ES2135964T3 - Procedimiento para la obtencion de poliestireno mediante polimerizacion anionica y continua. - Google Patents
Procedimiento para la obtencion de poliestireno mediante polimerizacion anionica y continua.Info
- Publication number
- ES2135964T3 ES2135964T3 ES97107043T ES97107043T ES2135964T3 ES 2135964 T3 ES2135964 T3 ES 2135964T3 ES 97107043 T ES97107043 T ES 97107043T ES 97107043 T ES97107043 T ES 97107043T ES 2135964 T3 ES2135964 T3 ES 2135964T3
- Authority
- ES
- Spain
- Prior art keywords
- monomer
- anionic
- continuous polymerization
- reactor
- procedure
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
- B01J19/2435—Loop-type reactors
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F112/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
- C08F112/02—Monomers containing only one unsaturated aliphatic radical
- C08F112/04—Monomers containing only one unsaturated aliphatic radical containing one ring
- C08F112/06—Hydrocarbons
- C08F112/08—Styrene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F12/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
- C08F12/02—Monomers containing only one unsaturated aliphatic radical
- C08F12/04—Monomers containing only one unsaturated aliphatic radical containing one ring
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/04—Polymerisation in solution
- C08F2/06—Organic solvent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
METODO PARA LA PREPARACION DE POLIESTIROL MEDIANTE POLIMERIZACION ANIONICA CONTINUA DE MONOMERO DE ESTIROL MEDIANTE UN CATALIZADOR A BASE DE UN ALQUILO METALICO, PREFERENTEMENTE EN PRESENCIA UN DISOLVENTE A UNA TEMPERATURA ENTRE 30 Y 70 (GRADOS) C, DE FORMA QUE EL MONOMERO DE ESTIROL SE CONDUCE A UN REACTOR DE CIRCULACION OPERADO ESENCIALMENTE DE FORMA ISOTERMICA Y CON TUBO QUE FORMA BUCLE DE RETROCESO EN SI MISMO, QUE PRESENTA POR EJEMPLO UNA SUPERFICIE REFRIGERANTE ESPECIFICA DE AL MENOS 50 M{SUP,2} POR M{SUP,3} DE VOLUMEN DE REACTOR; LA VELOCIDAD DE CIRCULACION DE LA MEZCLA DE REACCION Y EL TIEMPO DE ESTANCIA ESTAN AJUSTADOS DE MODO QUE EL GASTO DE MONOMERO LLEGA COMO MINIMO AL 50 % Y LA POLIMERIZACION TRANSCURRE HASTA EL FINAL EN UN REACTOR DE TUBO QUE OPERA ESENCIALMENTE SIN REMEZCLAS.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19618678A DE19618678A1 (de) | 1996-05-09 | 1996-05-09 | Verfahren zur Herstellung von Polystyrol durch kontinuierliche anionische Polymerisation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2135964T3 true ES2135964T3 (es) | 1999-11-01 |
Family
ID=7793836
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES97107043T Expired - Lifetime ES2135964T3 (es) | 1996-05-09 | 1997-04-29 | Procedimiento para la obtencion de poliestireno mediante polimerizacion anionica y continua. |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US5902865A (es) |
| EP (1) | EP0806437B1 (es) |
| JP (1) | JPH1045811A (es) |
| KR (1) | KR100391233B1 (es) |
| DE (2) | DE19618678A1 (es) |
| ES (1) | ES2135964T3 (es) |
Families Citing this family (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19941072A1 (de) * | 1999-08-30 | 2001-03-01 | Stockhausen Chem Fab Gmbh | Polymerisatzusammensetzung und ein Verfahren zu dessen Herstellung |
| IT1314260B1 (it) * | 1999-12-03 | 2002-12-06 | Enichem Spa | Procedimento per la produzione di polimeri vinilaromaticieventualmente contenenti un nitrile etilenicamente insaturo. |
| US6586541B2 (en) * | 2000-02-02 | 2003-07-01 | E. I. Du Pont De Nemours And Company | Process for production of polyolefins |
| AU2001237693A1 (en) | 2000-03-01 | 2001-09-12 | Michael L. Kagan | Wireless communications system and method |
| US7158753B2 (en) | 2001-03-01 | 2007-01-02 | Nokia Corporation | Wireless communications system and method |
