CA2493102A1 - Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties - Google Patents
Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties Download PDFInfo
- Publication number
- CA2493102A1 CA2493102A1 CA 2493102 CA2493102A CA2493102A1 CA 2493102 A1 CA2493102 A1 CA 2493102A1 CA 2493102 CA2493102 CA 2493102 CA 2493102 A CA2493102 A CA 2493102A CA 2493102 A1 CA2493102 A1 CA 2493102A1
- Authority
- CA
- Canada
- Prior art keywords
- polyol
- lbs
- mixture
- foam
- solid
- 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.)
- Granted
Links
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
- C08G18/409—Dispersions of polymers of C08G in organic compounds having active hydrogen
-
- 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
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- 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
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
- C08G18/4072—Mixtures of compounds of group C08G18/63 with other macromolecular compounds
-
- 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
- C08G2110/0025—Foam properties rigid
-
- 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
- C08G2110/0041—Foam properties having specified density
- C08G2110/0058—≥50 and <150kg/m3
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31573—Next to addition polymer of ethylenically unsaturated monomer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31573—Next to addition polymer of ethylenically unsaturated monomer
- Y10T428/31583—Nitrile monomer type [polyacrylonitrile, etc.]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31573—Next to addition polymer of ethylenically unsaturated monomer
- Y10T428/31587—Hydrocarbon polymer [polyethylene, polybutadiene, etc.]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31605—Next to free metal
Abstract
The present invention is directed to a process for preparing water~blown rig id polyurethane foams having at least an 80% closed-cell content which involves reacting a) at least one polyol mixture which is composed of (i) at least on e polymer polyol; (ii) at least one polyol having a hydroxyl value within the range of from about 200 to about 800; and (iii) optionally, at least one polyol having a hydroxyl value within the range of from about 25 to about 11 5; with b) at least one polymeric isocyanate and/or a prepolymer thereof; in th e presence of c) optionally, at least one catalyst; d) water; and e) optionall y, at least one additive or auxiliary agent. The present invention is also directed to the closed-cell water blown rigid polyurethane foams produced by the process of the present invention. The invention is further directed to a polyurethane-foam forming mixture which is used to produce the water-blown rigid polyurethane foams of the present invention. Foams produced according to the present invention have reduced friability and acceptable adhesion to substrates as well as acceptable compressive strength.
Claims
WHAT IS CLAIMED IS:
1. A process for preparing a water-blown rigid polyurethane foam having at least an 80% closed-cell content comprising reacting:
(a) at least one polyol mixture comprising:
(i) at least one polymer polyol;
(ii) at least one polyol having a hydroxyl value within the range of from about 200 to about 800; and (iii) optionally, at least one polyol having a hydroxyl value within the range of from about 25 to about 115;
with (b) at least one polymeric isocyanate and/or a prepolymer thereof;
in the presence of (c) optionally, at least one catalyst;
(d) water; and (e) optionally, at least one additive or auxiliary agent.
2. The process according to Claim 1 in which polymer polyol (i) is comprised of at least one solid which is the reaction product of a mixture of 2,4- and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol.
3. The process according to Claim 1 in which polymer polyol (i) is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol.
4. The process according to Claim 1 in which polymer polyol (i) has from about 10 to about 60 weight percent, based on the total weight of the polymer polyol, of at least one polymer solid as a dispersed phase.
5. A rigid polyurethane foam produced by the process of Claim 1.
6. The foam of Claim 5 which has a perpendicular compressive strength within the range of from about 35 to about 150 lbs/in2.
7. The foam of Claim 5 which has from about 1 to about 30 weight percent, based on the total weight of the foam, of at least one solid from a polymer polyol.
8. The foam of Claim 5, when having a density which is in the range of from about 5.66 to about 5.75 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2 and a closed-cell content of at least 84%.
9. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol and when having a density which is in the range of from about 5.66 to about 5.75 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2, and a closed-cell content of at least 84%.
10. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is the reaction product of a mixture of 2,4- and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol and when having a density of about 5.73 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2 and a closed-cell content of at least 84%.
11. The foam of Claim 5, when having a density of about 3.23 lbs/ft3, has a perpendicular compressive strength greater than 24 lbs/in2 and a closed-cell content of at least 84%.
12. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol and when having a density of about 3.23 lbs/ft3, has a perpendicular compressive strength greater than 24 lbs/in2 ana a closed-cell content of at least 84%.
13. A polyurethane-foam forming mixture comprising:
(a) at least one polyol mixture comprising:
(i) at least one polymer polyol;
(ii) at least one polyol having a hydroxyl value within the range of from about 200 to about 800; and (iii) optionally, at least one polyol having a hydroxyl value within the range of from about 25 to about 115;
(b) at least one polymeric isocyanate and/or a prepolymer thereof;
(c) optionally, at least one catalyst;
(d) water; and (e) optionally, at least one additive or auxiliary agent.
14. The mixture of Claim 13 in which polymer polyol (i) is comprised of at least one solid which is the reaction product of a mixture of 2,4-and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol.
15. The mixture of Claim 13 in which polymer polyol (i) is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol.
16. The mixture of Claim 13 in which polymer polyol (i) has from about 10 to about 60 weight percent, based on the total weight of the polymer polyol, of at least one polymer solid as a dispersed phase.
17. A rigid polyurethane foam produced with the polyurethane-foam forming mixture of Claim 13.
1. A process for preparing a water-blown rigid polyurethane foam having at least an 80% closed-cell content comprising reacting:
(a) at least one polyol mixture comprising:
(i) at least one polymer polyol;
(ii) at least one polyol having a hydroxyl value within the range of from about 200 to about 800; and (iii) optionally, at least one polyol having a hydroxyl value within the range of from about 25 to about 115;
with (b) at least one polymeric isocyanate and/or a prepolymer thereof;
in the presence of (c) optionally, at least one catalyst;
(d) water; and (e) optionally, at least one additive or auxiliary agent.
2. The process according to Claim 1 in which polymer polyol (i) is comprised of at least one solid which is the reaction product of a mixture of 2,4- and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol.
3. The process according to Claim 1 in which polymer polyol (i) is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol.
4. The process according to Claim 1 in which polymer polyol (i) has from about 10 to about 60 weight percent, based on the total weight of the polymer polyol, of at least one polymer solid as a dispersed phase.
5. A rigid polyurethane foam produced by the process of Claim 1.
6. The foam of Claim 5 which has a perpendicular compressive strength within the range of from about 35 to about 150 lbs/in2.
7. The foam of Claim 5 which has from about 1 to about 30 weight percent, based on the total weight of the foam, of at least one solid from a polymer polyol.
8. The foam of Claim 5, when having a density which is in the range of from about 5.66 to about 5.75 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2 and a closed-cell content of at least 84%.
9. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol and when having a density which is in the range of from about 5.66 to about 5.75 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2, and a closed-cell content of at least 84%.
10. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is the reaction product of a mixture of 2,4- and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol and when having a density of about 5.73 lbs/ft3, has a perpendicular compressive strength greater than 62 lbs/in2, a tensile adhesion greater than 105 lbs/in2 and a closed-cell content of at least 84%.
11. The foam of Claim 5, when having a density of about 3.23 lbs/ft3, has a perpendicular compressive strength greater than 24 lbs/in2 and a closed-cell content of at least 84%.
12. The foam of Claim 5 which, when prepared with a polymer polyol (i) which is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol and when having a density of about 3.23 lbs/ft3, has a perpendicular compressive strength greater than 24 lbs/in2 ana a closed-cell content of at least 84%.
