ES2087067T3 - Procedimiento para el mezclamiento in situ de polimeros. - Google Patents
Procedimiento para el mezclamiento in situ de polimeros.Info
- Publication number
- ES2087067T3 ES2087067T3 ES89121160T ES89121160T ES2087067T3 ES 2087067 T3 ES2087067 T3 ES 2087067T3 ES 89121160 T ES89121160 T ES 89121160T ES 89121160 T ES89121160 T ES 89121160T ES 2087067 T3 ES2087067 T3 ES 2087067T3
- Authority
- ES
- Spain
- Prior art keywords
- reactor
- ethylene
- alpha
- olefin
- copolymer
- 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
-
- 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
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- 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
- C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
- C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
- C08F297/08—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins
-
- 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
-
- 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
- C08F2/34—Polymerisation in gaseous state
-
- 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
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Polymerisation Methods In General (AREA)
- Superconductors And Manufacturing Methods Therefor (AREA)
- Road Paving Structures (AREA)
- Excavating Of Shafts Or Tunnels (AREA)
- Reinforced Plastic Materials (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
- Materials For Medical Uses (AREA)
- Electroluminescent Light Sources (AREA)
- Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)
Abstract
UN PROCESO PARA LA MEZCLA "IN SITU" DE POLIMEROS COMPRENDIENDO CONTACTAR CONTINUAMENTE, BAJO CONDICIONES DE POLIMERIZACION, UNA MEZCLA DE ETILENO Y AL MENOS UNA ALFA-OLEFINA, TENIENDO AL MENOS 3 ATOMOS DE CARBONO CON UN CATALIZADOR EN AL MENOS DOS LECHOS FLUIDOS REACTORES CONECTADOS EN SERIE, COMPRENDIENDO DICHO CATALIZADOR: (I) UN COMPLEJO CONSISTIENDO ESENCIALMENTE DE MAGNESIO, TITANIO, UN HALOGENO,Y UN DONADOR DE ELECTRON; (II) AL MENOS UN COMPUESTO ACTIVADOR PARA EL COMPLEJO TENIENDO LA FORMULA AIR''''EX''FHG EN DONDE X'' ES CL O OR'''''';R'''' Y R'''''' SON RADICALES HIDROCARBUROS ALIFATICOS TENIENDO DE 1 A 14 ATOMOS DE CARBONO Y SIENDO SIMILARES O DIFERENTES; F ES 0 A 1,5; G ES 0 O 1; Y E + F + G =3; Y (III) UN CATALIZADOR ALUMINO HIDROCARBILO, SIENDO LAS CONDICIONES DE POLIMERIZACION TALES QUE COPOLIMERO DE ETILENO TENIENDO UN ALTO INDICE DE FUSION EN EL MARGEN DE ALREDEDOR DE 0,1 A ALREDEDOR DE 1000 GRAMOS POR 10 MINUTOS SE FORMA EN AL MENOS UN REACTOR Y COPOLIMERO DE ETILENO TENIENDO UN BAJO INDICE DE FUSION EN EL MARGEN DE ALREDEDOR DE 0,001 A ALREDEDOR DE 1,0 GRAMOS POR 10 MINUTOS SE FORMA EN AL MENOS EL OTRO REACTOR, TENIENDO CADA COPOLIMERO UNA DENSIDAD DE ALREDEDOR DE 0,860 A ALREDEDOR DE 0,965 GRAMOS POR CENTIMETRO CUBICO Y UN MARGEN DE FLUJO FUNDIDO DE ALREDEDOR DE 20 A ALREDEDOR DE 70, Y ESTANDO MEZCLADOS CON CATALIZADOR ACTIVO, CON LA PROVISION DE QUE: (A)LA MEZCLA DE COPOLIMERO DE ETILENO Y CATALIZADOR ACTIVO FORMADO EN UN REACTOR DE LA SERIE SE TRANSFIERE AL REACTOR QUE LE SUCEDE INMEDIATAMENTE EN LA SERIE; (B)EN EL REACTOR EN EL CUAL SE HACE EL COPOLIMERO DE BAJO INDICE DE FUSION: (1)LA ALFA-OLEFINA ESTA PRESENTE EN UN MARGEN DE ALREDEDOR DE 0,02 A ALREDEDOR DE 3,5 MOLES DE ALFA-OLEFINA POR MOL DE ETILENO; Y (2)HIDROGENO ESTA OPCIONALMENTE PRESENTE EN EL MARGEN DE ALREDEDOR DE 0,001 A ALREDEDOR DE 0,5 MOLES DE HIDROGENO POR MOL DE ETILENO COMBINADO Y ALFA-OLEFINA; (C)EN EL REACTOR EN EL CUAL SE HACE EL COPOLIMERO DE BAJO INDICE DE FUSION: (1)LA ALFA-OLEFINA ESTA PRESENTE EN EL MARGEN DE ALREDEDOR DE 0,02 A ALREDEDOR DE 3,5 MOLES DE ALFA-OLEFINA POR MOL DE ETILENO; Y (2)HIDROGENO ESTA PRESENTE EN EL MARGEN DE ALREDEDOR DE 0,05 A ALREDEDOR DE 3 MOLES DE HIDROGENO POR MOL DE ETILENO COMBINADO Y ALFA-OLEFINA; Y (D)COCATALIZADOR ADICIONAL DE ALUMINO HIDROCARBILO SE INTRODUCE EN CADA REACTOR DE LA SERIE QUE SIGUE AL PRIMER REACTOR EN UNA CANTIDAD SUFICIENTE PARA RESTAURAR EL NIVEL DE LA ACTIVIDAD DEL CATALIZADOR TRANSFERIDO DEL REACTOR PRECEDENTE EN LA SERIE A ALREDEDOR DEL NIVEL INICIAL DE ACTIVIDAD EN EL PRIMER REACTOR.