A method for conditioning and tempering ammonium phosphate by using phosphoric acid production waste residue
A technology of waste residue and phosphoric acid, applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problems of unfavorable control of cost, environmental pollution, affecting the normal operation of production, etc., and achieves good popularization and application value, convenient use, and good equipment versatility. Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0024] A. Drying: The phosphoric acid produced by the wet method is separated from the liquid slag by the sedimentation method, and the separated waste residue is dried to a moisture content of 20%, which contains 85% of phosphogypsum;
[0025] B. Pulverization: Pulverize and sieve the dried waste residue with an airflow pulverizer to make the particle size 2~3mm;
[0026] C. Acid preparation: slowly add the screened waste residue to phosphoric acid with a solid content of 5% in an amount of 50kg / t, and stir evenly, adjust the solid content of the acid solution to 10%, and the concentration of phosphoric acid to 43.5%. Subsequent ammoniation reaction.
[0027] The tempering results show that the nutrient content of the produced monoammonium phosphate product is 58.5%, and the moisture content is 3%, which meets the requirements of the national standard.
Embodiment 2
[0029] A. Drying: The phosphoric acid produced by the wet method is separated from the liquid slag by the sedimentation method, and the separated waste residue is dried to a moisture content of 30%, which contains 78% of phosphogypsum;
[0030] B. Pulverization: pulverize and sieve the dried waste residue with a grinder to make the particle size 1~2mm;
[0031] C. Acid preparation: slowly add the screened waste residue to phosphoric acid with a solid content of 6% in an amount of 75kg / t, and stir evenly, adjust the solid content of the acid solution to 12%, and the concentration of phosphoric acid to 43%. Subsequent ammoniation reaction.
[0032] The tempering results show that the nutrient content of the produced monoammonium phosphate product is 58%, and the moisture content is 2%, which meets the requirements of the national standard.
Embodiment 3
[0034] A. Drying: The phosphoric acid produced by the wet method is separated from the liquid slag by the sedimentation method, and the separated waste residue is dried to a moisture content of 25%, which contains 70% of phosphogypsum;
[0035] B. Pulverization: pulverize and sieve the dried waste residue with a mechanical pulverizer to make the particle size 3~4mm;
[0036] C. Acid preparation: slowly add the sieved waste residue to phosphoric acid with a solid content of 8% in an amount of 100kg / t, and stir evenly, adjust the solid content of the acid solution to 14%, and the phosphoric acid concentration to 44.5%. Subsequent ammoniation reaction.
[0037] The tempering results show that the nutrient content of the produced monoammonium phosphate product is 58.5%, and the moisture content is 4%, which meets the requirements of the national standard.
PUM
| Property | Measurement | Unit |
|---|---|---|
| particle diameter | aaaaa | aaaaa |
| particle diameter | aaaaa | aaaaa |
| particle diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More