ES2075865T3 - Procedimiento para la hidroformilacion de una olefina. - Google Patents
Procedimiento para la hidroformilacion de una olefina.Info
- Publication number
- ES2075865T3 ES2075865T3 ES90119931T ES90119931T ES2075865T3 ES 2075865 T3 ES2075865 T3 ES 2075865T3 ES 90119931 T ES90119931 T ES 90119931T ES 90119931 T ES90119931 T ES 90119931T ES 2075865 T3 ES2075865 T3 ES 2075865T3
- Authority
- ES
- Spain
- Prior art keywords
- reactor
- stage
- liquid phase
- olephine
- type
- 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
- 238000000034 method Methods 0.000 title abstract 2
- 239000007791 liquid phase Substances 0.000 abstract 3
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical class [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract 1
- 150000001336 alkenes Chemical class 0.000 abstract 1
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 1
- 239000002131 composite material Substances 0.000 abstract 1
- 238000009792 diffusion process Methods 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract 1
- 229910052698 phosphorus Inorganic materials 0.000 abstract 1
- 239000011574 phosphorus Substances 0.000 abstract 1
- 229910052703 rhodium Inorganic materials 0.000 abstract 1
- 239000010948 rhodium Substances 0.000 abstract 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C47/00—Compounds having —CHO groups
- C07C47/02—Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
UN PROCESO PARA HIDROMORFILACION DE UNA OLEFINA, EL CUAL COMPRENDE REACCIONAR UNA OLEFINA CON MONOXIDO DE CARBONO E HIDROGENO EN PRESENCIA DE UN CATALIZADOR DE RODIO QUE TIENE UN COMPUESTO DE FOSFORO ORGANICO TRIVALENTE COMO LIGANTE, EN DONDE LA REACCION DE HIDROMORFILACION SE REALIZA MEDIANTE DOS SISTEMAS DE REACTOR DE ETAPA, P.EJ., UN PRIMER SISTEMA DE REACTOR DE ETAPA QUE COMPRENDE UN REACTOR O REACTORES TENIENDO UNA MEZCLA CARACTERISTICA DE LA FASE LIQUIDA QUE SUSTANCIALMENTE ES DEL TIPO DE MEZCLADO COMPLETO, Y UN SEGUNDO SISTEMA DE REACTOR DE ETAPA QUE ES UN SISTEMA DE REACCION DEL TIPO DE SOLUCION CATALIZADORA CIRCULANTE Y CONTENIENDO UN REACTOR O REACTORES QUE TIENEN UNA CARACTERISTICA DE MEZCLADO DEL TIPO DE FLUJO POR PISTON, EN DONDE, CUANDO LA CARACTERISTICA DE MEZCLADO DE LA FASE LIQUIDA ESTA REPRESENTADA POR UN MODELO DE DIFUSION Y UN NUMERO NO DIMENSIONAL U (REFERENCIADO A PARTIR DE AQUI COMO UN "PARAMETRO DE FLUJO DE MEZCLADO") DEFINIDO POR LA FORMULA (I): EN DONDE U ES UNA VELOCIDAD MEDIA DE FLUJO (CM/SEG), L ES LA LONGITUD (CM) DE LA CAPA DE REACCION, Y E ES UN COEFICIENTE MEDIO DE DIFUSION (CM2/SEG), VALE AL MENOS 0,4 , ENTONCES UN PRODUCTO GASEOSO O UNA MEZCLA DE GAS-LIQUIDO DESCARGADOS DEL PRIMER SISTEMA DE ETAPA DE REACTOR, SE SEPARA HACIA UNA CORRIENTE QUE CONTIENE LA OLEFINA NO REACCIONADA Y OTRA CORRIENTE, Y UNA PARTE O LA TOTALIDAD DE LA CORRIENTE QUE CONTIENE LA OLEFINA NO REACCIONADA SE SUMINISTRA AL SEGUNDO SISTEMA DE ETAPA DE REACTOR.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27227589 | 1989-10-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2075865T3 true ES2075865T3 (es) | 1995-10-16 |