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/271,639 US5047468A (en) | 1988-11-16 | 1988-11-16 | Process for the in situ blending of polymers |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2087067T3 true ES2087067T3 (es) | 1996-07-16 |
Family
ID=23036442
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES89121160T Expired - Lifetime ES2087067T3 (es) | 1988-11-16 | 1989-11-15 | Procedimiento para el mezclamiento in situ de polimeros. |
Country Status (25)
Country | Link |
---|---|
US (1) | US5047468A (es) |
EP (1) | EP0369436B1 (es) |
JP (1) | JPH07116256B2 (es) |
KR (1) | KR950000037B1 (es) |
CN (1) | CN1040219C (es) |
AT (1) | ATE138087T1 (es) |
AU (1) | AU619357B2 (es) |
BR (1) | BR8905803A (es) |
CA (1) | CA2002992C (es) |
CZ (1) | CZ282728B6 (es) |
DE (1) | DE68926490T2 (es) |
EG (1) | EG18942A (es) |
ES (1) | ES2087067T3 (es) |
FI (1) | FI895432A0 (es) |
GR (1) | GR3019960T3 (es) |
HU (1) | HU206508B (es) |
MY (1) | MY106027A (es) |
NO (1) | NO173242C (es) |
NZ (1) | NZ231393A (es) |
PH (1) | PH26989A (es) |
PL (1) | PL163483B1 (es) |
PT (1) | PT92322B (es) |
SK (1) | SK280092B6 (es) |
TR (1) | TR24887A (es) |
ZA (1) | ZA898724B (es) |
Families Citing this family (102)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6025448A (en) | 1989-08-31 | 2000-02-15 | The Dow Chemical Company | Gas phase polymerization of olefins |
US6538080B1 (en) | 1990-07-03 | 2003-03-25 | Bp Chemicals Limited | Gas phase polymerization of olefins |
US5688865A (en) * | 1991-03-06 | 1997-11-18 | Mobil Oil Corporation | Process and system for preventing pressure tap fouling in tandem polymerization reactors |
US6194520B1 (en) | 1991-03-06 | 2001-02-27 | Mobil Oil Corporation | Ethylene polymer resins for blow molding applications |
US6316546B1 (en) | 1991-03-06 | 2001-11-13 | Exxonmobil Oil Corporation | Ethylene polymer film resins |
DE69218995T2 (de) * | 1991-03-06 | 1997-10-16 | Mobil Oil Corp | Verfahren zur Herstellung von bimodale Polyethylen in Serien-Reaktoren |
EP0533452A1 (en) * | 1991-03-21 | 1993-03-24 | Mobil Oil Corporation | Production of bimodal ethylene polymers in tandem reactors |
US5693583A (en) * | 1991-06-10 | 1997-12-02 | Mobil Oil Corporation | High activity polyethylene catalysts which produce bimodal or trimodal product molecular weight distributions |
EP0528523B1 (en) * | 1991-07-24 | 2001-10-10 | Mobil Oil Corporation | Improved ethylene polymer film resins |
US5250612A (en) * | 1991-10-07 | 1993-10-05 | The Dow Chemical Company | Polyethylene films exhibiting low blocking force |
US5278272A (en) | 1991-10-15 | 1994-01-11 | The Dow Chemical Company | Elastic substantialy linear olefin polymers |
US5525695A (en) | 1991-10-15 | 1996-06-11 | The Dow Chemical Company | Elastic linear interpolymers |
US5674342A (en) | 1991-10-15 | 1997-10-07 | The Dow Chemical Company | High drawdown extrusion composition and process |
US5582923A (en) | 1991-10-15 | 1996-12-10 | The Dow Chemical Company | Extrusion compositions having high drawdown and substantially reduced neck-in |
US5395471A (en) | 1991-10-15 | 1995-03-07 | The Dow Chemical Company | High drawdown extrusion process with greater resistance to draw resonance |
US5847053A (en) * | 1991-10-15 | 1998-12-08 | The Dow Chemical Company | Ethylene polymer film made from ethylene polymer blends |
