Method for joint production of ammonium sulphate and calcium carbonate with phosphogypsum

A technology of phosphogypsum and ammonium sulfate, applied in the direction of calcium carbonate/strontium/barium, chemical instruments and methods, ammonia compounds, etc., can solve the problems of high production cost, complex ammonia synthesis process, low calcium carbonate content, etc. Liquid contact area, the effect of improving the reaction rate

Inactive Publication Date: 2009-07-29
WENGFU (GRP) CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The annual discharge of phosphogypsum in my country has exceeded 50 million tons, which not only occupies a large amount of land, but also seriously pollutes the environment
[0003] At present, ammonium sulfate is mostly produced by neutralizing synthetic ammonia and sulfuric acid to produce ammonium sulfate, but the synthetic ammonia process is complicated, so the production cost is high and cannot meet the needs of the market
The type and content of impurities in the industrial waste phosphogypsum of wet-process phosphoric acid are relatively high, which affects the conversion rate of ammonium sulfate from phosphogypsum. However, the content of calcium carbonate in the product is low and the particle size is large, which cannot reach the level of rubber, paint, PVC and Plastic Filler Requirements

Method used

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  • Method for joint production of ammonium sulphate and calcium carbonate with phosphogypsum
  • Method for joint production of ammonium sulphate and calcium carbonate with phosphogypsum
  • Method for joint production of ammonium sulphate and calcium carbonate with phosphogypsum

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Experimental program
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Effect test

Embodiment 1

[0014] The method for utilizing phosphogypsum to co-produce ammonium sulfate and calcium carbonate may further comprise the steps:

[0015] (1) Phosphogypsum, the waste of high-concentration phosphate fertilizer production, is processed through pulping, rinsing, sedimentation, and screening to obtain phosphogypsum with an average particle size of 20 μm and a whiteness of 75, and make a slurry containing 30% phosphogypsum (phosphorus Calcium sulfate dihydrate content in gypsum is 94.5%), get 6.07kg and join in the reaction kettle that stirring device and heating device are housed, start stirring device, be warming up to 35 ℃, adjust the speed of mixer to be 60 rev / min, add fatty alcohol Disodium polyoxyethylene ether sulfosuccinate monoester 1.34g; add 23% (NH 4 ) 2 CO 3 4.18kg of the solution (the molar ratio of ammonium carbonate and calcium sulfate is 1:1), continue stirring for 1h; turn off the heating and stirring device, drop to room temperature, filter, adjust the pH o...

Embodiment 2

[0020] The method for utilizing phosphogypsum to co-produce ammonium sulfate and calcium carbonate may further comprise the steps:

[0021] (1) The waste phosphogypsum produced from the production of high-concentration phosphate fertilizers undergoes pulping, rinsing, sedimentation, and screening to obtain phosphogypsum with an average particle size of 100 μm and a whiteness of 85 to make a slurry of 40% phosphogypsum (phosphogypsum Calcium sulfate dihydrate content is 92.7%), gets 4.64kg and joins in the reaction kettle that stirring device and heating device are housed, starts stirring device, is warming up to 40 ℃, adjusts the speed of mixer to be 200 revs / min, adds stearic acid Polyethylene glycol (10000) ester 8.3g; Add containing 25.2%% (NH 4 ) 2 CO 3 4.19kg of the solution (the molar ratio of ammonium carbonate and calcium sulfate is 1.1:1), continue to stir for 1.5h; turn off the heating and stirring device, drop to room temperature, filter, adjust the pH=5.5 of the ...

Embodiment 3

[0026] The method for utilizing phosphogypsum to co-produce ammonium sulfate and calcium carbonate may further comprise the steps:

[0027] (1) Phosphogypsum, the waste of high-concentration phosphate fertilizer production, undergoes pulping, rinsing, sedimentation, and screening to obtain phosphogypsum with an average particle size of 70 μm and a whiteness of 80 to make a slurry of 35% phosphogypsum (phosphogypsum Calcium sulfate dihydrate content is 93.9%), gets 5.24kg and joins in the reactor that stirrer and heating unit are housed, starts stirrer, is warming up to 40 ℃, adjusts the speed of mixer to be 100 rev / min, adds coconut oil Disodium monoethanolamide sulfosuccinate monoester 3.0g; add 25% (NH 4 ) 2 CO 3 4.04kg of the solution (the molar ratio of ammonium carbonate and calcium sulfate is 1:1.05), continue stirring for 1.5h; turn off the heating and stirring device, drop to room temperature, filter, adjust the pH of the filtrate=5.78, and obtain (NH 4 ) 2 SO 4 C...

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Abstract

The invention discloses a method for co-producing ammonia sulfate and calcium carbonate by ardealite. The method comprises that: the ardealite serous liquid is taken and added into a reaction kettle; a stirrer is started, and the reaction kettle is heated up to the temperature of between 30 and 60 DEG C; an additive and (NH4)2CO3 are added into the reaction kettle, the reaction temperature is controlled to be between 30 and 60 DEG C, and the reaction time is between 0.5 and 2 hours; after the reaction, the heating device and the stirrer are closed, the mixture in the reaction kettle is cooled down to the normal temperature and filtered, the pH value of the filtrate is adjusted to be between 5.5 and 6.0, and the filtrate is condensed, crystallized and dried to obtain the ammonia sulfate product; the filter residue is added with water to obtain solid pulp of which the content of CaCO3 is between 30 and 60 percent, and the solid pulp is placed into a reactor; and the stirrer is started, and solid pulp is heated up to the temperature of between 70 and 90 DEG C and mixed with a surface modifier, the reaction temperature is maintained for 0.5 to 1 hour, the heating device is closed, the mixture is continuously stirred, cooled down to the temperature of between 30 and 50 DEG C and filtered, and the filter residue is dried to obtain the modified CaCO3. The method has the advantages of preparing the ammonia sulfate and the calcium carbonate at the same time and improving the utility value of the calcium carbonate, along with simple process, high recovery rate and low production cost.

Description

technical field [0001] The invention relates to the field of chemical industry, in particular to a method for co-producing ammonium sulfate and calcium carbonate by using phosphogypsum. Background technique [0002] Phosphogypsum is an industrial waste discharged from the production process of wet-process phosphoric acid. Due to different production processes, it will contain dihydrate gypsum and hemihydrate gypsum, with dihydrate gypsum as the main component. In addition, it also contains a small amount of undecomposed phosphate rock powder, free phosphoric acid, iron phosphate, aluminum phosphate and fluorosilicate and other impurities. The annual discharge of phosphogypsum in my country has exceeded 50 million tons, which not only occupies a large amount of land, but also seriously pollutes the environment. [0003] At present, ammonium sulfate is mostly produced by neutralizing synthetic ammonia and sulfuric acid to obtain ammonium sulfate, but the synthetic ammonia pr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F11/18C01C1/244
Inventor 解田刘佳胡宏罗贵川周泳波柳玉松甘雄田仁道苏迪赵杰高晓明
Owner WENGFU (GRP) CO LTD
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