AR037136A1 - Procedimiento mejorado para la produccion de melamina con alto grado de pureza y excelente rendimiento - Google Patents
Procedimiento mejorado para la produccion de melamina con alto grado de pureza y excelente rendimientoInfo
- Publication number
- AR037136A1 AR037136A1 ARP020102098A ARP020102098A AR037136A1 AR 037136 A1 AR037136 A1 AR 037136A1 AR P020102098 A ARP020102098 A AR P020102098A AR P020102098 A ARP020102098 A AR P020102098A AR 037136 A1 AR037136 A1 AR 037136A1
- Authority
- AR
- Argentina
- Prior art keywords
- melamine
- pyrolysis
- postreactor
- recover
- urea
- Prior art date
Links
- 229920000877 Melamine resin Polymers 0.000 title abstract 8
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 title abstract 8
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 6
- 238000000197 pyrolysis Methods 0.000 abstract 5
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 abstract 4
- 239000004202 carbamide Substances 0.000 abstract 4
- 238000005496 tempering Methods 0.000 abstract 4
- XUMBMVFBXHLACL-UHFFFAOYSA-N Melanin Chemical compound O=C1C(=O)C(C2=CNC3=C(C(C(=O)C4=C32)=O)C)=C2C4=CNC2=C1C XUMBMVFBXHLACL-UHFFFAOYSA-N 0.000 abstract 2
- 239000007791 liquid phase Substances 0.000 abstract 2
- 229910000069 nitrogen hydride Inorganic materials 0.000 abstract 2
- 239000012071 phase Substances 0.000 abstract 2
- 239000000047 product Substances 0.000 abstract 2
- 241000209761 Avena Species 0.000 abstract 1
- 235000007319 Avena orientalis Nutrition 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 abstract 1
- 229910021529 ammonia Inorganic materials 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000002425 crystallisation Methods 0.000 abstract 1
- 230000008025 crystallization Effects 0.000 abstract 1
- 239000013067 intermediate product Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000012452 mother liquor Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
- 238000011282 treatment Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/54—Three nitrogen atoms
- C07D251/56—Preparation of melamine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/54—Three nitrogen atoms
- C07D251/56—Preparation of melamine
- C07D251/60—Preparation of melamine from urea or from carbon dioxide and ammonia
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Peptides Or Proteins (AREA)
Abstract
Procedimiento para la producción de melamina con alto grado de pureza y excelente rendimiento por medio de la pirólisis de la urea a una temperatura dentro de la escala de 360 a 420°C y una presión mayor que 7MPa donde los productos de la reacción, que comprenden una fase gaseosa y una fase líquida, se someten a tratamientos sucesivos para purificar y recuperar la melamina, caracterizado porque: a la fase líquida que sale del reactor de pirólisis que contiene melamina, urea no reaccionada, productos intermedios oxidados de la pirólisis (OAT) y productos de la condensación desamonizante de la melamina (policondensados), se envía a un reactor que se ubica corriente abajo (postreactor) que funciona bajo condiciones de temperatura y presión sustancialmente iguales a las del reactor de pirólisis; la fase gaseosa anhidro que sale del postreactor de pirólisis y del postreactor se somete a lavado con urea fundida para recuperar la melamina que ésta contiene en forma de vapor, antes de enviarla a la planta de síntesis de la urea para recuperar el NH3 y el CO2 que ésta contiene; el líquido purificado que sale del postreactor se trata en una columna de templado a una temperatura de entre 160 y 170°C en la presencia de, por lo menos, 10% en peso de NH3 a fin de eliminar los policondensados; el producto de la columna de templado se enfría y se separa por cristalización la melamina con alto grado de pureza del agua madre que se recicla directamente en un nivel del 80%, como mínimo, a la columna de templado, lo que permite que la melamina y el amoníaco se recuperen sin costos; el licor madre que no se recicla directamente se trata para la separación de las OAT y luego se vuelve a enviar a la columna de templado, que efectúa la recuperación completa de la melanina producida en el sistema de reacción.