Unlock instant, AI-driven research and patent intelligence for your innovation.

A method for producing industrial grade and battery grade monoammonium phosphate with fertilizer grade monoammonium phosphate

A monoammonium phosphate, battery-grade technology, applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problems of high production risk, troublesome regeneration, large amount of resin, etc.

Active Publication Date: 2018-11-09
湖北云翔聚能新能源科技有限公司
View PDF12 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The raw material used in this method is agricultural crystalline monoammonium phosphate, and the raw material cost is relatively high; and the method utilizes resin treatment, and the resin consumption is large, and regeneration is troublesome, and the process is long, the production speed is slow, and the cost is high, so it is not suitable for industrial production
Chinese patent CN105819414A reports a production process of battery-grade monoammonium phosphate, which mainly uses a certain proportion of phosphoric acid solution containing less impurities to neutralize with ammonia, adjusts a certain pH, and then obtains battery-grade monoammonium phosphate through cooling and crystallization. However, the purity of phosphoric acid used in this process is high, so the production cost is high, and the general battery-grade monoammonium phosphate is mainly generated by the reaction of high-purity thermal phosphoric acid and ammonia. Although the production process equipment is simple, the equipment and technology requirements are high, and the production is dangerous. Big, heavy pollution, high energy consumption;

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] a. Dissolve 600g of powdered chemical fertilizer monoammonium phosphate in 800g of pure water, heat to 40°C and stir for 30min, mix evenly and filter, and the filtrate is ready for use;

[0015] b. Into the filtrate obtained in step a, pass 5% of the decolorizing agent ozone into the filtrate mass, let stand for decolorization for 5 hours, add precipitant ammonia water and sodium carbonate, adjust pH=4, fully mix and stir evenly, let stand for 5 hours, filter, and the filtrate is set aside ;

[0016] c. Continue to add the precipitating agent ammonia water and potassium carbonate to the filtrate obtained in step b, adjust the pH=6, fully mix and stir evenly, let stand for 5h, filter, and the filtrate is set aside;

[0017] d. Continue to add the filtrate obtained in step c to potassium sulfide and sodium hydroxide, an impurity removal agent of 5% of the filtrate mass, fully mix and stir evenly, leave it for 0.5h, filter, and the filtrate is set aside;

[0018] e. ...

Embodiment 2

[0023] a. Dissolve 600g of powdered chemical fertilizer monoammonium phosphate in 800g of pure water, heat to 70°C and stir for 20 minutes, mix evenly and filter, and the filtrate is set aside;

[0024] b. Add 10% decolorizing agent calcium hypochlorite to the filtrate obtained in step a, let stand for decolorization for 12 hours, add precipitant ammonia water and ammonium carbonate, adjust pH=5, mix well and stir evenly, let stand for 3 hours, filter, and filtrate stand-by;

[0025] c. Continue to add the precipitant ammonia water and sodium carbonate to the filtrate obtained in step b, adjust the pH=7.5, fully mix and stir evenly, let stand for 3.5h, filter, and the filtrate is set aside;

[0026] d. Continue to add the filtrate obtained in step c to the impurity-removing agents sodium sulfide and potassium hydroxide of 2% of the filtrate quality, fully mix and stir evenly, let stand for 3.5h, filter, and the filtrate is set aside;

[0027] e. Heat the filtrate in b to...

Embodiment 3

[0032] a. Dissolve 600g of powdered fertilizer monoammonium phosphate in 800g of pure water, heat to 95°C and stir for 5 minutes, mix evenly and filter, and the filtrate is set aside;

[0033] b. Add 20% decolorizing agent hydrogen peroxide to the filtrate obtained in step a, let stand for decolorization for 25 hours, add precipitant ammonia water and potassium hydroxide, adjust pH=6, mix well and stir evenly, let stand for 5 hours, filter, and filtrate stand-by;

[0034] c. Continue to add the precipitating agent ammonia water and sodium hydroxide to the filtrate obtained in step b, adjust the pH=9, fully mix and stir evenly, let stand for 0.5h, filter, and the filtrate is set aside;

[0035] d. Continue to add the filtrate obtained in the c step to the impurity removal agent potassium sulfide and ammonium carbonate of 0.1% of the filtrate quality, fully mix and stir evenly, let stand for 5h, filter, and the filtrate is set aside;

[0036] e. Heat the filtrate in b to 9...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a method for producing industrial first-stage and battery-stage monoammonium phosphate by using fertilizer-stage monoammonium phosphate. The fertilizer-stage monoammonium phosphate is heated and dissolved by pure water and is then filtered; then, decolorizing agents and precipitants are added into filter liquid; after the pH value is regulated to a certain value, filtration is performed; filter liquid a is obtained; the filter liquid a is heated and concentrated and is then cooled for crystallization; after drying, the industrial first-stage monoammonium phosphate is obtained; if the precipitants are continuously added into the filter liquid a, filtering is performed after the pH value regulation; then, impurity removal medicaments are added into the filter liquid; still standing is performed; after impurities are separated out, filtering is performed; cooling crystallization is performed after the filter liquid is heated and concentrated; drying is performed; then, the battery-stage monoammonium phosphate is obtained. The powdery fertilizer-stage monoammonium phosphate with high impurity content and low price is used for producing the industrial first-stage and battery-stage monoammonium phosphate; in addition, three wastes in the production are totally recovered for fertilizer production; the process is reliable; the equipment is simple; the production safety is high; the energy is saved; the consumption is reduced; the production cost is greatly reduced.

Description

technical field [0001] The invention relates to a method for purifying powdered chemical fertilizer monoammonium phosphate, in particular to a powdery chemical fertilizer monoammonium phosphate containing more impurities such as sulfur, iron, magnesium, aluminum, manganese, titanium, etc. Monoammonium Phosphate method. Background technique [0002] As a compound with high nitrogen and phosphorus content, monoammonium phosphate is widely used in agricultural production, but fertilizer monoammonium phosphate is a low-end product with low added value. With the oversupply of phosphate fertilizer production in the world, market competition has intensified, and fertilizer monoammonium phosphate The profit margin of ammonium is further reduced, so it is imminent to expand new application fields of fertilizer ammonium dihydrogen phosphate, especially low-cost fertilizer monoammonium phosphate. Compared with low-end fertilizer monoammonium phosphate: industrial grade monoammonium ph...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C01B25/28
CPCC01B25/28C01P2006/80
Inventor 陶升东李荐周宏明李先柏
Owner 湖北云翔聚能新能源科技有限公司