CA2326444A1 - Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof - Google Patents
Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof Download PDFInfo
- Publication number
- CA2326444A1 CA2326444A1 CA002326444A CA2326444A CA2326444A1 CA 2326444 A1 CA2326444 A1 CA 2326444A1 CA 002326444 A CA002326444 A CA 002326444A CA 2326444 A CA2326444 A CA 2326444A CA 2326444 A1 CA2326444 A1 CA 2326444A1
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- CA
- Canada
- Prior art keywords
- polyol
- comonomer
- dmc
- catalysed
- mixture
- Prior art date
- Legal status (The legal status 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 status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/26—Macromolecular 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
- C08G65/2603—Macromolecular 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 the other compounds containing oxygen
- C08G65/2606—Macromolecular 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 the other compounds containing oxygen containing hydroxyl groups
- C08G65/2609—Macromolecular 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 the other compounds containing oxygen containing hydroxyl groups containing aliphatic hydroxyl groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4833—Polyethers containing oxyethylene units
- C08G18/4837—Polyethers containing oxyethylene units and other oxyalkylene units
- C08G18/4841—Polyethers containing oxyethylene units and other oxyalkylene units containing oxyethylene end groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4866—Polyethers having a low unsaturation value
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/26—Macromolecular 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
- C08G65/2642—Macromolecular 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
- C08G65/2645—Metals or compounds thereof, e.g. salts
- C08G65/2663—Metal cyanide catalysts, i.e. DMC's
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2110/00—Foam properties
- C08G2110/0083—Foam properties prepared using water as the sole blowing agent
Abstract
Copolymer DMC-catalyzed polyoxypropylene polyols which exhibit processing latitude similar to base-catalyzed copolymer analogs and homopolyoxypropylene analogs may be prepared by oxyalkylation with a mixture of propylene oxide and ethylene oxide such that a finite ethylene oxide content is maintained in the oxyalkylation reactor for the most substantial part of the oxyalkylation, the polyoxypropylene polyol having randomly distributed oxyethylene moieties which constitute 1.5 weight percent or more of the polyol product. Block copolymer polyols having external blocks containing lesser oxyethylene content than internal blocks and bicompositional compositions containing discrete multimodal and dissimilar and optionally multimodal polyols produced by a continuous addition of starter process are useful as polyols exhibiting greater processing latitude.
Claims (10)
1. A multiblock DMC-catalysed polyol comprising oxypropylene units which comprises:
i) an internal block comprising oxypropylene units and comonomer units copolymerised therewith which internal block is preparable by oxyalkylating one or more initiators, in the presence of a DMC-catalyst or a non-DMC catalyst, with a first oxyalkylation mixture comprising propylene oxide and at least one comonomer copolymerisable therewith; and ii) at least one external block comprising oxypropylene units and comonomer units copolymerised therewith which external block is preparable by oxyalkylating in the presence of a DMC-catalyst i) with a second oxyalkylation mixture comprising propylene oxide and at least one comonomer copolymerisable therewith such that:
~ the concentration and/or nature of the at least one comonomer in the second mixture differs from that in the first mixture; and ~ at least 95 wt% of the polymerised oxypropylene units are randomly copolymerised into the comonomer units in bock the internal and the external locks; and ~ the copolymerised comonomer content in the external block is less than that in the internal block.
i) an internal block comprising oxypropylene units and comonomer units copolymerised therewith which internal block is preparable by oxyalkylating one or more initiators, in the presence of a DMC-catalyst or a non-DMC catalyst, with a first oxyalkylation mixture comprising propylene oxide and at least one comonomer copolymerisable therewith; and ii) at least one external block comprising oxypropylene units and comonomer units copolymerised therewith which external block is preparable by oxyalkylating in the presence of a DMC-catalyst i) with a second oxyalkylation mixture comprising propylene oxide and at least one comonomer copolymerisable therewith such that:
~ the concentration and/or nature of the at least one comonomer in the second mixture differs from that in the first mixture; and ~ at least 95 wt% of the polymerised oxypropylene units are randomly copolymerised into the comonomer units in bock the internal and the external locks; and ~ the copolymerised comonomer content in the external block is less than that in the internal block.
