DK1660229T3 - Fremgangsmåde og anordning til optimering af katalysatortilförsel til en polymeriseringsreaktor - Google Patents
Fremgangsmåde og anordning til optimering af katalysatortilförsel til en polymeriseringsreaktorInfo
- Publication number
- DK1660229T3 DK1660229T3 DK05707962T DK05707962T DK1660229T3 DK 1660229 T3 DK1660229 T3 DK 1660229T3 DK 05707962 T DK05707962 T DK 05707962T DK 05707962 T DK05707962 T DK 05707962T DK 1660229 T3 DK1660229 T3 DK 1660229T3
- Authority
- DK
- Denmark
- Prior art keywords
- slurry
- catalyst
- vessel
- polymerization reactor
- catalyst feed
- Prior art date
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
- B01J19/18—Stationary reactors having moving elements inside
-
- 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
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
-
- 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
-
- 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
-
- 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
-
- 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
- B01J8/0035—Periodical feeding or evacuation
-
- 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
- B01J2208/00548—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
- 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
- B01J2208/00663—Concentration
-
- 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
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00752—Feeding
-
- 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
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00069—Flow rate measurement
-
- 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
- B01J2219/00191—Control algorithm
- B01J2219/00193—Sensing a parameter
- B01J2219/00195—Sensing a parameter of the reaction system
- B01J2219/002—Sensing a parameter of the reaction system inside 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00211—Control algorithm comparing a sensed parameter with a pre-set value
- B01J2219/00213—Fixed parameter value
-
- 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
- B01J2219/00191—Control algorithm
- B01J2219/00222—Control algorithm taking actions
- B01J2219/00227—Control algorithm taking actions modifying the operating conditions
- B01J2219/00229—Control algorithm taking actions modifying the operating conditions of the reaction system
- B01J2219/00231—Control algorithm taking actions modifying the operating conditions of the reaction system at the reactor inlet
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)
- Combustion & Propulsion (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Polymerisation Methods In General (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04100569A EP1563901A1 (fr) | 2004-02-13 | 2004-02-13 | Procede et dispositif d'optimisation d'alimentation en catalyseur dans un reacteur de polymerisation |
PCT/EP2005/050538 WO2005079971A1 (fr) | 2004-02-13 | 2005-02-08 | Procede et dispositif d'optimisation de l'apport en catalyseur dans un reacteur de polymerisation |
Publications (1)
Publication Number | Publication Date |
---|---|
DK1660229T3 true DK1660229T3 (da) | 2007-05-21 |
Family
ID=34684742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK05707962T DK1660229T3 (da) | 2004-02-13 | 2005-02-08 | Fremgangsmåde og anordning til optimering af katalysatortilförsel til en polymeriseringsreaktor |
Country Status (12)
Country | Link |
---|---|
US (3) | US20070032612A1 (fr) |
EP (2) | EP1563901A1 (fr) |
JP (1) | JP4880482B2 (fr) |
KR (1) | KR101170190B1 (fr) |
CN (1) | CN1917948B (fr) |
