AU2001289899A1 - Method for preactivating catalysts - Google Patents
Method for preactivating catalystsInfo
- Publication number
- AU2001289899A1 AU2001289899A1 AU2001289899A AU8989901A AU2001289899A1 AU 2001289899 A1 AU2001289899 A1 AU 2001289899A1 AU 2001289899 A AU2001289899 A AU 2001289899A AU 8989901 A AU8989901 A AU 8989901A AU 2001289899 A1 AU2001289899 A1 AU 2001289899A1
- Authority
- AU
- Australia
- Prior art keywords
- catalyst
- preactivated
- cocatalyst
- catalysts
- monomer
- 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
- 239000003054 catalyst Substances 0.000 title abstract 5
- 238000000034 method Methods 0.000 title abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- 239000000178 monomer Substances 0.000 abstract 2
- 238000006116 polymerization reaction Methods 0.000 abstract 2
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
- C08F4/00—Polymerisation catalysts
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2405—Stationary reactors without moving elements inside provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
-
- 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
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/04—Monomers containing three or four carbon atoms
- C08F10/06—Propene
-
- 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
- B01J2208/00548—Flow
-
- 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
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- 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
- B01J2219/00189—Controlling or regulating processes controlling the stirring velocity
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Polymerisation Methods In General (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
- Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
Abstract
Catalysts for the polymerization of C2-C20-olefins are preactivated by a process in which the catalyst is first mixed with the respective monomer, then, if appropriate, the respective cocatalyst is added and the resulting mixture is subsequently subjected to preactivation in a tube reactor and the catalyst which has been preactivated in this way is finally introduced into the actual polymerization reactor, wherein the mixture of catalyst, any cocatalyst and monomer is passed through the tube reactor in turbulent plug flow at a Reynolds number of at least 2 300.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10048003A DE10048003A1 (en) | 2000-09-26 | 2000-09-26 | Process for preactivating catalysts |
| EP10048003 | 2000-09-26 | ||
| PCT/EP2001/010847 WO2002026841A1 (en) | 2000-09-26 | 2001-09-20 | Method for preactivating catalysts |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU2001289899A1 true AU2001289899A1 (en) | 2002-04-08 |
Family
ID=7657916
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2001289899A Abandoned AU2001289899A1 (en) | 2000-09-26 | 2001-09-20 | Method for preactivating catalysts |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US20040044148A1 (en) |
| EP (1) | EP1320559B1 (en) |
| JP (1) | JP2004510036A (en) |
| KR (1) | KR100789690B1 (en) |
| CN (1) | CN1210313C (en) |
| AT (1) | ATE366756T1 (en) |
| AU (1) | AU2001289899A1 (en) |
| BR (1) | BR0114228B1 (en) |
| CA (1) | CA2424944C (en) |
| DE (2) | DE10048003A1 (en) |
| ES (1) | ES2290168T3 (en) |
| RU (1) | RU2275381C2 (en) |
| WO (1) | WO2002026841A1 (en) |
Families Citing this family (26)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PT2311897E (en) | 2000-12-07 | 2015-08-25 | Grupo Petrotemex Sa De Cv | Low cost polyester process using a pipe reactor |
| US6906164B2 (en) | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
| DE10257762B4 (en) * | 2002-12-10 | 2005-02-24 | Autoliv Development Ab | Safety belt arrangement with two retractors and padlock |
| US7135541B2 (en) | 2003-06-06 | 2006-11-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
| US7074879B2 (en) | 2003-06-06 | 2006-07-11 | Eastman Chemical Company | Polyester process using a pipe reactor |
| CN101163723B (en) * | 2003-07-04 | 2010-12-22 | 巴塞尔聚烯烃股份有限公司 | Olefin Polymerization Process |
| US7332548B2 (en) | 2004-03-04 | 2008-02-19 | Eastman Chemical Company | Process for production of a polyester product from alkylene oxide and carboxylic acid |
| US8058367B2 (en) | 2004-08-27 | 2011-11-15 | Chevron Phillips Chemical Company Lp | Methods and systems for controlling polymer particle size |
| US7645841B2 (en) * | 2004-08-27 | 2010-01-12 | Chevron Phillips Chemical Company Lp | Method and system to reduce polymerization reactor fouling |
