CA2329070A1 - Polyol blend for the preparation of open cell rigid polyurethane foams - Google Patents
Polyol blend for the preparation of open cell rigid polyurethane foams Download PDFInfo
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- CA2329070A1 CA2329070A1 CA002329070A CA2329070A CA2329070A1 CA 2329070 A1 CA2329070 A1 CA 2329070A1 CA 002329070 A CA002329070 A CA 002329070A CA 2329070 A CA2329070 A CA 2329070A CA 2329070 A1 CA2329070 A1 CA 2329070A1
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- polyol
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- open cell
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- 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
- C08G18/50—Polyethers having heteroatoms other than oxygen
- C08G18/5021—Polyethers having heteroatoms other than oxygen having nitrogen
- C08G18/5024—Polyethers having heteroatoms other than oxygen having nitrogen containing primary and/or secondary amino 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
- C08G18/4009—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
- C08G2110/005—< 50kg/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
Abstract
Polyol blend comprising: (a) a polyol component having an average hydroxyl value of 150 to 850 mg KOH/g and (b) a polymer polyol comprising a polymer stably dispersed in a base polyol medium, which base polyol medium has an average primary hydroxyl content of less than 20 %. This polyol blend is suitably applied in a process for the preparation of open cell rigid polyurethane foams, wherein it is reacted with a polyisocyanate component in the presence of at least a catalyst, a foam stabilising agent and a blowing agent. The resulting open cell rigid polyurethane foam has a density of less than 50 kg/m3 and a closed cell content of less than 10 %, preferably of less than 5 % and can suitably be applied as heat insulating material.
Description
POLYOL BLEND FOR THE PREPARATION OF OPEN CELL
RIGID POLYURETHANE FOAMS
The present invention relates to a polyol blend for the preparation of open cell rigid polyurethane foams, to a process for preparing open cell rigid polyurethane foams, to the polyurethane foams obtainable by this process and to shaped articles comprising these polyurethane foams.
In general, rigid polyurethane foams are well known for their excellent heat insulating properties.
Particularly closed cell polyurethane foams, are widely used as heat insulating material in e.g. pipings, storage tanks, buildings and refrigerators. Closed cell polyurethane foams used to be made with blowing agents based on chlorofluorocarbons (CFC's) of which R-11 (trichlorofluoromethane) was a frequently applied example. The heat insulating properties were for a large part determined by the thermal conductivity of CFC gases, which filled the cells of the foam. However, due to the ozone depleting effect of CFC's their use has become subject to strict environmental regulations and hence is limited nowadays. Alternative blowing agents have been investigated and are actually used, but is very difficult to find substitutes for CFC as a blowing agent, which have equally low thermal conductivity properties.
Although open cell rigid polyurethane foams have not ' 25 such excellent heat insulating properties as closed cell rigid foams, their thermal conductivity is still ' sufficient to be useful as a heat insulating material.
Furthermore, the dimensional stability at low foam density of open cell foams is better than that of closed-cell foams. Open cell rigid polyurethane foams, accordingly, are very suitable for application as the core material in vacuum insulation panels. Such panels usually comprise a core material enclosed in a vacuum container of metal and/or plastic films. Furthermore, open cell rigid polyurethane foams can be used in those rigid foam applications, which do not require any heat insulating properties, but which do require some structural support, for instance, use for automotive headliners or packaging.
Several methods have been proposed to prepare open cell rigid polyurethane foams. For instance, in EP-A-0,547,515 a method for preparing open cell rigid polyurethane foams is disclosed, wherein a polymethylene polyphenylisocyanate prepolymer with a polyol at an NCO/OH equivalent ratio of 1.3 to 3.0 using water as the sole blowing agent in the presence of a catalyst, a foam stabiliser and a cell opening agent. The cell opening agent suitably is a divalent metal salt of a fatty acid, such as calcium stearate, magnesium stearate, strontium stearate or calcium myristate.
According to EP-A-0,567,027 open cell rigid polyurethane foams are prepared by using water as a blowing agent in combination with a specific polyol mixture comprising two or three polyols having different hydroxyl values, said mixture having a hydroxyl value of 160-360 mg KOH/g.
Another method is described in EP-A-0,581,191, where an open cell rigid polyurethane foam is prepared by reacting a polyol with a prepolymer obtained by reacting polymethylene polyphenyl polyisocyanate with a monohydric alcohol using a CFC-substitute as blowing agent in the presence of a catalyst, a foam stabiliser and a cell opening agent. The cell opening agent suitably is a divalent metal salt of a fatty acid, such as calcium stearate.
23-12-1999 ' EP 009903453 ..
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In G. Burkhart and H. Schator, 35th Annual Polyurethane Technical/Marketing Conference, October 9-12, 1994, pp. 311-315 a method for producing open cell rigid polyurethane foams is disclosed, wherein the open cell structure is achieved by using a specific anti-foaming agent (viz. Tegostab 8919; Tegostab is a trademark) in combination with an appropriate silicone surfactant.
. US-A-5,248,704 discloses an energy absorbing, predominantly open-celled, rigid polyurethane foam prepared using a polyol component which is a mixture of hydroxyl terminated polyethers.and graft polymer dispersions. The foam has a density of from 2.0 to 4.5 pounds per square foot, which corresponds with 32 to 288 kg/m3. In Comparative Examples 2 and 3 of US-A-5,248,704 polyol blends are used consisting of a rigid polyol having a hydroxyl number of 390 and a propylene oxide adduct of propylene glycol having an hydroxyl number of 69 and containing styrene-acrylonitril polymer particles dispersed therein. In the comparative examples the amounts of polymer polyo:l-and rigid polyol are 21.56 parts by weight rigid polyo:l plus 30.81 parts by weight polymer polyol (Comparative Example 2) and 29.29 parts by weight rigid polyol plus 41.84 parts by weight polymer polyol (Comparative Example 3). In both cases this corresponds with about 143 parts by weight per 100 parts by weight of the rigid polyol. The density of the foams prepared in Comparative Examples 2 and_3 is 2.5-2.8 pounds per cubic foot or 40-45 kg/m3.
US-A-4,866,102 also discloses an energy-absorbing rigid polyurethane foam, wherein the polyol component used comprises a polymer polyol. One formulation disclosed in D2 (Formulation U) comprises 35 parts by weight of a rigid polyol having a hydroxyl number of 390, AMENDED SHEET
23-12-1999 ~ CA 02329070 2000-io-i9 .. .... . .. .. ..