AT (1) | ATE352371T1 (fr) |
DE (1) | DE602005000510T2 (fr) |
DK (1) | DK1660229T3 (fr) |
EA (1) | EA010362B1 (fr) |
ES (1) | ES2280077T3 (fr) |
PT (1) | PT1660229E (fr) |
WO (1) | WO2005079971A1 (fr) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1563901A1 (fr) * | 2004-02-13 | 2005-08-17 | Total Petrochemicals Research Feluy | Procede et dispositif d'optimisation d'alimentation en catalyseur dans un reacteur de polymerisation |
US7615596B2 (en) | 2005-09-30 | 2009-11-10 | Chevron Phillips Chemical Company Lp | Multiple component feed methods and systems |
EP1832338A1 (fr) * | 2006-03-07 | 2007-09-12 | Total Petrochemicals Research Feluy | Procédé et système pour déterminer l'activité d'un catalyseur |
WO2010057925A1 (fr) * | 2008-11-18 | 2010-05-27 | Total Petrochemicals Research Feluy | Procédé d’optimisation de l’introduction d’une pâte catalytique dans un réacteur de polymérisation |
JP5481060B2 (ja) * | 2008-12-01 | 2014-04-23 | 住友化学株式会社 | 予備重合触媒製造方法 |
US8217124B2 (en) * | 2009-01-16 | 2012-07-10 | Basell Polyolefine Gmbh | Ethylene polymerization in a high pressure reactor with improved initiator feeding |
EP2379606B1 (fr) | 2009-01-16 | 2012-11-28 | Basell Polyolefine GmbH | Procédé pour la polymérisation d'éthylène dans un réacteur tubulaire présentant un débit réduit |
US8609791B2 (en) † | 2009-12-18 | 2013-12-17 | Total Research & Technology Feluy | Method for replacing compatible ethylene polymerization catalysts |
EP2489431B1 (fr) | 2011-02-16 | 2013-05-01 | Linde AG | Procédé de préparation d'une composition de catalyseur pour l'oligomérisation de l'éthylène et unité de préformation de la composition de catalyseur correspondante |
KR101486135B1 (ko) | 2013-04-03 | 2015-01-23 | 삼성토탈 주식회사 | 올레핀 중합용 희석 촉매의 제조 방법 및 이를 이용한 올레핀 중합 방법 |
EP3102616B1 (fr) * | 2014-02-03 | 2020-10-14 | Saudi Basic Industries Corporation | Pré-unité de formation d'une composition de catalyseur pour la préparation d'une composition de catalyseur pour l'oligomérisation d'éthylène |
CN105413589A (zh) * | 2015-11-13 | 2016-03-23 | 中国石油集团东北炼化工程有限公司吉林设计院 | 乙丙橡胶生产的催化剂的卸料方法 |
US11331655B2 (en) | 2016-12-30 | 2022-05-17 | Sabic Global Technologies B.V. | Method for preparation of homogenous catalyst for selective 1-hexene production |
US11285469B2 (en) | 2016-12-30 | 2022-03-29 | Sabic Global Technologies B.V. | Method for preparation of a catalyst solution for selective 1-hexene production |
US10179826B2 (en) * | 2017-05-05 | 2019-01-15 | Chevron Phillips Chemical Company Lp | Polymerization catalyst delivery |
RU2695667C1 (ru) * | 2018-11-26 | 2019-07-25 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) | Устройство для получения суспензии наноразмерного катализатора и способ ее получения |
RU195804U1 (ru) * | 2019-07-19 | 2020-02-05 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А. В. Топчиева Российской академии наук (ИНХС РАН) | Устройство для проведения каталитических процессов в трехфазном суспензионном слое |
CN112403420A (zh) * | 2020-11-12 | 2021-02-26 | 湖北汇锋钻石有限公司 | 一种金刚石生产用反应釜酸处理系统 |
US11673975B2 (en) | 2021-08-24 | 2023-06-13 | Chevron Phillips Chemical Company Lp | System and method for improving dump tank purge time |
CN116212809B (zh) * | 2023-03-10 | 2024-01-19 | 宁夏宝丰昱能科技有限公司 | 电池浆料制备装置和相关的控制方法 |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2917465A (en) * | 1956-04-27 | 1959-12-15 | Phillips Petroleum Co | Polymerization catalyst feed control |
US3726845A (en) * | 1971-03-22 | 1973-04-10 | Exxon Research Engineering Co | Supplying catalyst to a reaction zone |