US5783638A (en) | 1991-10-15 | 1998-07-21 | The Dow Chemical Company | Elastic substantially linear ethylene polymers |
US5284613A (en) * | 1992-09-04 | 1994-02-08 | Mobil Oil Corporation | Producing blown film and blends from bimodal high density high molecular weight film resin using magnesium oxide-supported Ziegler catalyst |
US5314746A (en) * | 1992-11-12 | 1994-05-24 | Quantum Chemical Corporation | Soft, puncture- and tear-resistant polyolefin films |
US5705576A (en) * | 1992-11-12 | 1998-01-06 | Quantum Chemical Corporation | Process for controlling production of in-situ thermoplastic polyolefins and products |
US5587436A (en) * | 1992-11-12 | 1996-12-24 | Quantum Chemical Corporation | Process for controlling the polymerization of propylene and ethylene and copolymer products |
GB9224876D0 (en) † | 1992-11-27 | 1993-01-13 | Exxon Chemical Patents Inc | Improved processing polyolefin blends |
BE1006439A3 (fr) * | 1992-12-21 | 1994-08-30 | Solvay Societe Annonyme | Procede de preparation d'une composition de polymeres d'ethylene, composition de polymeres d'ethylene et son utilisation. |
US5371145A (en) * | 1993-06-08 | 1994-12-06 | Union Carbide Chemicals & Plastics Technology Corporation | High density, high molecular weight polyethylene |
ES2155095T5 (es) * | 1993-10-21 | 2006-04-16 | Exxonmobil Oil Corporation | Mezclas de poliolefinas con distribucion bimodal de pesos moleculares. |
US5442018A (en) * | 1994-04-01 | 1995-08-15 | Union Carbide Chemicals & Plastics Technology Corporation | Ethylene polymerization using a titanium and vanadium catalyst system in staged reactors |
CN1068018C (zh) * | 1994-05-09 | 2001-07-04 | 陶氏化学公司 | 中等模量的薄膜及制造方法 |
TW354791B (en) * | 1994-06-20 | 1999-03-21 | Borealis Polymers Oy | Procatalyst for ethylene polymer production, method for its preparation and use |
FI942949A0 (fi) * | 1994-06-20 | 1994-06-20 | Borealis Polymers Oy | Prokatalysator foer producering av etenpolymerer och foerfarande foer framstaellning daerav |
US5405901A (en) * | 1994-07-06 | 1995-04-11 | Union Carbide Chemicals & Plastics Technology Corporation | Process of producing ethylene polymer blends in gas phase |
US5503914A (en) | 1994-07-08 | 1996-04-02 | Union Carbide Chemicals & Plastics Technology Corporation | Film extruded from an in situ blend of ethylene copolymers |
US5514455A (en) | 1994-07-08 | 1996-05-07 | Union Carbide Chemicals & Plastics Technology Corporation | Film extruded from an in situ blend of ethylene copolymers |
US5792534A (en) | 1994-10-21 | 1998-08-11 | The Dow Chemical Company | Polyolefin film exhibiting heat resistivity, low hexane extractives and controlled modulus |
US5589539A (en) | 1994-11-23 | 1996-12-31 | Union Carbide Chemicals & Plastics Technology Corporation | Process for preparing an in situ polyethylene blend |
EP0713889A2 (en) | 1994-11-23 | 1996-05-29 | Union Carbide Chemicals & Plastics Technology Corporation | In situ polyethylene blend |
CN1285624C (zh) * | 1994-12-16 | 2006-11-22 | 三菱化学株式会社 | 乙烯聚合物 |
US5882750A (en) * | 1995-07-03 | 1999-03-16 | Mobil Oil Corporation | Single reactor bimodal HMW-HDPE film resin with improved bubble stability |
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US6070394A (en) * | 1997-09-12 | 2000-06-06 | Eastman Chemical Company | Lownoise stretch wrapping process |
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SE9802087D0 (sv) | 1998-06-12 | 1998-06-12 | Borealis Polymers Oy | An insulating composition for communication cables |
SE9802386D0 (sv) | 1998-07-03 | 1998-07-03 | Borealis As | Composition for elektric cables |
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US6599991B1 (en) | 1999-12-30 | 2003-07-29 | Eastman Kodak Company | In-situ blending of polyesters with poly(ether imide) |