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RIGID POLYURETHANE FOAMS
The present invention relates to a polyol blend for the preparation of open cell rigid polyurethane foams, to a process for preparing open cell rigid polyurethane foams, to the polyurethane foams obtainable by this process and to shaped articles comprising these polyurethane foams.
In general, rigid polyurethane foams are well known for their excellent heat insulating properties.
Particularly closed cell polyurethane foams, are widely used as heat insulating material in e.g. pipings, storage tanks, buildings and refrigerators. Closed cell polyurethane foams used to be made with blowing agents based on chlorofluorocarbons (CFC's) of which R-11 (trichlorofluoromethane) was a frequently applied example. The heat insulating properties were for a large part determined by the thermal conductivity of CFC gases, which filled the cells of the foam. However, due to the ozone depleting effect of CFC's their use has become subject to strict environmental regulations and hence is limited nowadays. Alternative blowing agents have been investigated and are actually used, but is very difficult to find substitutes for CFC as a blowing agent, which have equally low thermal conductivity properties.
Although open cell rigid polyurethane foams have not ' 25 such excellent heat insulating properties as closed cell rigid foams, their thermal conductivity is still ' sufficient to be useful as a heat insulating material.
Furthermore, the dimensional stability at low foam density of open cell foams is better than that of closed-cell foams. Open cell rigid polyurethane foams, accordingly, are very suitable for application as the core material in vacuum insulation panels. Such panels usually comprise a core material enclosed in a vacuum container of metal and/or plastic films. Furthermore, open cell rigid polyurethane foams can be used in those rigid foam applications, which do not require any heat insulating properties, but which do require some structural support, for instance, use for automotive headliners or packaging.
Several methods have been proposed to prepare open cell rigid polyurethane foams. For instance, in EP-A-0,547,515 a method for preparing open cell rigid polyurethane foams is disclosed, wherein a polymethylene polyphenylisocyanate prepolymer with a polyol at an NCO/OH equivalent ratio of 1.3 to 3.0 using water as the sole blowing agent in the presence of a catalyst, a foam stabiliser and a cell opening agent. The cell opening agent suitably is a divalent metal salt of a fatty acid, such as calcium stearate, magnesium stearate, strontium stearate or calcium myristate.
According to EP-A-0,567,027 open cell rigid polyurethane foams are prepared by using water as a blowing agent in combination with a specific polyol mixture comprising two or three polyols having different hydroxyl values, said mixture having a hydroxyl value of 160-360 mg KOH/g.
Another method is described in EP-A-0,581,191, where an open cell rigid polyurethane foam is prepared by reacting a polyol with a prepolymer obtained by reacting polymethylene polyphenyl polyisocyanate with a monohydric alcohol using a CFC-substitute as blowing agent in the presence of a catalyst, a foam stabiliser and a cell opening agent. The cell opening agent suitably is a divalent metal salt of a fatty acid, such as calcium stearate.
23-12-1999 ' EP 009903453 ..
.. .... . .. .. ..
.. .. . . . .. . . . . .
. . . . . . . ..
. . . . . ... ...
, .... .: 3 - ... .... .. ..
In G. Burkhart and H. Schator, 35th Annual Polyurethane Technical/Marketing Conference, October 9-12, 1994, pp. 311-315 a method for producing open cell rigid polyurethane foams is disclosed, wherein the open cell structure is achieved by using a specific anti-foaming agent (viz. Tegostab 8919; Tegostab is a trademark) in combination with an appropriate silicone surfactant.
. US-A-5,248,704 discloses an energy absorbing, predominantly open-celled, rigid polyurethane foam prepared using a polyol component which is a mixture of hydroxyl terminated polyethers.and graft polymer dispersions. The foam has a density of from 2.0 to 4.5 pounds per square foot, which corresponds with 32 to 288 kg/m3. In Comparative Examples 2 and 3 of US-A-5,248,704 polyol blends are used consisting of a rigid polyol having a hydroxyl number of 390 and a propylene oxide adduct of propylene glycol having an hydroxyl number of 69 and containing styrene-acrylonitril polymer particles dispersed therein. In the comparative examples the amounts of polymer polyo:l-and rigid polyol are 21.56 parts by weight rigid polyo:l plus 30.81 parts by weight polymer polyol (Comparative Example 2) and 29.29 parts by weight rigid polyol plus 41.84 parts by weight polymer polyol (Comparative Example 3). In both cases this corresponds with about 143 parts by weight per 100 parts by weight of the rigid polyol. The density of the foams prepared in Comparative Examples 2 and_3 is 2.5-2.8 pounds per cubic foot or 40-45 kg/m3.
US-A-4,866,102 also discloses an energy-absorbing rigid polyurethane foam, wherein the polyol component used comprises a polymer polyol. One formulation disclosed in D2 (Formulation U) comprises 35 parts by weight of a rigid polyol having a hydroxyl number of 390, AMENDED SHEET
23-12-1999 ~ CA 02329070 2000-io-i9 .. .... . .. .. ..
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.... i. a - ... .... .. ..
parts by weight a propylene oxide-ethylene oxide adduct of glycerine having an ethylene oxide content of 75~ and 50 parts by weight of a propylene oxide adduct of propylene glycol having an hydroxyl number of 69 and 5 containing 50~ of styrene-acrylonitril polymer particles dispersed therein. The amount of polymer polyol, thus, corresponds with 143 parts by weight per 100 parts by weight of rigid polyol. The density of the foam prepared from this formulation (Example 45) is 1.58 pounds per cubic foot or 25.3 kg/m3. .
Although these methods are effective in producing open cell rigid polyurethane foams, there is still room for improvement. It would be beneficial if open cell rigid polyurethane foams could be provided having a very low density in combination with good mechanical or structural stability, as such low density foams are attractive for use in a wide variety of applications including the application as heat insulating material.
The low density is especially desired, because the low weight of the foam facilitates transportation and handling of e.g. insulation panels. Moreover, a lower density also means that less starting material is necessary to prepare the same volume of foam as compared to the situation in which a higher density foam is to be prepared. Clearly this is advantageous from an economic perspective. Furthermore, it would be attractive if low density open cell rigid foams could be prepared without needing any cell-opener or anti-foaming agent, thus facilitating the manufacture whilst still obtaining excellent foams.
