Controlling biuret in urea production
US-2019194127-A1 · Jun 27, 2019 · US
US12116335B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12116335-B2 |
| Application number | US-202118035030-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 10, 2021 |
| Priority date | Nov 6, 2020 |
| Publication date | Oct 15, 2024 |
| Grant date | Oct 15, 2024 |
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A process for the production of feed grade urea starting from a liquid urea melt, the process comprising processing the urea melt (6) to promote the formation of biuret until a concentration of at least 3% biuret, and subjecting the so obtained biuret-containing urea melt (8) to a shaping process to obtain a granular urea product.
Opening claim text (preview).
What is claimed is: 1. A process for the production of feed grade urea starting from a liquid urea melt, the process comprising: processing the urea melt to form biuret from urea, until a target concentration of biuret in the melt is reached, said target concentration being 3% by weight or higher; subjecting the so obtained biuret-containing urea melt to a shaping process to obtain a granular urea product. 2. The process according to claim 1 , wherein the target concentration of biuret in the melt is 5% by weight or greater. 3. The process according to claim 1 , wherein the step of processing the urea melt to form biuret includes maintaining the urea melt in a reaction space under biuret-forming conditions for a predetermined residence time until said target concentration of biuret is reached. 4. The process according to claim 3 , wherein the biuret-forming conditions includes a temperature of 160° C. to 180° C. 5. The process according to claim 3 , wherein the residence time is 5 min to 60 min. 6. The process according to claim 3 , wherein said reaction space is maintained under a continuously stirred condition during the processing of the urea melt to form biuret. 7. The process according to claim 3 , wherein said reaction space is maintained at atmospheric pressure. 8. The process according to claim 1 , wherein the urea melt contains at least 96% urea by weight. 9. The process according to claim 1 , wherein no formaldehyde is added to the urea melt before the shaping process. 10. The process according to claim 1 , wherein the shaping process includes granulation or prilling. 11. The process according to claim 1 , further comprising: reacting ammonia and carbon dioxide at a synthesis pressure in a urea synthesis plant to obtain a reaction effluent containing urea, water and unconverted ammonium carbamate; processing said reaction effluent in one or more recovery steps at a lower pressure to recover unconverted reagents, obtaining a purified aqueous solution of urea; and processing said aqueous solution in an evaporation step to remove water and obtain the urea melt. 12. The process according to claim 11 , further comprising: removing gaseous ammonia from a reaction space during the formation of biuret; and recycling the gaseous ammonia to the urea synthesis plant as a source material for the synthesis of urea. 13. The process according to claim 12 , further comprising: condensing the gaseous ammonia with water; and recycling said condensed gaseous ammonia and water as aqueous solution of ammonia. 14. The process according to claim 2 , wherein the target concentration of biuret in the melt is in a range of 5% to 15% by weight. 15. The process according to claim 3 , wherein the biuret-forming conditions includes a temperature of 160° C. to 170° C. 16. The process according to claim 3 , wherein the biuret-forming conditions includes a temperature of 165° C. 17. The process according to claim 3 , wherein the residence time is 20 min. 18. The process according to claim 1 , wherein the urea melt contains at least 99% urea by weight.
Post-treatment · CPC title
Improvements relating to the production of bulk chemicals · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
of urea, its salts, complexes or addition compounds · CPC title
Separation; Purification · CPC title
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