ES2079844T3 - Proceso en varias etapas para producir polietileno. - Google Patents

Proceso en varias etapas para producir polietileno.

Info

Publication number
ES2079844T3
ES2079844T3 ES92900629T ES92900629T ES2079844T3 ES 2079844 T3 ES2079844 T3 ES 2079844T3 ES 92900629 T ES92900629 T ES 92900629T ES 92900629 T ES92900629 T ES 92900629T ES 2079844 T3 ES2079844 T3 ES 2079844T3
Authority
ES
Spain
Prior art keywords
pct
ethylene
loop reactor
polymerization
mixture
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
Application number
ES92900629T
Other languages
English (en)
Inventor
Antero Ahvenainen
Kari Sarantila
Henrik Andtsjo
Jouni Takakarhu
Ari Palmroos
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Borealis Polymers Oy
Original Assignee
Borealis Polymers Oy
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=8531654&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ES2079844(T3) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Borealis Polymers Oy filed Critical Borealis Polymers Oy
Application granted granted Critical
Publication of ES2079844T3 publication Critical patent/ES2079844T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F297/00Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/06Macromolecular 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
    • C08F297/08Macromolecular 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
    • C08F297/083Macromolecular 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 the monomers being ethylene or propylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • B01J19/2435Loop-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/02Ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/905Polymerization in presence of transition metal containing catalyst in presence of hydrogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Engineering & Computer Science (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Polyethers (AREA)
  • Peptides Or Proteins (AREA)
  • Image Processing (AREA)
  • Nuclear Medicine (AREA)

Abstract

LA INVENCION SE REFIERE A UN PROCESO MULTIETAPA PARA PRODUCIR POLIETILENO QUE TENGA UNA DISTRIBUCION DE PESO MOLECULAR BIMODAL Y / O ESTRECHA EN LA PRESENCIA DE UN SISTEMA CATALIZADOR DE POLIMERIZACION DEL ETILENO EN UNA SECUENCIA DE REACCION MULTIETAPA, EN LA CUAL EL PRIMER PASO DE REACCION ES UN PASO DE POLIMERIZACION DE LA FASE LIQUIDA Y EL SEGUNDO PASO DE REACCION ESTA FORMADO POR UNO O MAS PASOS DE POLIMERIZACION DE FASE GASEOSA. DE ACUERDO CON EL PROCESO DE LA INVENCION EN EL PRIMER PASO DE LA REACCION EL ETILENO SE POLIMERIZA EN UN REACTOR DE BUCLE (10) EN UN MEDIO DE HIDROCARBONO INERTE DE BAJA EBULLICION, EL TIEMPO DE RESIDENCIA SERA DE AL MENOS 10 MINUTOS, LA MEZCLA DE REACCION SE DESCARGA DEL REACTOR DE BUCLE (10) Y AL MENOS UNA PARTE SUBSTANCIAL DE LA MEZCLA DE HIDROCARBONO INERTE SE SEPARA Y EL POLIMERO SE TRANSFIERE AL INTERIOR DE UNO O MAS REACTORES DE FASE GASEOSA (30), DONDE SE COMPLETA LA POLIMERIZACION EN LA PRESENCIA DE ETILENO Y OPCIONALMENTE DE HIDROGENO Y UN COMONOMERO. COMO MEDIO DE HIDROCARBONO INERTE EN EL REACTOR DE BUCLE (10) PUEDE USARSE EL PROPANO Y LA POLIMERIZACION PUEDE LLEVARSE A CABO TAMBIEN DE FORMA QUE LA MEZCLA DEL HIDROCARBONO INERTE, EL MONOMERO, EL HIDROGENO Y EL COMONOMERO OPCIONAL SE ENCUENTRE BAJO CONDICIONES SUPERCRITICAS.
ES92900629T 1990-12-28 1991-12-20 Proceso en varias etapas para producir polietileno. Expired - Lifetime ES2079844T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FI906428A FI86867C (fi) 1990-12-28 1990-12-28 Flerstegsprocess foer framstaellning av polyeten

Publications (1)

Publication Number Publication Date
ES2079844T3 true ES2079844T3 (es) 1996-01-16

Family

ID=8531654

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92900629T Expired - Lifetime ES2079844T3 (es) 1990-12-28 1991-12-20 Proceso en varias etapas para producir polietileno.

Country Status (11)

Country Link
US (1) US5326835A (es)
EP (1) EP0517868B1 (es)
JP (1) JP2529923B2 (es)
AT (1) ATE130316T1 (es)
DE (2) DE517868T1 (es)
DK (1) DK0517868T3 (es)
ES (1) ES2079844T3 (es)
FI (1) FI86867C (es)
GR (1) GR3018786T3 (es)
NO (1) NO179286C (es)
WO (1) WO1992012182A1 (es)

Families Citing this family (765)

* Cited by examiner, † Cited by third party
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DE69606188T2 (de) * 1995-10-10 2000-06-08 Borealis A/S, Lyngby Verfahren zur herstellung von propylen homo- oder copolymeren
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SE9703798D0 (sv) 1997-10-20 1997-10-20 Borealis As Electric cable and a method an composition for the production thereof
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EP0517868B1 (en) 1995-11-15
FI86867C (fi) 1992-10-26
US5326835A (en) 1994-07-05
NO923334L (no) 1992-08-26
NO179286C (no) 1996-09-11
DK0517868T3 (da) 1996-03-18
NO923334D0 (no) 1992-08-26
FI906428A (fi) 1992-06-29
EP0517868A1 (en) 1992-12-16
JP2529923B2 (ja) 1996-09-04
WO1992012182A1 (en) 1992-07-23
JPH05504786A (ja) 1993-07-22
GR3018786T3 (en) 1996-04-30
FI86867B (fi) 1992-07-15
DE517868T1 (de) 1993-07-22
DE69114696T2 (de) 1996-04-11
ATE130316T1 (de) 1995-12-15
DE69114696D1 (de) 1995-12-21
NO179286B (no) 1996-06-03
FI906428A0 (fi) 1990-12-28

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