Accordingly, the present invention relates to a polyol blend comprising:
(a) a polyol component having an average hydroxyl value of 150 to 850 mg KOH/g and (b) a polymer polyol comprising a polymer stably AMENDED SHEET
WO 99/60045 _ 4 , _ PCT/EP99103453 dispersed in a base polyol medium, which base polyol medium has an average primary hydroxyl content of less than 20~.
Essentially, the present invention combines a rigid polyol component (component (a)) with a particular polymer polyol (component (b)), which is normally used in the manufacture of flexible polyurethane foams. This specific combination of polyols has been found to result in open cell rigid foams having excellent properties without the need to apply cell-opening agents or anti-foaming agents.
The quantities in which the polyol and the polymer polyol are used may vary within broad limits, but preferably the polyol blend according to the present invention comprises 2 to 25 parts by weight, more preferably 2 to 10 parts by weight, of polymer polyol (b) per 100 parts by weight of polyol component (a).
The polyol component (a) can be any rigid polyol or combination of rigid polyols having an average hydroxyl value of 150 to 850 mg KOH/g. Such rigid polyols are known in the art. Commonly applied rigid polyols, which can be suitably applied in the polyol blend of the present invention, are polyoxyalkylene polyols have a nominal molecular weight of from 300 to 1500, suitably 500 to 1000, and a nominal average functionality of at least 2.0, suitably from 2.5 to 6. For the purpose of the present invention the average hydroxyl number preferably has a value in the range of from 150 to 650 mg KOH/g. The polyol component (a) may comprise a single rigid polyol, but may also comprise two or more rigid poiyols. In a preferred embodiment the polyol component (a) comprises a polyol having a hydroxyl value of 150 to 400 mg KOH/g and a polyol having a hydroxyl value of 900 to 650 mg KOH/g.
An example of a rigid polyol having a lower hydroxyl value is CARADOL GB250-O1, while examples of rigid polyols having a higher hydroxyl value are CARADOL LP530-03 and CARADOL LP585-Ol (CARADOL is a trademark) .
The polymer polyol used as component (b) may in ~ 5 principle be any polymer polyol comprising a polymer stably dispersed in a base polyol medium, provided the base polyol medium has an average primary hydroxyl content of less than 20°s based on the total of hydroxyl groups present on the polyol(s) forming the base polyol medium. Accordingly, the base polyol medium may consist of one or more polyols provided the average primary hydroxyl content of these polyol(s) is less than 20~, preferably less than 10$ and most preferably less than 5~. The polymer polyol component (b) suitably comprises such a base polyol medium and a polymer stably dispersed therein in an amount of 5 to 40~ by weight based on total weight of polymer polyol. In a further preferred embodiment the base polyol medium consists of a polyoxyalkylene polyol having a molecular weight in the range of from 250 to 12,000, preferably from 500 to 6,500, more preferably from 2,500 to 6,000; an average nominal functionality (Fn) of at least 2.0, more preferably from 2.5 to 6.0 and most preferably from 2.5 to 3.5; and a primary hydroxyl content of at most 10~, more preferably at most 50. Since the base polyol medium most preferably has a very low average primary hydroxyl content, very good base polyols are those having a very low ethylene oxide (EO) content resulting from EO
tipping. Suitably, the ethylene oxide content resulting ,' 30 from ethylene oxide tipping is less than 1°s by weight, while most suitably the polyol has not been tipped with EO at all.
The polymer, which is stably dispersed in the base polyol medium, may in principle be any such polymer known to be applicable for this purpose. Thus, suitable polymers include the polymers based on ethylenically unsaturated monomers and particularly polymers of vinyl aromatic hydrocarbons, like styrene, alpha-methyl styrene, methyl styrene and various other alkyl-s substituted styrenes. Of these, the use of styrene is preferred. The vinyl aromatic monomer may be used alone or in combination with other ethylenically unsaturated monomers, such as acrylonitrile, methacrylonitrile, vinylidene chloride, various acrylates and conjugated dimes like 1,3-butadiene and isoprene. Preferred polymers, however, are polystyrene and styrene-acrylonitrile (SAN) copolymers. Another suitable class of polymers are the polyurea and polyurethane polymers.
Particularly the condensation products of polyhydric alcohol amines and aromatic diisocyanates are very useful in this respect. A very much preferred polymer is the condensation product of triethanol amine and toluene diisocyanate (TDI). For the purpose of the present invention it is preferred that the dispersed polymer is polystyrene, SAN copolymer, polyurea or the polyurethane polymer obtained as the condensation product of triethanolamine and toluene diisocyanate.
The dispersed polymer is suitably present in an amount of from 5 to 40o by weight based on total weight of polymer polyol. In case the polymer is polystyrene or SAN polymer, preferred amounts are between 5 and 35o by weight, whilst in case of polyurea polyurethane polymers the preferred amount of polymer is between 5 and 20s by weight.
The polyol blend according to the present invention is very suitable for the preparation of open cell rigid polyurethane foams. Thus, the present invention also relates to a process for the preparation of open cell rigid polyurethane foams, which process comprises reacting the polyol blend described herein before with a WO 99/60045 PCT/EP99l03453 polyisocyanate component in the presence of at least a catalyst, a foam stabilising agent and a blowing agent.
Polyisocyanates that may be used are those conventionally applied in the production of rigid polyurethane foams. Useful polyisocyanates should contain at least two isocyanate groups and include both aliphatic -usually alkylene- and aromatic di-, tri-, tetra- and higher isocyanates known in the art to be suitably applied in the production of rigid polyurethane foams.
Mixtures of two or more of such aliphatic and/or aromatic polyisocyanates may also be applied. Examples of suitable polyisocyanates, then, include 2,4-toluene diisocyanate (2,4-TDI), 2,6-TDI, mixtures of 2,4-TDI and 2,6-TDI, 1,5-naphthene diisocyanate, 2,4-methoxyphenyl diisocyanate, 9,4'-diphenylmethane diisocyanate (MDI);
parts by weight a propylene oxide-ethylene oxide adduct of glycerine having an ethylene oxide content of 75~ and 50 parts by weight of a propylene oxide adduct of propylene glycol having an hydroxyl number of 69 and 5 containing 50~ of styrene-acrylonitril polymer particles dispersed therein. The amount of polymer polyol, thus, corresponds with 143 parts by weight per 100 parts by weight of rigid polyol. The density of the foam prepared from this formulation (Example 45) is 1.58 pounds per cubic foot or 25.3 kg/m3. .