13. A polyurethane-foam forming mixture comprising:
(a) at least one polyol mixture comprising:
(i) at least one polymer polyol;
(ii) at least one polyol having a hydroxyl value within the range of from about 200 to about 800; and (iii) optionally, at least one polyol having a hydroxyl value within the range of from about 25 to about 115;
(b) at least one polymeric isocyanate and/or a prepolymer thereof;
(c) optionally, at least one catalyst;
(d) water; and (e) optionally, at least one additive or auxiliary agent.
14. The mixture of Claim 13 in which polymer polyol (i) is comprised of at least one solid which is the reaction product of a mixture of 2,4-and 2,6-toluene diisocyanate and hydrazine polymerized in situ in a polyether polyol.
15. The mixture of Claim 13 in which polymer polyol (i) is comprised of at least one solid which is a styrene/acrylonitrile mixture polymerized in situ in a polyether polyol.
16. The mixture of Claim 13 in which polymer polyol (i) has from about 10 to about 60 weight percent, based on the total weight of the polymer polyol, of at least one polymer solid as a dispersed phase.
17. A rigid polyurethane foam produced with the polyurethane-foam forming mixture of Claim 13.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/200,532 | 2002-07-22 | ||
US10/200,532 US6833390B2 (en) | 2002-07-22 | 2002-07-22 | Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties |
PCT/US2003/022555 WO2004009667A1 (en) | 2002-07-22 | 2003-07-18 | Process for preparing closed-cell water blown rigid polyurethane foams having improved mechanical properties |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2493102A1 true CA2493102A1 (en) | 2004-01-29 |
CA2493102C CA2493102C (en) | 2011-05-03 |
Family
ID=30443532
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA 2493102 Expired - Fee Related CA2493102C (en) | 2002-07-22 | 2003-07-18 | Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties |
Country Status (5)
Country | Link |
---|---|
US (3) | US6833390B2 (en) |
AU (1) | AU2003263789A1 (en) |
CA (1) | CA2493102C (en) |
MX (1) | MXPA05000864A (en) |
WO (1) | WO2004009667A1 (en) |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6833390B2 (en) * | 2002-07-22 | 2004-12-21 | Bayer Polymers Llc | Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties |
PT1554329E (en) * | 2002-10-15 | 2012-04-23 | Basf Se | Method for producing rigid polyurethane foams by means of graft polyhydric alcohols |
DE102004017294A1 (en) * | 2004-04-05 | 2005-10-20 | Basf Ag | Process for the production of polyurethane foams |
US20060116435A1 (en) * | 2004-12-01 | 2006-06-01 | Housel Tyler L | High strength polyurethane foam |
DK1896040T3 (en) | 2005-06-29 | 2012-09-03 | Threshold Pharmaceuticals Inc | Phosphoramidate alkylator prodrugs |
US7456229B2 (en) * | 2006-05-31 | 2008-11-25 | Bayer Materialscience Llc | Process for the production of rigid and semi-rigid foams with low amounts of diisocyanate using polymer polyols characterized by high solids and a high hydroxyl number and the resultant foams |
KR100969016B1 (en) * | 2007-12-13 | 2010-07-09 | 현대자동차주식회사 | Polyurethane foam for steering wheel having improved water resistance |
PL2483323T3 (en) | 2009-09-29 | 2014-04-30 | Basf Se | Process for preparing polyurethane rigid foams |
KR101955730B1 (en) * | 2010-09-22 | 2019-03-07 | 바스프 에스이 | Fixing of vacuum insulation panels in cooling apparatuses |
KR101356402B1 (en) * | 2010-11-30 | 2014-01-28 | 한국타이어 주식회사 | Polyurethane foam and pneumatic tire |
