US20110201707A1 - Isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid polyisocyanurate/polyurethane foams made therefrom, and a process for making such foams - Google Patents

Isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid polyisocyanurate/polyurethane foams made therefrom, and a process for making such foams Download PDF

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US20110201707A1
US20110201707A1 US13/125,481 US200913125481A US2011201707A1 US 20110201707 A1 US20110201707 A1 US 20110201707A1 US 200913125481 A US200913125481 A US 200913125481A US 2011201707 A1 US2011201707 A1 US 2011201707A1
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group
trimerisation
optionally
isocyanate
catalyst system
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Phillip S. Athey
Nathan Wilmot
Richard Keaton
David A. Babb
Cecile Boyer
Timothy Morley
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Dow Chemical Co
Dow Global Technologies LLC
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Dow Global Technologies LLC
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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
    • C08G18/02—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only
    • C08G18/022—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only the polymeric products containing isocyanurate 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
    • C08G18/08—Processes
    • C08G18/09—Processes comprising oligomerisation of isocyanates or isothiocyanates involving reaction of a part of the isocyanate or isothiocyanate groups with each other in the reaction mixture
    • C08G18/092—Processes comprising oligomerisation of isocyanates or isothiocyanates involving reaction of a part of the isocyanate or isothiocyanate groups with each other in the reaction mixture oligomerisation to isocyanurate 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
    • C08G18/08—Processes
    • C08G18/16—Catalysts
    • C08G18/166—Catalysts not provided for in the groups C08G18/18 - C08G18/26
    • C08G18/168—Organic 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
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08—Processes
    • C08G18/16—Catalysts
    • C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
    • C08G18/1875—Catalysts containing secondary or tertiary amines or salts thereof containing ammonium salts or mixtures of secondary of tertiary amines and acids
    • 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
    • C08G18/16—Catalysts
    • C08G18/166—Catalysts not provided for in the groups C08G18/18 - C08G18/26
    • 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
    • C08G2115/00—Oligomerisation
    • C08G2115/02—Oligomerisation to isocyanurate groups

Definitions

  • the instant invention relates to an isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid polyisocyanurate/polyurethane foams made therefrom, and a process for making such foams.
  • PIR foams are widely known and are used in numerous industries.
  • PIR foams are hybrid structures having both groups: urethane groups (resulting from the reaction of —NCO groups of isocyanates with the hydroxyl groups of polyols) and isocyanurate rings, derived from the trimerisation of an excess of —NCO groups against the hydroxyl groups (isocyanate index of greater than 100, for example, 180-600). Trimerisation of —NCO groups is typically catalyzed by special catalysts, such as tris(dimethylaminomethyl) phenol, potassium acetate and other catalysts.
  • the highly crosslinked structure of the PIR foams is derived from the isocyanurate rings generated by the trimerisation of the excess of —NCO groups.
  • PIR foams are continuously subjected to increased regulations with respect to flame retardant traits and reduced smoke generation. Flame retardant traits and reduced smoke generation are typically improved because of the presence of isocyanurate rings.
  • existing trimerisation catalyst systems for producing such isocyanurate rings tend to be active only at high temperatures, which is typical within the core zone of PR foams. Therefore, the existing trimerisation catalyst systems tend to facilitate the formation of isocyanurate rings mainly in the core zone of the PR foams.
  • the use of existing trimerisation catalyst systems improves the flame retardant and smoke generation traits of the core zone of PIR foams, there is still a need to further improve such properties within the outer zones of such PIR foams.
  • the instant invention facilaites the formation of isocyanurate rings within the outer zones of such PR foams, and as a result facilitating the improvement of flame retardant and smoke generation traits of the outer zones of PIR foams.
  • the instant invention facilitates and increases the trimerisation of the isocyanurate rings in the outer zones of PIR foams by requiring lower activation temperatures.
  • the instant invention may further provide improved bonding properties, for example, in lamination processes, that is, tensile bond strength of double steel facers of PR foam panels.
  • the instant invention provides an isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams.
  • the present invention provides a trimerisation catalyst system comprising: (a) a phosphatrane cation; and (b) an isocyanate-trimer inducing anion; wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.
  • the present invention further provides a precursor formulation comprising: (1) at least 25 percent by weight of polyol, based on the weight of the precursor formulation; (2) less than 15 percent by weight of a trimerisation catalyst system, based on the weight of the precursor formulation, comprising; (a) a phosphatrane cation; and (c) an isocyanate-trimer inducing anion; wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.; and (3) optionally one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts (other than the trimerisation catalyst system, as described herein), or combinations thereof.
