CZ289005B6 - Způsob zastavení reakce v plynné fázi polymeračního reakčního systému a zařízení k provádění tohoto způsobu - Google Patents
Způsob zastavení reakce v plynné fázi polymeračního reakčního systému a zařízení k provádění tohoto způsobu Download PDFInfo
- Publication number
- CZ289005B6 CZ289005B6 CZ199397A CZ9793A CZ289005B6 CZ 289005 B6 CZ289005 B6 CZ 289005B6 CZ 199397 A CZ199397 A CZ 199397A CZ 9793 A CZ9793 A CZ 9793A CZ 289005 B6 CZ289005 B6 CZ 289005B6
- Authority
- CZ
- Czechia
- Prior art keywords
- gas
- reactor
- circulator
- recycle
- reaction
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 58
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 46
- 238000012685 gas phase polymerization Methods 0.000 title description 4
- 239000007789 gas Substances 0.000 claims abstract description 138
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 36
- 239000003054 catalyst Substances 0.000 claims abstract description 22
- 239000000178 monomer Substances 0.000 claims abstract description 16
- 150000001336 alkenes Chemical class 0.000 claims abstract description 10
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000001257 hydrogen Substances 0.000 claims abstract description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 7
- -1 comonomer Substances 0.000 claims abstract description 5
- 229910052723 transition metal Inorganic materials 0.000 claims abstract description 4
- 150000003624 transition metals Chemical class 0.000 claims abstract description 4
- 239000003085 diluting agent Substances 0.000 claims abstract description 3
- 230000008569 process Effects 0.000 claims description 49
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 16
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 8
- 239000001569 carbon dioxide Substances 0.000 claims description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 7
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 5
- 229920001577 copolymer Polymers 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 229920001519 homopolymer Polymers 0.000 claims description 2
- 229920001384 propylene homopolymer Polymers 0.000 claims description 2
- 239000002826 coolant Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 description 24
- 229920000642 polymer Polymers 0.000 description 23
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000005243 fluidization Methods 0.000 description 8
- 238000009423 ventilation Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 239000002574 poison Substances 0.000 description 5
- 231100000614 poison Toxicity 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229920000573 polyethylene Polymers 0.000 description 4
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 229920001038 ethylene copolymer Polymers 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010574 gas phase reaction Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
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
- C08F2/00—Processes of polymerisation
- C08F2/34—Polymerisation in gaseous state
-
- 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
-
- 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
- B01J2208/00548—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
- B01J2219/00245—Avoiding undesirable reactions or side-effects
- B01J2219/00272—Addition of reaction inhibitor
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)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/827,649 US5270408A (en) | 1992-01-29 | 1992-01-29 | Method and apparatus for stopping reaction in a gas phase polymerization reactor system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CZ9793A3 CZ9793A3 (en) | 1994-01-19 |
| CZ289005B6 true CZ289005B6 (cs) | 2001-10-17 |
Family
ID=25249772