CN102190950B (en) * | 2011-03-30 | 2013-06-05 | 深圳市奥顺达实业有限公司 | Polyurea court material, and preparation method and use method thereof |
CN102391775A (en) * | 2011-09-14 | 2012-03-28 | 可利亚多元醇(南京)有限公司 | High-temperature-resistant composite material for polyurethane heat-preserving pipeline |
PL2870188T3 (en) * | 2012-07-04 | 2017-03-31 | Basf Se | Production of foams having improved properties |
US8883869B2 (en) | 2012-08-08 | 2014-11-11 | Provee Technologies, Llc | Impact absorbing foam |
CA2838056C (en) * | 2012-12-21 | 2021-07-13 | Michael L. Jackson | Rigid polyurethane foam with high adhesion properties |
PL3077435T3 (en) * | 2013-12-04 | 2018-07-31 | Covestro Deutschland Ag | Reaction system for a monomer-depleted 1-component polyurethane foam |
CN105899564A (en) * | 2013-12-04 | 2016-08-24 | 科思创德国股份有限公司 | Reaction system for a low-monomer-content single-component polyurethane foam ii |
MX2017016695A (en) | 2015-06-18 | 2018-03-15 | Basf Se | Method for producing a rigid polyurethane foam. |
EP3717243A4 (en) * | 2017-11-28 | 2021-04-28 | Dow Global Technologies LLC | Polyurethane-based insulation board |
CN108047442B (en) * | 2017-12-20 | 2020-02-07 | 上海东大化学有限公司 | Rigid foam composite polyether polyol and preparation method thereof |
US11407874B2 (en) | 2019-10-07 | 2022-08-09 | Covestro Llc | Polyol premixes, thermally insulating rigid polyurethane foams and methods for their production |
Family Cites Families (37)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2754565A (en) * | 1951-06-12 | 1956-07-17 | Parks & Woolson Machine Co | Burling machine and method |
US2764565A (en) * | 1951-12-24 | 1956-09-25 | Bayer Ag | Process and apparatus for the manufacture of polyurethane plastics |
US3523093A (en) * | 1961-11-28 | 1970-08-04 | Paul Stamberger | Method of producing polyurethanes by reacting polyisocyanate with a preformed polymer resulting from polymerization of ethylenically unsaturated monomers |
US3304273A (en) * | 1963-02-06 | 1967-02-14 | Stamberger Paul | Method of preparing polyurethanes from liquid, stable, reactive, filmforming polymer/polyol mixtures formed by polymerizing an ethylenically unsaturated monomer in a polyol |
GB1022434A (en) * | 1961-11-28 | 1966-03-16 | Union Carbide Corp | Improvements in and relating to polymers |
USRE29118E (en) * | 1963-02-06 | 1977-01-18 | Method of preparing polyurethanes from liquid, stable, reactive, film-forming polymer/polyol mixtures formed by polymerizing an ethylenically unsaturated monomer in a polyol | |
USRE28715E (en) * | 1964-08-12 | 1976-02-17 | Polyurethanes, reactive solutions and methods and their production | |
BE759006A (en) * | 1969-11-20 | 1971-05-17 | Marles Kuhlmann Wyandotte | COPOLYMERS GRAFTS AND PREPARATION OF POLYURETHANES |
US3823201A (en) * | 1972-12-04 | 1974-07-09 | Basf Wyandotte Corp | Highly-stable graft copolymer dispersions in polyols containing unsaturation and polyurethanes prepared therefrom |
CA1043948A (en) * | 1974-05-17 | 1978-12-05 | Manfred Dahm | Process for the production of polyurethane foams |
US4104236A (en) * | 1974-08-28 | 1978-08-01 | Union Carbide Corporation | Liquid polymer/polyols and polyurethane elastomers based thereon |
CA1074049A (en) * | 1974-11-13 | 1980-03-18 | Russell Van Cleve | Polymer/polyols and polyurethane derivatives thereof |
US4089835A (en) * | 1975-03-27 | 1978-05-16 | Bayer Aktiengesellschaft | Stable polyurethane dispersions and process for production thereof |
US4172825A (en) * | 1975-07-10 | 1979-10-30 | Union Carbide Corporation | Polymer/polyols and process for production thereof |
