ES2184210T3 - Procedimiento alterno para la metatesis de las olefinas. - Google Patents
Procedimiento alterno para la metatesis de las olefinas.Info
- Publication number
- ES2184210T3 ES2184210T3 ES98403070T ES98403070T ES2184210T3 ES 2184210 T3 ES2184210 T3 ES 2184210T3 ES 98403070 T ES98403070 T ES 98403070T ES 98403070 T ES98403070 T ES 98403070T ES 2184210 T3 ES2184210 T3 ES 2184210T3
- Authority
- ES
- Spain
- Prior art keywords
- reactor
- phase
- regeneration
- catalyst
- olefins
- 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 3
- 230000008929 regeneration Effects 0.000 abstract 7
- 238000011069 regeneration method Methods 0.000 abstract 7
- 239000003054 catalyst Substances 0.000 abstract 5
- 150000001336 alkenes Chemical class 0.000 abstract 4
- 239000008267 milk Substances 0.000 abstract 2
- 210000004080 milk Anatomy 0.000 abstract 2
- 235000013336 milk Nutrition 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 238000010926 purge Methods 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
- C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/32—Manganese, technetium or rhenium
- C07C2523/36—Rhenium
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
LA PRESENTE INVENCION SE REFIERE A UN PROCEDIMIENTO PARA EFECTUAR CONTINUAMENTE LA REACCION DE METATESIS O DE DESPROPORCIONAMIENTO DE LAS OLEFINAS QUE COMPRENDE AL MENOS 2 FASES, UNA FASE A) DE REACCION EN UNA ZONA QUE COMPRENDE AL MENOS UN REACTOR QUE CONTIENE AL MENOS UN CATALIZADOR EN LECHO FIJO Y UNA FASE B) DE REGENERACION EN UNA ZONA QUE COMPRENDE AL MENOS UN REACTOR QUE CONTIENE AL MENOS UN CATALIZADOR E LECHO FIJO CARACTERIZADO PORQUE ALTERNATIVAMENTE AL MENOS UN REACTOR PASA DE UNA FASE A LA OTRA. SEGUN LA FIGURA 1, LA CARGA QUE CONTIENE LAS OLEFINAS ATRAVIESA EL REACTOR R1 SEGUN UN MODO CON FLUJO ASCENDENTE. LA CARGA QUE HAY QUE TRATAR QUE CONTIENEN LAS OLEFINAS SE INTRODUCE EN EL REACTOR R1 POR LA LINEA 1A. EN ESTE REACTOR, LAS OLEFINAS CONTENIDAS EN LA CARGA SOPORTAN UNA METATESIS O UN DESPROPORCIONAMIENTO, Y A CONTINUACION EL EFLUENTE SALE DEL CIRCUITO POR LA LINEA 11. SIMULTANEAMENTE EL REACTOR R2 SE COLOCA EN FASE DE REGENERACION DE SU CATALIZADOR, SE INTRODUCEN LOS DIFERENTES GASES DE REGENERACION R2 POR LA LINEA 2B Y VUELVEN A SALIR DE ESTE REACTOR POR LA LINEA 2C. EL PASO DE LA FASE DE FUNCIONAMIENTO DE UN REACTOR A LA FASE DE REGENERACION DE SU CATALIZADOR SE EFECTUA SEGUN EL SIGUIENTE PROCEDIMIENTO: EL REACTOR CUYO CATALIZADOR DEBE REGENERARSE SE AISLA DEL RESTO DEL DISPOSITIVO, LOS HIDROCARBUROS CONTENIDOS EN ESTE REACTOR SE EVACUAN, Y ESTE REACTOR SE PURGA. DICHO REACTOR SE CONECTA A CONTINUACION CON UN BUCLE DE REGENERACION Y SE SOMETE A UN TRATAMIENTO DE REGENERACION DE SU CATALIZADOR, AL FINAL DE LA FASE DE REGENERACION, SE PURGAN EL REACTOR Y EL BUCLE DE REGENERACION.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9715743A FR2772022B1 (fr) | 1997-12-10 | 1997-12-10 | Procede alterne pour la metathese des olefines |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2184210T3 true ES2184210T3 (es) | 2003-04-01 |
Family
ID=9514509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES98403070T Expired - Lifetime ES2184210T3 (es) | 1997-12-10 | 1998-12-07 | Procedimiento alterno para la metatesis de las olefinas. |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US6281402B1 (es) |
| EP (1) | EP0933344B1 (es) |
| KR (1) | KR100523181B1 (es) |
| CN (1) | CN1200918C (es) |
| DE (1) | DE69808040T2 (es) |
| ES (1) | ES2184210T3 (es) |
| FR (1) | FR2772022B1 (es) |
| MY (1) | MY126576A (es) |
| TW (1) | TW575553B (es) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10309070A1 (de) * | 2003-03-03 | 2004-09-16 | Basf Ag | Verfahren zur Regenerierung von Re207 dotierten Trägerkatalysatoren |