Family
ID=17511582
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES90119931T Expired - Lifetime ES2075865T3 (es) | 1989-10-19 | 1990-10-17 | Procedimiento para la hidroformilacion de una olefina. |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5105018A (es) |
| EP (1) | EP0423769B1 (es) |
| JP (1) | JP2893902B2 (es) |
| KR (1) | KR0152655B1 (es) |
| BR (1) | BR9005296A (es) |
| CA (1) | CA2027991C (es) |
| DE (1) | DE69017346T2 (es) |
| ES (1) | ES2075865T3 (es) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117120946A (zh) * | 2021-04-26 | 2023-11-24 | 三菱电机株式会社 | 数控装置、学习装置及颤振的抑制方法 |
Families Citing this family (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5426238A (en) * | 1993-06-10 | 1995-06-20 | Mitsubishi Kasei Corporation | Method for producing an aldehyde |
| US5367106A (en) * | 1993-09-20 | 1994-11-22 | Hoechst Celanese Corporation | Coupled secondary oxo reaction system |
| US5410091A (en) * | 1994-06-02 | 1995-04-25 | Quimica Oxal C.A. | Rhodium catalyzed oxo process in tubular reactor |
| ZA96178B (en) * | 1995-01-18 | 1997-06-30 | Exxon Chemical Patents Inc | Organic compounds and processes for their manufacture |
| DE19530698A1 (de) * | 1995-08-21 | 1997-02-27 | Basf Ag | Verfahren zur Aufarbeitung eines flüssigen Hydroformylierungsaustrags |
| US5741944A (en) * | 1995-12-06 | 1998-04-21 | Union Carbide Chemicals & Plastics Technology Corporation | Hydroformaylation processes |
| FR2763938B1 (fr) * | 1997-05-27 | 1999-10-22 | Inst Francais Du Petrole | Procede pour l'hydroformylation d'olefines |
| DE19836807A1 (de) | 1998-08-14 | 2000-02-17 | Basf Ag | Verfahren zur Herstellung von Aldehyden und/oder Alkoholen oder Aminen |
| US7217321B2 (en) * | 2001-04-06 | 2007-05-15 | California Institute Of Technology | Microfluidic protein crystallography techniques |
| DE19954665B4 (de) * | 1999-11-13 | 2004-02-12 | Celanese Chemicals Europe Gmbh | Verfahren zur Hydroformylierung olefinisch ungesättigter Verbindungen |
| US6906164B2 (en) * | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
| BR0116914B1 (pt) * | 2001-03-08 | 2012-05-15 | processo para a produção de aldeìdos. | |
| DE10160368B4 (de) * | 2001-12-08 | 2004-04-08 | Celanese Chemicals Europe Gmbh | Verfahren zur Herstellung von Aldehyden |
| WO2004035595A1 (en) * | 2002-10-15 | 2004-04-29 | Union Carbide Chemicals & Plastics Technology Corporation | Bis-chelating ligand and use thereof in carbonylation processes |
| US7615645B2 (en) | 2003-10-21 | 2009-11-10 | Basf Aktiengesellschaft | Method for the continuous production of aldehydes |
| DE10357718A1 (de) | 2003-12-09 | 2005-07-21 | Basf Ag | Verfahren zur Herstellung von Tricyclodecandialdehyd |
| KR100547587B1 (ko) | 2004-06-12 | 2006-01-31 | 주식회사 엘지화학 | 인을 포함하는 촉매 조성물 및 이를 이용한히드로포르밀화 방법 |
| US7943094B2 (en) * | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
