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Method for producing industrial and agricultural monoammonium phosphate and magnesium ammonium phosphate with wet-process phosphoric acid

A technology of high-grade monoammonium phosphate and wet-process phosphoric acid, which is applied in the chemical industry, can solve the problems of not meeting the requirements of fully water-soluble phosphate fertilizers, poor water solubility of products, and low production costs, so as to save the desulfurization process, solve subsequent processing problems, and avoid The effect of fluorine pollution

Active Publication Date: 2011-04-20
昆明隆祥化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Both methods belong to a one-stage neutralization process. Although the scale is large and the production cost is low, they can only produce agricultural-grade monoammonium phosphate, and the product has poor water solubility, which cannot meet the requirements of modern facility agriculture for fully water-soluble phosphate fertilizers.
Although some manufacturers use the two-stage neutralization process to produce industrial-grade monoammonium phosphate, the filter cake of the two-stage neutralization method needs the support of the traditional one-stage neutralization method system to be converted into qualified agricultural grade monoammonium phosphate Ammonium, the ammonium phosphate solution after magnesium removal needs to adjust the pH value with thermal phosphoric acid to produce industrial grade monoammonium phosphate, so its cost is still high

Method used

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  • Method for producing industrial and agricultural monoammonium phosphate and magnesium ammonium phosphate with wet-process phosphoric acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] A, get 8000 grams of wet dilute phosphoric acid from a phosphate fertilizer factory (wherein: P 2 o 5 24.11%; F1.67%; SO 3 1.97%; CaO 0.25%; MgO1.06%; Fe 2 o 3 0.87%; AL 2 o 3 0.49%), slowly add 126 grams of industrial-grade sodium carbonate, fully react for 1 hour under normal temperature stirring, filter and separate the filtrate and filter residue, wash the filter residue with 200 grams of water, and then dry it to obtain 150 grams of sodium fluorosilicate product (Na 2 SiF 6 Content 98.10%), wash water and merge in the filtrate, then add 1400 grams of water and dilute to obtain 9460 grams of defluorinated dilute phosphoric acid;

[0032] B, get A step gained defluorinated dilute phosphoric acid 7730 grams, slowly add technical grade ammonium bicarbonate under stirring at normal temperature and carry out neutralization reaction to pH value 4.6 rear filtration separation, filtrate is monoammonium phosphate solution, and filter cake is subsequent use;

[003...

Embodiment 2

[0038] A, get 8000 grams of wet dilute phosphoric acid from a phosphate fertilizer factory (wherein: P 2 o 5 24.11%; F1.67%; SO 3 1.97%; CaO 0.25%; MgO1.06%; Fe 2 o 3 0.87%; AL 2 o 3 0.49%), slowly add 95 grams of industrial-grade sodium hydroxide, fully react for 1 hour under normal temperature stirring, and then filter and separate the filtrate and filter residue; wash the filter residue with 200 grams of water several times until it is acid-free, and dry to obtain 151 grams of sodium fluorosilicate Product (Na 2 SiF 6 Content 98.05%), wash water and merge in the filtrate, then add 1400 grams of water to dilute to obtain 9480 grams of defluorinated dilute phosphoric acid;

[0039] B. Take 7200 grams of defluorinated dilute phosphoric acid obtained in step A, and slowly add industrial grade ammonium bicarbonate under normal temperature stirring to carry out neutralization reaction to pH value 4.9 and then filter and separate. The filtrate is monoammonium phosphate so...

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Abstract

The invention provides a method for producing industrial and agricultural grade monoammonium phosphate and magnesium ammonium phosphate with wet-process phosphoric acid. The wet-process phosphoric acid is taken as a raw material. Sodium fluosilicate, monoammonium phosphate solution, monoammonium phosphate filter cakes and magnesium ammonium phosphate are respectively obtained through defluorination and a three-section substep neutralization process, wherein the monoammonium phosphate solution is concentrated and crystallized to obtain high-quality water soluble industrial monoammonium phosphate, and the monoammonium phosphate filter cakes and the monoammonium phosphate mother solution subjected to repeated crystallization are subjected to size mixed and dried to obtain qualified agricultural monoammonium phosphate. The magnesium ammonium phosphate is a good slow release nitrogenous fertilizer per se. The process has the advantages of little investment of equipment, good adaptability of raw material, low production cost and good product quality. The water soluble industrial monoammonium phosphate with low cost can provide a cheap and good water soluble phosphatic fertilizer for modern facility agriculture.

Description

technical field [0001] The invention relates to a method for producing monoammonium phosphate and magnesium ammonium phosphate, in particular to a method for graded production of industrial grade monoammonium phosphate and agricultural grade monoammonium phosphate and magnesium ammonium phosphate by wet-process phosphoric acid, belonging to the technical field of chemical industry. Background technique [0002] With the popularization of modern facility agriculture, the market demand for fully water-soluble phosphate fertilizers is increasing. The traditional monoammonium phosphate production process such as "concentration method" is to concentrate phosphoric acid first, and then neutralize it with ammonia; while "dilute acid slurry method" is to neutralize phosphoric acid with ammonia first, then concentrate and dry it. Both methods belong to a one-stage neutralization process. Although the scale is large and the production cost is low, they can only produce agricultural-gr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/28C01B25/45
Inventor 马健李庆
Owner 昆明隆祥化工有限公司
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