2. A bicompositional DMC-catalysed polyol comprising:
a) a first, multiblock polyol, said polyol having a first block comprising:
i) a non-DMC-catalysed oxypropylene-containing block; or ii) a DMC-catalysed, oxypropylene-containing block further comprising copolymerized comonomers selected from the group consisting of ethylene oxide, stabilization-modifying comonomers, and mixtures thereof, with the proviso that when only oxyethylene moieties are present as comonomers, they are present in an amount greater than about 1.5 wt%, and at least a second, external block comprising:
iii) a DMC-catalysed mixture of propylene oxide and an effective stabilizing amount of one or both of ethylene oxide and a stabilization-modifying comonomer; and b) a random polyoxypropylene copolymer polyol having no internal block derived from an oligomeric starter molecule with equivalent with greater than 200 Da, and containing a monomer distribution which is the same as the monomer distribution of a)iii).
a) a first, multiblock polyol, said polyol having a first block comprising:
i) a non-DMC-catalysed oxypropylene-containing block; or ii) a DMC-catalysed, oxypropylene-containing block further comprising copolymerized comonomers selected from the group consisting of ethylene oxide, stabilization-modifying comonomers, and mixtures thereof, with the proviso that when only oxyethylene moieties are present as comonomers, they are present in an amount greater than about 1.5 wt%, and at least a second, external block comprising:
iii) a DMC-catalysed mixture of propylene oxide and an effective stabilizing amount of one or both of ethylene oxide and a stabilization-modifying comonomer; and b) a random polyoxypropylene copolymer polyol having no internal block derived from an oligomeric starter molecule with equivalent with greater than 200 Da, and containing a monomer distribution which is the same as the monomer distribution of a)iii).
3. A bicompositional DMC-catalysed polyol according to Claim 2, wherein the weight ratio of the copolymerised comonomer in the oligomeric initiator to the total copolymerised comonomer content in the polyol is at least 0.3.
4. A bicompositional DMC-catalysed polyol according to Claims 2 or 3, wherein the oligomeric initiator has an equivalent weight from 200 to 700 Da.
5. A bicompositional DMC-catalysed polyol according to any of Claims 2 to 4, wherein the first, multiblock polyol comprises from 1 to 60 wt% of the bicompositional polyol.
6. A polyol according to any preceding claim wherein from 5 to 40 wt% of the total copolymerised comonomer is located in internal blocks.
7. A polyol according to any preceding claim, wherein the comonomer comprises a substituted or unsubstituted C4 to C20 alkylene oxide, oxetane, methyl oxetane, a copolymerisable internal carboxylic ester or inner carboxylic anhydride; or a mixture thereof.
8. A process for the preparation of a DMC-catalysed polyol according to any preceding claim, which process comprises:
a) supplying an activated DMC catalyst/initiator mixture to a reactor;
b) polyoxyalkylating said initiator with an oxyalkylation mixture containing propylene oxide and at least one comonomer polymerisable therewith such that the concentration of the comonomer during the oxyalkylation is above zero for at least 95 % of the total oxyalkylation to produce an intermediate copolymer polyol;
c) polyoxyalkylating the intermediate copolymer polyol with an oxyalkylation mixture containing propylene oxide and at least one comonomer polymerisable therewith such that the concentration and/or nature of the at least one comonomer in step (c) differs from that in step (b);
d) recovering a polyol in which the copolymerised comonomer content is at least 1.5 wt%.
a) supplying an activated DMC catalyst/initiator mixture to a reactor;
b) polyoxyalkylating said initiator with an oxyalkylation mixture containing propylene oxide and at least one comonomer polymerisable therewith such that the concentration of the comonomer during the oxyalkylation is above zero for at least 95 % of the total oxyalkylation to produce an intermediate copolymer polyol;
c) polyoxyalkylating the intermediate copolymer polyol with an oxyalkylation mixture containing propylene oxide and at least one comonomer polymerisable therewith such that the concentration and/or nature of the at least one comonomer in step (c) differs from that in step (b);
d) recovering a polyol in which the copolymerised comonomer content is at least 1.5 wt%.