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT2001MI001216A ITMI20011216A1 (it) | 2001-06-08 | 2001-06-08 | Procedimento migliorato per la produzione con alte rese di melanina |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR037136A1 true AR037136A1 (es) | 2004-10-27 |
Family
ID=11447835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP020102098A AR037136A1 (es) | 2001-06-08 | 2002-06-06 | Procedimiento mejorado para la produccion de melamina con alto grado de pureza y excelente rendimiento |
Country Status (17)
| Country | Link |
|---|---|
| US (1) | US7125992B2 (es) |
| EP (1) | EP1404658B1 (es) |
| KR (1) | KR20040023610A (es) |
| CN (1) | CN1276915C (es) |
| AR (1) | AR037136A1 (es) |
| AT (1) | ATE397594T1 (es) |
| BR (1) | BR0210984A (es) |
| CA (1) | CA2449995A1 (es) |
| DE (1) | DE60226980D1 (es) |
| EA (1) | EA005993B1 (es) |
| ES (1) | ES2307763T3 (es) |
| IT (1) | ITMI20011216A1 (es) |
| MY (1) | MY138822A (es) |
| PL (1) | PL367884A1 (es) |
| TW (1) | TWI255814B (es) |
| UA (1) | UA76757C2 (es) |
| WO (1) | WO2002100839A1 (es) |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PL209035B1 (pl) | 2001-11-16 | 2011-07-29 | Ami Agrolinz Melamine Int Gmbh | Sposób wytwarzania melaminy pozbawionej melemu oraz bezprzeponowa chłodnica do stosowania tego sposobu |
| DE102004051432A1 (de) * | 2004-10-20 | 2006-04-27 | Ami-Agrolinz Melamine International Gmbh | Verfahren zur Behandlung von triazinhaltigem Wasser einer Melaminanlage |
| ITMI20060759A1 (it) * | 2006-04-14 | 2007-10-15 | Eurotecnica Melamine Luxemburg | Processo migliorato per la produzione di melammina con incremento di resa |
| EP2098516A1 (en) * | 2008-03-04 | 2009-09-09 | Urea Casale S.A. | Process for the production of high purity melamine from urea |
| US8472683B2 (en) * | 2008-05-09 | 2013-06-25 | General Electric Company | Motion correction in tomographic images |
| ITMI20080861A1 (it) | 2008-05-13 | 2009-11-14 | Eurotecnica Melamine Luxembourg | Processo migliorato per la purificazione della melammina e relativa apparecchiatura |
| EP2168643A1 (en) * | 2008-09-29 | 2010-03-31 | Applied Materials, Inc. | Evaporator for organic materials |
| IT1391372B1 (it) * | 2008-10-07 | 2011-12-13 | Eurotecnica Melamine Luxemburg Zweigniederlassung In Ittigen | Procedimento e apparecchiatura per la produzione di melammina da urea |
| EP2308856A1 (en) | 2009-10-09 | 2011-04-13 | Borealis Agrolinz Melamine GmbH | Water recycling in a melamine production process |
| CN101838246B (zh) * | 2010-04-29 | 2012-04-18 | 聊城市鲁西化工工程设计有限责任公司 | 利用三聚氰胺尾气进行倒吹的工艺及设备 |
| IT1400090B1 (it) * | 2010-05-06 | 2013-05-17 | Eurotecnica Melamine Luxemburg Zweigniederlassung In Ittigen | Procedimento a basso consumo energetico per la produzione di melammina ad elevata purezza tramite pirolisi dell'urea, e relativa apparecchiatura |
| CN101863848B (zh) * | 2010-05-28 | 2012-07-18 | 四川金象赛瑞化工股份有限公司 | 用于制备三聚氰胺的系统及方法 |
| RU2495876C1 (ru) * | 2012-09-10 | 2013-10-20 | Открытое Акционерное Общество "Научно-Исследовательский И Проектный Институт Карбамида И Продуктов Органического Синтеза" (Оао Ниик) | Способ очистки меламина |
| ITUB20152258A1 (it) * | 2015-07-17 | 2017-01-17 | Eurotecnica Melamine Luxemburg Zweigniederlassung In Ittigen | Procedimento per la produzione di melammina con separazione e recupero di CO2 e NH3 aventi elevata purezza |
| EP3208264A1 (en) | 2016-02-19 | 2017-08-23 | Casale SA | Method for revamping a high pressure melamine plant |