Although these methods are effective in producing open cell rigid polyurethane foams, there is still room for improvement. It would be beneficial if open cell rigid polyurethane foams could be provided having a very low density in combination with good mechanical or structural stability, as such low density foams are attractive for use in a wide variety of applications including the application as heat insulating material.
The low density is especially desired, because the low weight of the foam facilitates transportation and handling of e.g. insulation panels. Moreover, a lower density also means that less starting material is necessary to prepare the same volume of foam as compared to the situation in which a higher density foam is to be prepared. Clearly this is advantageous from an economic perspective. Furthermore, it would be attractive if low density open cell rigid foams could be prepared without needing any cell-opener or anti-foaming agent, thus facilitating the manufacture whilst still obtaining excellent foams.
Accordingly, the present invention relates to a polyol blend comprising:
(a) a polyol component having an average hydroxyl value of 150 to 850 mg KOH/g and (b) a polymer polyol comprising a polymer stably AMENDED SHEET
WO 99/60045 _ 4 , _ PCT/EP99103453 dispersed in a base polyol medium, which base polyol medium has an average primary hydroxyl content of less than 20~.
Essentially, the present invention combines a rigid polyol component (component (a)) with a particular polymer polyol (component (b)), which is normally used in the manufacture of flexible polyurethane foams. This specific combination of polyols has been found to result in open cell rigid foams having excellent properties without the need to apply cell-opening agents or anti-foaming agents.
The quantities in which the polyol and the polymer polyol are used may vary within broad limits, but preferably the polyol blend according to the present invention comprises 2 to 25 parts by weight, more preferably 2 to 10 parts by weight, of polymer polyol (b) per 100 parts by weight of polyol component (a).
The polyol component (a) can be any rigid polyol or combination of rigid polyols having an average hydroxyl value of 150 to 850 mg KOH/g. Such rigid polyols are known in the art. Commonly applied rigid polyols, which can be suitably applied in the polyol blend of the present invention, are polyoxyalkylene polyols have a nominal molecular weight of from 300 to 1500, suitably 500 to 1000, and a nominal average functionality of at least 2.0, suitably from 2.5 to 6. For the purpose of the present invention the average hydroxyl number preferably has a value in the range of from 150 to 650 mg KOH/g. The polyol component (a) may comprise a single rigid polyol, but may also comprise two or more rigid poiyols. In a preferred embodiment the polyol component (a) comprises a polyol having a hydroxyl value of 150 to 400 mg KOH/g and a polyol having a hydroxyl value of 900 to 650 mg KOH/g.
An example of a rigid polyol having a lower hydroxyl value is CARADOL GB250-O1, while examples of rigid polyols having a higher hydroxyl value are CARADOL LP530-03 and CARADOL LP585-Ol (CARADOL is a trademark) .
The polymer polyol used as component (b) may in ~ 5 principle be any polymer polyol comprising a polymer stably dispersed in a base polyol medium, provided the base polyol medium has an average primary hydroxyl content of less than 20°s based on the total of hydroxyl groups present on the polyol(s) forming the base polyol medium. Accordingly, the base polyol medium may consist of one or more polyols provided the average primary hydroxyl content of these polyol(s) is less than 20~, preferably less than 10$ and most preferably less than 5~. The polymer polyol component (b) suitably comprises such a base polyol medium and a polymer stably dispersed therein in an amount of 5 to 40~ by weight based on total weight of polymer polyol. In a further preferred embodiment the base polyol medium consists of a polyoxyalkylene polyol having a molecular weight in the range of from 250 to 12,000, preferably from 500 to 6,500, more preferably from 2,500 to 6,000; an average nominal functionality (Fn) of at least 2.0, more preferably from 2.5 to 6.0 and most preferably from 2.5 to 3.5; and a primary hydroxyl content of at most 10~, more preferably at most 50. Since the base polyol medium most preferably has a very low average primary hydroxyl content, very good base polyols are those having a very low ethylene oxide (EO) content resulting from EO
tipping. Suitably, the ethylene oxide content resulting ,' 30 from ethylene oxide tipping is less than 1°s by weight, while most suitably the polyol has not been tipped with EO at all.
The polymer, which is stably dispersed in the base polyol medium, may in principle be any such polymer known to be applicable for this purpose. Thus, suitable polymers include the polymers based on ethylenically unsaturated monomers and particularly polymers of vinyl aromatic hydrocarbons, like styrene, alpha-methyl styrene, methyl styrene and various other alkyl-s substituted styrenes. Of these, the use of styrene is preferred. The vinyl aromatic monomer may be used alone or in combination with other ethylenically unsaturated monomers, such as acrylonitrile, methacrylonitrile, vinylidene chloride, various acrylates and conjugated dimes like 1,3-butadiene and isoprene. Preferred polymers, however, are polystyrene and styrene-acrylonitrile (SAN) copolymers. Another suitable class of polymers are the polyurea and polyurethane polymers.
Particularly the condensation products of polyhydric alcohol amines and aromatic diisocyanates are very useful in this respect. A very much preferred polymer is the condensation product of triethanol amine and toluene diisocyanate (TDI). For the purpose of the present invention it is preferred that the dispersed polymer is polystyrene, SAN copolymer, polyurea or the polyurethane polymer obtained as the condensation product of triethanolamine and toluene diisocyanate.
The dispersed polymer is suitably present in an amount of from 5 to 40o by weight based on total weight of polymer polyol. In case the polymer is polystyrene or SAN polymer, preferred amounts are between 5 and 35o by weight, whilst in case of polyurea polyurethane polymers the preferred amount of polymer is between 5 and 20s by weight.
The polyol blend according to the present invention is very suitable for the preparation of open cell rigid polyurethane foams. Thus, the present invention also relates to a process for the preparation of open cell rigid polyurethane foams, which process comprises reacting the polyol blend described herein before with a WO 99/60045 PCT/EP99l03453 polyisocyanate component in the presence of at least a catalyst, a foam stabilising agent and a blowing agent.
