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Method for producing fully water-soluble monoammonium phosphate and co-producing ammonium magnesium phosphate by wet process phosphoric acid

A technology of water-soluble monoammonium phosphate and wet-process phosphoric acid, which is applied in the fields of phosphate, phosphorus oxyacids, chemical instruments and methods, etc., can solve the problems of product impurity, filtration and impurity removal, etc., to improve production efficiency and benefit, Good filtration performance, enhanced purity and solubility effects

Active Publication Date: 2016-02-03
SHENZHEN BATIAN ECOTYPIC ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the above method has defects in the purification of wet-process phosphoric acid. After the first neutralization, the first neutralization is directly ammoniated to pH=4.5-5.0, and the crystals formed by metal ions such as iron and aluminum have not had time to grow into large crystals, making It is very difficult to remove impurities by filtration; when the pH is controlled at 5.8-6.2 during the production of ammonium magnesium phosphate, the by-product diammonium phosphate will be formed and the product will be impure, and the pH needs to be adjusted again accurately to ensure the concentration of monoammonium phosphate Purity, which increases the difficulty and cost of production

Method used

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  • Method for producing fully water-soluble monoammonium phosphate and co-producing ammonium magnesium phosphate by wet process phosphoric acid

Examples

Experimental program
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Effect test

Embodiment 1

[0042] S10. Add 20 g of sodium sulfate to the raw material liquid of wet-process phosphoric acid, react at room temperature for 1-2 hours to perform pre-defluorination, remove 70% of fluorine in wet-process phosphoric acid, filter to obtain defluorinated filtrate and filter residue, and use 50 g of filter residue to deionize The water was washed several times until it was acid-free, and 23g of sodium fluorosilicate product was obtained after drying. Since the washing water contained the material components of wet-process phosphoric acid, it was returned to the defluorination filtrate during operation to avoid waste of raw materials, and 1040g of defluorination filtrate was obtained. Fluorine wet-process phosphoric acid.

[0043] S20, passing ammonia gas into 1040 g of defluorinated wet-process phosphoric acid obtained in the step S10 to carry out ammoniation once until the pH is 2.5, and aging for 20 minutes to obtain the first aging solution;

[0044] S30, feeding gaseous amm...

Embodiment 2

[0049] S10. Add 24g of sodium nitrate to the raw material liquid of wet-process phosphoric acid, react at room temperature for 1-2 hours for pre-defluorination, filter to obtain defluorination filtrate and filter residue, filter residue with 50g of deionized water until it is acid-free, and dry to obtain 24g sodium fluorosilicate product, washing water is returned in the defluorination filtrate, always gets 1045g of defluorination filtrate.

[0050] S20, pass gas ammonia into the 1045g defluorination filtrate obtained in step S10 to carry out ammoniation for the first time until the pH is 2.4, and age for 20min to obtain the first aging liquid;

[0051] S30, inject gaseous ammonia into the first aging liquid to carry out the second ammoniation to pH = 4.6, and centrifuge to obtain the supernatant liquid and the bottom slag liquid;

[0052] S40, 945g of the supernatant obtained in the S30 step is concentrated to 62%, after cooling and crystallization for 1h, centrifuged to obta...

Embodiment 3

[0056] S10. Add 20 g of sodium sulfate to the wet-process phosphoric acid raw material liquid, react at room temperature for 1 to 2 hours for pre-defluorination, filter to obtain the defluorination filtrate and filter residue, wash the filter residue with 50 g of deionized water until it is acid-free, and dry it to obtain 23g of sodium fluorosilicate product, because the washing water contains the material composition of wet-process phosphoric acid, so it is returned in the defluorination filtrate during operation, and a total of 1040g of defluorination filtrate is defluorinated wet-process phosphoric acid.

[0057] S20, passing ammonia gas into 1040 g of defluorinated wet-process phosphoric acid obtained in step S10 to carry out ammoniation once until the pH is 2.0, and aging for 10 minutes to obtain the first aging solution;

[0058] S30, feeding gaseous ammonia into the first aging liquid to carry out the second ammoniation until the pH is 4.0, and then obtaining the superna...

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Abstract

The invention provides a method for producing fully water-soluble monoammonium phosphate and co-producing ammonium magnesium phosphate by a wet process phosphoric acid. The method comprises the following steps: deflurinating the wet process phosphoric acid and taking deflurinating filtrate; carrying out first ammoniated treatment on the deflurinating filtrate until the pH value is 2.0-3.0, and then first ageing to obtain a first ageing solution; carrying out second ammoniated treatment on the first ageing solution until the pH value is 4.0-5.0, and carrying out solid-liquid separation to obtain supernatant liquid and bottom slag liquid; carrying out concentration, crystallization and crystal-liquid separation on the supernatant liquid to obtain a crystal substance which is a monoammonium phosphate product; and carrying out third ammoniated treatment on the bottom slag liquid until the pH value is 5.6-6.0, carrying out second ageing and drying to obtain an ammonium magnesium phosphate product. According to the method provided by the invention, products of the fully water-soluble monoammonium phosphate and the ammonium magnesium phosphate are produced by three ammoniated treatments and one separation, iron and aluminum crystals gradually grow by ageing for a period of time after the first ammoniated treatment, precipitate particle size is increased, filtering performance is improved, impurity ions can be totally precipitated by the second ammoniated treatment, and water solubility of the monoammonium phosphate product is improved remarkably.

Description

technical field [0001] The invention belongs to the technical field of phosphoric acid agricultural fertilizer production, and in particular relates to a method for producing fully water-soluble monoammonium phosphate and co-producing magnesium ammonium phosphate with wet-process phosphoric acid. Background technique [0002] With the development of modern agriculture, the original artificial irrigation method is gradually replaced by large-scale sprinkler irrigation facilities. Originally suitable for artificial irrigation, the fertilizer monoammonium phosphate produced by the traditional "concentration method" and "dilute acid slurry method" has poor water solubility and contains more insoluble metal salt impurities, which may easily cause blockage of drip irrigation heads in drip irrigation facilities. [0003] In order to solve the above problems, Ma Jian et al. used wet-process phosphoric acid as raw material in CN102020256A patent to produce industrial monoammonium pho...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/28C01B25/45
Inventor 沈鹏鹏江寿良禇红艳
Owner SHENZHEN BATIAN ECOTYPIC ENG
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