| US7939694B2 (en) * | 2007-05-29 | 2011-05-10 | Lg Chem, Ltd. | Method for the hydroformylation of olefins and apparatus using the same |
| US8739145B2 (en) * | 2008-03-26 | 2014-05-27 | Avaya Inc. | Super nested block method to minimize coverage testing overhead |
| KR101229195B1 (ko) * | 2009-10-07 | 2013-02-01 | 주식회사 엘지화학 | 올레핀으로부터 고 수율의 알데히드 제조 방법 및 이에 사용되는 반응 장치 |
| CN102115433B (zh) * | 2010-12-06 | 2013-09-11 | 淄博诺奥化工有限公司 | 一种乙烯低压羰基合成生产丙醛的方法 |
| CN102826972B (zh) * | 2011-06-17 | 2015-05-13 | 中国石油化工股份有限公司 | 一种烯烃氢甲酰化反应制备醛的方法 |
| JP5890535B2 (ja) | 2011-12-20 | 2016-03-22 | ダウ テクノロジー インベストメンツ リミティド ライアビリティー カンパニー | 改良されたヒドロホルミル化プロセス |
| PL2822921T3 (pl) | 2012-03-07 | 2018-11-30 | Basf Se | SPOSÓB INTEGRACJI CIEPŁA PRZY UWODORNIANIU I DESTYLACJI C<sub>3</sub>-C<sub>20</sub>- ALDEHYDÓW |
| WO2013144735A1 (en) | 2012-03-26 | 2013-10-03 | Sasol Technology (Proprietary) Limited | Conversion of a mixture of c2 - and c3 -olefins to butanol |
| US8889917B2 (en) | 2012-04-12 | 2014-11-18 | Basf Se | Method of supplementing the catalyst in continuous hydroformylation |
| WO2013153136A1 (de) | 2012-04-12 | 2013-10-17 | Basf Se | Verfahren zur ergänzung des katalysators bei der kontinuierlichen hydroformylierung |
| US9340480B2 (en) | 2013-04-30 | 2016-05-17 | Oxea Corporation | Aldehyde production process with multi-stage condensation |
| CN104725170B (zh) | 2013-12-19 | 2019-08-23 | 陶氏技术投资有限责任公司 | 加氢甲酰化方法 |
| WO2015094781A1 (en) | 2013-12-19 | 2015-06-25 | Dow Technology Investments Llc | Hydroformylation process |
| WO2017009205A1 (de) | 2015-07-10 | 2017-01-19 | Basf Se | Verfahren zur hydroformylierung von 2-substituierten butadienen und zur herstellung von folgeprodukten davon, speziell von ambrox |
| CN108137451A (zh) | 2015-10-12 | 2018-06-08 | 巴斯夫欧洲公司 | 用于生产1,6-二取代己烷衍生物的氢甲酰化方法 |
| CN109071394B (zh) | 2016-03-18 | 2022-02-08 | 陶氏技术投资有限责任公司 | 加氢甲酰化工艺 |
| TW201840362A (zh) | 2016-11-08 | 2018-11-16 | 美商陶氏科技投資有限公司 | 使去活化的氫甲醯化催化劑溶液再生的方法 |
| TWI758353B (zh) | 2016-11-08 | 2022-03-21 | 美商陶氏科技投資有限公司 | 使去活化的氫甲醯化催化劑溶液再生的方法 |
| TW201840363A (zh) | 2016-11-08 | 2018-11-16 | 美商陶氏科技投資有限公司 | 處理氫甲醯化催化劑溶液之方法 |
| US10941092B2 (en) | 2017-06-13 | 2021-03-09 | Basf Se | Hydroformylation process for producing 1,6-hexanediol derivatives |
| SE1930249A1 (en) | 2019-07-18 | 2020-11-17 | Perstorp Ab | USE OF A METHOD FOR REDUCTION OF HEAVY END FORMATION AND CATALYST LOSS IN A HYDROFORMYLATION PROCESS COMPRISING A BIDENTATE PHOSPHITE LIGAND |
| WO2021029983A1 (en) | 2019-08-09 | 2021-02-18 | OQ Chemicals Corporation | Hydroformylation system with vent reactor recycle to primary reactor |
| US12281063B2 (en) | 2020-02-11 | 2025-04-22 | Basf Se | Low-pressure hydroformylation of diisobutene |
| MX2023006537A (es) | 2020-12-22 | 2023-06-16 | Dow Technology Investments Llc | Procesos de reaccion de hidroformilacion. |
| CN117942895A (zh) * | 2024-01-23 | 2024-04-30 | 兖矿鲁南化工有限公司 | 一种丁醇装置反应器气液混合反应系统 |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3239566A (en) * | 1960-07-22 | 1966-03-08 | Shell Oil Co | Hydroformylation of olefins |