Polyisocyanates that may be used are those conventionally applied in the production of rigid polyurethane foams. Useful polyisocyanates should contain at least two isocyanate groups and include both aliphatic -usually alkylene- and aromatic di-, tri-, tetra- and higher isocyanates known in the art to be suitably applied in the production of rigid polyurethane foams.
Mixtures of two or more of such aliphatic and/or aromatic polyisocyanates may also be applied. Examples of suitable polyisocyanates, then, include 2,4-toluene diisocyanate (2,4-TDI), 2,6-TDI, mixtures of 2,4-TDI and 2,6-TDI, 1,5-naphthene diisocyanate, 2,4-methoxyphenyl diisocyanate, 9,4'-diphenylmethane diisocyanate (MDI);
4,4'-biphenylene diisocyanate, 3,3'-dimethoxy-4,4'-bi-phenylene diisocyanate, 3,3'-dimethyl-4,9'-biphenylene diisocyanate and 3,3'-dimethyl-4,4'-diphenylmethane diisocyanate, 4,4',4"-triphenylmethane triisocyanate, 2,4,6-toluene triisocyanate, 9,4'-dimethyl-2,2', 5,5'-diphenylmethane tetraisocyanate, polymethylene-polyphenylene polyisocyanate and mixtures of two or more of these. Polymeric MDI, a mixture of polyisocyanates with MDI as the main component, may also be used. For the purpose of the present invention it has been found particularly advantageous to use polymeric MDI.
The quantity of polyisocyanate component to be used should suitably be such that the isocyanate index has a value between 50 and 150, most suitably between 80 and 130. However, isocyanate indices outside these ranges may also be used.
Catalysts for the production of rigid polyurethane foams are known in the art and include many different compounds. For the purpose of the present invention suitable catalysts include tertiary amines, such as, for _ g _ instance, bis(2,2'-dimethylamino)ethyl ether, trimethylamine, triethylamine, triethylenediamine and dimethylethanolamine (DMEA). Tin-based catalysts may also be applied and include tin salts and dialkyl tin salts of carboxylic acids. Specific examples are dibutyltin dilaureate, stannous octoate, stannous oleate, dibutyltin acetate and dibutyltin diacetate. Also trimerisation catalysts like potassium acetate may be applied. The catalyst is typically used in an amount of from 0.01 to 7 php (parts by weight per 100 parts of polyol).
The foam stabiliser (or surfactant) used in the present process may be any polyurethane foam stabiliser useful in the production of rigid polyurethane foams.
Organosilicone or organopolysiloxane surfactants are most conventionally applied as foam stabilisers in polyurethane production. A large variety of such surfactants is commercially available. Usually, such foam stabiliser is used in an amount of up to 3 php.
A blowing agent is also present in the process according to the present invention. Suitable blowing agents include water, aceton, (liquid) carbon dioxide, halogenated hydrocarbons, aliphatic alkanes, such as n-pentane and isopentane, and alicyclic alKanes, such as cyclopentane and cyclohexane. It will be understood that these blowing agents may be used singly or in mixtures of two or more. For the purpose of the present invention, it has been found particularly advantageous to use water as the sole blowing agent. The amount in which the water is used may vary between wide limits, but very good results , have been achieved when using water in an amount of 2-12 php.
In addition, other well known auxiliaries, such as flame retardants, antioxidants, colouring agents and fillers may also be used.
_g_ In a further aspect the present invention relates to an open cell rigid polyurethane foam obtainable by the process described herein before, which polyurethane foam has a density of less than 50 kg/m3 and a closed cell content of less than 100, preferably of less than 5%.
Preferred foams, which are obtainable by the present process, have densities of 10 to 30 kg/m3, more preferably 10 to 25 kg/m3.
The present invention also relates to shaped articles comprising the open cell rigid polyurethane foam defined in the preceding paragraph as well as t:o heat insulating materials comprising this open celled rigid polyurethane foam in a laminate structure.
The invention is further illustrated by the following examples, but is by no means limited to the specific embodiments demonstrated therein.
The components used in the examples are:
Polyol components Polyol A: A rigid, aromatic, amine-group containing, propylene oxide(PO)-based polyether polyol having a hydroxyl value of 530 mg KOH/g.
Polyol B: A rigid, glycerol initiated polyether polyol having a hydroxyl value of 250 mg KOH/g.
pp-A: A polymer polyol containing ii) a base polyol being a EO/PO based, glycerol initiated polyether polyol having a primary hydroxyl content of essentially Oa, a molecular weight of 3500 and a hydroxyl value of 37 mg KOH/g and (ii) stably dispersed therein 20 wt~
polystyrene.
pp-B: A polymer polyol containing (i) the same base polyol as PP-A, and (ii) stably dispersed therein 40 wt°s styrene-acrylonitrile copolymer.
PP-C: A polymer polyol containing (i) a base polyol being a EO/PO based, glycerol initiated polyether polyol having a primary hydroxyl content of 800, a molecular weight of 4700 and a hydroxyl value of 25 mg KOH/g and ' containing 19 wt°s EO-tip and (ii) stably dispersed therein 28 wt% polystyrene.
PP-D: A polymer polyol containing (i) the same base polyol as PP-C, and (ii) stably dispersed therein 15 wto styrene-acrylonitrile copolymer.
Ancillary chemicals DMEA . Dimethylethanolamine AM58 . trimerisation catalyst ex Resina Chemie TCPP . tris(chloropropyl)phosphate (flame retardant) B8404 . Tegostab B8404 (silicone surfactant) ex Goldschmidt Isocyanate MDI . polymeric diphenylmethane diisocyanate Example 1 A polyol formulation was prepared consisting of parts by weight (pbw) Polyol A, 70 pbw Polyol B and 10 pbw of PP-A. Subsequently a foaming formulation (Ex-1) was prepared having a composition as indicated in 25 Table I.
The formulation was allowed to foam in a bag. After foaming a sample of the foam was taken and density and closed cell content were determined.
Example 2 30 Example 1 was repeated except that 10 pbw of PP-B
were added (Ex-2) in stead of PP-A.
The composition of the foaming formulation and the properties of the resulting foam are indicated in Table I.
. CA 02329070 2000-10-19 WO 99/60045 PCTlEP99/03453 Comparative Examples 1 and 2 Example 1 was repeated except that 10 pbw of PP-C
(CEx-1) or 10 pbw of PP-D (CEx-2) were used in stead of IO pbw of PP-A.
- 5 The composition of the.foaming formulations and the properties of the resulting foam are indicated in Table I.