US4119586A (en) * | 1976-06-24 | 1978-10-10 | Union Carbide Corporation | Polymer/polyol compositions, processes for making same and processes for making polyurethane products therefrom |
US4125505A (en) * | 1976-07-06 | 1978-11-14 | Union Carbide Corporation | Polymer/polyols from high ethylene oxide content polyols |
DE2639254A1 (en) * | 1976-09-01 | 1978-03-02 | Bayer Ag | PROCESS FOR THE PRODUCTION OF STABLE DISPERSIONS |
US4148840A (en) * | 1978-03-29 | 1979-04-10 | Union Carbide Corporation | Polymer/polyol compositions made from preformed polymer/polyols, processes for making same and processes for making polyurethane products therefrom |
US4374209A (en) * | 1980-10-01 | 1983-02-15 | Interchem International S.A. | Polymer-modified polyols useful in polyurethane manufacture |
US4524157A (en) * | 1981-07-01 | 1985-06-18 | Union Carbide Corporation | Adducts and polymer-polyols useful in the preparation of improved plastics, including polyurethane foams, elastomers and the like |
US4689354A (en) * | 1982-04-01 | 1987-08-25 | Basf Corporation | Process for the preparation of white graft polymer dispersions and flame-retardant polyurethane foams |
US5013766A (en) * | 1989-09-15 | 1991-05-07 | Mobay Corporation | Closed cell, rigid polyurethane foam |
DE4001249A1 (en) * | 1990-01-18 | 1991-07-25 | Bayer Ag | Cold formable open cell rigid polyurethane foam prodn. - from specified poly:ol component and crude MDI, used for car canopy |
DE4007330A1 (en) * | 1990-03-08 | 1991-09-12 | Bayer Ag | METHOD FOR THE PRODUCTION OF URETHANE, UREA AND BIURET GROUPS IN THE ESSENTIAL CLOSED CELLS GROUP AND USE THEREOF |
JPH04239516A (en) | 1991-01-22 | 1992-08-27 | Achilles Corp | Production of rigid polyurethane foam |
US5232957A (en) * | 1992-09-11 | 1993-08-03 | Davidson Textron Inc. | RIM molded energy absorbing polyurethane foam |
DE4315874A1 (en) * | 1993-05-12 | 1994-11-17 | Basf Ag | Process for the production of polyurethane foams |
DE4318962A1 (en) * | 1993-06-08 | 1994-12-15 | Basf Ag | Process for the production of rigid polyurethane foams |
JPH09132631A (en) | 1995-11-06 | 1997-05-20 | Sanyo Chem Ind Ltd | Production of rigid polyurethane foam |
JP3694139B2 (en) | 1997-02-21 | 2005-09-14 | アキレス株式会社 | Expandable polyurethane composition |
US5852065A (en) * | 1998-01-15 | 1998-12-22 | Air Products And Chemicals, Inc. | Low emission, cell opening surfactants for polyurethane flexible and rigid foams |
AU3827999A (en) * | 1998-05-21 | 1999-12-13 | Huntsman Ici Chemicals Llc | Hydrocarbon blown rigid polyurethane foams having improved flammability performance |
BR9902239A (en) * | 1998-06-17 | 2000-04-11 | Air Prod & Chem | Process and composition of banknote additives for rigid flexible polyurethane foams. |
US6127443A (en) * | 1998-11-06 | 2000-10-03 | Bayer Antwerp N.V. | Energy management polyurethane rigid foams with high recovery |
AU2829900A (en) | 1999-03-04 | 2000-09-21 | Asahi Glass Company Limited | Method for producing thermally insulating plate |
US6833390B2 (en) * | 2002-07-22 | 2004-12-21 | Bayer Polymers Llc | Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties |
US7660938B1 (en) * | 2004-10-01 | 2010-02-09 | Super Talent Electronics, Inc. | Flash card reader and data exchanger utilizing low power extended USB protocol without polling |
-
2002
- 2002-07-22 US US10/200,532 patent/US6833390B2/en not_active Expired - Fee Related
-
2003
- 2003-07-18 MX MXPA05000864A patent/MXPA05000864A/en active IP Right Grant
- 2003-07-18 WO PCT/US2003/022555 patent/WO2004009667A1/en not_active Application Discontinuation