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CZ199397A CZ289005B6 (cs) | 1992-01-29 | 1993-01-28 | Způsob zastavení reakce v plynné fázi polymeračního reakčního systému a zařízení k provádění tohoto způsobu |
Country Status (24)
| Country | Link |
|---|---|
| US (2) | US5270408A (Direct) |
| EP (1) | EP0553809B1 (Direct) |
| JP (1) | JP2651985B2 (Direct) |
| KR (1) | KR0150014B1 (Direct) |
| CN (1) | CN1084753C (Direct) |
| AR (1) | AR246069A1 (Direct) |
| AT (1) | ATE140241T1 (Direct) |
| AU (1) | AU653093B2 (Direct) |
| BR (1) | BR9300359A (Direct) |
| CA (1) | CA2088304C (Direct) |
| CZ (1) | CZ289005B6 (Direct) |
| DE (1) | DE69303501T2 (Direct) |
| ES (1) | ES2089597T3 (Direct) |
| FI (1) | FI930365A7 (Direct) |
| GR (1) | GR3020516T3 (Direct) |
| HU (1) | HU212488B (Direct) |
| MY (1) | MY109128A (Direct) |
| NO (1) | NO930293L (Direct) |
| NZ (1) | NZ245780A (Direct) |
| PL (1) | PL297563A1 (Direct) |
| SK (1) | SK3593A3 (Direct) |
| TR (1) | TR26967A (Direct) |
| TW (1) | TW284766B (Direct) |
| ZA (1) | ZA93623B (Direct) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6117399A (en) * | 1997-04-23 | 2000-09-12 | Union Carbide Chemicals & Plastics Technology Corporation | Fluidized bed polymerization reactor with multiple fluidization grids |
| US6113862A (en) * | 1997-04-23 | 2000-09-05 | Union Carbide Chemicals & Plastics Technology Corporation | Fluidized bed polymerization reactor with multiple fluidization grids |
| EP1153934A1 (en) * | 2000-05-09 | 2001-11-14 | BP Chemicals S.N.C. | Method for deactivating a polymerisation reaction |
| US6339133B1 (en) * | 2000-07-05 | 2002-01-15 | Solvay Polyolefins Europe - Belgium | Emergency stop of a polymerization in the gas phase |
| US6365681B1 (en) * | 2001-01-16 | 2002-04-02 | Union Carbide Chemicals & Plastics Technology Corporation | Preventing upsets in polymerization reactors |
| US6897269B2 (en) * | 2002-12-27 | 2005-05-24 | Univation Technologies, Llc | Processes for transitioning between Ziegler-Natta and alumoxane-based single-site polymerization catalysts |
| US6858684B2 (en) * | 2002-12-30 | 2005-02-22 | Univation Technologies, Llc | Processes for transitioning between various polymerization catalysts |
| US6841630B2 (en) * | 2002-12-31 | 2005-01-11 | Univation Technologies, Llc | Processes for transitioning between chrome-based and mixed polymerization catalysts |
| US6949612B2 (en) * | 2002-12-31 | 2005-09-27 | Univation Technologies, Llc | Processes for transitioning between metallocene and Ziegler-Natta polymerization catalysts |
| US6833417B2 (en) * | 2002-12-31 | 2004-12-21 | Univation Technologies, Llc | Processes for transitioning between chrome-based and mixed polymerization catalysts |
| JP4295196B2 (ja) * | 2004-11-09 | 2009-07-15 | 住友化学株式会社 | 連続重合の停止方法 |
| US6987152B1 (en) | 2005-01-11 | 2006-01-17 | Univation Technologies, Llc | Feed purification at ambient temperature |
| JP4506549B2 (ja) * | 2005-05-10 | 2010-07-21 | 住友化学株式会社 | オレフィン重合体の製造設備 |
| US7381777B1 (en) | 2007-02-26 | 2008-06-03 | Exxonmobil Chemical Patents Inc. | Method for controlling fouling in slurry-type polymerization reactors |
| TW200936564A (en) * | 2007-11-15 | 2009-09-01 | Univation Tech Llc | Methods for the removal of impurities from polymerization feed streams |
| CN101619112B (zh) * | 2008-07-03 | 2011-10-12 | 中国石油化工股份有限公司 | 一种防止气相流化床烯烃聚合反应器结块的方法及其设备 |
| US9637570B2 (en) * | 2009-06-11 | 2017-05-02 | Exxonmobil Chemical Patents Inc. | Method and apparatus for reducing fouling |
| US8440772B2 (en) | 2011-04-28 | 2013-05-14 | Chevron Phillips Chemical Company Lp | Methods for terminating olefin polymerizations |
| US10273315B2 (en) | 2012-06-20 | 2019-04-30 | Chevron Phillips Chemical Company Lp | Methods for terminating olefin polymerizations |
