IN2014DN08663A - - Google Patents

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Publication number
IN2014DN08663A
IN2014DN08663A IN8663DEN2014A IN2014DN08663A IN 2014DN08663 A IN2014DN08663 A IN 2014DN08663A IN 8663DEN2014 A IN8663DEN2014 A IN 8663DEN2014A IN 2014DN08663 A IN2014DN08663 A IN 2014DN08663A
Authority
IN
India
Prior art keywords
loop reactor
monomer
polyolefin
optionally
interconnected pipes
Prior art date
Application number
Inventor
Robin Giguere
Denis Mignon
Philippe Tanguy
Louis Fradette
Original Assignee
Total Res & Technology Feluy
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Total Res & Technology Feluy filed Critical Total Res & Technology Feluy
Publication of IN2014DN08663A publication Critical patent/IN2014DN08663A/en

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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
    • C08F2/01—Processes of polymerisation characterised by special features of the polymerisation apparatus used
    • 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
    • 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
    • B01J19/1862—Stationary reactors having moving elements inside placed in series
    • 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
    • B01J19/2455—Stationary reactors without moving elements inside provoking a loop type movement of the reactants
    • 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
    • B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
    • 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
    • C08F10/02—Ethene
    • 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
    • C08F2/44—Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
    • 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
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside

Abstract

The present invention relates to a process for preparing polyolefin in a polymerization loop reactor said loop reactor comprising: a plurality of interconnected pipes defining a flow path for a polyolefin slurry and one or more settling legs provided on at least one horizontal part of said interconnected pipes said process comprising the steps of: feeding olefin monomer liquid diluent polymerization catalyst optionally hydrogen and optionally olefin co monomer into said loop reactor; and polymerizing said olefin monomer and said optionally co monomer to produce said polyolefin slurry in said loop reactor; wherein the circulation velocity of the polyolefin slurry inside at least one horizontal part of said interconnected pipes provided with one or more settling legs is reduced by at least 20% and at most 60% compared to the circulation velocity inside the remainder of said loop reactor.
IN8663DEN2014 2012-05-04 2013-05-03 IN2014DN08663A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP12166881 2012-05-04
PCT/EP2013/059217 WO2013164437A1 (en) 2012-05-04 2013-05-03 Process for preparing a polyethylene product in a polymerization loop reactor

Publications (1)

Publication Number Publication Date
IN2014DN08663A true IN2014DN08663A (en) 2015-05-22

Family

ID=48407480

Family Applications (1)

Application Number Title Priority Date Filing Date
IN8663DEN2014 IN2014DN08663A (en) 2012-05-04 2013-05-03

Country Status (10)

Country Link
US (1) US9296834B2 (en)
EP (1) EP2844384B1 (en)
KR (1) KR101695623B1 (en)
CN (2) CN108097174B (en)
BR (1) BR112014026777A2 (en)
EA (1) EA025081B1 (en)
ES (1) ES2564035T3 (en)
HU (1) HUE026900T2 (en)
IN (1) IN2014DN08663A (en)
WO (1) WO2013164437A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9296834B2 (en) * 2012-05-04 2016-03-29 Total Research & Technology Feluy Process for preparing a polyethylene product in a polymerization loop reactor
CN107835822B (en) * 2015-07-15 2020-06-09 道达尔研究技术弗吕公司 Process for preparing polyethylene products
CN110385099A (en) * 2018-04-20 2019-10-29 中国科学院过程工程研究所 A kind of control method of annular-pipe reactor and annular-pipe reactor

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3293000A (en) 1962-10-05 1966-12-20 Phillips Petroleum Co Withdrawal of solids from a flowing stream comprising a slurry of same
US6930071B2 (en) 1997-01-28 2005-08-16 Fina Technology, Inc. Ziegler-natta catalyst for polyolefins
US6864207B2 (en) 1997-01-28 2005-03-08 Fina Technology, Inc. Ziegler-Natta catalyst for polyolefins
US7033545B2 (en) 1997-07-15 2006-04-25 Chevon Phillips Chemical Company, Lp Slurry polymerization reactor having large length/diameter ratio
CN1361794A (en) 1999-07-15 2002-07-31 菲利浦石油公司 Slotted slurry take off
WO2004024781A1 (en) 2002-09-13 2004-03-25 Chevron Phillips Chemical Company Lp Process and apparatus for reducing take-off valve plugging in a polymerization process
WO2004027264A2 (en) 2002-09-17 2004-04-01 Chevron Phillips Chemical Company Lp Improved pumping apparatus and process for slurry polymerization in loop reactors
CN100475851C (en) 2002-09-17 2009-04-08 切夫里昂菲利普化学有限责任公司 Pumping apparatus and process for slurry polymerization in loop reactors
PT1542793E (en) * 2002-09-23 2007-09-17 Total Petrochemicals Res Feluy Slurry loop polyolefin reactor
EP1663475B1 (en) * 2003-09-24 2016-11-09 Basell Polyolefine GmbH Process with a loop reactor with varying diameter for olefin polymerization
EP1563898A1 (en) * 2004-02-13 2005-08-17 Total Petrochemicals Research Feluy Olefin polymerization process with optimized product discharge
CN100432111C (en) * 2004-02-13 2008-11-12 托塔尔石油化学产品研究弗吕公司 Multiple loop reactor for olefin polymerization
EP1825911A1 (en) * 2006-02-27 2007-08-29 Total Petrochemicals Research Feluy Transfer pipe between loop reactors
EP2030678A1 (en) * 2007-08-31 2009-03-04 Total Petrochemicals Research Feluy Loop reactor suitable for olefin polymerization with improved product removal means
EP2316863A1 (en) * 2009-10-30 2011-05-04 INEOS Manufacturing Belgium NV Slurry phase polymerisation process
US9296834B2 (en) * 2012-05-04 2016-03-29 Total Research & Technology Feluy Process for preparing a polyethylene product in a polymerization loop reactor

Also Published As

Publication number Publication date
CN104271230B (en) 2019-02-22
CN104271230A (en) 2015-01-07
EA025081B1 (en) 2016-11-30
EA201491902A1 (en) 2016-01-29
BR112014026777A2 (en) 2017-06-27
CN108097174A (en) 2018-06-01
US20150112034A1 (en) 2015-04-23
EP2844384A1 (en) 2015-03-11
KR20150004419A (en) 2015-01-12
EP2844384B1 (en) 2015-12-09
US9296834B2 (en) 2016-03-29
CN108097174B (en) 2020-12-04
WO2013164437A1 (en) 2013-11-07
ES2564035T3 (en) 2016-03-17
KR101695623B1 (en) 2017-01-13
HUE026900T2 (en) 2016-07-28

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