| US3518319A (en) * | 1965-03-30 | 1970-06-30 | Exxon Research Engineering Co | Process for improving oxo selectivity to unbranched alcohols |
| US3590087A (en) * | 1968-02-28 | 1971-06-29 | Shell Oil Co | Trans-annular sec-phosphine in complex combination with cobalt and carbon monoxide as a catalyst in the oxo alcohol process |
| US3636159A (en) * | 1968-12-19 | 1972-01-18 | Phillips Petroleum Co | Hydroformylation process and catalyst |
| FR2053177B1 (es) * | 1969-07-26 | 1973-03-16 | Basf Ag | |
| US3868422A (en) * | 1971-12-23 | 1975-02-25 | Eastman Kodak Co | Multistage hydroformylation process |
| GB1387657A (en) * | 1972-08-25 | 1975-03-19 | Davy Powergas Ltd | Hydroformylation process |
| SU827476A1 (ru) * | 1978-12-26 | 1981-05-07 | Предприятие П/Я Р-6913 | Способ получени -цианпропионовогоАльдЕгидА и ЕгО диМЕТилАцЕТАл |
| DE2965157D1 (en) * | 1979-03-21 | 1983-05-11 | Davy Mckee London | Process for the production of aldehydes by hydroformylation of alkenes |
| US4528404A (en) * | 1983-03-16 | 1985-07-09 | Exxon Research And Engineering Co. | High temperature hydroformylation in the presence of triarylphosphine rhodium carbonyl hydride complex catalyst systems |
| CA1259331A (en) * | 1984-03-30 | 1989-09-12 | Gregory J. Dembowski | Process for recovery of phosphorus ligand from vaporized aldehyde |
| US4593127A (en) * | 1985-01-11 | 1986-06-03 | Union Carbide Corporation | Hydroformylation process |
-
1990
- 1990-09-12 JP JP2242038A patent/JP2893902B2/ja not_active Expired - Fee Related
- 1990-10-12 US US07/596,383 patent/US5105018A/en not_active Expired - Lifetime
- 1990-10-17 EP EP90119931A patent/EP0423769B1/en not_active Expired - Lifetime
- 1990-10-17 DE DE69017346T patent/DE69017346T2/de not_active Expired - Lifetime
- 1990-10-17 ES ES90119931T patent/ES2075865T3/es not_active Expired - Lifetime
- 1990-10-18 CA CA002027991A patent/CA2027991C/en not_active Expired - Lifetime
- 1990-10-19 BR BR909005296A patent/BR9005296A/pt not_active IP Right Cessation
- 1990-10-19 KR KR1019900016731A patent/KR0152655B1/ko not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117120946A (zh) * | 2021-04-26 | 2023-11-24 | 三菱电机株式会社 | 数控装置、学习装置及颤振的抑制方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| DE69017346D1 (de) | 1995-04-06 |
| BR9005296A (pt) | 1991-09-17 |
| CA2027991C (en) | 2001-04-24 |
| US5105018A (en) | 1992-04-14 |
| EP0423769A3 (en) | 1991-07-24 |
| EP0423769B1 (en) | 1995-03-01 |
| EP0423769A2 (en) | 1991-04-24 |
| DE69017346T2 (de) | 1995-10-12 |
| CA2027991A1 (en) | 1991-04-20 |
| KR0152655B1 (ko) | 1998-10-15 |
| KR910007852A (ko) | 1991-05-30 |
| JP2893902B2 (ja) | 1999-05-24 |
| JPH03204831A (ja) | 1991-09-06 |
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Legal Events
| Date | Code | Title | Description |
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| FG2A | Definitive protection |
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