| EP3483189A1 (en) | 2017-11-14 | 2019-05-15 | Borealis AG | Automated method for terminating an olefin polymerization reaction under emergency conditions |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4482687A (en) * | 1979-10-26 | 1984-11-13 | Union Carbide Corporation | Preparation of low-density ethylene copolymers in fluid bed reactor |
| US4328186A (en) * | 1979-10-29 | 1982-05-04 | The Dow Chemical Company | Recirculating polymerization method and apparatus with evaporative cooling |
| US4372919A (en) * | 1980-03-14 | 1983-02-08 | Nippon Oil Company, Limited | Vapor phase polymerization apparatus for olefins |
| US4326048A (en) * | 1980-05-27 | 1982-04-20 | Standard Oil Company (Indiana) | Method for emergency shutdown of gas phase polyolefin reactor |
| US4834947A (en) * | 1983-09-01 | 1989-05-30 | Mobil Oil Corporation | Reactor system for rapid kill gas injection to gas phase polymerization reactors |
| EP0136029A3 (en) * | 1983-09-01 | 1986-08-20 | Mobil Oil Corporation | Method and system for injecting a kill gas into a gas phase catalytic polymerization reactor |
| US4786695A (en) * | 1983-09-01 | 1988-11-22 | Mobil Oil Corporation | Method and reactor system for rapid kill gas injection to gas phase polymerization reactors |
| US4666999A (en) * | 1983-09-01 | 1987-05-19 | Mobil Oil Corporation | Method and reactor system for rapid kill gas injection to gas phase polymerization reactors |
| US4547555A (en) * | 1983-09-01 | 1985-10-15 | Mobil Oil Corporation | Method for rapid kill gas injection to gas phase polymerization reactors during power failures |
| US4826662A (en) * | 1984-12-19 | 1989-05-02 | Mobil Oil Corporation | Apparatus for feeding an MTG conversion reactor |
| FR2665704B1 (fr) * | 1990-08-07 | 1994-04-08 | Bp Chemicals Snc | Procede pour arreter une reaction de (co-)polymerisation effectuee a l'aide d'un catalyseur a base d'oxyde de chrome. |
-
1992
- 1992-01-29 US US07/827,649 patent/US5270408A/en not_active Expired - Lifetime
-
1993
- 1993-01-27 KR KR1019930000943A patent/KR0150014B1/ko not_active Expired - Fee Related
- 1993-01-27 SK SK3593A patent/SK3593A3/sk unknown
- 1993-01-28 AT AT93101304T patent/ATE140241T1/de not_active IP Right Cessation
- 1993-01-28 NO NO93930293A patent/NO930293L/no unknown
- 1993-01-28 ES ES93101304T patent/ES2089597T3/es not_active Expired - Lifetime
- 1993-01-28 DE DE69303501T patent/DE69303501T2/de not_active Expired - Lifetime
- 1993-01-28 AR AR93324177A patent/AR246069A1/es active
- 1993-01-28 EP EP93101304A patent/EP0553809B1/en not_active Expired - Lifetime
- 1993-01-28 MY MYPI93000139A patent/MY109128A/en unknown
- 1993-01-28 CZ CZ199397A patent/CZ289005B6/cs not_active IP Right Cessation
- 1993-01-28 BR BR9300359A patent/BR9300359A/pt not_active IP Right Cessation
- 1993-01-28 HU HU9300227A patent/HU212488B/hu not_active IP Right Cessation
- 1993-01-28 CA CA002088304A patent/CA2088304C/en not_active Expired - Lifetime
- 1993-01-28 PL PL29756393A patent/PL297563A1/xx unknown
- 1993-01-28 ZA ZA93623A patent/ZA93623B/xx unknown
- 1993-01-28 FI FI930365A patent/FI930365A7/fi not_active Application Discontinuation
- 1993-01-28 CN CN93100939A patent/CN1084753C/zh not_active Expired - Lifetime
- 1993-01-28 TR TR00085/93A patent/TR26967A/xx unknown
- 1993-01-28 AU AU32065/93A patent/AU653093B2/en not_active Ceased
- 1993-01-28 JP JP5031106A patent/JP2651985B2/ja not_active Expired - Lifetime
- 1993-01-28 NZ NZ245780A patent/NZ245780A/en unknown
- 1993-02-19 TW TW082101185A patent/TW284766B/zh active
- 1993-09-10 US US08/119,714 patent/US5399320A/en not_active Expired - Lifetime
-
1996
- 1996-07-11 GR GR960401783T patent/GR3020516T3/el unknown
Also Published As
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PD00 | Pending as of 2000-06-30 in czech republic | ||
| MM4A | Patent lapsed due to non-payment of fee |
Effective date: 20100128 |