Check patentability & draft patents in minutes with Patsnap Eureka AI!

Method for co-producing industrial grade diammonium phosphate during production of industrial grade monoammonium phosphate of phosphoric acid by wet process

A technology of high-grade diammonium phosphate and wet-process phosphoric acid, which is applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problems of unstable product quality, large pollution, high production cost and energy consumption of diammonium phosphate, and increase product diversity Sexuality, lower production costs, and enhanced competitiveness

Active Publication Date: 2013-04-03
GUIZHOU KAILIN GRP CO LTD
View PDF5 Cites 21 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The purpose of the present invention is to provide a method for wet-process phosphoric acid to produce industrial-grade monoammonium phosphate and co-produce industrial-grade diammonium phosphate, so as to solve the problem of high production cost, high energy consumption, large pollution, and poor product quality in the production of monoammonium phosphate and diammonium phosphate in the prior art. unstable problem

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

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for co-producing industrial grade diammonium phosphate during production of industrial grade monoammonium phosphate of phosphoric acid by wet process
  • Method for co-producing industrial grade diammonium phosphate during production of industrial grade monoammonium phosphate of phosphoric acid by wet process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Will P 2 o 5 Wet-process phosphoric acid with a concentration of 25% is sent into the desulfurization tank, and the sulfate content is analyzed by sampling. The amount of calcium hydrogen phosphate added is 0.85 to 1.0 times the amount of sulfate. In the neutralization tank, feed ammonia gas into the neutralization tank under the condition of stirring, stop the ammonia flow when the pH value of the slurry is 4.3, filter the slurry while it is hot, and send the filter cake to the compound fertilizer device to produce compound fertilizer, the filtrate Enter the purification tank; add ammonium sulfide solution in the purification tank, stir the reaction to remove impurities, and filter out the filter residue after passing the inspection. After the filter residue is collected, it is used to extract the metal, and the filtrate enters the concentrated crystallization tank. When the specific gravity reaches 1.32, the concentration is stopped. , into the cooling crystallizatio...

Embodiment 2

[0028] Add P in the neutralization tank 2 o 5 The wet-process phosphoric acid with a concentration of 35% is sent into the desulfurization tank, and the sulfate content is analyzed by sampling. The amount of calcium hydrogen phosphate added is 0.85 to 1.0 times the amount of sulfate. In the neutralization tank, add ammonia water with a mass concentration of 25% while stirring, stop adding ammonia water when the pH value of the ammonium phosphate slurry is 4.2, filter the slurry while it is hot, send the filter cake to the compound fertilizer device to produce compound fertilizer, and send the filtrate to into the purification tank; add ammonium sulfide solution in the purification tank to further remove impurities, and after passing the inspection, the filtrate enters the concentration tank for concentration, stops concentration when the specific gravity in the concentration tank reaches 1.29, and sends it into the cooling crystallization tank at a temperature of 35°C. Filtra...

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 co-producing industrial grade diammonium phosphate during the production of industrial grade monoammonium phosphate of phosphoric acid by a wet process. The method comprises the steps of: making filtrate obtained after carrying out desulfurization on calcium hydrophosphate and wet-process phosphoric acid neutralize with ammonia gas or ammonia water to obtain ammonium phosphate slurry, making ammonium sulfide react with the ammonium phosphate slurry, and concentrating, crystallizing and drying the filtrate to obtain an industrial grade monoammonium phosphate product; secondly, making a primary mother solution obtained through filtering after crystallizing secondarily neutralize with the ammonia gas or ammonia water; and finally, concentrating, crystallizing and drying the filtrate obtained through secondary neutralizing to obtain an industrial grade diammonium phosphate product, and returning a secondary mother solution obtained through filtering after crystallizing to a concentrating tank and continuously concentrating. The method is used for co-producing the diammonium phosphate during the production of the monoammonium phosphate, has the advantages of saving production cost, reducing energy consumption, reducing pollution and ensuring quality of the monoammonium phosphate and the diammonium phosphate through effective impurity removal, and has good economic benefits.

Description

technical field [0001] The invention relates to a method for producing industrial-grade monoammonium phosphate by wet-process phosphoric acid and co-producing industrial-grade diammonium phosphate. Background technique [0002] Industrial grade monoammonium phosphate and diammonium phosphate are widely used in fire protection, drip irrigation fertilizer, medicine and food. At present, the production of industrial grade monoammonium phosphate and diammonium phosphate generally adopts thermal phosphoric acid or purified phosphoric acid process. The disadvantages are high production cost, complicated process, high energy consumption and large pollution. Some manufacturers also adopt the wet-process phosphoric acid production process, but there are certain problems in the impurity removal process, such as high metal content in the product, which will change with the quality of phosphoric acid, making it difficult to guarantee product quality. In the prior art, the production eq...

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
IPC IPC(8): C01B25/28
Inventor 廖吉星朱飞武彭宝林潘礼富周勇郑超宋同斌王先炜谢静张丽韩朝应张强星
Owner GUIZHOU KAILIN GRP CO LTD
Features
  • R&D
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More