
  • Method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction
  • Method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction

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[0033] by attached figure 1 , figure 2 , image 3 , Figure 4 Shown, a kind of metathesis reaction produces the method for potassium nitrate and ammonium chloride, is raw material with ammonium nitrate and potassium chloride, carries out metathesis production potassium nitrate and by-product ammonium chloride with mother liquor circulation, and reaction formula is:

[0034] NH 4 NO 3 +KCI→KNO 3 +NH 4 CI

[0035] The technological process for producing potassium nitrate and ammonium chloride is:

[0036] A. When starting production, heat the water, add ammonium nitrate and potassium chloride, and dissolve ammonium nitrate and potassium chloride in water at a temperature of 110°C in a ratio of 1:2 between ammonium ions and chloride ions, and place in the reaction Carry out metathesis reaction in the still, form the generation material that reaches the initial co-saturation point of potassium nitrate and ammonium chloride;

[0037] B. In the reaction kettle, continue to...

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Abstract

A method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction comprises the following steps: dissolving ammonium nitrate and potassium chloride in water according to a defined ratio at 110 DEG C, continuously adding potassium chloride and water, heating while stirring to ensure that potassium nitrate is in supersaturation state, after stopping heating, cooling the solution in a vacuum cooling crystallizer to 36-40 DEG C to separate potassium nitrate crystal, placing the potassium nitrate crystal in a centrifugal machine with a filter cloth lining to obtain coarse potassium nitrate, then washing the potassium nitrate with cold water, drying to obtain the finished potassium nitrate; in addition, adding ammonium nitrate in mother solution I and cleaning solution to adjust solution concentration so that ammonium chloride can reach supersaturation state, using a vacuum concentration device to perform negative pressure evaporation, separating and precipitating ammonium chloride by centrifuging and obtaining a solid ammonium chloride product, wherein, when dissolving ammonium nitrate and potassium chloride, the ratio of ammonium ion to chlorine ion is 1:2 and when using the centrifugal machine to obtain the coarse potassium nitrate, the separated mother solution is another mother solution I sharing the same saturation point of potassium nitrate and ammonium chloride. The solution of feed liquid circular reaction overcomes the defects of the prior art that the price of potassium nitrate used in reaction is high, the resource of potassium nitrate is in short supply and the cost of devices used in ion-exchange method is high, thus being applicable to the production of potassium nitrate.

Description

technical field [0001] The invention relates to a method for producing potassium nitrate and ammonium chloride by metathesis reaction. Background technique [0002] Potassium nitrate is an important inorganic chemical product. Industrial potassium nitrate is mainly used to make black gunpowder, fireworks, matches, glass products and optical glass, etc. Agricultural potassium nitrate is a high-quality compound fertilizer. For a long time, potassium nitrate The market is in short supply and is a product in short supply. Domestic potassium nitrate production methods mainly include: sodium nitrate-potassium chloride conversion method, mixing sodium nitrate and potassium chloride to an appropriate concentration, reacting at 80-90°C, and then evaporating while separating out sodium chloride and separating out Sodium chloride: properly dilute the mother liquor to prevent the precipitation of sodium salt, and then cool to about 5°C to precipitate the product potassium nitrate. Afte...

Claims

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Application Information

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IPC IPC(8): C01D9/10C01C1/16
Inventor 左启群
Owner 湖南丹化农资有限公司
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