TABLE I Foaming formulations Ex-1 Ex-2 CEx-1 CEx-2 Polyol A (pbw) 70 70 70 70 Polyol B (pbw) 30 30 30 30 PP-A (pbw) 10 - - -PP-B (pbw) - 10 - -PP-C (pbw) - - 10 -PP-D (pbw) _ _ - 10 DMEA (pbw) 2.4 2.4 2.9 2.4 AM58 (pbw) 1.6 1.6 1.6 1.6 B8904 (pbw) 2.0 2.0 2.0 2.0 water (pbw) 10.2 10.2 10.2 10.2 TCPP (pbw) 10 10 10 10 MDI (pbw) 208 208 208 208 Isocyanate index 90 90 90 90 Density (kg/m3) 16.8 16.6 17.52 17.5 Closed cell content (%) 2 3 42 60 From Table I it can be seen that the polyol formulation according to the present invention result in foams having a slightly lower density and a much lower closed cell content.
Example 3 A laminate with a open cell polyurethane foam prepared with a polyol blend according to the present invention, was made on a continuous laminator machine.
CA 02329070 2000-10-19 .
The laminator machine is a high pressure, multi-component unit, manufactured by Cannon/Viking UK. The urethane system, being a blend of four different streams, was dispensed on the bottom facing through a perforated pipe, fitted to a traversing mixing head. As the facing, polyethylene coated kraft paper was used. The machine output was adjusted to produce 60 mm thick, 600 mm wide laminates at an overall target density of 22 kg/m3 at a belt speed of 2.9 m/min. The 6 meter conveyor section was working in free rise mode.
As stated above, four streams (denoted as "polyol blend" , "cat 1 blend" , "cat 2 blend" and "MDI" ) are pumped into the mixing head, where they are thoroughly mixed and dispensed onto the facing. The MDI stream consisted of polymeric MDI. The compositions of the other three streams are indicated in Table II. The amounts are indicated in parts by weight (pbw).
TABLE II Feed stream compositions polyol blend cat 1 blend cat 2 blend Polyol A 30 - -Polyol B 56.2 15 10 water - 15 -The stream rates were:
Output polyol blend 0.84 1/min :
Output MDI . 1.08 1/min Output cat 1 blend 0.136 1/min .
Output cat 2 blend 0.033 1/min .
WO 99!60045 . PCT/EP99/03453 The temperature of both polyol blend and MDI stream was 19 C, the temperature of the belt was kept at 35 C.
The properties of the open cel l rigid foam-based laminate were:
Density . 22 kg/m3 Closed cell content . 2$
Compressive strength in rise direction . 80 kPa in production direction . 55 kPa in side direction . 55 kPa Dimensional stability at 70 C at 95$ relative humidity h ours after in rise direction . 3.5~
in production direction . -0.5~
in side direction . -0.7~
Thermal conductivity at 10 C . 35 mW/(m.K) Thermal conductivity at 10 C was determined by putting the laminate between two plates, one having a temperature of 0 C and the other having a temperature of 20 C, and determining the amount of heat transferred through the laminate from the warm plate to the cold plate per second per meter of lami nate per degree Kelvin temperature difference.
From these data it can be seen that the laminate has ~ a relatively low density and a low closed cell content, while at the same time exhibiting excellent mechanical stability and low thermal conducti vity, thus making it very useful as an insulating mater ial.
The quantity of polyisocyanate component to be used should suitably be such that the isocyanate index has a value between 50 and 150, most suitably between 80 and 130. However, isocyanate indices outside these ranges may also be used.
Catalysts for the production of rigid polyurethane foams are known in the art and include many different compounds. For the purpose of the present invention suitable catalysts include tertiary amines, such as, for _ g _ instance, bis(2,2'-dimethylamino)ethyl ether, trimethylamine, triethylamine, triethylenediamine and dimethylethanolamine (DMEA). Tin-based catalysts may also be applied and include tin salts and dialkyl tin salts of carboxylic acids. Specific examples are dibutyltin dilaureate, stannous octoate, stannous oleate, dibutyltin acetate and dibutyltin diacetate. Also trimerisation catalysts like potassium acetate may be applied. The catalyst is typically used in an amount of from 0.01 to 7 php (parts by weight per 100 parts of polyol).
The foam stabiliser (or surfactant) used in the present process may be any polyurethane foam stabiliser useful in the production of rigid polyurethane foams.
Organosilicone or organopolysiloxane surfactants are most conventionally applied as foam stabilisers in polyurethane production. A large variety of such surfactants is commercially available. Usually, such foam stabiliser is used in an amount of up to 3 php.
A blowing agent is also present in the process according to the present invention. Suitable blowing agents include water, aceton, (liquid) carbon dioxide, halogenated hydrocarbons, aliphatic alkanes, such as n-pentane and isopentane, and alicyclic alKanes, such as cyclopentane and cyclohexane. It will be understood that these blowing agents may be used singly or in mixtures of two or more. For the purpose of the present invention, it has been found particularly advantageous to use water as the sole blowing agent. The amount in which the water is used may vary between wide limits, but very good results , have been achieved when using water in an amount of 2-12 php.
In addition, other well known auxiliaries, such as flame retardants, antioxidants, colouring agents and fillers may also be used.
_g_ In a further aspect the present invention relates to an open cell rigid polyurethane foam obtainable by the process described herein before, which polyurethane foam has a density of less than 50 kg/m3 and a closed cell content of less than 100, preferably of less than 5%.
Preferred foams, which are obtainable by the present process, have densities of 10 to 30 kg/m3, more preferably 10 to 25 kg/m3.
The present invention also relates to shaped articles comprising the open cell rigid polyurethane foam defined in the preceding paragraph as well as t:o heat insulating materials comprising this open celled rigid polyurethane foam in a laminate structure.
The invention is further illustrated by the following examples, but is by no means limited to the specific embodiments demonstrated therein.
The components used in the examples are:
Polyol components Polyol A: A rigid, aromatic, amine-group containing, propylene oxide(PO)-based polyether polyol having a hydroxyl value of 530 mg KOH/g.
