AU2001248577A1 - Apparatus and process for gas phase fluidized-bed polymerization - Google Patents
Apparatus and process for gas phase fluidized-bed polymerizationInfo
- Publication number
- AU2001248577A1 AU2001248577A1 AU2001248577A AU4857701A AU2001248577A1 AU 2001248577 A1 AU2001248577 A1 AU 2001248577A1 AU 2001248577 A AU2001248577 A AU 2001248577A AU 4857701 A AU4857701 A AU 4857701A AU 2001248577 A1 AU2001248577 A1 AU 2001248577A1
- Authority
- AU
- Australia
- Prior art keywords
- fluidized bed
- particles
- gas
- stream
- gas streams
- 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.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title abstract 3
- 238000006116 polymerization reaction Methods 0.000 title abstract 3
- 239000002245 particle Substances 0.000 abstract 4
- 150000001336 alkenes Chemical class 0.000 abstract 2
- 239000010419 fine particle Substances 0.000 abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 abstract 1
- 230000000630 rising effect Effects 0.000 abstract 1
Classifications
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- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1809—Controlling processes
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical 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
- B01J8/38—Chemical 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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical 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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/388—Chemical 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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
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- 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
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from the reactor
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00292—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00654—Controlling the process by measures relating to the particulate material
- B01J2208/00707—Fouling
-
- 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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/901—Monomer polymerized in vapor state in presence of transition metal containing catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Polymerisation Methods In General (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
A process for the continuous gas-phase (co)polymerization of one or more olefins for which a rising stream of a gas mixture, comprising at least one olefin to be (co)polymerized, maintains polymer particles in the course of formation in the fluidized state in a polymerization reactor, the said stream entraining fine particles above the fluidized bed outside the reactor, the said fine particles being substantially separated from the gas mixture using a separator, thus dividing the said stream into (i) one or more gas streams (A) substantially devoid of solid particles which is cooled and reintroduced below and/or into the bottom part of the fluidized bed, and (ii) one or more gas streams (B) comprising at least a portion of the said particles which is introduced into or above the fluidized bed, which process is characterized in that at least one of the gas streams (B) comprising the solid particles is introduced directly into the fluidized bed by a dilute-phase transport in a simple pipe, that is to say preferably without using equipment for setting in motion.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0004757 | 2000-04-13 | ||
FR0004757A FR2807758A1 (en) | 2000-04-13 | 2000-04-13 | Continuous gas-phase (co)polymerization of olefins involves introducing gas streams comprising solid particles into fluidized bed via dilute-phase transport in simple pipe |
PCT/GB2001/001727 WO2001079306A1 (en) | 2000-04-13 | 2001-04-12 | Apparatus and process for gas phase fluidized-bed polymerization |
Publications (1)
Publication Number | Publication Date |
---|---|
AU2001248577A1 true AU2001248577A1 (en) | 2001-10-30 |
Family
ID=8849221
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2001248577A Abandoned AU2001248577A1 (en) | 2000-04-13 | 2001-04-12 | Apparatus and process for gas phase fluidized-bed polymerization |
Country Status (7)
Country | Link |
---|---|
US (1) | US6911504B2 (en) |
EP (1) | EP1274747B1 (en) |
AT (1) | ATE290023T1 (en) |
AU (1) | AU2001248577A1 (en) |