  • the present invention further provides a process for trimerisation of isocyanates comprising the steps of: (1) providing one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof; (2) providing a trimerisation catalyst system comprising; (a) an phosphatrane cation; and (b) an isocyanate-trimer inducing anion; wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.; (3) trimerising the one or more monomers in the presence of the trimerisation catalyst; and (4) thereby forming an isocyanurate ring.
  • the present invention further provides a method for making a PIR foam comprising the steps of: (1) providing one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof; (2) providing polyol; (3) providing a trimerisation catalyst system comprising; (a) a phosphatrane cation; and (b) an isocyanate-trimer inducing anion; wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.; and (4) optionally providing one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts, or combinations thereof; (5) contacting the one or more monomers, and the polyol, and optionally the one or more surfact
  • the present invention further provides a PIR foam comprising the reaction product of one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof with polyol in the presence of a trimerisation catalyst system comprising a phosphatrane cation, and an isocyanate-trimer inducing anion, and optionally one or more surfactants, optionally one or more flame retardants, optionally water, optionally one or more antioxidants, optionally one or more auxiliary blowing agents, optionally one or more additional urethane catalysts, and optionally one or more auxiliary trimerisation catalysts, or optionally combinations thereof, wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.
  • the present invention further provides a PIR foam comprising the reaction product of one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof with polyol in the presence of a trimerisation catalyst system comprising a phosphatrane cation, and an isocyanate-trimer inducing anion, and optionally one or more surfactants, optionally one or more flame retardants, optionally water, optionally one or more antioxidants, optionally one or more auxiliary blowing agents, optionally one or more additional polyurethane catalysts, and optionally one or more auxiliary trimerisation catalysts, or optionally combinations thereof, wherein the PIR foam has a polyisocyanurate trimer ratio (Abs 1410 /Abs 1595 ) of at least 5 at a depth of 12 mm from the rising surface of the rigid foam having a thickness of 80 mm,
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the phosphatrane cation has the following structure
  • E 1 is selected from the group consisting of N, O, S, P, As, and Se
  • E 2 is selected from the group consisting of N, O, S, P, As, and Se
  • E 3 is selected from the group consisting of N, O, S, P, As, and Se
  • R 1 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • R 2 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • R 3 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • D is selected from the group consisting of N, P, C, As, and Si
  • X is selected from the group consisting of H, C 1 -C 18 , P, Si, N and any combination thereof.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the E 1 is selected from the group consisting of N, O, and P, and E 2 is selected from the group consisting of N, O, and P; and E 3 is selected from the group consisting of N, O, and P; and R 1 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and R 2 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and R 3 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and D is selected from the group consisting of N, and P; and X is selected from the group consisting of H, C 1 -C 18 , and any combination thereof.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the E 1 is N, and E 2 is N; and E 3 is N; and R 1 is selected from the group consisting of C 1 -C 18 , and any combination thereof; and R 2 is selected from the group consisting of C 1 -C 18 , and any combination thereof; and R 3 is selected from the group consisting of C 1 -C 18 , and any combination thereof; and D is N; and X is H.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the E 1 , E 2 , E 3 , and D are not all N at the same time.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the phosphatrane cation is azaphosphatrane cation.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the isocyanate-trimer inducing anion is selected from the group consisting of carboxylate, carbonate, phenoxide, amide, amidinate, imides, phosphidos, thiocyanate, thioisocyanate, isocyanate, cyanate, and fluoride.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the isocyanate-trimer inducing anion is selected from the group consisting of carboxylate, carbonate, phenoxide, and fluoride.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the isocyanate-trimer inducing anion is carboxylate.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the carboxylate has the following structure
  • X′ is selected from the group consisting of H, C 1 -C 18 , aliphatic, aromatic, cyclic, acyclic, acyl, and derivatives thereof.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the carboxylate is selected from the group consisting of formate, acetate, octanoate, 2-ethylhexanoate, benzoate, and substituted derivatives thereof.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the isocyanate-trimer inducing anion is acetate.
  • the present invention provides an isocyanate trimerisation catalyst, a precursor formulation, a process for trimerising isocyanates, foams made therefrom, and a process for making such foams, in accordance with any of the preceding embodiments, except that the trimerisation catalyst system is 2,8,9-trimethyl-2,5,8,9-tetraaza-1-phosphabicyclo[3.3.3]undecane monoacetate.
  • the present invention provides PIR foams, and a process for making such foams, in accordance with any of the preceding embodiments, except that the foam is used as thermal insulation such as construction thermal insulation foams or appliance thermal insulation foams.
  • FIG. 1 is an illustrative graph showing the trimer content of one exemplary inventive foam versus a comparative foam.
  • the instant invention provides an isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, PIR foams made therefrom, and a process for making such foams.
  • the isocyanate trimerisation catalyst system comprises: (a) a phosphatrane cation; and (b) an isocyanate-trimer inducing anion.
