AR046117A1 - Monitoreo de la polimerizacion y metodo para seleccionar indicadores guia - Google Patents
Monitoreo de la polimerizacion y metodo para seleccionar indicadores guiaInfo
- Publication number
- AR046117A1 AR046117A1 ARP040103745A ARP040103745A AR046117A1 AR 046117 A1 AR046117 A1 AR 046117A1 AR P040103745 A ARP040103745 A AR P040103745A AR P040103745 A ARP040103745 A AR P040103745A AR 046117 A1 AR046117 A1 AR 046117A1
- Authority
- AR
- Argentina
- Prior art keywords
- polymer
- reactor
- guide indicator
- flow rate
- target
- Prior art date
Links
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
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0033—Optimalisation processes, i.e. processes with adaptive control systems
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1812—Tubular reactors
- B01J19/1837—Loop-type reactors
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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
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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
- C08F2/00—Processes of polymerisation
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
- B01J2219/00081—Tubes
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/00108—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
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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
- 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
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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
- 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
- B01J2219/00202—Sensing a parameter of the reaction system at the reactor outlet
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00209—Control algorithm transforming a sensed parameter
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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
- 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
- B01J2219/00218—Dynamically variable (in-line) parameter values
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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
- 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
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00243—Mathematical modelling
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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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
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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
- 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
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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
- C08F2400/00—Characteristics for processes of polymerization
- C08F2400/02—Control or adjustment of polymerization parameters
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Automation & Control Theory (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Las realizaciones se relacionan, en general, con métodos para el monitoreo o control de reacciones de polimerización que incluyen reacciones que producen productos poliméricos multimodales que emplean catalizadores múltiples en un reactor único. Las realizaciones presentan métodos para monitorear rápidamente y controlar las reacciones de polimerización sin necesidad de tomar muestras y analizar las propiedades del polímero. El método utiliza datos de control del reactor y datos de la existencia de material en una función matemática de indicador guía para controlar las condiciones del reactor y, de esa manera, de los productos producidos en esas condiciones. Reivindicación 1: Un método para calcular un valor de indicador guía target (LIT para controlar un reactor de polimerización y, de esa manera, controlar las propiedades de un producto polimérico producido en el mismo, propiedades que comprenden el índice de flujo (FI) determinado según el Procedimiento Bn de ASTM D1238-01 en la condición 190/21.6, que comprende: a) calcular un indicador guía target (LIT) que corresponde a un producto polimérico objetivo, donde dicho indicador guía target,(LIT) se define de la siguiente manera: LIT=(In(FIT)-A1-C´1 x FIH)/C´2; donde FIT es el índice de flujo target del polímero que se ha de producir después del ajuste de las condiciones de reacción según un nuevo indicador guía (el índice de flujo se determina de acuerdo con el Procedimiento B de ASTM D1238-01 en la condición 190/21.6 en el cual: A1=In(FIT)-C´2 x LIP-C´1 x FIHO; y donde FIO es el índice e flujo medido del polímero producido de acuerdo con el indicador guía anterior de las condiciones del reactor; donde C´1 es una constante relacionada con el sistema catalítico; donde LIP es el indicador guía calculado por una técnica de promedios exponencialmente ponderados del período de tiempo anterior para el período en el cual se determina el FIT y FIHO de las muestras, donde el LIP es un promedio móvil exponencialmente ponderado del LI, calculado con un factor