DE (1) | DE60109144T2 (en) |
FR (1) | FR2807758A1 (en) |
WO (1) | WO2001079306A1 (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1651679B1 (en) * | 2003-08-07 | 2014-06-18 | Westlake Longview Corporation | Polymerization process and associated apparatus |
BRPI0821808A2 (en) * | 2007-12-27 | 2015-06-16 | Univation Tech Llc | Systems and methods for removing charged particulates from gas streams, and reactor systems that implement them |
US8129482B2 (en) * | 2008-02-27 | 2012-03-06 | Westlake Longview Corporation | Method of preventing or reducing polymer agglomeration on grid in fluidized-bed reactors |
US8124697B2 (en) * | 2008-02-27 | 2012-02-28 | Westlake Longview Corporation | Method of preventing or reducing agglomeration on grid in fluidized-bed vessel |
US8067509B2 (en) | 2008-04-22 | 2011-11-29 | Univation Technologies, Llc | Reactor systems and processes for using the same |
EP2348056A1 (en) | 2010-01-26 | 2011-07-27 | Ineos Europe Limited | Process for the gas phase polymerisation of olefins |
EP2465877A1 (en) | 2010-12-20 | 2012-06-20 | Ineos Commercial Services UK Limited | Process |
US8198384B1 (en) | 2011-01-10 | 2012-06-12 | Westlake Longview Corporation | Method for preventing or reducing clogging of a fines ejector |
ES2813282T3 (en) | 2011-03-02 | 2021-03-23 | Borealis Ag | High-performance reactor assembly for olefin polymerization |
PT2495038T (en) | 2011-03-02 | 2020-11-06 | Borealis Ag | Flexible reactor assembly for polymerization of olefins |
US9120580B2 (en) * | 2011-08-31 | 2015-09-01 | United Technologies Corporation | Ejector-driven fuel stabilization system |
US8888899B2 (en) * | 2012-04-12 | 2014-11-18 | Kellogg Brown & Root Llc | Transfer line for the primary cyclone of a gasifier |
CN102675513B (en) * | 2012-06-06 | 2013-08-07 | 吉林众鑫化工集团有限公司 | Polymerization reactor for producing ethylene propylene diene monomer by using solution method and process flow control method |
EP2890490B1 (en) | 2012-08-29 | 2020-05-06 | Borealis AG | Reactor assembly and method for polymerization of olefins |
KR101462466B1 (en) * | 2013-03-07 | 2014-11-17 | 대림산업 주식회사 | Method for polymerization of olefin |
BR112019016739B1 (en) | 2017-02-20 | 2021-11-03 | Nous, Llc | FLUIDIZED BED SYSTEMS AND METHOD |
CN113274952B (en) * | 2021-05-19 | 2022-07-26 | 浙江大学 | Method for stably controlling external circulation of fluidized bed |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2124776A1 (en) * | 1971-05-19 | 1972-12-07 | Metallgesellschaft Ag | |
FR2207145B1 (en) * | 1972-11-17 | 1975-09-12 | Naphtachimie Sa | |
DE3688007D1 (en) * | 1985-06-12 | 1993-04-22 | Metallgesellschaft Ag | COMBUSTION DEVICE WITH CIRCULATING FLUID BED. |
FR2618786B1 (en) * | 1987-07-31 | 1989-12-01 | Bp Chimie Sa | PROCESS FOR THE POLYMERIZATION OF GASEOUS OLEFINS IN A FLUIDIZED BED REACTOR |
US5345896A (en) * | 1993-04-05 | 1994-09-13 | A. Ahlstrom Corporation | Method and apparatus for circulating solid material in a fluidized bed reactor |
US5421842A (en) * | 1994-09-06 | 1995-06-06 | Exxon Research And Engineering Company | High energy level in situ attrition and break up of catalyst to maintain bed fluidization during high temperature operations |
IT1275573B (en) * | 1995-07-20 | 1997-08-07 | Spherilene Spa | PROCESS AND EQUIPMENT FOR GAS PHASE POMIMERIZATION OF ALPHA-OLEFINS |
US5969061A (en) * | 1995-10-16 | 1999-10-19 | Eastman Chemical Company | Suppression of fines in a fluid bed polyethylene process |
-
2000
- 2000-04-13 FR FR0004757A patent/FR2807758A1/en not_active Withdrawn
-
2001
- 2001-04-12 AU AU2001248577A patent/AU2001248577A1/en not_active Abandoned
- 2001-04-12 US US10/257,357 patent/US6911504B2/en not_active Expired - Fee Related
- 2001-04-12 WO PCT/GB2001/001727 patent/WO2001079306A1/en active IP Right Grant
- 2001-04-12 EP EP01921606A patent/EP1274747B1/en not_active Expired - Lifetime
- 2001-04-12 AT AT01921606T patent/ATE290023T1/en not_active IP Right Cessation
- 2001-04-12 DE DE60109144T patent/DE60109144T2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP1274747B1 (en) | 2005-03-02 |
ATE290023T1 (en) | 2005-03-15 |
DE60109144D1 (en) | 2005-04-07 |
DE60109144T2 (en) | 2005-08-04 |
EP1274747A1 (en) | 2003-01-15 |
WO2001079306A1 (en) | 2001-10-25 |
FR2807758A1 (en) | 2001-10-19 |
US20030162914A1 (en) | 2003-08-28 |
US6911504B2 (en) | 2005-06-28 |
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