| US6906164B2 (en) * | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
| ES2540542T3 (es) * | 2000-12-07 | 2015-07-10 | Grupo Petrotemex, S.A. De C.V. | Procedimiento de poliéster de bajo coste que usa un reactor tubular |
| US6979717B2 (en) * | 2001-08-13 | 2005-12-27 | Moore Eugene R | Anionic process design for rapid polymerization of polystyrene without gel formation and product produced there from |
| US7074879B2 (en) * | 2003-06-06 | 2006-07-11 | Eastman Chemical Company | Polyester process using a pipe reactor |
| US7135541B2 (en) | 2003-06-06 | 2006-11-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
| US20050159552A1 (en) * | 2004-01-21 | 2005-07-21 | Reed Jon S. | Flame retarded fibers and filaments and process of production therefor |
| US7666944B2 (en) * | 2004-01-21 | 2010-02-23 | Albemarle Corporation | Flame retarded fibers and filaments and process of production therefor |
| US7332548B2 (en) * | 2004-03-04 | 2008-02-19 | Eastman Chemical Company | Process for production of a polyester product from alkylene oxide and carboxylic acid |
| BRPI0418907A (pt) * | 2004-05-20 | 2007-11-27 | Albemarle Corp | aglomerados de polìmeros estirênicos aniÈnicos bromatadas inalterados e método de preparação |
| US7858715B2 (en) * | 2005-09-12 | 2010-12-28 | Crown Brands Limited | Loop reactor for emulsion polymerisation |
| US7906598B2 (en) * | 2006-08-30 | 2011-03-15 | Intertape Polymer Corp. | Recirculation loop reactor bulk polymerization process |
| US20100105847A1 (en) | 2006-01-24 | 2010-04-29 | Intertape Polymer Corp. | Plug flow bulk polymerization of vinyl monomers |
| EP2044133B1 (en) | 2006-07-20 | 2015-01-28 | Albemarle Corporation | Process technology for recovering brominated styrenic polymers from reaction mixtures in which they are formed and/or converting such mixtures into pellets or into granules or pastilles |
| JP2010502786A (ja) * | 2006-08-30 | 2010-01-28 | インターテープ ポリマー コーポレーション | 再循環ループ反応装置によるバルク重合方法 |
| WO2008066970A1 (en) | 2006-11-28 | 2008-06-05 | Albemarle Corporation | Converting brominated anionic styrenic polymer into harder and larger form for storage, shipment, and use |
| US7943094B2 (en) | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
| US7649109B2 (en) * | 2006-12-07 | 2010-01-19 | Eastman Chemical Company | Polyester production system employing recirculation of hot alcohol to esterification zone |
| US20080139780A1 (en) * | 2006-12-07 | 2008-06-12 | Debruin Bruce Roger | Polyester production system employing short residence time esterification |
| US7863477B2 (en) * | 2007-03-08 | 2011-01-04 | Eastman Chemical Company | Polyester production system employing hot paste to esterification zone |
| MX2009013127A (es) | 2007-06-07 | 2010-01-15 | Albemarle Corp | Polimeros bromados de bajo peso molecular y su uso en formulaciones termoplasticas. |
| US7847053B2 (en) * | 2007-07-12 | 2010-12-07 | Eastman Chemical Company | Multi-level tubular reactor with oppositely extending segments |
| US7872089B2 (en) | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Multi-level tubular reactor with internal tray |
| US7868129B2 (en) * | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Sloped tubular reactor with spaced sequential trays |
| US7858730B2 (en) * | 2007-07-12 | 2010-12-28 | Eastman Chemical Company | Multi-level tubular reactor with dual headers |
| US7842777B2 (en) * | 2007-07-12 | 2010-11-30 | Eastman Chemical Company | Sloped tubular reactor with divided flow |
| US7872090B2 (en) * | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Reactor system with optimized heating and phase separation |
| US7829653B2 (en) * | 2007-07-12 | 2010-11-09 | Eastman Chemical Company | Horizontal trayed reactor |