de ponderación l =1-exp(-Dt/(tiempo de permanencia del polímero) sobre la base del tiempo de permanencia del polímero en el reactor, donde el cálculo es LIP = (l + LI)+(1-l)xLIT-1; donde FIHO es el índice de flujo del polímero de mayor peso molecular medido en el polímero producido de acuerdo con las condiciones del indicador guía anterior, determinado por la fórmula: FIHO = In (-0,33759 + 0,516577*In(I21.6)-0,01523*(I21.6/I21.6)); en la cual se determina el índice de flujo del polímero de peso molecular más elevado producido por el sistema catalítico bajo los parámetros actuales del reactor, estimados según los modelos que exhiben cambios del FIH basados en los cambios de las condiciones del reactor; C´2 es una constante relacionada con el sistema catalítico y b) cambiar por lo menos un parámetro del reactor a fin de ajustar el indicador guía en pos del nuevo valor de indicador guía objetivo.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US51235503P | 2003-10-17 | 2003-10-17 | |
US51250203P | 2003-10-17 | 2003-10-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR046117A1 true AR046117A1 (es) | 2005-11-23 |
Family
ID=35414966
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP040103744A AR046181A1 (es) | 2003-10-17 | 2004-10-15 | Monitoreo y control de la polimerizacion usando indicadores guia mejorados |
ARP040103745A AR046117A1 (es) | 2003-10-17 | 2004-10-20 | Monitoreo de la polimerizacion y metodo para seleccionar indicadores guia |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP040103744A AR046181A1 (es) | 2003-10-17 | 2004-10-15 | Monitoreo y control de la polimerizacion usando indicadores guia mejorados |
Country Status (10)
Country | Link |
---|---|
US (2) | US7838605B2 (es) |
EP (2) | EP1675877B1 (es) |
JP (2) | JP2007508444A (es) |
CN (3) | CN100579990C (es) |
AR (2) | AR046181A1 (es) |
BR (2) | BRPI0415515B1 (es) |
CA (2) | CA2542736A1 (es) |
RU (2) | RU2361883C2 (es) |
TW (2) | TW200523272A (es) |
WO (2) | WO2005040226A2 (es) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
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EP1336625A1 (en) * | 2002-02-14 | 2003-08-20 | Novolen Technology Holdings C.V. | Solid catalytic component and catalytic system of the Ziegler-Natta type, process for their preparation and their use in the polymerisation of alk-1-enes |
US8058366B2 (en) * | 2003-10-17 | 2011-11-15 | Univation Technologies, Llc | Polymerization monitoring and method of selecting leading indicators |
US7321015B2 (en) * | 2004-12-07 | 2008-01-22 | Nova Chemicals (International) S.A. | Adjusting polymer characteristics through process control |
US7323523B2 (en) * | 2004-12-07 | 2008-01-29 | Nova Chemicals (International) S.A. | Adjusting polymer characteristics through process control |
US7790816B2 (en) * | 2006-08-04 | 2010-09-07 | Univation Technologies, Llc | Method of maintaining heat transfer capacity in a polymerization reaction system |
WO2008076386A1 (en) * | 2006-12-18 | 2008-06-26 | Univation Technologies, Llc | Method for reducing and/or preventing production of excessively low density polymer product during polymerization transitions |
EP2055721A1 (en) * | 2007-11-05 | 2009-05-06 | Total Petrochemicals Research Feluy | Method for optimising the transition from one polymer grade to another |
EP2222725B1 (en) * | 2007-12-27 | 2019-06-19 | Univation Technologies, LLC | Systems and methods for removing entrained particulates from gas streams |
EP2172490A1 (en) * | 2008-10-03 | 2010-04-07 | Ineos Europe Limited | Controlled polymerisation process |
WO2010077606A1 (en) * | 2008-12-08 | 2010-07-08 | Rensselaer Polytechnic Institute | Redox-initiated cationic polymerization using vapor-state reducing agents |
US8822610B2 (en) * | 2008-12-22 | 2014-09-02 | ATRP Solutions, Inc. | Control over controlled radical polymerization processes |
US8940842B2 (en) | 2012-09-24 | 2015-01-27 | Chevron Phillips Chemical Company Lp | Methods for controlling dual catalyst olefin polymerizations |
CN104662048B (zh) * | 2012-09-28 | 2018-03-30 | 英尼奥斯欧洲股份公司 | 制备聚合物的方法 |
US8957168B1 (en) * | 2013-08-09 | 2015-02-17 | Chevron Phillips Chemical Company Lp | Methods for controlling dual catalyst olefin polymerizations with an alcohol compound |
TWI526972B (zh) * | 2013-12-24 | 2016-03-21 | 財團法人工業技術研究院 | 聚合烯類的融熔指數推估方法 |
US9469698B2 (en) * | 2014-04-29 | 2016-10-18 | Chevron Phillips Chemical Company Lp | Process for forming polyolefins |
WO2015197558A1 (en) * | 2014-06-25 | 2015-12-30 | Basell Polyolefine Gmbh | Process for controlling an ethylene polymerization process |
CN105327656A (zh) * | 2014-08-06 | 2016-02-17 | 南京化工职业技术学院 | 一种多工艺气固相反应装置 |
US10837912B2 (en) | 2014-10-01 | 2020-11-17 | Advanced Polymer Monitoring Technologies, Inc. | Systems and methods for control of polymer reactions and processing using automatic continuous online monitoring |
WO2016085945A1 (en) | 2014-11-25 | 2016-06-02 | Univation Technologies, Llc | Methods of monitoring and controlling the melt index of a polyolefin product during production |