| US7649109B2 (en) | 2006-12-07 | 2010-01-19 | Eastman Chemical Company | Polyester production system employing recirculation of hot alcohol to esterification zone |
| US7943094B2 (en) | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
| US7863477B2 (en) | 2007-03-08 | 2011-01-04 | Eastman Chemical Company | Polyester production system employing hot paste to esterification zone |
| US7858730B2 (en) | 2007-07-12 | 2010-12-28 | Eastman Chemical Company | Multi-level tubular reactor with dual headers |
| 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 |
| 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 |
| US7872090B2 (en) | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Reactor system with optimized heating and phase separation |
| US7842777B2 (en) | 2007-07-12 | 2010-11-30 | Eastman Chemical Company | Sloped tubular reactor with divided flow |
| US7847053B2 (en) | 2007-07-12 | 2010-12-07 | Eastman Chemical Company | Multi-level tubular reactor with oppositely extending segments |
| EP3010947B2 (en) * | 2013-06-19 | 2020-02-12 | Borealis AG | Process for production of polypropylene with high polydispersity |
| WO2016201008A1 (en) | 2015-06-08 | 2016-12-15 | Jaques Reifman | Method and system for measuring, predicting and optimizing human cognitive performance |
| US11866522B2 (en) | 2018-12-28 | 2024-01-09 | Braskem S.A. | Process for introducing catalyst in a polymerization process |
| US12518866B2 (en) | 2019-04-16 | 2026-01-06 | The Government Of The United States, As Represented By The Secretary Of The Army | Method and system for measuring, predicting and optimizing human alertness |
| WO2021058607A1 (en) | 2019-09-24 | 2021-04-01 | Sabic Global Technologies B.V. | Polymerization process for olefins |
| US11254761B1 (en) * | 2020-10-15 | 2022-02-22 | Chevron Phillips Chemical Company Lp | Catalyst pretreatment and feeding system for polypropylene production |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2157911T3 (en) * | 1987-02-02 | 2001-09-01 | Fina Technology | PROCEDURE TO INCREASE THE EFFECTIVENESS OF A PRE-POLYMERIZED CATALYST. |
| US4966722A (en) * | 1988-11-16 | 1990-10-30 | Exxon Chemical Patents Inc. | Oil additive compositions exhibiting reduced haze containing polymeric viscosity index improver |
| US5256732A (en) * | 1990-08-13 | 1993-10-26 | Dainippon Ink And Chemicals, Inc. | Method for the continuous bulk polymerization for impact resistant styrene resin |
| ES2114969T3 (en) * | 1992-06-18 | 1998-06-16 | Montell Technology Company Bv | PROCEDURE AND APPARATUS FOR THE GASEOUS PHASE POLYMERIZATION OF OLEFINS. |
| CA2181413A1 (en) * | 1995-07-18 | 1998-01-18 | Edwar S. Shamshoum | Process for the syndiotactic propagation of olefins |
| FI990081A0 (en) * | 1999-01-18 | 1999-01-18 | Borealis Polymers Oy | Process for transferring a polymer to a gas phase reactor |
-
2000
- 2000-09-26 DE DE10048003A patent/DE10048003A1/en not_active Withdrawn
-
2001
- 2001-09-20 CN CNB018193080A patent/CN1210313C/en not_active Expired - Fee Related
- 2001-09-20 BR BRPI0114228-3A patent/BR0114228B1/en not_active IP Right Cessation
- 2001-09-20 AT AT01969741T patent/ATE366756T1/en active
- 2001-09-20 RU RU2003112219/04A patent/RU2275381C2/en active
- 2001-09-20 AU AU2001289899A patent/AU2001289899A1/en not_active Abandoned
- 2001-09-20 US US10/380,549 patent/US20040044148A1/en not_active Abandoned
- 2001-09-20 JP JP2002531223A patent/JP2004510036A/en active Pending
- 2001-09-20 EP EP01969741A patent/EP1320559B1/en not_active Expired - Lifetime
- 2001-09-20 CA CA002424944A patent/CA2424944C/en not_active Expired - Fee Related
- 2001-09-20 ES ES01969741T patent/ES2290168T3/en not_active Expired - Lifetime
- 2001-09-20 DE DE50112723T patent/DE50112723D1/en not_active Expired - Lifetime
- 2001-09-20 KR KR1020037004002A patent/KR100789690B1/en not_active Expired - Lifetime
- 2001-09-20 WO PCT/EP2001/010847 patent/WO2002026841A1/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| DE50112723D1 (en) | 2007-08-23 |
| BR0114228A (en) | 2003-07-22 |
| EP1320559B1 (en) | 2007-07-11 |
| CN1210313C (en) | 2005-07-13 |
| CN1476454A (en) | 2004-02-18 |
| RU2275381C2 (en) | 2006-04-27 |
| ES2290168T3 (en) | 2008-02-16 |
| KR20030034195A (en) | 2003-05-01 |
| US20040044148A1 (en) | 2004-03-04 |
| KR100789690B1 (en) | 2008-01-02 |
| BR0114228B1 (en) | 2011-05-03 |
| EP1320559A1 (en) | 2003-06-25 |
| DE10048003A1 (en) | 2002-04-11 |
| JP2004510036A (en) | 2004-04-02 |
| CA2424944A1 (en) | 2003-03-25 |
| WO2002026841A1 (en) | 2002-04-04 |
| ATE366756T1 (en) | 2007-08-15 |
| CA2424944C (en) | 2010-01-12 |
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