ES2121114T3 - Reactor y procedimiento continuo, a realizar con este, para la obtencion de carbonato de etilenglicol, o bien carbonato de propilenglicol. - Google Patents
Reactor y procedimiento continuo, a realizar con este, para la obtencion de carbonato de etilenglicol, o bien carbonato de propilenglicol.Info
- Publication number
- ES2121114T3 ES2121114T3 ES94108037T ES94108037T ES2121114T3 ES 2121114 T3 ES2121114 T3 ES 2121114T3 ES 94108037 T ES94108037 T ES 94108037T ES 94108037 T ES94108037 T ES 94108037T ES 2121114 T3 ES2121114 T3 ES 2121114T3
- Authority
- ES
- Spain
- Prior art keywords
- reaction mixture
- egc
- pgc
- bubble column
- glycol carbonate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- NPAXBRSUVYCZGM-UHFFFAOYSA-N carbonic acid;propane-1,2-diol Chemical compound OC(O)=O.CC(O)CO NPAXBRSUVYCZGM-UHFFFAOYSA-N 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 title 1
- 239000011541 reaction mixture Substances 0.000 abstract 5
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 abstract 2
- 239000012429 reaction media Substances 0.000 abstract 2
- CQDGTJPVBWZJAZ-UHFFFAOYSA-N monoethyl carbonate Chemical compound CCOC(O)=O CQDGTJPVBWZJAZ-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
- C07D317/32—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D317/34—Oxygen atoms
- C07D317/36—Alkylene carbonates; Substituted alkylene carbonates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
- C07D317/32—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D317/34—Oxygen atoms
- C07D317/36—Alkylene carbonates; Substituted alkylene carbonates
- C07D317/38—Ethylene carbonate
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
SE DESDESCRIBE UN REACTOR DE COLUMNA DE BURBUJAS, QUE ESTA CARACTERIZADO A TRAVES DE UN GRADO DE ESBELTEZ CON UNA RELACION DE LA ALTURA A SU DIAMETRO DESDE 2 HASTA 50, CON UNA AFLUENCIA PARA LOS ELEMENTOS QUE SIRVEN COMO MEDIO DE REACCION, EL CARBONATO ETILENGLICOL (EGC) PRESENTE O EL CARBONATO PROPILENGLICOL (PGC), EN EL EXTREMO INFERIOR DE LA COLUMNA DE BURBUJAS Y/O UNO O MULTIPLES LUGARES DOSIFICADORES PARA LOS EDUCTOS CO2 Y OXIDO DE ETILENO (EOX) U OXIDO DE PROPILENO (POX) POR ENCIMA DE LA AFLUENCIA PARA EL MEDIO DE REACCION, CON UNA EVACUACION PARA LA MEZCLA DE REACCION EN EL EXTREMO SUPERIOR DE LA COLUMNA DE BURBUJAS. CON UN DISPOSITIVO DE DISTRIBUCION A CONTINUACION PARA LA MEZCLA DE REACCION DESARROLLADA PARA LA DISTRIBUCION DE LA MEZCLA DE REACCION A SER EXTRAIDA Y A SER PREPARADA POR UNA PARTE Y LA MEZCLA DE REACCION CICLIDIZADA POR OTRA PARTE, Y ADEMAS CON UNA CONDUCCION DE GUIA DE RETORNO PARA LA ADICION DE LA MEZCLA DE REACCION RECICLIDIZADA. ESTE REACTOR DE COLUMNA DE BURBUJAPUEDE SER UTILIZADO EN FORMA VENTAJOSA EN UN PROCESO PARA LA ELABORACION CONTINUA DE EGC O PGC, DE FORMA QUE SE REALIZA EN UNA ZONA DE TEMPERATURAS DESDE 100 HASTA 200 UNA ZONA DE PRESION DESDE 5 HASTA 200 BAR Y EN UNA RELACION MOLAR DESDE 1,01 HASTA 1,5 MOLES DE CO2 POR MOL DE OXIDO ALQUILENO EN PRESENCIA DE EGC O PGC COMO MEDIOS DE REACCION EN UNA CANTIDAD QUE ALCANZA DESDE 7 HASTA 350 VECES LA CANTIDAD EGC O PGC NUEVA FORMADA.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4318893A DE4318893A1 (de) | 1993-06-07 | 1993-06-07 | Reaktor und damit durchzuführendes kontinuierliches Verfahren zur Herstellung von Ethylenglykolcarbonat bzw. Propylenglykolcarbonat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2121114T3 true ES2121114T3 (es) | 1998-11-16 |
Family
ID=6489815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES94108037T Expired - Lifetime ES2121114T3 (es) | 1993-06-07 | 1994-05-25 | Reactor y procedimiento continuo, a realizar con este, para la obtencion de carbonato de etilenglicol, o bien carbonato de propilenglicol. |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US5508442A (es) |
| EP (1) | EP0628553B1 (es) |
| JP (1) | JPH06345699A (es) |
| CA (1) | CA2125073C (es) |
| DE (2) | DE4318893A1 (es) |
| ES (1) | ES2121114T3 (es) |
Families Citing this family (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3781549B2 (ja) * | 1998-03-19 | 2006-05-31 | 三菱化学株式会社 | モノエチレングリコールの製造方法 |