  • the isocyanate trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C. All individual values and subranges from less than 73° C. are included herein and disclosed herein; for example, the activation temperature can be from a lower limit of 25, 35, 45, or 55° C. to an upper limit of 45, 55, 65, 70 or 73° C.
  • the isocyanate trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 70° C., or equal to or less than 68° C., or equal to or less than 66° C., or equal to or less than 65° C.
  • the isocyanate trimerisation catalyst system is free of any polymeric support.
  • the phosphatrane cation component of the isocyanate trimerisation catalyst system has the following structure
  • E 1 is selected from the group consisting of N, O, S, P, As, and Se
  • E 2 is selected from the group consisting of N, O, S, P, As, and Se
  • E 3 is selected from the group consisting of N, O, S, P, As, and Se
  • R 1 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • R 2 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • R 3 is selected from the group consisting of H, C 1 -C 18 , P, Si, and any combination thereof
  • D is selected from the group consisting of N, P, C, As, and Si
  • X is selected from the group consisting of H, C 1 -C 18 , P, Si, N and any combination thereof.
  • E 1 is selected from the group consisting of N, O, and P; and E 2 is selected from the group consisting of N, O, and P; and E 3 is selected from the group consisting of N, O, and P; and R 1 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and R 2 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and R 3 is selected from the group consisting of H, C 1 -C 18 , Si, and any combination thereof; and D is selected from the group consisting of N, and P; and X is selected from the group consisting of H, C 1 -C 18 , and any combination thereof. In one embodiment, however, E 1 , E 2 , E 3 , and D are not all N at the same time.
  • the phosphatrane cation may, for example, be azaphosphatrane cation.
  • the isocyanate-trimer inducing anion refers to an anion, which facilitates the trimerisation of isocyanates in the presence of one or more phosphatrane cations.
  • the isocyanate-trimer inducing anion is, for example, an anion selected from the group consisting of carboxylate, carbonate, phenoxide, amide, amidinate, imides, phosphidos, thiocyanate, thioisocyanate, isocyanate, cyanate, and fluoride.
  • the isocyanate-trimer inducing anion is selected from the group consisting of carboxylate, carbonate, phenoxide, and fluoride.
  • the isocyanate-trimer inducing anion is carboxylate.
  • the carboxylate may, for example, have the following structure:
  • X′ is selected from the group consisting of H, C 1 -C 18 , aliphatic, aromatic, cyclic, acyclic, acyl, and derivatives thereof.
  • the carboxylate may, for example, be selected from the group consisting of formate, acetate, octanoate, 2-ethylhexanoate, benzoate, and substituted derivatives thereof.
  • the isocyanate-trimer inducing anion is acetate.
  • the trimerisation catalyst system is 2,8,9-trimethyl-2,5,8,9-tetraaza-1-phosphabicyclo[3.3.3]undecane monoacetate.
  • the precursor formulation according to the instant invention comprises (a) one or more polyols; (b) the inventive trimerisation catalyst system, as described hereinabove; and (c) optionally one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts, or combinations thereof.
  • the precursor formulation comprises at least 25 percent by weight of one or more polyols, as described hereinbelow, based on the weight of the precursor formulation.
  • the weight percent of one or more polyols can be from a lower limit of 25, 30, 35, 40 or 45 weight percent (W percent) to an upper limit of 45, 50, 55, 65, 75, 85, 90, 95, or 98 W percent.
  • the precursor formulation comprises 25 to 98; or 30 to 98; or 35 to 98; or 45 to 95 percent by weight of one or more polyols, based on the weight of the precursor formulation.
  • the precursor formulation comprises less than or equal to 15 percent by weight of the inventive trimerisation catalyst system, as described hereinabove, based on the weight of the precursor formulation.
  • the weight percent of the trimerisation catalyst system can be from a lower limit of 0.1, 1, 2, 4, 5, 7, or 10 W percent to an upper limit of 10, 12, 14, or 15 W percent.
  • the precursor formulation comprises 2 to 15; or 4 to 15; or 5 to 15 or 7 to 15; or 10 to 15 percent by weight of the inventive trimerisation catalyst system, based on the weight of the precursor formulation.
  • the inventive trimerisation catalyst system may, for example, be employed to trimerise one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof to form one or more isocyanurate rings.
  • the inventive trimerisation catalyst system may further be employed to form a PIR foam.
  • the process for forming a PR foam may generally include the following steps: (1) providing one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof; (2) providing polyol; (3) providing a trimerisation catalyst system comprising; (a) a phosphatrane cation; and (b) an isocyanate-trimer inducing anion; wherein said trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73° C.; and (4) optionally providing one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts, or combinations thereof; (5) contacting the one or more
  • PIR foams according to the instant invention may, preferably, be produced by employing the trimerisation catalyst system, as described above, in combination with conventional urethane catalysts in the urethane formulation.