| DE10344690A1 (de) * | 2003-09-25 | 2005-04-14 | Basf Ag | Verfahren zur Herstellung von 1,7-Octadien und dessen Verwendung |
| US20060129013A1 (en) * | 2004-12-09 | 2006-06-15 | Abazajian Armen N | Specific functionalization and scission of linear hydrocarbon chains |
| EP2829317A1 (en) | 2013-07-23 | 2015-01-28 | Borealis AG | Improved catalyst bed configuration for olefin production |
| EP2848300A1 (en) | 2013-09-13 | 2015-03-18 | Borealis AG | Process for olefin production by metathesis and reactor system therefore |
| EP2862629A1 (en) | 2013-10-15 | 2015-04-22 | Borealis AG | Catalyst and process for olefin metathesis reaction |
| CN104557399B (zh) * | 2013-10-28 | 2017-07-14 | 中国石油化工股份有限公司 | 戊烯与乙烯歧化制丙烯的方法 |
| EP2873459A1 (en) | 2013-11-14 | 2015-05-20 | Borealis AG | Catalyst bed configuration for olefin conversion and process for obtaining olefins |
| EP2886189A1 (en) | 2013-12-20 | 2015-06-24 | Borealis AG | Process for olefin production by metathesis and reactor system therefor |
| EP2891643A1 (en) | 2014-01-02 | 2015-07-08 | Borealis AG | Process for obtaining olefins by metathesis |
| FR3077073B1 (fr) * | 2018-01-24 | 2020-02-07 | IFP Energies Nouvelles | Procede de vapocraquage d'ethane |
| FR3097779A1 (fr) * | 2019-06-26 | 2021-01-01 | IFP Energies Nouvelles | Réacteur de traitement catalytique d’hydrocarbures avec remplacement semi-continu de catalyseur |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH298872A (de) * | 1950-03-02 | 1954-05-31 | Techn Steiner Walter Dr Sc | Verfahren zur Synthese von Kohlenwasserstoffen. |
| FR1199407A (fr) * | 1957-09-27 | 1959-12-14 | Cie Francaise Procedes Houdry | Procédé et dispositif pour la conversion catalytique d'hydrocarbures |
| US3261879A (en) * | 1963-09-27 | 1966-07-19 | Phillips Petroleum Co | Olefin disproportionation |
| US3365512A (en) * | 1964-09-23 | 1968-01-23 | Phillips Petroleum Co | Dehydration of a gas employed in cooling a catalyst |
| US3676520A (en) * | 1964-12-31 | 1972-07-11 | Phillips Petroleum Co | Conversion of olefins |
| FR91345E (es) * | 1965-11-22 | 1968-09-09 | ||
| US4072629A (en) * | 1973-12-18 | 1978-02-07 | Shell Oil Company | Regeneration of alkene disproportionation catalyst |
| FR2608595B1 (fr) * | 1986-12-17 | 1989-04-28 | Inst Francais Du Petrole | Procede de metathese d'olefines |
| US5336393A (en) * | 1991-06-12 | 1994-08-09 | Idemitsu Kosan Co., Ltd. | Process for catalytically converting organic compounds |
| US5491277A (en) * | 1993-12-28 | 1996-02-13 | Uop | Mixed-phase solid bed hydrocarbon alkylation process |
-
1997
- 1997-12-10 FR FR9715743A patent/FR2772022B1/fr not_active Expired - Fee Related
-
1998
- 1998-12-07 EP EP98403070A patent/EP0933344B1/fr not_active Expired - Lifetime
- 1998-12-07 DE DE69808040T patent/DE69808040T2/de not_active Expired - Lifetime
- 1998-12-07 ES ES98403070T patent/ES2184210T3/es not_active Expired - Lifetime
- 1998-12-09 MY MYPI98005552A patent/MY126576A/en unknown
- 1998-12-10 KR KR1019980054101A patent/KR100523181B1/ko not_active Expired - Fee Related
- 1998-12-10 US US09/208,585 patent/US6281402B1/en not_active Expired - Lifetime
- 1998-12-10 CN CNB981265278A patent/CN1200918C/zh not_active Expired - Fee Related
-
1999
- 1999-02-12 TW TW87120532A patent/TW575553B/zh not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| CN1200918C (zh) | 2005-05-11 |
| TW575553B (en) | 2004-02-11 |
| FR2772022B1 (fr) | 2000-01-14 |
| KR100523181B1 (ko) | 2006-01-27 |
| US6281402B1 (en) | 2001-08-28 |
| DE69808040D1 (de) | 2002-10-24 |
| DE69808040T2 (de) | 2003-02-06 |
| FR2772022A1 (fr) | 1999-06-11 |
| MY126576A (en) | 2006-10-31 |
| EP0933344B1 (fr) | 2002-09-18 |
| EP0933344A1 (fr) | 1999-08-04 |
| CN1223991A (zh) | 1999-07-28 |
| KR19990062956A (ko) | 1999-07-26 |
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