A urea process with high-temperature stripping
US-2018362452-A1 · Dec 20, 2018 · US
US12110264B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12110264-B2 |
| Application number | US-202118267826-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 19, 2021 |
| Priority date | Dec 16, 2020 |
| Publication date | Oct 8, 2024 |
| Grant date | Oct 8, 2024 |
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A process for the production of urea wherein: production of pure urea (U) includes the concentration of an aqueous urea solution (23) by crystallization; a urea crystallization purge aqueous phase (32) comprising urea, water and biuret, which is purged from the urea crystallization process, is used in a high-biuret urea processing section (34) for additional production of urea with a high content of biuret.
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What is claimed is: 1. A process for the production of urea, the process comprising: concentrating an aqueous urea solution by crystallization in a crystallization section to produce solid crystals of urea and a urea crystallization purge aqueous phase comprising urea, water and biuret; purging the urea crystallization purge aqueous phase from the crystallization process; and further processing at least a portion of said urea crystallization purge aqueous phase in a high-biuret urea processing section to produce a high-biuret urea in a solid form, wherein the high-biuret urea comprises at least 55% by weight of biuret; wherein urea is produced at a high pressure of synthesis in a urea synthesis section, obtaining a synthesis effluent; said effluent is processed in a recovery section at one or more pressure levels lower than the synthesis pressure to recover unconverted reagents which are recycled to the synthesis section, and said aqueous urea solution is obtained in the recovery section. 2. The process according to claim 1 , wherein said high-biuret urea contains at least 70% by weight of biuret. 3. The process according to claim 1 , wherein the sum of biuret and urea in the high-biuret urea is at least 80% by weight. 4. The process according to claim 1 , wherein the urea crystallization purge aqueous phase is diluted with water before or during the processing in the high-biuret urea processing section. 5. The process according to claim 1 , wherein the processing of the urea crystallization purge aqueous phase in the high-biuret urea processing section further includes a step of crystallization wherein solid crystals containing biuret and urea are obtained. 6. The process according to claim 5 , wherein processing in the high-biuret urea processing section further includes separation of the crystals from a crystallization slurry and further processing of said crystals to remove residual water and obtain said high-biuret urea. 7. The process according to claim 1 , wherein said urea crystallization purge aqueous phase contains at least 5% by weight of biuret. 8. The process according to claim 1 , wherein said urea crystallization purge aqueous phase contains by weight 50% to 65% urea, 5% to 20% biuret, the balance being water and impurities. 9. The process according to claim 1 , wherein all of the urea crystallization purge aqueous phase produced in the urea crystallization section is sent to the high-biuret urea processing section and no part of said urea crystallization purge aqueous phase is reintroduced into the urea synthesis section. 10. The process according to claim 1 , further comprising: withdrawing a residual aqueous phase from the high-biuret urea processing section; and recycling said residual aqueous phase to the urea crystallization section. 11. A plant for producing pure urea and high-biuret urea with a process in accordance with claim 1 , the plant comprising: a high-pressure urea synthesis section to obtain a synthesis effluent; a recovery section connected to the urea synthesis section, the recovery section arranged to process said synthesis effluent at one or more pressure levels lower than the synthesis pressure to recover unconverted reagents and arranged to recycle said unconverted reagents to said urea synthesis section, and to obtain an aqueous urea solution; a urea crystallization section arranged to process said aqueous urea solution and to obtain solid crystals of urea and a urea crystallization purge aqueous phase comprising urea, water and biuret; a processing section and a line arranged to feed a said urea crystallization purge aqueous phase separated in the urea crystallization section to said processing section; the processing section being arranged to obtain, from said urea crystallization purge aqueous phase, a high-biuret urea in a solid form; wherein said processing section includes a crystallization section arranged to produce crystals containing biuret and a centrifuge arranged to separate the crystals from a crystallization mother liquor. 12. A method of modifying a urea plant, wherein: the plant includes a urea crystallization section arranged to produce solid urea by crystallization of an aqueous urea solution, to obtain solid crystals of urea and a crystallization aqueous phase comprising urea, water and biuret; the method including: adding a processing section to the plant, wherein the processing section is arranged to obtain, from said aqueous phase, a high-biuret urea in the form of a solid product made predominantly of biuret and urea; providing a line to feed part or all of the crystallization aqueous phase withdrawn from the urea crystallization section to the newly-installed processing section for the production of high-biuret urea; said modified urea plant comprising: a high-pressure urea synthesis section to obtain a synthesis effluent; a recovery section arranged to process said synthesis effluent at one or more pressure levels lower than the synthesis pressure to recover unconverted reagents and arranged to recycle said unconverted reagents to said urea synthesis section, and to obtain an aqueous urea solution; a urea crystallization section arranged to process said aqueous urea solution and to obtain solid crystals of urea and a urea crystallization purge aqueous phase comprising urea, water and biuret; a processing section and a line arranged to feed a said urea crystallization purge aqueous phase separated in the urea crystallization section to said processing section; the processing section being arranged to obtain, from said urea crystallization purge aqueous phase, a high-biuret urea in a solid form; wherein said processing section includes a crystallization section arranged to produce crystals containing biuret and a centrifuge arranged to separate the crystals from a crystallization mother liquor. 13. The process according to claim 1 , wherein said urea crystallization purge aqueous phase contains at least 10% by weight of biuret.
Recycling of unreacted starting or intermediate materials · CPC title
from urea · CPC title
Separation; Purification · CPC title
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