9. A process according to Claim 8, which is a continuous process wherein additional initiator molecules are continually or incrementally added to said reactor.
10. A process for the preparation of a polyurethane slab or molded foam by the reaction of a di- or polyisocyanate with a polyether polyol in the presence of customary blowing agent(s), additives and auxiliaries, which process comprises:
selecting as at least a portion of said polyol component a polyol according to any of Claims 1 to 7 and reacting the polyol with a di- or polyisocyanate to produce polyurethane slab or molded foam.
selecting as at least a portion of said polyol component a polyol according to any of Claims 1 to 7 and reacting the polyol with a di- or polyisocyanate to produce polyurethane slab or molded foam.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/054,554 US6008263A (en) | 1998-04-03 | 1998-04-03 | Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof |
US09/054,554 | 1998-04-03 | ||
PCT/EP1999/002229 WO1999051657A1 (en) | 1998-04-03 | 1999-03-31 | Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2326444A1 true CA2326444A1 (en) | 1999-10-14 |
CA2326444C CA2326444C (en) | 2010-03-09 |
Family
ID=21991912
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002326444A Expired - Fee Related CA2326444C (en) | 1998-04-03 | 1999-03-31 | Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof |
Country Status (17)
Country | Link |
---|---|
US (1) | US6008263A (en) |
EP (1) | EP1082372B1 (en) |
JP (1) | JP4931278B2 (en) |
KR (1) | KR100556181B1 (en) |
CN (1) | CN1152902C (en) |
AR (1) | AR014816A1 (en) |
AU (1) | AU3603899A (en) |
BR (1) | BR9909907B1 (en) |
CA (1) | CA2326444C (en) |
DE (1) | DE69922805T2 (en) |
ES (1) | ES2235477T3 (en) |
HK (1) | HK1038762B (en) |
HU (1) | HU227437B1 (en) |
ID (1) | ID28736A (en) |
PT (1) | PT1082372E (en) |
TW (1) | TW444028B (en) |
WO (1) | WO1999051657A1 (en) |
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DE19918727A1 (en) | 1999-04-24 | 2000-10-26 | Bayer Ag | Polyether polyol useful for production of polyurethanes and/or polyureas has poly(oxyethylene/oxypropylene) endblock prepared in presence of double metal cyanide catalyst |
DE19928156A1 (en) † | 1999-06-19 | 2000-12-28 | Bayer Ag | Polyetherpolyols for preparation of soft polyurethane foams avoid increase in monofunctional polyethers and decrease in functionality with increased chain length and difficulty in alkoxylation of conventional starting compounds |
DE19960148A1 (en) * | 1999-12-14 | 2001-06-21 | Basf Ag | Process for the preparation of polyether alcohols |
ATE328925T1 (en) | 2000-04-14 | 2006-06-15 | Asahi Glass Co Ltd | METHOD FOR PRODUCING FLEXIBLE POLYURETHANE FOAM |
WO2001083107A2 (en) | 2000-04-28 | 2001-11-08 | Synuthane International, Inc. | Double metal cyanide catalysts containing polyglycol ether complexing agents |
US20060183882A1 (en) * | 2001-12-21 | 2006-08-17 | Dexheimer Edward M | Continuous process for preparation of polyether polyols |
US7511111B2 (en) * | 2002-03-08 | 2009-03-31 | Bayer Materialscience Llc | Polyurethane elastomers having improved physical properties and a process for the production thereof |
US6824703B2 (en) * | 2002-03-08 | 2004-11-30 | Bayer Materialscience Llc | Polyurethane elastomers having improved physical properties and a process for the production thereof |
US6906111B2 (en) * | 2002-05-10 | 2005-06-14 | Kao Corporation | Foamed article |
