BRPI0408669A - processo e sistema contìnuos para produzir polióis poliéteres - Google Patents

processo e sistema contìnuos para produzir polióis poliéteres

Info

Publication number
BRPI0408669A
BRPI0408669A BRPI0408669-4A BRPI0408669A BRPI0408669A BR PI0408669 A BRPI0408669 A BR PI0408669A BR PI0408669 A BRPI0408669 A BR PI0408669A BR PI0408669 A BRPI0408669 A BR PI0408669A
Authority
BR
Brazil
Prior art keywords
loop reactor
rate
continuous process
reactor
polyether polyols
Prior art date
Application number
BRPI0408669-4A
Other languages
English (en)
Inventor
Jan W Verwijs
Walter J S Papadopulos
John W Weston
Richard J Elwell
Carlos M Villa
Original Assignee
Dow Global Technologies Inc
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 Dow Global Technologies Inc filed Critical Dow Global Technologies Inc
Publication of BRPI0408669A publication Critical patent/BRPI0408669A/pt

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/1812Tubular reactors
    • B01J19/1837Loop-type reactors
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/16Catalysts
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2642Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the catalyst used
    • C08G65/2645Metals or compounds thereof, e.g. salts
    • C08G65/2663Metal cyanide catalysts, i.e. DMC's
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2696Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the process or apparatus used

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Toxicology (AREA)
  • Polyethers (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

"PROCESSO E SISTEMA CONTìNUOS PARA PRODUZIR POLIóIS POLIéTERES". Um processo e sistema continuos para produzir polióis poliéteres que permitem adicionar continuamente um óxido não reagido a um reator de loop enquanto adicionando pelo menos um catalisador desativável termicamente capaz de se desativar termicamente antes da decomposição do poliol poliéter que podem permitir maiores concentrações de óxidos não reagidos e/ou uma taxa de reação no reator de loop que seja pelo menos duas vezes mais rápida do que uma taxa de reação em um reator de loop contendo menos que 14 por cento em peso de óxido não reagido. Em uma configuração preferida, o catalisador é um catalisador de cianeto metálico duplo e um reator tubular de fluxo pistonado é formado em série com o reator de loop sendo que nenhum reator contém um espaço de vapor.
BRPI0408669-4A 2003-03-07 2004-03-05 processo e sistema contìnuos para produzir polióis poliéteres BRPI0408669A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US45307303P 2003-03-07 2003-03-07
PCT/US2004/006643 WO2004081082A1 (en) 2003-03-07 2004-03-05 Continuous process and system of producing polyether polyols

Publications (1)

Publication Number Publication Date
BRPI0408669A true BRPI0408669A (pt) 2006-03-28

Family

ID=32990720

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0408669-4A BRPI0408669A (pt) 2003-03-07 2004-03-05 processo e sistema contìnuos para produzir polióis poliéteres

Country Status (13)

Country Link
US (2) US7378559B2 (pt)
EP (1) EP1603965B1 (pt)
JP (1) JP2007524719A (pt)
KR (1) KR20050107604A (pt)
CN (1) CN1867609A (pt)
AT (1) ATE353348T1 (pt)
AU (1) AU2004220072A1 (pt)
BR (1) BRPI0408669A (pt)
CA (1) CA2518201A1 (pt)
DE (1) DE602004004639T2 (pt)
MX (1) MXPA05009512A (pt)
WO (1) WO2004081082A1 (pt)
ZA (1) ZA200506576B (pt)