| US7868130B2 (en) * | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Multi-level tubular reactor with vertically spaced segments |
| US8993684B2 (en) | 2008-06-06 | 2015-03-31 | Albemarle Corporation | Low molecular weight brominated polymers, processes for their manufacture and their use in thermoplastic formulations |
| KR20110100216A (ko) | 2008-12-02 | 2011-09-09 | 알베마를 코포레이션 | 분지형 또는 별모양 분지형 스티렌 폴리머, 텔로머, 및 부가물, 그의 합성, 그의 브롬화, 및 그의 용도 |
| US8642821B2 (en) | 2008-12-02 | 2014-02-04 | Albemarle Corporation | Bromination of telomer mixtures derived from toluene and styrene |
| JO3423B1 (ar) | 2008-12-02 | 2019-10-20 | Albemarle Corp | مؤخرات لهب معالجة بالبروم و مواد مشتقه منها |
| CN102224122B (zh) | 2008-12-02 | 2014-09-03 | 雅宝公司 | 甲苯和苯乙烯衍生的调聚物分布物及由其制备的溴化阻燃剂 |
| JO3059B1 (ar) | 2009-05-01 | 2017-03-15 | Albemarle Corp | معالجة بالبروم لتراكيب بوليمرات عطرية ذات وزن جزيئي منخفض |
| US8753554B2 (en) | 2009-05-01 | 2014-06-17 | Albemarle Corporation | Pelletized low molecular weight brominated aromatic polymer compositions |
| EP2596860A1 (de) * | 2011-11-25 | 2013-05-29 | Fluitec Invest AG | Mit einem Wärmetauscher versehener Kreislaufreaktor |
| US9023962B2 (en) * | 2012-08-20 | 2015-05-05 | Honeywell International Inc. | Synthesis of high molecular weight poly(2,3,3,3-tetrafluoropropene) |
| US9321867B2 (en) * | 2012-12-21 | 2016-04-26 | Honeywell International Inc. | Synthesis of 2,3,3,3-tetrafluoropropene/vinylidene fluoride copolymers |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3035033A (en) * | 1957-12-12 | 1962-05-15 | Dow Chemical Co | Molding grade copolymers and process for preparing the same |
| NL7700412A (nl) * | 1977-01-15 | 1978-07-18 | Synres Internationaal Nv | Continu bereiding van polymeren in de massa. |
| US4200713A (en) * | 1977-05-04 | 1980-04-29 | Bayer Aktiengesellschaft | Process for the anionic homo- or co-polymerization of aromatic vinyl compounds |
| US4442273A (en) * | 1983-04-06 | 1984-04-10 | Atlantic Richfield Company | Process and apparatus for continuous polymerization of a monovinyl aromatic monomer |
| US4572819A (en) * | 1983-08-24 | 1986-02-25 | The Dow Chemical Company | Apparatus for anionic polymerization wherein the molecular weight of the polymer is closely controlled |
| JP2560342B2 (ja) * | 1987-09-11 | 1996-12-04 | 大日本インキ化学工業株式会社 | スチレン系樹脂の連続塊状重合法 |
| US5194525A (en) * | 1988-12-12 | 1993-03-16 | Dainippon Ink And Chemicals, Inc. | Continuous mass polymerization process for making styrene copolymers |
| EP0373883B1 (en) * | 1988-12-12 | 1996-03-06 | Dainippon Ink And Chemicals, Inc. | Continuous mass polymerization process for making styrene copolymers |
| DE4235980A1 (de) * | 1992-10-24 | 1994-04-28 | Basf Ag | Verfahren zur Herstellung einer vinylaromatischen Verbindung |
-
1996
- 1996-05-09 DE DE19618678A patent/DE19618678A1/de not_active Withdrawn
-
1997
- 1997-04-29 ES ES97107043T patent/ES2135964T3/es not_active Expired - Lifetime
- 1997-04-29 DE DE59700250T patent/DE59700250D1/de not_active Expired - Fee Related
- 1997-04-29 EP EP97107043A patent/EP0806437B1/de not_active Expired - Lifetime
- 1997-05-06 US US08/851,353 patent/US5902865A/en not_active Expired - Fee Related
- 1997-05-07 JP JP9116820A patent/JPH1045811A/ja not_active Withdrawn
- 1997-05-08 KR KR1019970017597A patent/KR100391233B1/ko not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EP0806437B1 (de) | 1999-07-07 |
| US5902865A (en) | 1999-05-11 |
| KR100391233B1 (ko) | 2003-10-10 |
| JPH1045811A (ja) | 1998-02-17 |
| DE19618678A1 (de) | 1997-11-13 |
| DE59700250D1 (de) | 1999-08-12 |
| EP0806437A1 (de) | 1997-11-12 |
| KR970074806A (ko) | 1997-12-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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