US7094811B2 (en) * | 2002-10-03 | 2006-08-22 | Bayer Corporation | Energy absorbing flexible foams produced in part with a double metal cyanide catalyzed polyol |
WO2004050737A1 (en) * | 2002-12-04 | 2004-06-17 | Huntsman Petrochemical Corporation | Improved molded foams |
DE10317789A1 (en) | 2003-04-16 | 2004-12-02 | Tesa Ag | Pressure sensitive adhesive made of polyurethane |
DE10317788A1 (en) | 2003-04-16 | 2004-12-02 | Tesa Ag | Reusable, residue-free and damage-free removable elastic adhesive film |
DE10317791A1 (en) | 2003-04-16 | 2004-12-02 | Tesa Ag | Pressure sensitive adhesive made of polyurethane for sensitive surfaces |
US7005552B2 (en) | 2003-11-03 | 2006-02-28 | Bayer Materialscience Llc | Single reactor synthesis of KOH-capped polyols based on DMC-synthesized intermediates |
US20050101681A1 (en) * | 2003-11-07 | 2005-05-12 | Kaushiva Bryan D. | Molded polyurethane foam with property enhancements for improved comfort and greater durability |
US8470927B2 (en) * | 2004-02-26 | 2013-06-25 | Bayer Materialscience Llc | Process for production of polymer polyols |
DE102004047524A1 (en) * | 2004-09-28 | 2006-03-30 | Basf Ag | Process for the production of flexible polyurethane foams |
DE102004047406A1 (en) * | 2004-09-28 | 2006-03-30 | Basf Ag | Process for the production of flexible polyurethane foams |
DE102006020482A1 (en) | 2006-04-28 | 2007-10-31 | Tesa Ag | Repositionable polyurethane adhesive |
DE102006033796A1 (en) | 2006-07-19 | 2008-01-31 | Tesa Ag | Pressure-sensitive adhesives made from a resin-modified polyurethane |
US8367870B2 (en) | 2007-09-19 | 2013-02-05 | Air Products And Chemicals, Inc. | Autocatalytic polyols |
DE102008023252A1 (en) | 2008-05-13 | 2009-11-19 | Tesa Se | Hotmelt process for producing a chemically crosslinked polyurethane film |
DE102009009757A1 (en) | 2009-02-20 | 2010-08-26 | Tesa Se | PSA |
DE102009046657A1 (en) | 2009-11-12 | 2011-05-19 | Tesa Se | Pressure-sensitive adhesive based on polyurethane |
US9163099B2 (en) | 2013-03-08 | 2015-10-20 | Bayer Materialscience Llc | Polybutadiene modified polymer polyols, foams prepared from polybutadiene modified polymer polyols, and processes for the production thereof |
US9562134B2 (en) | 2013-03-12 | 2017-02-07 | Covestro Llc | Catalyst for the production of polyols having lower amounts of high molecular weight tail |
US9051412B2 (en) | 2013-03-14 | 2015-06-09 | Bayer Materialscience Llc | Base-catalyzed, long chain, active polyethers from short chain DMC-catalyzed starters |
EP3126428B1 (en) | 2014-04-01 | 2019-02-06 | Dow Global Technologies LLC | Polyether polyol providing good blow-gel balance for polyurethane products made therefrom |
BR112017025328A2 (en) | 2015-06-19 | 2018-07-31 | Dow Global Technologies Llc | autocatalytic polyol useful for making polyurethane foam |
ES2927381T3 (en) | 2015-06-30 | 2022-11-04 | Dow Global Technologies Llc | Method for making propylene oxide/ethylene oxide copolymers using double metal cyanide catalysts and copolymers made in this way |
KR20180097552A (en) * | 2015-12-21 | 2018-08-31 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | Method for producing polyurethane foam |
BR112018075802B1 (en) | 2016-06-13 | 2022-12-20 | Dow Global Technologies Llc | POLYMERIC POLYOL COMPOSITION AND PROCESS FOR MAKING A POLYURETHANE POLYMER |
CN112703215B (en) * | 2018-09-28 | 2023-04-14 | 陶氏环球技术有限责任公司 | Polyurethane and method for producing polyurethane |
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JP2615927B2 (en) * | 1988-10-25 | 1997-06-04 | 旭硝子株式会社 | Method for producing polyurethane foam |