KR102001610B1 (ko) * | 2016-03-31 | 2019-10-01 | 주식회사 엘지화학 | 고분자 구조의 정량 분석방법 및 분석장치 |
WO2018045231A1 (en) * | 2016-08-31 | 2018-03-08 | Advanced Polymer Monitoring Technologies, Inc., Dba/Fluence Analytics | Device and methods to actively control the production of multi-stage polymer production |
WO2018081226A1 (en) * | 2016-10-28 | 2018-05-03 | Univation Technologies, Llc | Controlling reactor split and a product parameter |
CN109983035B (zh) | 2016-12-15 | 2022-02-11 | 尤尼威蒂恩技术有限责任公司 | 对聚合工艺进行评定 |
US11186654B2 (en) | 2016-12-20 | 2021-11-30 | Exxonmobil Chemical Patents Inc. | Methods for controlling start up conditions in polymerization processes |
US11098139B2 (en) * | 2018-02-28 | 2021-08-24 | Chevron Phillips Chemical Company Lp | Advanced quality control tools for manufacturing bimodal and multimodal polyethylene resins |
EP3584726A1 (en) * | 2018-06-18 | 2019-12-25 | Covestro Deutschland AG | Method and computer system for determining polymeric product properties |
CN111748049B (zh) * | 2019-03-27 | 2021-07-16 | 中国石油化工股份有限公司 | 一种烯烃聚合方法及系统 |
CN112195695B (zh) * | 2020-09-27 | 2022-03-22 | 四川紫荆花开智能网联汽车科技有限公司 | 一种智能网联汽车动态封闭测试系统 |
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US4243619A (en) | 1978-03-31 | 1981-01-06 | Union Carbide Corporation | Process for making film from low density ethylene hydrocarbon copolymer |
US4588790A (en) | 1982-03-24 | 1986-05-13 | Union Carbide Corporation | Method for fluidized bed polymerization |
US4543399A (en) | 1982-03-24 | 1985-09-24 | Union Carbide Corporation | Fluidized bed reaction systems |
FR2625506B1 (fr) * | 1987-12-31 | 1992-02-21 | Bp Chimie Sa | Procede et appareillage de fabrication de polymeres controlee a l'aide d'un systeme de regulation comprenant un spectrophotometre infrarouge |
US5151474A (en) | 1990-02-16 | 1992-09-29 | The Dow Chemical Company | Process control method for manufacturing polyolefin |
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JP3077940B2 (ja) | 1993-04-26 | 2000-08-21 | エクソン・ケミカル・パテンツ・インク | 流動層重合法のための安定な操作条件を決定する方法 |
US5326853A (en) * | 1993-09-16 | 1994-07-05 | Gencorp Inc. | Low formaldehyde, high gel fraction latex binder |
US5525678A (en) | 1994-09-22 | 1996-06-11 | Mobil Oil Corporation | Process for controlling the MWD of a broad/bimodal resin produced in a single reactor |
BE1009406A3 (fr) * | 1995-06-09 | 1997-03-04 | Solvay | Methode de regulation de procedes de synthese de produits chimiques. |
US6207606B1 (en) * | 1998-05-15 | 2001-03-27 | Univation Technologies, Llc | Mixed catalysts and their use in a polymerization process |
DE19823599A1 (de) | 1998-05-27 | 1999-12-09 | Beb Erdgas & Erdoel Gmbh | Verfahren und Vorrichtungen zur Überwachung von Anlagen der chemischen Industrie |
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BR9906022A (pt) | 1999-12-30 | 2001-09-25 | Opp Petroquimica S A | Processo para a produção controlada de polietileno e seus copolìmeros |
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WO2003022890A1 (en) * | 2001-09-11 | 2003-03-20 | Exxonmobil Chemical Patents Inc. | Method for preparing polyolefins |
EP1453865A4 (en) | 2001-11-15 | 2005-02-09 | Exxonmobil Chem Patents Inc | MONITORING AND CONTROL OF POLYMERIZATION USING ADVANCED INDICATORS |
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2004
- 2004-09-28 US US10/953,263 patent/US7838605B2/en not_active Expired - Fee Related
- 2004-09-29 US US10/953,262 patent/US7585923B2/en not_active Expired - Fee Related
- 2004-09-30 EP EP04785316A patent/EP1675877B1/en not_active Expired - Lifetime
- 2004-09-30 CN CN200480028781A patent/CN100579990C/zh not_active Expired - Fee Related
- 2004-09-30 WO PCT/US2004/032173 patent/WO2005040226A2/en active Application Filing
- 2004-09-30 CN CN2008101701003A patent/CN101539758B/zh not_active Expired - Fee Related
- 2004-09-30 BR BRPI0415515-7A patent/BRPI0415515B1/pt not_active IP Right Cessation
- 2004-09-30 RU RU2006116624/04A patent/RU2361883C2/ru not_active IP Right Cessation
- 2004-09-30 EP EP04789353A patent/EP1732954B1/en not_active Expired - Lifetime
- 2004-09-30 WO PCT/US2004/032174 patent/WO2005040227A2/en active Application Filing
- 2004-09-30 CA CA002542736A patent/CA2542736A1/en not_active Abandoned
- 2004-09-30 CA CA002542378A patent/CA2542378A1/en not_active Abandoned
- 2004-09-30 JP JP2006535526A patent/JP2007508444A/ja not_active Abandoned
- 2004-09-30 BR BRPI0415451-7B1A patent/BRPI0415451B1/pt not_active IP Right Cessation
- 2004-09-30 CN CNB2004800303210A patent/CN100535019C/zh not_active Expired - Fee Related
- 2004-09-30 RU RU2006116625/04A patent/RU2342402C2/ru not_active IP Right Cessation
- 2004-09-30 JP JP2006535525A patent/JP2007509205A/ja not_active Abandoned
- 2004-10-13 TW TW093131049A patent/TW200523272A/zh unknown
- 2004-10-13 TW TW093131050A patent/TW200517404A/zh unknown
- 2004-10-15 AR ARP040103744A patent/AR046181A1/es unknown
- 2004-10-20 AR ARP040103745A patent/AR046117A1/es unknown
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