  • isocyanate refers to any compound including polymers that contain at least one isocyanate group such as monoisocyanates and organic polyisocyanates.
  • organic polyisocyanates suitably employed include, but are not limited to, for example, the aromatic diisocyanates, such as 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, mixtures of 2,4- and 2,6-toluene diisocyanate, crude toluene diisocyanate, methylene diphenyl diisocyanate, crude methylene diphenyl diisocyanate and the like; aromatic triisocyanates such as tris-(4-isocyanatophenyl)methane; 2,4,6-toluene tris(isocyanates); the aromatic tetra(isocyanates), such as 4,4′-dimethyldiphenylmethane-2,2′,5′,5′-tetra(is
  • organic polyisocyanates include polymethylene polyphenyl isocyanate, hydrogenated methylene diphenylisocyanate, m-phenylene diisocyanate, naphthylene-1,5-diisocyanate, 1-methoxyphenyl-2,4-diisocyanate, diphenylmethane-4,4′-biphenylene diisocyanate, 3,3′-dimethoxy-4,4′-biphenyl diisocyanate, 3,3′-dimethyl-4,4′-biphenyl diisocyanate, 3,3′-dimethyldiphenylmethane-4,4′-diisocyanate, isophorone diisocyanate, 1,3-bis-(isocyanatomethyl)benzene, cumene-2,4-diisocyanate, 4-methoxy-1,3-phenylene diisocyanate, 4-chloro-1,3-phenylene diisocyanate, 4-bromo
  • polyisocyanates of higher functionality such as dimers and particularly NCO-terminated oligomers of isocyanates containing isocyanate rings as well as prepolymers and mixtures of the aforementioned isocyanates.
  • polyisocyanates of higher functionality such as dimers and particularly NCO-terminated oligomers of isocyanates containing isocyanate rings as well as prepolymers and mixtures of the aforementioned isocyanates.
  • quasi-prepolymers of such isocyanates prepared by reacting an excess of isocyanate with an active hydrogen compound such as a polyol, preferably those made by reacting at least 2 moles of isocyanate group with one mole of active hydrogen-containing compound.
  • active hydrogen compound such as a polyol
  • These polyisocyanates are prepared by conventional methods known in the art such as phosgenation of the corresponding organic amine.
  • aromatic polyisocyanates for production of the PIR foam include, but are not limited to, the diphenylmethane diisocyanates (MDI) in the form of its 2,4′-, 2,2′-, and 4,4′-isomers and mixtures thereof and/or mixtures of MDI oligomers known as polymeric MDI.
  • MDI diphenylmethane diisocyanates
  • polymeric MDI polymeric MDI products, which are a mixture of polymethylene polyphenylene polyisocyanates in monomeric MDI.
  • the amount of monoisocyonate is generally less than 10 weight percent of total isocyanate; less than 7 weight percent of total isocyanate, less than 5 weight percent of total isocyanate, less 2 weight percent of total isocyanate, or none.
  • Active hydrogen compounds suitably reacted with the isocyanate in the practice of this invention include any compounds including polymers containing at least one active hydrogen moiety.
  • an active hydrogen moiety refers to a moiety containing a hydrogen atom which, because of its position in the molecule, displays significant activity according to the Zerewitnoff test described by Kohler in the Journal of American Chemical Society, Vol. 49, page 3181 (1927).
  • Illustrative of such active hydrogen moieties are —COOH, —OH, —NH 2 , —CONH 2 , —SH and —CONH—.
  • Polyol(s) or polyol blends suitable for producing PIR foams of the instant invention may, for example, have a number average functionality in the range of 2 to 8, or in the alternative in the range of 3 to 8, and a hydroxyl equivalent weight of 60 to 560, or in the alternative in the range of 90 to 400.
  • Typical active hydrogen compounds include monols and polyols, amines including polyamines, amides including polyamides, mercaptans including polymercaptans, acids including polyacids and the like.
  • suitable hydroxyl compounds are the following (including mixtures thereof): monohydric alcohols such as ethanol, propanol and butanol as well as monohydric phenols such as phenol.
  • polyols such as polyether polyols, the polyester polyols, homopolymers and copolymers of hydroxyalkyl acrylates and methacrylates, polyepoxide resins, phenol-formaldehyde resins, polyhydroxy terminated polyurethane polymers, polyhydroxyl-containing phosphorus compounds and alkylene oxide adducts of polyhydric thioethers, acetals including polyacetals, aliphatic and aromatic polyols and thiols including polythioethers, ammonium and amines including aromatic, aliphatic and heterocyclic amines including polyamines as well as mixtures thereof.