- 2003-07-18 AU AU2003263789A patent/AU2003263789A1/en not_active Abandoned
- 2003-07-18 CA CA 2493102 patent/CA2493102C/en not_active Expired - Fee Related
-
2004
- 2004-08-20 US US10/922,399 patent/US20050020705A1/en not_active Abandoned
-
2008
- 2008-09-30 US US12/241,146 patent/US7750058B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US20050020705A1 (en) | 2005-01-27 |
CA2493102C (en) | 2011-05-03 |
US20090036562A1 (en) | 2009-02-05 |
US6833390B2 (en) | 2004-12-21 |
AU2003263789A1 (en) | 2004-02-09 |
US7750058B2 (en) | 2010-07-06 |
MXPA05000864A (en) | 2005-07-29 |
WO2004009667A1 (en) | 2004-01-29 |
US20040014828A1 (en) | 2004-01-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2493102A1 (en) | Process for preparing closed-cell water-blown rigid polyurethane foams having improved mechanical properties | |
MX2010005757A (en) | Compositions and use of cis-1,1,1,4,4,4-hexafluoro-2-butene foam-forming composition in the preparation of polyisocyanate-based foams. | |
TW200712083A (en) | Composition for polyurethane foam, polyol, polyurethane foam obtained from the composition and its manufacturing method, and use of the foam | |
EP2567993A3 (en) | Foam-forming compositions containing azeotropic or azeotrope-like mixtures containing z-1,1,1,4,4,4-hexafluoro-2-butene and their uses in the preparation of polyisocyanate-based foams | |
AU2007260123B2 (en) | Composite panel | |
JP2002536480A5 (en) | ||
PL2029651T3 (en) | A process for the production of rigid and semi-rigid foams with low amounts of diisocyanate using polymer polyols characterized by high solids and a high hydroxyl number and the resultant foams | |
TW200639202A (en) | Class fiber reinforced polyurethane/polyisocyanurate foam | |
WO2006019757A2 (en) | Water blown polyurethane spray foam system | |
WO2009148559A3 (en) | Process for preparing ridig polyisocyanurate foams using natural-oil polyols | |
NO20054612L (en) | Soft elastic foams of low steering densities and deformation hardness | |
PL2001922T3 (en) | Process for making a polyurethane foam | |
WO2006039298A3 (en) | Molded flexible polyurethane foams with reduced flammability and superior durability | |
CA2292510A1 (en) | Method for producing closed-cell rigid polyurethane foams having low thermal conductivity | |
EP1457506A4 (en) | Process for producing synthetic resin foam | |
KR20150138215A (en) | Expanded polyurethane and production method for same | |
WO2002100916A1 (en) | Process for producing flexible polyurethane foams and apparatus for producing flexible polyurethane foams | |
TW200610780A (en) | Process for making polyurethane and polyisocyanurate foams using mixtures of a hydrofluorocarbon and methyl formate as a blowing agent | |
MX2009008916A (en) | Polyvinylchloride/polyurethane hybrid foams with improved burn properties. | |
CA2443130A1 (en) | Energy absorbing flexible foams produced in part with a double metal cyanide catalyzed polyol | |
CA2394169A1 (en) | Method for producing soft to semi-rigid polyurethane integral foamed materials | |
MX2011008048A (en) | Foam-forming compositions containing mixtures of cis-1,1,1,4,4,4-hexafluoro-2-butene and 1,1,1,3,3-pentafluoropro pane and their uses in the preparation of polyisocyanate-based foams. | |
AU2002229537A1 (en) | Method of preparing polyurethane-modified polyisocyanurate foam | |
MXPA02011229A (en) | Polyurethanes containing dispersed crystalline polyesters. | |
WO2004110621A3 (en) | Foam catalyst systems |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |
Effective date: 20140718 |