Polyol B: A rigid, glycerol initiated polyether polyol having a hydroxyl value of 250 mg KOH/g.
pp-A: A polymer polyol containing ii) a base polyol being a EO/PO based, glycerol initiated polyether polyol having a primary hydroxyl content of essentially Oa, a molecular weight of 3500 and a hydroxyl value of 37 mg KOH/g and (ii) stably dispersed therein 20 wt~
polystyrene.
pp-B: A polymer polyol containing (i) the same base polyol as PP-A, and (ii) stably dispersed therein 40 wt°s styrene-acrylonitrile copolymer.
PP-C: A polymer polyol containing (i) a base polyol being a EO/PO based, glycerol initiated polyether polyol having a primary hydroxyl content of 800, a molecular weight of 4700 and a hydroxyl value of 25 mg KOH/g and ' containing 19 wt°s EO-tip and (ii) stably dispersed therein 28 wt% polystyrene.
PP-D: A polymer polyol containing (i) the same base polyol as PP-C, and (ii) stably dispersed therein 15 wto styrene-acrylonitrile copolymer.
Ancillary chemicals DMEA . Dimethylethanolamine AM58 . trimerisation catalyst ex Resina Chemie TCPP . tris(chloropropyl)phosphate (flame retardant) B8404 . Tegostab B8404 (silicone surfactant) ex Goldschmidt Isocyanate MDI . polymeric diphenylmethane diisocyanate Example 1 A polyol formulation was prepared consisting of parts by weight (pbw) Polyol A, 70 pbw Polyol B and 10 pbw of PP-A. Subsequently a foaming formulation (Ex-1) was prepared having a composition as indicated in 25 Table I.
The formulation was allowed to foam in a bag. After foaming a sample of the foam was taken and density and closed cell content were determined.
Example 2 30 Example 1 was repeated except that 10 pbw of PP-B
were added (Ex-2) in stead of PP-A.
The composition of the foaming formulation and the properties of the resulting foam are indicated in Table I.
. CA 02329070 2000-10-19 WO 99/60045 PCTlEP99/03453 Comparative Examples 1 and 2 Example 1 was repeated except that 10 pbw of PP-C
(CEx-1) or 10 pbw of PP-D (CEx-2) were used in stead of IO pbw of PP-A.
- 5 The composition of the.foaming formulations and the properties of the resulting foam are indicated in Table I.
TABLE I Foaming formulations Ex-1 Ex-2 CEx-1 CEx-2 Polyol A (pbw) 70 70 70 70 Polyol B (pbw) 30 30 30 30 PP-A (pbw) 10 - - -PP-B (pbw) - 10 - -PP-C (pbw) - - 10 -PP-D (pbw) _ _ - 10 DMEA (pbw) 2.4 2.4 2.9 2.4 AM58 (pbw) 1.6 1.6 1.6 1.6 B8904 (pbw) 2.0 2.0 2.0 2.0 water (pbw) 10.2 10.2 10.2 10.2 TCPP (pbw) 10 10 10 10 MDI (pbw) 208 208 208 208 Isocyanate index 90 90 90 90 Density (kg/m3) 16.8 16.6 17.52 17.5 Closed cell content (%) 2 3 42 60 From Table I it can be seen that the polyol formulation according to the present invention result in foams having a slightly lower density and a much lower closed cell content.
Example 3 A laminate with a open cell polyurethane foam prepared with a polyol blend according to the present invention, was made on a continuous laminator machine.
CA 02329070 2000-10-19 .
The laminator machine is a high pressure, multi-component unit, manufactured by Cannon/Viking UK. The urethane system, being a blend of four different streams, was dispensed on the bottom facing through a perforated pipe, fitted to a traversing mixing head. As the facing, polyethylene coated kraft paper was used. The machine output was adjusted to produce 60 mm thick, 600 mm wide laminates at an overall target density of 22 kg/m3 at a belt speed of 2.9 m/min. The 6 meter conveyor section was working in free rise mode.
As stated above, four streams (denoted as "polyol blend" , "cat 1 blend" , "cat 2 blend" and "MDI" ) are pumped into the mixing head, where they are thoroughly mixed and dispensed onto the facing. The MDI stream consisted of polymeric MDI. The compositions of the other three streams are indicated in Table II. The amounts are indicated in parts by weight (pbw).
TABLE II Feed stream compositions polyol blend cat 1 blend cat 2 blend Polyol A 30 - -Polyol B 56.2 15 10 water - 15 -The stream rates were:
Output polyol blend 0.84 1/min :
Output MDI . 1.08 1/min Output cat 1 blend 0.136 1/min .
Output cat 2 blend 0.033 1/min .
WO 99!60045 . PCT/EP99/03453 The temperature of both polyol blend and MDI stream was 19 C, the temperature of the belt was kept at 35 C.
The properties of the open cel l rigid foam-based laminate were:
Density . 22 kg/m3 Closed cell content . 2$
Compressive strength in rise direction . 80 kPa in production direction . 55 kPa in side direction . 55 kPa Dimensional stability at 70 C at 95$ relative humidity h ours after in rise direction . 3.5~
in production direction . -0.5~
in side direction . -0.7~
Thermal conductivity at 10 C . 35 mW/(m.K) Thermal conductivity at 10 C was determined by putting the laminate between two plates, one having a temperature of 0 C and the other having a temperature of 20 C, and determining the amount of heat transferred through the laminate from the warm plate to the cold plate per second per meter of lami nate per degree Kelvin temperature difference.
From these data it can be seen that the laminate has ~ a relatively low density and a low closed cell content, while at the same time exhibiting excellent mechanical stability and low thermal conducti vity, thus making it very useful as an insulating mater ial.
Claims (16)
1. Polyol blend comprising:
(a) a polyol component having an average hydroxyl value of 150 to 850 mg KOH/g and (b) 2 to 25 parts by weight per 100 parts by weight of polyol component (a) of a polymer polyol comprising a polymer stably dispersed in a base polyol medium, which base polyol medium has an average primary hydroxyl content of less than 20%.
(a) a polyol component having an average hydroxyl value of 150 to 850 mg KOH/g and (b) 2 to 25 parts by weight per 100 parts by weight of polyol component (a) of a polymer polyol comprising a polymer stably dispersed in a base polyol medium, which base polyol medium has an average primary hydroxyl content of less than 20%.
2. Polyol blend according to claim 1, wherein the polyol component (a) comprises a polyol having a hydroxyl value of 150 to 400 mg KOH/g and a polyol having a hydroxyl value of 400 to 650 mg KOH/g.