  • polyether polyols such as polyether polyols, the polyester polyols, homopolymers and copolymers of hydroxyalkyl acrylates and methacrylates, polyepoxide resins, phenol-formaldehyde resins, polyhydroxy terminated polyurethane polymers, polyhydroxyl-containing
  • Alkylene oxide adducts of compounds which contain two or more different groups within the above-defined classes may also be used such as amino alcohols which contain an amino group and a hydroxyl group.
  • alkylene adducts of compounds which contain one —SH group and one —OH group as well as those which contain an amino group and a —SH group may be used.
  • Exemplary polyether polyols, employed as the polyol in the practice of this invention, include polyalkylene polyether polyols, for example, diols such as ethylene glycol, propylene glycol, butylene glycol, and diethylene glycol.
  • Exemplary alcohols that are advantageously employed as initiators in making the polyether polyol include, but are not limited to, methanol, ethanol, ethylene glycol, 1,3-propylene glycol, 1,2-propylene glycol, 1,4-butylene glycol, 1,3-butylene glycol, 1,2-butylene glycol, 1,5-pentane diol, 1,7-heptane diol, glycerol, 1,1,1-trimethylolpropane, 1,1,1-trimethylolethane, hexane-1,2,6-triol, ⁇ -methyl glucoside, pentaerythritol, and sorbitol.
  • alcohol compounds derived from phenol such as 2,2-(4,4′-hydroxyphenyl)propane, commonly known as bisphenol A; sugars such as sucrose, glucose, fructose and the like.
  • alkylene oxides that are advantageously employed in the preparation of the polyether polyol include ethylene oxide, propylene oxide, butylene oxide, amylene oxide and random or block copolymers of two or more of these oxides; glycidol; glycidyl ethers or thioethers such as methyl glycidyl ethers, t-butyl glycidyl ether and phenyl glycidyl ether.
  • the polyester polyols are reaction products of polycarboxylic acids and alcohols particularly polyhydric alcohols.
  • suitable polycarboxylic acids include oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, brassylic acid, thapsic acid, maleic acid, fumaric acid, glutaconic acid, ⁇ -hydromuconic acid, ⁇ -hydromuconic acid, ⁇ -butyl- ⁇ -ethyl-glutaric acid, ⁇ , ⁇ -diethylsuccinic acid, isophthalic acid, terephthalic acid, hemimellitic acid and 1,4-cyclohexane-dicarboxylic acid.
  • Any suitable alcohol including both aliphatic and aromatic may be used.
  • suitable alcohols are those polyhydric alcohols described hereinbefore.
  • polyhydric alcohol compounds derived from phenol such as 2,2-(4,4′-hydroxyphenyl)propane, commonly known as bisphenol A; polyacetone polyols and the like.
  • polystyrene resins such as urea-formaldehyde and melamineformaldehyde
  • lactone polyols prepared by reacting a lactone such as ⁇ -caprolactone or a mixture of ⁇ -caprolactone and an alkylene oxide with a polyfunctional initiator such as a polyhydric alcohol, an amine or an amino alcohol.
  • the polyalkylene ether diols may be ethylene glycol, diethylene glycol, triethylene glycol, ethoxylated glycerin, polyether diols of ethylene oxide and/or propylene oxide.
  • the particular isocyanate and active hydrogen compound as well as quantities thereof to be employed in the practice of this invention depend upon the particular end use application desired. Such choices are within the skill of the art to which such end use is directed.
  • ingredients of the FIR foam formulation include surfactants, blowing agents, fillers, dyes, pigments, cross-linking agents, chain extenders, flame retarding agents and smoke suppressing agents.
  • the trimerisation catalyst system according to the instant invention is useful in the formation of foam products for rigid and flame retardant applications, which usually require a high Isocyanate Index.
  • Isocyanate Index refers to the actual amount of polyisocyanate used divided by the theoretically required stoichiometric amount of polyisocyanate required to react with all the active hydrogen in the reaction mixture, multiplied by 100.
  • Foam products which are produced with an Isocyanate Index from 80 to 800 are within the scope of this invention.
  • the Isocyanate Index is from 100 to 700, from 150 to 650, from 150 to 600, or from 180 to 500.
  • Blowing agents include, but are not limited to, isobutene, dimethyl ether, water, methylene chloride, acetone, chlorofluorocarbons (CFCs), hydrofluorocarbons (HFCs), hydrochlorofluorocarbons (HCFCs), and hydrocarbons.
  • HFCs include HFC-245fa, HFC-134a, HFC-152a, HFC-227ea, and HFC-365.
  • Illustrative examples of HCFCs include HCFC-141b, HCFC-22, and HCFC-123.
  • Exemplary hydrocarbons include n-pentane, isopentane, cyclopentane, and the like, or any combination thereof.