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US7495063B2 (en) 2006-02-03 2009-02-24 Dow Global Technologies Inc. Reduced oligomer concentration in high purity polyalkylene glycols
EP2035479B1 (de) * 2006-06-23 2010-07-07 Basf Se Verfahren zur kontinuierlichen herstellung von polyetheralkoholen
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AR073933A1 (es) * 2008-05-19 2010-12-15 Dow Global Technologies Inc Procedimiento de flujo de recirculacion continuo para la produccion de poliol de polieter
JP6022770B2 (ja) * 2008-10-13 2016-11-09 ブルー キューブ アイピー エルエルシー 塩素化及び/又はフッ素化プロペンの製造方法
JP5767231B2 (ja) 2009-10-09 2015-08-19 ダウ グローバル テクノロジーズ エルエルシー 塩素化及び/又はフッ素化されたプロペン及びより高級なアルケンを製造するプロセス
JP5782038B2 (ja) * 2009-10-09 2015-09-24 ダウ グローバル テクノロジーズ エルエルシー 等温多管式反応器及び該反応器を組み込んだプロセス
BR112012007916A2 (pt) * 2009-10-09 2019-09-24 Dow Global Technologies Llc processo de etapa para a produção de propenos clorados ou fluorados e processo para preparar 1,1,3,3 - tetrafluorprop-1-eno
US9074044B2 (en) 2009-12-14 2015-07-07 Dow Global Technologies Llc Method for continuously producing low equivalent weight polyols using double metal cyanide catalysts
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SG185607A1 (en) 2010-05-18 2012-12-28 Bayer Ip Gmbh Method for producing polyether carbonate polyols
DE102010040517A1 (de) 2010-09-09 2012-03-15 Bayer Materialscience Aktiengesellschaft Verfahren zur Herstellung von Polyetherpolyolen
DE102010043409A1 (de) 2010-11-04 2012-05-10 Bayer Materialscience Aktiengesellschaft Verfahren zur Herstellung von Polycarbonatpolyolen durch immortale Polymerisation von cyclischen Carbonaten
EP2465890A1 (de) 2010-12-17 2012-06-20 Bayer MaterialScience AG Verfahren zur Herstellung von Polyethercarbonatpolyolen mit primären Hydroxyl-Endgruppen und daraus hergestellte Polyurethanpolymere
KR20140007852A (ko) * 2011-02-24 2014-01-20 쉘 인터내셔날 리써취 마트샤피지 비.브이. 폴리에테르 폴리올의 제조를 위한 방법 및 반응기 시스템
WO2012166394A1 (en) 2011-05-31 2012-12-06 Dow Global Technologies, Llc Process for the production of chlorinated propenes
JP6212035B2 (ja) 2011-05-31 2017-10-11 ブルー キューブ アイピー エルエルシー 塩素化プロペンの製造方法
JP6267114B2 (ja) 2011-06-08 2018-01-24 ダウ アグロサイエンシィズ エルエルシー 塩素化および/またはフッ素化プロペンを生成するためのプロセス
CN108929192A (zh) 2011-08-07 2018-12-04 蓝立方知识产权有限责任公司 生产氯化的丙烯的方法
CN103717557A (zh) 2011-08-07 2014-04-09 陶氏环球技术有限责任公司 生产氯化的丙烯的方法
IN2014CN03748A (pt) 2011-11-21 2015-09-25 Dow Global Technologies Llc
JP6050375B2 (ja) 2011-12-02 2016-12-21 ブルー キューブ アイピー エルエルシー クロロアルカンの製造方法
CA2856545A1 (en) 2011-12-02 2013-06-06 Dow Global Technologies Llc Process for the production of chlorinated alkanes
JP6170068B2 (ja) 2011-12-13 2017-07-26 ブルー キューブ アイピー エルエルシー 塩素化プロパン及びプロペンの製造方法
IN2014CN04418A (pt) 2011-12-22 2015-09-04 Dow Global Technologies Llc
WO2013096706A1 (en) 2011-12-23 2013-06-27 Dow Global Technologies, Llc Process for the production of alkenes and/or aromatic compounds
US9598334B2 (en) 2012-09-20 2017-03-21 Blue Cube Ip Llc Process for the production of chlorinated propenes
EP2897930A1 (en) 2012-09-20 2015-07-29 Dow Global Technologies LLC Process for the production of chlorinated propenes
CA2885329A1 (en) 2012-09-30 2014-03-04 Dow Global Technologies Llc Weir quench and processes incorporating the same
US10065157B2 (en) 2012-10-26 2018-09-04 Blue Cube Ip Llc Mixer and processes incorporating the same
JP6247311B2 (ja) 2012-12-18 2017-12-13 ブルー キューブ アイピー エルエルシー 塩素化プロペンを生成するための方法
CA2894168C (en) 2012-12-19 2018-04-24 Dow Global Technologies Llc Process for the production of chlorinated propenes
CA2901450A1 (en) 2013-02-27 2014-09-04 Blue Cube Ip Llc Process for the production of chlorinated propenes
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Also Published As

Publication number Publication date
MXPA05009512A (es) 2006-02-22
CA2518201A1 (en) 2004-09-23
AU2004220072A1 (en) 2004-09-23
US20080221281A1 (en) 2008-09-11
US20060155151A1 (en) 2006-07-13
WO2004081082A1 (en) 2004-09-23
ATE353348T1 (de) 2007-02-15
JP2007524719A (ja) 2007-08-30
US7378559B2 (en) 2008-05-27
EP1603965B1 (en) 2007-02-07
CN1867609A (zh) 2006-11-22
ZA200506576B (en) 2006-12-27
EP1603965A1 (en) 2005-12-14
DE602004004639T2 (de) 2007-11-08
DE602004004639D1 (de) 2007-03-22
KR20050107604A (ko) 2005-11-14

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