FI111954B (fi) * | 2000-02-21 | 2003-10-15 | Borealis Tech Oy | Menetelmä polyeteenipäällysteen valmistamiseksi substraatille |
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US7211534B2 (en) * | 2003-02-12 | 2007-05-01 | Formosa Plastics Corporation, U.S.A. | Preparation of a magnesium halide support for olefin polymerization and a catalyst composition using the same |
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JPS56166207A (en) * | 1980-05-27 | 1981-12-21 | Mitsui Petrochem Ind Ltd | Gas-phase polymerization of olefin |
JPS581708A (ja) * | 1981-06-25 | 1983-01-07 | Mitsubishi Chem Ind Ltd | ポリオレフインの製造法 |
JPS588712A (ja) * | 1981-07-08 | 1983-01-18 | Showa Denko Kk | エチレン系共重合体の製造方法 |
JPS58122908A (ja) * | 1982-01-19 | 1983-07-21 | Mitsubishi Chem Ind Ltd | オレフインの重合方法 |
JPS59115310A (ja) * | 1982-12-22 | 1984-07-03 | Mitsubishi Chem Ind Ltd | ポリオレフインの製造法 |
JPS59179508A (ja) * | 1983-03-29 | 1984-10-12 | Toa Nenryo Kogyo Kk | エチレン共重合体の製造法 |
US4525322A (en) * | 1983-06-28 | 1985-06-25 | E. I. Du Pont De Nemours And Company | Ethylene polymer composition for blow molding |
DE3324793A1 (de) * | 1983-07-09 | 1985-01-17 | Basf Ag, 6700 Ludwigshafen | Verfahren zum herstellen von propylen-ethylen-polymerisaten vom typ der sogenannten block-copolymerisate |
US4520163A (en) * | 1984-01-09 | 1985-05-28 | Shell Oil Company | Process of sequentially copolymerizing propylene-ethylene copolymers and catalyst therefor |
FR2577558B1 (fr) * | 1985-02-19 | 1987-03-06 | Bp Chimie Sa | Polymerisation en plusieurs etapes d'alpha-olefines en phase gazeuse |
US4882380A (en) * | 1987-07-07 | 1989-11-21 | Union Carbide Chemicals And Plastics Company Inc. | Process for the production of impact polypropylene copolymers |
DE3723526A1 (de) * | 1987-07-16 | 1989-01-26 | Hoechst Ag | Verfahren zur herstellung eines polyolefins mit einer breiten molmassenverteilung |
AU599201B2 (en) * | 1988-01-29 | 1990-07-12 | Basf Aktiengesellschaft | Preparation of propylene/ethylene polymers |
-
1988
- 1988-11-16 US US07/271,639 patent/US5047468A/en not_active Expired - Lifetime
-
1989
- 1989-11-15 ZA ZA898724A patent/ZA898724B/xx unknown
- 1989-11-15 EP EP89121160A patent/EP0369436B1/en not_active Expired - Lifetime
- 1989-11-15 KR KR1019890016523A patent/KR950000037B1/ko not_active IP Right Cessation
- 1989-11-15 HU HU895915A patent/HU206508B/hu not_active IP Right Cessation
- 1989-11-15 NO NO894548A patent/NO173242C/no unknown
- 1989-11-15 AU AU44699/89A patent/AU619357B2/en not_active Expired
- 1989-11-15 PL PL89282312A patent/PL163483B1/pl unknown
- 1989-11-15 PH PH39533A patent/PH26989A/en unknown
- 1989-11-15 ES ES89121160T patent/ES2087067T3/es not_active Expired - Lifetime
- 1989-11-15 FI FI895432A patent/FI895432A0/fi not_active Application Discontinuation
- 1989-11-15 NZ NZ231393A patent/NZ231393A/xx unknown
- 1989-11-15 SK SK6463-89A patent/SK280092B6/sk unknown
- 1989-11-15 MY MYPI89001690A patent/MY106027A/en unknown
- 1989-11-15 AT AT89121160T patent/ATE138087T1/de not_active IP Right Cessation
- 1989-11-15 CA CA002002992A patent/CA2002992C/en not_active Expired - Lifetime
- 1989-11-15 PT PT92322A patent/PT92322B/pt not_active IP Right Cessation
- 1989-11-15 CZ CS896463A patent/CZ282728B6/cs not_active IP Right Cessation
- 1989-11-15 JP JP1295174A patent/JPH07116256B2/ja not_active Expired - Lifetime
- 1989-11-15 DE DE68926490T patent/DE68926490T2/de not_active Expired - Lifetime
- 1989-11-15 CN CN89109264A patent/CN1040219C/zh not_active Expired - Fee Related
- 1989-11-16 EG EG56389A patent/EG18942A/xx active
- 1989-11-16 BR BR898905803A patent/BR8905803A/pt not_active IP Right Cessation
- 1989-11-21 TR TR89/0983A patent/TR24887A/xx unknown
-
1996
- 1996-05-17 GR GR960401333T patent/GR3019960T3/el unknown
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