  • the amount of blowing agent used can vary based on, for example, the intended use and application of the foam product and the desired foam stiffness and density.
  • the blowing agent is present in amounts from 1 to 80 parts by weight per hundred weight parts polyol (pphp), from 5 to 60 pphp, from 7 to 60 pphp, from 10 to 60 pphp, from 12 to 60 pphp, from 14 to 40 pphp, or from 16 to 25 pphp.
  • water is present in the formulation, for use as a blowing agent or otherwise, water is present in amounts up to 15 pphp. In other words, water can range from 0 to 15 pphp. In another aspect, water can range from 0 to 10 pphp, from 0.1 to 10 pphp, from 0 to 8 pphp, from 0 to 6 pphp, from 0.3 to 5, or from 0.4 to 4 pphp.
  • Urethane catalysts accelerate the reaction to form polyurethanes, in the process of making PR foams.
  • Urethane catalysts suitable for use herein include, but are not limited to, metal salt catalysts, such as organotins, and amine compounds, such as triethylenediamine (TEDA), N-methylimidazole, 1,2-dimethylimidazole, N-methylmorpholine, N-ethylmorpholine, triethylamine, N,N′-dimethylpiperazine, 1,3,5-tris(dimethylaminopropyl)hexahydrotriazine, 2,4,6-tris(dimethylaminomethyl)phenol, N-methyldicyclohexylamine, pentamethyldipropylene triamine, N-methyl-N′-(2-dimethylamino)-ethyl-piperazine, tributylamine, pentamethyldiethylenetriamine, hexamethyltriethylenetetramine,
  • the urethane catalyst can be present in the formulation from 0 to 15 pphp, from 0 to 10 pphp, from 0 to 8 pphp, from 0 to 6 pphp, from 0 to 4 pphp, from 0 to 2 pphp, or from 0 to 1 pphp.
  • the urethane catalyst is present from 0 to 0.8 pphp, from 0 to 0.6 pphp, from 0 to 0.4 pphp, or from 0 to 0.2 pphp.
  • an optional auxiliary trimerisation catalyst can be present in the formulation from 0 to 15 pphp, from 0 to 10 pphp, from 0 to 8 pphp, from 0 to 6 pphp, from 0 to 4 pphp, from 0 to 2 pphp, or from 0 to 1 pphp.
  • the urethane catalyst is present from 0 to 0.8 pphp, from 0 to 0.6 pphp, from 0 to 0.4 pphp, or from 0 to 0.2 pphp.
  • various additives can be employed in the PIR foam formulation to tailor specific properties. These include, but are not limited to, cell stabilizers, flame retardants, chain extenders, epoxy resins, acrylic resins, fillers, pigments, or any combination thereof. It is understood that other mixtures or materials that are known in the art can be included in the foam formulations and are within the scope of the present invention.
  • Cell stabilizers include surfactants such as organopolysiloxanes.
  • Surfactants can be present in the PR foam formulation in amounts from 0.5 to 10 pphp, 0.6 to 9 pphp, 0.7 to 8 pphp, 0.8 to 7 pphp, 0.9 to 6 pphp, 1 to 5 pphp, or 1.1 to 4 pphp.
  • Useful flame retardants include halogenated organophosphorous compounds and non-halogenated compounds. For example, trichloropropylphosphate (TCPP) is a halogenated flame retardant, and triethylphosphate ester (TEP) is a non-halogenated flame retardant.
  • TCPP trichloropropylphosphate
  • TEP triethylphosphate ester
  • flame retardants can be present in the foam formulation in amounts from 0 to 50 pphp, from 0 to 40 pphp, from 0 to 30 pphp, or from 0 to 20 pphp. In another aspect, the flame retardant is present from 0 to 15 pphp, 0 to 10 pphp, 0 to 7 pphp, or 0 to 5 pphp. Chain extenders such as ethylene glycol and butane diol can also be employed in the present invention.
  • the present invention further provides a method for preparing a PIR foam which comprises contacting at least one polyisocyanate with at least one active hydrogen-containing compound, in the presence of an effective amount of the inventive trimerisation catalyst system.
  • the trimerisation catalyst system should be present in the foam formulation in a catalytically effective amount.
  • the trimerisation catalyst system is present in amounts from 0.05 to 15 parts by weight per hundred weight parts of the at least one active hydrogen-containing compound, including the weight contribution of the catalyst system diluent, for example, diethylene glycol.
  • the trimerisation catalyst system is present in amounts from 0.4 to 10 parts, or from 0.4 to 9 parts, or from 0.8 to 8 parts, by weight per hundred weight parts of the at least one active hydrogen-containing compound.