3. Polyol blend according to any one of the preceding claims, wherein the polymer polyol (b) comprises a base polyol medium having an average primary hydroxyl content of at most 10% and a polymer stably dispersed therein in an amount of 5 to 40% by weight based on total weight of polymer polyol.
4. Polyol blend according to claim 3, wherein the base polyol medium has an average primary hydroxyl content of at most 5%.
5. Polyol blend according to any one of the preceding claims, wherein the polymer polyol (b) comprises a base polyol medium consisting of a polyoxyalkylene polyol having a molecular weight in the range of from 250 to 12,000, an average nominal functionality (Fn) of at least 2.0 and a primary hydroxyl content of at most 10% and a polymer stably dispersed therein in an amount of 5 to 40%
by weight based on total weight of polymer polyol.
by weight based on total weight of polymer polyol.
6. Polyol blend according to claim 5, wherein the polyoxyalkylene polyol has a molecular weight in the range of from 2,500 to 6,000, a Fn in the range of from 2.5 to 3.5 and a primary hydroxyl content of at most 55.
7. Polyol blend according to claim 5 or 6, wherein the polyoxyalkylene polyol has an ethylene oxide content resulting from ethylene oxide tipping of less than 1% by weight.
8. Polyol component according to any one of claims 3 to 7, wherein the stably dispersed polymer is polystyrene, SAN copolymer, polyurea or the polyurethane polymer obtained as the condensation product of triethanolamine and toluene diisocyanate.
9. Process for the preparation of open cell rigid polyurethane foams, which process comprises reacting a polyol blend as claimed in any one of claims 1-9 with a polyisocyanate component in the presence of at least a catalyst, a foam stabilising agent and a blowing agent.
10. Process according to claim 9, wherein the polyisocyanate component comprises polymeric MDI.
11. Process according to claim 9 or 10, wherein the blowing agent is water.
12. Process according to claim 11, wherein water is present in an amount of 2-12 parts by weight per 100 parts by weight of polyol component (a).
13. An open cell rigid polyurethane foam obtainable by the process according to any one of claims 9-12, which polyurethane foam has a density of less than 50 kg/m3 and a closed cell content of less than 10%.
14. Open cell rigid polyurethane foam according to claim 13 having a density of 10 to 30 kg/m3.
15. Shaped article comprising the open cell rigid polyurethane foam according to claim 13 or 14.
16. A heat insulating material comprising the open celled rigid polyurethane foam according to claim 13 or 14 in a laminate structure.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP98201681 | 1998-05-20 | ||
| EP98201681.8 | 1998-05-20 | ||
| PCT/EP1999/003453 WO1999060045A1 (en) | 1998-05-20 | 1999-05-18 | Polyol blend for the preparation of open cell rigid polyurethane foams |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2329070A1 true CA2329070A1 (en) | 1999-11-25 |
Family
ID=8233741
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002329070A Abandoned CA2329070A1 (en) | 1998-05-20 | 1999-05-18 | Polyol blend for the preparation of open cell rigid polyurethane foams |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP1086158A1 (en) |
| JP (1) | JP2002515527A (en) |
| AU (1) | AU4363899A (en) |
| CA (1) | CA2329070A1 (en) |
| WO (1) | WO1999060045A1 (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ATE552285T1 (en) * | 2002-10-15 | 2012-04-15 | Basf Se | METHOD FOR PRODUCING HARD POLYURETHANE FOAM WITH GRAFT POLYOLS |
| CN102070764B (en) * | 2010-12-24 | 2012-07-18 | 东莞市源聚德实业有限公司 | Carrier sponge for medical framework accessory and preparation method thereof |
| CN105518049B (en) * | 2013-09-13 | 2019-09-03 | 陶氏环球技术有限责任公司 | The polyurethane foam of combustion modifications based on PIPA |
| PL3024866T3 (en) * | 2013-09-13 | 2017-08-31 | Dow Global Technologies Llc | Polyisocyanate polyaddition polyol manufacturing process and product |
| EP3519478B1 (en) | 2016-09-30 | 2020-07-08 | Dow Global Technologies LLC | Polyol compositions |
| JP6921506B2 (en) * | 2016-11-25 | 2021-08-18 | コベストロ、ドイチュラント、アクチエンゲゼルシャフトＣｏｖｅｓｔｒｏ Ｄｅｕｔｓｃｈｌａｎｄ Ａｇ | Manufacturing method of open cell rigid polyurethane foam |
| EP3717243A4 (en) * | 2017-11-28 | 2021-04-28 | Dow Global Technologies LLC | Polyurethane-based insulation board |
| CN112368315B (en) * | 2018-06-27 | 2023-07-04 | 巴斯夫欧洲公司 | Method for producing rigid polyurethane foams and their use as heat insulation materials |
| US11739176B2 (en) | 2018-10-15 | 2023-08-29 | Dow Global Technologies Llc | Formulated polyol compositons |
| US11407874B2 (en) | 2019-10-07 | 2022-08-09 | Covestro Llc | Polyol premixes, thermally insulating rigid polyurethane foams and methods for their production |
| MX2022007552A (en) * | 2019-12-17 | 2022-07-19 | Basf Se | A flexible foaming process for producing thermally insulated articles. |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4866102A (en) * | 1987-11-20 | 1989-09-12 | Pray Edward R | Moldable energy absorbing rigid polyurethane foams |
| US5248704A (en) * | 1992-06-04 | 1993-09-28 | Basf Corporation | Energy absorbing, water blown, rigid polyurethane foam |
| US5698609A (en) * | 1996-11-14 | 1997-12-16 | Imperial Chemical Industries Plc | Energy absorbing polyurethane foams |
-
1999
- 1999-05-18 JP JP2000549662A patent/JP2002515527A/en active Pending
- 1999-05-18 EP EP99926339A patent/EP1086158A1/en not_active Withdrawn
- 1999-05-18 WO PCT/EP1999/003453 patent/WO1999060045A1/en not_active Application Discontinuation
- 1999-05-18 CA CA002329070A patent/CA2329070A1/en not_active Abandoned
- 1999-05-18 AU AU43638/99A patent/AU4363899A/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| WO1999060045A1 (en) | 1999-11-25 |
| EP1086158A1 (en) | 2001-03-28 |
| JP2002515527A (en) | 2002-05-28 |
| AU4363899A (en) | 1999-12-06 |
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