CA1171065A (fr) * | 1981-01-06 | 1984-07-17 | Vaclav G. Zboril | Methode de preparation de polymeres d'olefines alpha par recours a des temperatures elevees |
JPS57126808A (en) * | 1981-01-30 | 1982-08-06 | Sumitomo Chem Co Ltd | Production of ethylene copolymer having wide molecular weight distribution |
US4780513A (en) * | 1982-09-30 | 1988-10-25 | Exxon Research & Engineering Co. | Modified Lewis acid catalyzed polymerization |
US4619901A (en) * | 1985-02-21 | 1986-10-28 | Phillips Petroleum Company | Control of polymerization reaction |
JPH0286834A (ja) * | 1988-09-22 | 1990-03-27 | Hitachi Ltd | スタティックミキサーを有する反応槽 |
US5098667A (en) * | 1989-05-05 | 1992-03-24 | Phillips Petroleum Company | Particulate flow control |
US5962606A (en) * | 1997-02-19 | 1999-10-05 | Union Carbide Chemicals & Plastics Technology Corporation | Control of solution catalyst droplet size with an effervescent spray nozzle |
JP2000086705A (ja) * | 1998-09-11 | 2000-03-28 | Idemitsu Petrochem Co Ltd | ポリプロピレン気相重合法における固体重合触媒の連続供給方法 |
US6916892B2 (en) * | 2001-12-03 | 2005-07-12 | Fina Technology, Inc. | Method for transitioning between Ziegler-Natta and metallocene catalysts in a bulk loop reactor for the production of polypropylene |
ES2342932T3 (es) * | 2002-09-16 | 2010-07-19 | Chevron Phillips Chemical Company Lp | Dispositivo de alimentacion de una suspension de catalizador para un reactor de polimerizacion. |
EP1563901A1 (fr) * | 2004-02-13 | 2005-08-17 | Total Petrochemicals Research Feluy | Procede et dispositif d'optimisation d'alimentation en catalyseur dans un reacteur de polymerisation |
-
2004
- 2004-02-13 EP EP04100569A patent/EP1563901A1/fr not_active Withdrawn
-
2005
- 2005-02-08 AT AT05707962T patent/ATE352371T1/de not_active IP Right Cessation
- 2005-02-08 JP JP2006552614A patent/JP4880482B2/ja not_active Expired - Fee Related
- 2005-02-08 EA EA200601491A patent/EA010362B1/ru not_active IP Right Cessation
- 2005-02-08 KR KR1020067018047A patent/KR101170190B1/ko active IP Right Grant
- 2005-02-08 DK DK05707962T patent/DK1660229T3/da active
- 2005-02-08 CN CN2005800048781A patent/CN1917948B/zh active Active
- 2005-02-08 EP EP05707962A patent/EP1660229B1/fr active Active
- 2005-02-08 PT PT05707962T patent/PT1660229E/pt unknown
- 2005-02-08 DE DE602005000510T patent/DE602005000510T2/de active Active
- 2005-02-08 ES ES05707962T patent/ES2280077T3/es active Active
- 2005-02-08 WO PCT/EP2005/050538 patent/WO2005079971A1/fr active IP Right Grant
-
2006
- 2006-08-01 US US11/499,043 patent/US20070032612A1/en not_active Abandoned
-
2010
- 2010-05-12 US US12/778,401 patent/US8258245B2/en not_active Expired - Fee Related
-
2012
- 2012-07-12 US US13/547,624 patent/US8501883B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN1917948B (zh) | 2013-09-11 |
CN1917948A (zh) | 2007-02-21 |
DE602005000510D1 (de) | 2007-03-15 |
ATE352371T1 (de) | 2007-02-15 |
KR101170190B1 (ko) | 2012-07-31 |
EP1563901A1 (fr) | 2005-08-17 |
US20130011310A1 (en) | 2013-01-10 |
WO2005079971A1 (fr) | 2005-09-01 |
DE602005000510T2 (de) | 2007-11-08 |
EA200601491A1 (ru) | 2007-02-27 |
US20100267904A1 (en) | 2010-10-21 |
US8501883B2 (en) | 2013-08-06 |
US8258245B2 (en) | 2012-09-04 |
EP1660229A1 (fr) | 2006-05-31 |
EA010362B1 (ru) | 2008-08-29 |
KR20060126593A (ko) | 2006-12-07 |
PT1660229E (pt) | 2007-04-30 |
US20070032612A1 (en) | 2007-02-08 |
JP4880482B2 (ja) | 2012-02-22 |
ES2280077T3 (es) | 2007-09-01 |
JP2007522311A (ja) | 2007-08-09 |
EP1660229B1 (fr) | 2007-01-24 |
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