  • the at least one active hydrogen-containing compound is an at least one polyol
  • the trimerisation catalyst system is present in amounts from 0.05 to 15 parts by weight per hundred weight parts polyol (pphp).
  • the catalyst composition is present in amounts from 0.2 to 10 pphp; from 0.2 to 9.5 pphp, from 0.4 to 9 pphp, from 0.6 to 8.5 pphp, or from 0.8 to 8 pphp.
  • the method of producing PIR foams can further comprise the presence of at least one additive selected from at least one cell stabilizer, at least one flame retardant, at least one chain extender, at least one epoxy resin, at least one acrylic resin, at least one filler, at least one pigment, or any combination thereof.
  • a premix of ingredients other than the at least one polyisocyanate can be contacted first, followed by the addition of the at least one polyisocyanate.
  • the at least one active hydrogen-containing compound, the at least one blowing agent, and the inventive trimerisation catalyst system are contacted initially to form a premix.
  • the premix is then contacted with the at least one polyisocyanate to produce PIR foams in accordance with the method of the present invention.
  • the same method can be employed, wherein the premix further comprises at least one urethane catalyst.
  • the premix can further comprise at least one additive selected from at least one cell stabilizer, at least one flame retardant, at least one chain extender, at least one epoxy resin, at least one acrylic resin, at least one filler, at least one pigment, or any combination thereof.
  • One aspect of the present invention provides a method for preparing a PIR foam comprising (a) forming a premix comprising: (i) at least one active hydrogen-containing polyol; (ii) 10 to 80 parts by weight per hundred weight parts of the polyol (pphp) blowing agent; (iii) 0.5 to 10 pphp surfactant; (iv) zero to 10 pphp water; (v) zero to 50 pphp flame retardant; (vi) zero to 10 pphp urethane catalyst; and (vii) 0.05 to 15 pphp of the inventive trimerisation catalyst system; and (b) contacting the premix with at least one polyisocyanate at an Isocyanate Index from 80 to 800.
  • the PIR foams of the instant invention may be used as thermal insulation such as construction thermal insulation foams or appliance thermal insulation foams.
  • the above described components required for making a PIR foam are sprayed together and mixed at the departure point from the spray nozzle to form a thermal insulation foam on a wall.
  • TCS trimerisation catalyst systems
  • Comparative sample 1-3 are prepared according to the same method as inventive samples 1-5, described above.
  • the catalyst activation temperature of each comparative sample is measured via DSC method as described below.
  • the trimmer formation is confirmed via IR. The results are shown in Table 1.
  • Inventive foams are produced via a Cannon HP-60 and a Hi Tech Eco-RIM high pressure machine. Total machine through put was from ⁇ 200 to 225 g/second. Foam samples were generated using molds preheated to 51.7° C., while chemical temperature varied between 21 and 27° C. for the following formulation: a premix of the polyol (aromatic polyester polyol, 100 phpp), the trimerisation catalyst system (less than 6 phpp); flame retardant (TCPP, 4.7 phpp), surfactant (1.7 phpp), urethane catalyst (PolycatTM 5 catalyst, 0.15 phpp), blowing agent (n-pentane, 17 phpp), and water.
  • a premix of the polyol aromatic polyester polyol, 100 phpp
  • the trimerisation catalyst system less than 6 phpp
  • flame retardant TCPP, 4.7 phpp
  • surfactant 1.7 phpp
  • urethane catalyst PolycatTM 5 catalyst, 0.15 phpp
  • Comparative foams are produced via a Cannon HP-60 and a Hi Tech Eco-RIM high pressure machine. Total machine through put was from ⁇ 200 to 225 g/second. Foam samples were generated using molds preheated to 51.7° C., while chemical temperature varied between 21 and 27° C. for the following formulation: a premix of the polyol (aromatic polyester polyol, 100 phpp), DABCO TMR-2 catalyst (less than 6 phpp); flame retardant (TCPP, 4.7 phpp), surfactant (1.7 phpp), urethane catalyst (PolycatTM 5 catalyst, 0.15 phpp), blowing agent (n-pentane, 17 phpp), and water.
  • a premix of the polyol aromatic polyester polyol, 100 phpp
  • DABCO TMR-2 catalyst less than 6 phpp
  • flame retardant TCPP, 4.7 phpp
  • surfactant 1.7 phpp
  • urethane catalyst PolycatTM 5 catalyst, 0.15 phpp
  • the trimer content comparative foam 1 is measured via ATR-FTIR spectroscopy, and the results are shown in FIG. 1 .
  • Test methods include the following:
  • DSC Differential Scanning Calorimetry
  • the isocyanate index of the “formulations” may range between 1000 and 3500. At a 1000 index formulation, 90 percent of the initial isocyanate is available solely for the trimerisation reaction with the remaining 10 percent being available to react with the hydroxyl groups of the catalyst solvent. It is assumed that at these levels, the major exotherm would be that of the trimerisation reaction.
