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Method for producing large dicalcium phosphate crystals by utilizing seed crystals and returned material

A calcium hydrogen phosphate, large crystal technology, applied in chemical instruments and methods, phosphorus compounds, inorganic chemistry and other directions, can solve the problems of increased labor intensity of packaging, difficult control of unit weight, difficult solid-liquid separation, etc., to improve the packaging environment, The effect of reducing the manpower of packaging and improving the process

Active Publication Date: 2015-04-29
YUNNAN COPPER IND SUNWARD CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this process, there are two reaction tanks, and they are single-connected, without returning materials (such as figure 1 ), produced fine crystals with an average particle size of 130 μm, 30% of which were below 60 μm, which brought difficulties in the process of solid-liquid separation, and the moisture content was as high as 28%, and the phosphorus yield was 98.3%. The large proportion of crystals increases the labor intensity of the packaging, and the unit weight is difficult to control

Method used

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  • Method for producing large dicalcium phosphate crystals by utilizing seed crystals and returned material
  • Method for producing large dicalcium phosphate crystals by utilizing seed crystals and returned material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] (1) In the conventional production process of calcium hydrogen phosphate, the neutralization reaction first tank and the second neutralization reaction tank are connected by adding lime milk to adjust the pH, and then the neutralization reaction is carried out according to the return ratio L / L of 1:12. Part of the slurry in the second tank is returned to the first tank of neutralization reaction by stirring, thereby reducing the supersaturation of the first tank of neutralization reaction and increasing the crystal growth time; controlling the pH of the first tank of neutralization reaction to 4.0, and the second tank of neutralization reaction The pH is 4.8, which creates a good environment for the crystallization process, and the growth rate is accelerated at this time;

[0018] (2) Put the slurry reacted in the second tank of neutralization reaction in step (1) into the third tank of neutralization reaction, and add milk of lime to adjust the pH to 6.3. At this time, ...

Embodiment 2

[0022] (1) In the conventional production process of calcium hydrogen phosphate, the first neutralization reaction tank and the second neutralization reaction tank are connected by adding lime milk to adjust the pH, and then the neutralization reaction is carried out according to the return ratio L / L of 1:15. Part of the slurry in the second tank is returned to the first tank of neutralization reaction by stirring, thereby reducing the supersaturation of the first tank of neutralization reaction and increasing the crystal growth time; controlling the pH of the first tank of neutralization reaction to 3.5, and the second tank of neutralization reaction The pH is 4.5, which creates a good environment for the crystallization process, and the growth rate is accelerated at this time;

[0023] (2) Put the slurry reacted in the second tank of the neutralization reaction in step (1) into the third tank of the neutralization reaction, and add milk of lime to adjust the pH to 6.0. At thi...

Embodiment 3

[0027] (1) In the conventional production process of calcium hydrogen phosphate, the neutralization reaction first tank and the second neutralization reaction tank are connected by adding lime milk to adjust the pH, and then the neutralization reaction is carried out according to the return ratio L / L of 1:20. Part of the slurry in the second tank is returned to the first tank of neutralization reaction by stirring, thereby reducing the supersaturation of the first tank of neutralization reaction and increasing the crystal growth time; controlling the pH of the first tank of neutralization reaction to 3.6, and the second tank of neutralization reaction The pH is 4.6, which creates a good environment for the crystallization process, and the growth rate is accelerated at this time;

[0028] (2) Put the slurry reacted in the second tank of neutralization reaction in step (1) into the third tank of neutralization reaction, and add milk of lime to adjust the pH to 6.2. At this time, ...

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Abstract

The invention provides a method for producing large dicalcium phosphate crystals by utilizing seed crystals and a returned material. The method comprises the following steps: returning a part of slurry in a second neutralization reaction tank into a first neutralization reaction tank, and controlling the pH value of the neutralization reaction tank; causing the slurry reacted in the second neutralization reaction tank to enter a third neutralization reaction tank, and adding lime milk to regulate the pH value; fractionating the slurry in the third neutralization reaction tank, concentrating coarse grains with grain sizes of more than 150 [mu]m to obtain a dicalcium phosphate semi-finished product, performing solid-liquid separation to obtain solids, drying the solids to obtain the large dicalcium phosphate crystals, and causing discharged fine crystals with grain sizes of smaller than 150[mu]m to enter the first neutralization reaction tank as the reaction seed crystals. According to the method, the moisture content of a separated solid phase can be reduced without reducing the phosphorus yield, a drying system and procedures of packaging and the like are greatly improved, coal power consumption is reduced, the packaging environment is improved, and packaging labor is reduced.

Description

technical field [0001] The invention relates to a method for producing large-crystal feed-grade calcium hydrogen phosphate with wet-process phosphoric acid, in particular to a method for producing large-crystal calcium hydrogen phosphate by using crystal seeds and returning materials. Background technique [0002] The current method of producing calcium hydrogen phosphate is to react phosphoric acid pulp with sulfuric acid to generate phosphoric acid, and then separate the liquid and solid after filtration to obtain phosphoric acid, then add limestone powder for rough adjustment, and finely adjust lime milk to control the neutralization pH value, so as to meet the standard for producing feed grade calcium hydrogen phosphate For the required phosphoric acid, after clarification and removal of impurities, lime milk is added to neutralize the pH to 6-6.3 to generate calcium hydrogen phosphate. In this process, there are two reaction tanks, and they are single-connected, without...

Claims

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Application Information

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IPC IPC(8): C01B25/32
Inventor 赵玉群赵磊
Owner YUNNAN COPPER IND SUNWARD CHEM
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