| US6080897A (en) * | 1998-03-19 | 2000-06-27 | Mitsubishi Chemical Corporation | Method for producing monoethylene glycol |
| EP1119561B1 (en) * | 1998-10-07 | 2003-04-16 | Huntsman Petrochemical Corporation | Process for the preparation of alkylene carbonate |
| MY141209A (en) * | 2003-03-13 | 2010-03-31 | Chiyoda Corp | Method of manufacturing acetic acid |
| CN101023046B (zh) * | 2004-09-02 | 2019-01-18 | 奇派特石化有限公司 | 优化的液相氧化 |
| JP4738786B2 (ja) * | 2004-10-01 | 2011-08-03 | 旭化成ケミカルズ株式会社 | エチレンカーボネートの製造方法 |
| JP4673028B2 (ja) * | 2004-10-04 | 2011-04-20 | 旭化成ケミカルズ株式会社 | エチレンカーボネートの精製方法 |
| KR100668043B1 (ko) | 2005-06-14 | 2007-01-15 | 한국과학기술연구원 | 루프 반응기를 이용한 에틸렌카보네이트 제조방법 |
| TWI383976B (zh) * | 2006-02-22 | 2013-02-01 | Shell Int Research | 製備碳酸二烷酯及烷二醇的方法 |
| TW200740731A (en) * | 2006-02-22 | 2007-11-01 | Shell Int Research | Process for the preparation of alkanediol |
| TWI382979B (zh) * | 2006-02-22 | 2013-01-21 | Shell Int Research | 碳酸伸烷酯之生產方法及由此生產的碳酸伸烷酯於烷二醇及碳酸二烷酯之製造中的用途 |
| TWI378087B (en) * | 2006-02-22 | 2012-12-01 | Shell Int Research | Process for the preparation of an alkanediol and a dialkyl carbonate |
| TW200740749A (en) * | 2006-02-22 | 2007-11-01 | Shell Int Research | Process for the preparation of an alkanediol and a dialkyl carbonate |
| TWI387584B (zh) * | 2006-03-13 | 2013-03-01 | Shell Int Research | 碳酸伸烷酯之生產方法及由此生產之碳酸伸烷酯於烷二醇及碳酸二烷酯之製造中之用途 |
| EP2337774B1 (en) | 2008-10-20 | 2013-12-04 | Shell Internationale Research Maatschappij B.V. | Process for removing an alkanol impurity from an organic carbonate stream |
| CN102471223B (zh) | 2009-08-12 | 2015-03-25 | 国际壳牌研究有限公司 | 自碳酸二烷基酯流除去链烷醇杂质的方法 |
| TWI473786B (zh) | 2009-11-16 | 2015-02-21 | Shell Int Research | 製備烷二醇及碳酸二烷酯的方法 |
| DE102010042937A1 (de) | 2010-10-08 | 2012-04-12 | Bayer Materialscience Aktiengesellschaft | Verfahren zur Herstellung von Diarylcarbonaten aus Dialkylcarbonaten |
| KR102048110B1 (ko) | 2012-07-11 | 2019-11-22 | 코베스트로 도이칠란드 아게 | 이소시아네이트 제조에서 증류 잔류물의 후처리 방법 |
| KR102505184B1 (ko) * | 2019-08-21 | 2023-03-02 | 주식회사 엘지화학 | 폴리알킬렌 카보네이트의 제조방법 |
| WO2021110627A1 (en) | 2019-12-06 | 2021-06-10 | Shell Internationale Research Maatschappij B.V. | Process for removing an ether alkanol impurity from an organic carbonate stream |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU172342A (es) * | ||||
| US4314945A (en) | 1977-12-22 | 1982-02-09 | Union Carbide Corporation | Alkylene carbonate process |
| RO76854A2 (ro) * | 1979-03-06 | 1981-08-30 | Centrala Industriala De Fire Si Fibre Sintetice,Ro | Reactor termostatat pentru sinteze etilencarbonatului |
| JPS6059218B2 (ja) * | 1980-12-23 | 1985-12-24 | 株式会社日本触媒 | アルキレングリコ−ルの製造方法 |
| DE3736988C1 (de) | 1987-10-31 | 1989-03-23 | Bayer Ag | Verfahren zur kontinuierlichen Herstellung von organischen Mono- und Polyisocyanaten |
| DE3744001C1 (de) | 1987-12-24 | 1989-06-08 | Bayer Ag | Verfahren zur kontinuierlichen Herstellung von Mono- oder Polyisocyanaten |
| DE4210943A1 (de) | 1992-04-02 | 1993-10-07 | Bayer Ag | Verfahren zur Herstellung von Alkylencarbonaten |
| DE4141189A1 (de) * | 1991-12-13 | 1993-06-17 | Bayer Ag | Verfahren zur herstellung von ethylenglykolcarbonat |
-
1993
- 1993-06-07 DE DE4318893A patent/DE4318893A1/de not_active Withdrawn
-
1994
- 1994-05-25 EP EP94108037A patent/EP0628553B1/de not_active Expired - Lifetime
- 1994-05-25 ES ES94108037T patent/ES2121114T3/es not_active Expired - Lifetime
- 1994-05-25 DE DE59406801T patent/DE59406801D1/de not_active Expired - Fee Related
- 1994-05-31 US US08/251,229 patent/US5508442A/en not_active Expired - Lifetime
- 1994-06-03 CA CA002125073A patent/CA2125073C/en not_active Expired - Fee Related
- 1994-06-06 JP JP6145809A patent/JPH06345699A/ja active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| US5508442A (en) | 1996-04-16 |
| DE4318893A1 (de) | 1994-12-08 |
| CA2125073A1 (en) | 1994-12-08 |
| CA2125073C (en) | 2005-07-26 |
| DE59406801D1 (de) | 1998-10-08 |
| EP0628553B1 (de) | 1998-09-02 |
| EP0628553A1 (de) | 1994-12-14 |
| JPH06345699A (ja) | 1994-12-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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