  • a 1′′ ⁇ 1′′ ⁇ 3′′ sample spanning the panel thickness is collected in the center of each rigid foam panel. Each sample is subsequently sectioned along the 3′′ thickness into 5 mm thick slices, except for the very outer edges (that is, the skin) which are cut to 2-3 mm thickness.
  • ATR-FTIR measurements are performed on a Nicolet Magna FTIR instrument equipped with a Durascope 1 Bounce ATR diamond crystal accessory. Typically, 16 scans are acquired in the 4000-600 cm ⁇ 1 spectral range; the resolution is 4 cm ⁇ 1 , the velocity 0.6329, and the aperture 138.
  • FTIR spectra are acquired at each depth on 6 different locations (3 on each facing section at a given depth) except for the outer faces, which are measured on 4 locations each.
  • ATR-FTIR spectrum of a rigid PIR foam is shown below.
  • the 1410 cm ⁇ 1 peak is specific to the trimer 6-membered ring, while vibration modes of the various carbonyls found in urethanes, urea, trimers, and ester moieties all appear as a single peak around 1700 cm ⁇ 1 .
  • the small peak at 2275 cm ⁇ 1 corresponds to free, unreacted isocyanate groups, while the aromatic peak at 1595 cm ⁇ 1 is generally used as an internal reference to normalize the data.
  • the NCO peak height ( ⁇ 2275 cm ⁇ 1 ) normalized by the aromatic peak height ( ⁇ 1595 cm ⁇ 1 ) typically indicates the amount of unreacted isocyanate groups in the foam
  • the trimer peak height ( ⁇ 1410 cm ⁇ 1 ) again normalized by the aromatic peak height typically indicates the amount of isocyanurate trimer species in the foam panel.
  • a sample is collected, sliced, and FTIR spectra are acquired according to the method described above.
  • the peak ratios at a given depth are averaged and the standard deviation represents the spread of the peak ratio values over various locations at a given depth in the sample.

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US20170184963A1 (en) * 2015-12-28 2017-06-29 Shin-Etsu Chemical Co., Ltd. Resist composition and patterning process
US20180134835A1 (en) * 2015-04-21 2018-05-17 Covestro Deutschland Ag Polyisocyanurate polymer and process for the production of polyisocyanurate polymers
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JP7221580B2 (ja) * 2015-08-27 2023-02-14 積水化学工業株式会社 発泡性ポリウレタン組成物及びポリウレタン発泡体
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US20110201709A1 (en) * 2008-11-10 2011-08-18 Dow Global Technologies Llc Isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid polyisocyanurate/polyurethane foams made therefrom, and a process for making such foams
US20110201706A1 (en) * 2008-11-10 2011-08-18 Dow Global Technologies Llc Isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid polyisocyanurate/polyurethane foams made therefrom, and a process for making such foams

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US9988504B2 (en) 2014-03-28 2018-06-05 Huntsman International Llc Reinforced organic natural fiber composites
WO2015150408A1 (fr) 2014-04-03 2015-10-08 Huntsman International Llc Catalyseur de trimérisation d'isocyanate pour réaliser des mousses comprenant du polyisocyanurate
US11548973B2 (en) 2014-04-03 2023-01-10 Huntsman International Llc Isocyanate trimerization catalyst for making polyisocyanurate comprising foams
US20180134835A1 (en) * 2015-04-21 2018-05-17 Covestro Deutschland Ag Polyisocyanurate polymer and process for the production of polyisocyanurate polymers
US10752723B2 (en) * 2015-04-21 2020-08-25 Covestro Deutschland Ag Polyisocyanurate polymer and process for the production of polyisocyanurate polymers
US11390707B2 (en) 2015-04-21 2022-07-19 Covestro Deutschland Ag Polyisocyanurate polymers and process for the production of polyisocyanurate polymers
US20170184963A1 (en) * 2015-12-28 2017-06-29 Shin-Etsu Chemical Co., Ltd. Resist composition and patterning process
US9897914B2 (en) * 2015-12-28 2018-02-20 Shin-Etsu Chemical Co., Ltd. Resist composition and patterning process

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WO2010054315A2 (fr) 2010-05-14
EP2346918B1 (fr) 2013-09-18
EP2346918A2 (fr) 2011-07-27
US10294322B2 (en) 2019-05-21
WO2010054315A3 (fr) 2010-12-02
CN102272182A (zh) 2011-12-07
US20170283541A1 (en) 2017-10-05
JP2012508302A (ja) 2012-04-05
CN102272182B (zh) 2014-02-12
ES2437604T3 (es) 2014-01-13

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