US5100997A (en) * | 1990-05-29 | 1992-03-31 | Olin Corporation | Preparation of elastomers using high molecular weight polyols or polyamines, said polyols prepared using a double metal cyanide complex catalyst |
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EP0677543B2 (en) * | 1994-04-12 | 2006-11-15 | Mitsui Chemicals, Inc. | Preparation of polyoxyalkylene polyols, polymer polyols and flexible polyurethane foams |
US5482908A (en) * | 1994-09-08 | 1996-01-09 | Arco Chemical Technology, L.P. | Highly active double metal cyanide catalysts |
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US5563221A (en) * | 1995-06-21 | 1996-10-08 | Arco Chemical Technology, L.P. | Process for making ethylene oxide-capped polyols from double metal cyanide-catalyzed polyols |
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US5545601A (en) * | 1995-08-22 | 1996-08-13 | Arco Chemical Technology, L.P. | Polyether-containing double metal cyanide catalysts |
EP0781791B1 (en) * | 1995-12-29 | 1998-07-22 | Basf Corporation | Low unsaturation polyoxyalkylene polyether polyols |
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US5777177A (en) * | 1996-02-07 | 1998-07-07 | Arco Chemical Technology, L.P. | Preparation of double metal cyanide-catalyzed polyols by continuous addition of starter |
-
1998
- 1998-04-03 US US09/054,554 patent/US6008263A/en not_active Expired - Lifetime
-
1999
- 1999-03-31 CA CA002326444A patent/CA2326444C/en not_active Expired - Fee Related
- 1999-03-31 ES ES99917941T patent/ES2235477T3/en not_active Expired - Lifetime
- 1999-03-31 JP JP2000542376A patent/JP4931278B2/en not_active Expired - Lifetime
- 1999-03-31 AR ARP990101510A patent/AR014816A1/en unknown
- 1999-03-31 BR BRPI9909907-1A patent/BR9909907B1/en not_active IP Right Cessation
- 1999-03-31 HU HU0101583A patent/HU227437B1/en not_active IP Right Cessation
- 1999-03-31 PT PT99917941T patent/PT1082372E/en unknown
- 1999-03-31 WO PCT/EP1999/002229 patent/WO1999051657A1/en active IP Right Grant
- 1999-03-31 AU AU36038/99A patent/AU3603899A/en not_active Abandoned
- 1999-03-31 EP EP99917941A patent/EP1082372B1/en not_active Expired - Lifetime
- 1999-03-31 KR KR1020007010984A patent/KR100556181B1/en not_active IP Right Cessation
- 1999-03-31 CN CNB998070017A patent/CN1152902C/en not_active Expired - Lifetime
- 1999-03-31 DE DE69922805T patent/DE69922805T2/en not_active Expired - Lifetime
- 1999-03-31 ID IDW20001971A patent/ID28736A/en unknown
- 1999-04-02 TW TW088105332A patent/TW444028B/en not_active IP Right Cessation
-
2002
- 2002-01-09 HK HK02100144.3A patent/HK1038762B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
ID28736A (en) | 2001-06-28 |
EP1082372B1 (en) | 2004-12-22 |
HK1038762B (en) | 2005-03-18 |
ES2235477T3 (en) | 2005-07-01 |
JP4931278B2 (en) | 2012-05-16 |
TW444028B (en) | 2001-07-01 |
BR9909907B1 (en) | 2008-11-18 |
WO1999051657A1 (en) | 1999-10-14 |
EP1082372A1 (en) | 2001-03-14 |
HU227437B1 (en) | 2011-06-28 |
PT1082372E (en) | 2005-05-31 |
DE69922805D1 (en) | 2005-01-27 |
HUP0101583A2 (en) | 2001-10-28 |
HK1038762A1 (en) | 2002-03-28 |
CN1152902C (en) | 2004-06-09 |
KR100556181B1 (en) | 2006-03-03 |
DE69922805T2 (en) | 2005-12-08 |
KR20010042408A (en) | 2001-05-25 |
BR9909907A (en) | 2000-12-26 |
US6008263A (en) | 1999-12-28 |
AU3603899A (en) | 1999-10-25 |
AR014816A1 (en) | 2001-03-28 |
CA2326444C (en) | 2010-03-09 |
CN1304422A (en) | 2001-07-18 |
JP2002510724A (en) | 2002-04-09 |
HUP0101583A3 (en) | 2002-03-28 |
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