| CN109761922B (zh) * | 2017-11-09 | 2023-11-21 | 欧技三聚氰胺有限公司 | 通过脲的热解生产高纯度三聚氰胺的改进方法和相关装置 |
| IT201800006795A1 (it) | 2018-06-29 | 2019-12-29 | Procedimento di conversione diretta di off-gas anidri da impianti melammina in urea | |
| IT201800007367A1 (it) | 2018-07-20 | 2020-01-20 | Procedimento a basso consumo energetico e ridotto consumo di ammoniaca per la produzione di melammina a elevata purezza tramite pirolisi dell’urea, e relativo impianto | |
| IT202200004898A1 (it) | 2022-03-14 | 2023-09-14 | Eurotecnica Melamine Ag | Procedimento migliorato per la produzione di melammina ad alta purezza da pirolisi di urea, a ridotto consumo energetico e migliorata integrazione con l’impianto urea |
| CA3270599A1 (en) | 2022-10-14 | 2024-04-18 | Stamicarbon B.V. | UREA AND MELAMINE PRODUCTION |
| CA3274511A1 (en) | 2022-11-22 | 2024-05-30 | Stamicarbon B.V. | LOW-BUIRET MULTI-PRODUCT UREA PRODUCTION |
| CA3274505A1 (en) | 2022-11-22 | 2024-05-30 | Stamicarbon B.V. | COUPLED PRODUCTION OF UREA AND MELAMINE WITH HP CO2 EXTRACTION |
| WO2024112196A1 (en) | 2022-11-22 | 2024-05-30 | Stamicarbon B.V. | Coupled urea melamine plant |
| AU2024237078A1 (en) | 2023-03-10 | 2025-09-04 | Casale Sa | A process and plant for the synthesis of urea and melamine |
| IT202300019557A1 (it) | 2023-09-26 | 2025-03-26 | Proman Ag | Processo per la produzione di melammina |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3161638A (en) * | 1964-12-15 | Filter | ||
| US3637686A (en) * | 1969-02-10 | 1972-01-25 | Nissan Chemical Ind Ltd | Process for recovering purified melamine |
| EP1054006A1 (en) | 1999-05-20 | 2000-11-22 | Dsm N.V. | Method for preparing melamine |
-
2001
- 2001-06-08 IT IT2001MI001216A patent/ITMI20011216A1/it unknown
-
2002
- 2002-05-30 EA EA200400015A patent/EA005993B1/ru not_active IP Right Cessation
- 2002-05-30 UA UA20031213204A patent/UA76757C2/uk unknown
- 2002-05-30 CN CNB02815259XA patent/CN1276915C/zh not_active Expired - Fee Related
- 2002-05-30 CA CA002449995A patent/CA2449995A1/en not_active Abandoned
- 2002-05-30 PL PL02367884A patent/PL367884A1/xx not_active Application Discontinuation
- 2002-05-30 WO PCT/IT2002/000348 patent/WO2002100839A1/en not_active Ceased
- 2002-05-30 KR KR10-2003-7015932A patent/KR20040023610A/ko not_active Abandoned
- 2002-05-30 DE DE60226980T patent/DE60226980D1/de not_active Expired - Fee Related
- 2002-05-30 ES ES02741165T patent/ES2307763T3/es not_active Expired - Lifetime
- 2002-05-30 EP EP02741165A patent/EP1404658B1/en not_active Revoked
- 2002-05-30 AT AT02741165T patent/ATE397594T1/de not_active IP Right Cessation
- 2002-05-30 US US10/479,931 patent/US7125992B2/en not_active Expired - Lifetime
- 2002-05-30 BR BR0210984-0A patent/BR0210984A/pt not_active IP Right Cessation
- 2002-05-31 TW TW091111733A patent/TWI255814B/zh not_active IP Right Cessation
- 2002-06-04 MY MYPI20022050A patent/MY138822A/en unknown
- 2002-06-06 AR ARP020102098A patent/AR037136A1/es not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| TWI255814B (en) | 2006-06-01 |
| EA005993B1 (ru) | 2005-08-25 |
| EP1404658A1 (en) | 2004-04-07 |
| PL367884A1 (en) | 2005-03-07 |
| EP1404658B1 (en) | 2008-06-04 |
| KR20040023610A (ko) | 2004-03-18 |
| US7125992B2 (en) | 2006-10-24 |
| BR0210984A (pt) | 2004-06-08 |
| US20040162429A1 (en) | 2004-08-19 |
| ITMI20011216A0 (it) | 2001-06-08 |
| EA200400015A1 (ru) | 2004-04-29 |
| ITMI20011216A1 (it) | 2002-12-08 |
| MY138822A (en) | 2009-07-31 |
| UA76757C2 (uk) | 2006-09-15 |
| WO2002100839A1 (en) | 2002-12-19 |
| DE60226980D1 (de) | 2008-07-17 |
| CN1276915C (zh) | 2006-09-27 |
| ATE397594T1 (de) | 2008-06-15 |
| CN1538961A (zh) | 2004-10-20 |
| CA2449995A1 (en) | 2002-12-19 |
| ES2307763T3 (es) | 2008-12-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FA | Abandonment or withdrawal |