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US4386166A Expired / Lapsed US ⏱️ 0.0 years remaining

Foam prepared from an unsaturated polyester resin copolymerization monomer, low molecular weight polyol, and isocyanate

Assignee: BP Corp North America Inc
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Filing: 1981-05-07
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Granted: 1983-05-31
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Expires: 2001-05-07
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Abstract

Abstract A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing on a weight basis a polyol composition A comprising unsaturated polyester resin dissolved in a copolymerizable monomer containing 30-80% nonvolatile matter on a weight basis, at least one urethane reaction catalyst, at least one polyisocyanate trimerization catalyst, at least one organic compound functional as a peroxide decomposition catalysty, at least one low molecular weight polyol, and at least one silicone surface active agent, and an isocyanate composition B comprising a polyisocyanate, at least one organic peroxide functional as an unsaturated polyester resin curing catalyst, and a urethane reaction catalyst, at least one of compositions A and B containing a blowing agent, and allowing said mixture to cream and foam as a result of the heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyols and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the copolymerizable monomer. The products of the invention are especially suitable as foam board useful in building insulation.

Inventors

  • 👤 Gregory P. Peterson
  • 👤 Alan D. Hamilton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 23:53
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/67; C08G18/68; C08G18/08; C08G18/09; C08G18/092; C08G2110/00; C08G2110/0025; C08G2110/0041; Y; Y10; Y10T; Y10T428/00; Y10T428/31504; Y10T428/31547

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 181 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing on a weight basis a polyol composition A comprising unsaturated polyester resin dissolved in a copolymerizable monomer containing 30-80% non-volatile matter on a weight basis, at least one urethane reaction catalyst, at least one polyisocyanate trimerization catalyst, at least one organic compound functional as a peroxide decomposition catalyst, at least one low molecular weight polyol, and at least one silicone surface active agent, and an isocyanate composition B comprising a polyisocyanate, at least one organic peroxide functional as an unsaturated polyester resin curing catalyst, and a urethane reaction catalyst, at least one of compositions A and B containing a blowing agent, and allowing said mixture to cream and foam as a result of the heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyols and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the copolymerizable monomer.
Claim 2
Dependent Claim 181 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing on a weight basis a polyol composition A comprising unsaturated polyester resin dissolved in a copolymerizable monomer containing 30-80% non-volatile matter on a weight basis, at least one urethane reaction catalyst, at least one polyisocyanate trimerization catalyst, at least one organic compound functional as a peroxide decomposition catalyst, at least one low molecular weight polyol, and at least one silicone surface active agent, and an isocyanate composition B comprising a polyisocyanate, at least one organic peroxide functional as an unsaturated polyester resin curing catalyst, and a urethane reaction catalyst, at least one of compositions A and B containing a blowing agent, and allowing said mixture to cream and foam as a result of the heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyols and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the copolymerizable monomer.
Claim 3
Dependent Claim 15 words
The process of claim 1 wherein said blowing agent comprises a portion of Composition A.
Claim 4
Dependent Claim 14 words
The process of claim 2 wherein said blowing agent comprises at least one halohydrocarbon.
Claim 5
Dependent Claim 19 words
The process of claim 1 wherein said foam is a sheet having a thickness 0.25 to 4 inches thick.
Claim 6
Dependent Claim 19 words
The process of claim 4 wherein a facing material is applied to upper and lower surfaces of said foam.
Claim 7
Dependent Claim 41 words
The process of claim 1 wherein an inorganic filler is incorporated in Composition A in an amount of 80 to 150 parts by weight based on one hundred parts by weight of the unsaturated polyester/unsaturated monomer mixture in the Composition A.
Claim 8
Dependent Claim 10 words
A foam product produced by the process of claim 1.
Claim 9
Dependent Claim 185 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing, on a weight basis, 0.2 to 4.4 parts of polyol composition A comprising ______________________________________ unsaturated polyester resin dissolved in styrene containing 30 to 80% non- volatile matter on a weight basis, 100 organic cobalt salt solution (12% cobalt) 0.1 to 1.5 organic potassium salt solution (15% K) 0.005 to 8 triethylene diamine 0-5 N,N',N"--tris(dimethylaminopropyl)- symhexahydrotriazine 0-5 ethylene glycol 1.7-25 diethylene glycol 1.7-25 glycerol 1.7-25 O,O--diethyl-N,N--bis (2-hydroxyethyl) amino-methyl phosphonate 0-40 hydrated alummina 0-150 trichlorofluoromethane 20-50 silicone-glycol copolymer 0.5-4 and one part of an isocyanate composition B comprising polymethylene polyphenylisocyanate having a functionality of 1 to 4 110 2,5-dimethyl-2,5-bis (2-ethylhex- anoylperoxy) hexane 0.2-4 dimethyl tin dimercaptide 0.1-1 ______________________________________ and allowing said mixture to cream and foam as a result of the heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyols and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the styrene.
Claim 10
Dependent Claim 185 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing, on a weight basis, 0.2 to 4.4 parts of polyol composition A comprising ______________________________________ unsaturated polyester resin dissolved in styrene containing 30 to 80% non- volatile matter on a weight basis, 100 organic cobalt salt solution (12% cobalt) 0.1 to 1.5 organic potassium salt solution (15% K) 0.005 to 8 triethylene diamine 0-5 N,N',N"--tris(dimethylaminopropyl)- symhexahydrotriazine 0-5 ethylene glycol 1.7-25 diethylene glycol 1.7-25 glycerol 1.7-25 O,O--diethyl-N,N--bis (2-hydroxyethyl) amino-methyl phosphonate 0-40 hydrated alummina 0-150 trichlorofluoromethane 20-50 silicone-glycol copolymer 0.5-4 and one part of an isocyanate composition B comprising polymethylene polyphenylisocyanate having a functionality of 1 to 4 110 2,5-dimethyl-2,5-bis (2-ethylhex- anoylperoxy) hexane 0.2-4 dimethyl tin dimercaptide 0.1-1 ______________________________________ and allowing said mixture to cream and foam as a result of the heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyols and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the styrene.
Claim 11
Dependent Claim 10 words
A foam product produced by the process of claim 8.
Claim 12
Dependent Claim 157 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing unsaturated polyester resin dissolved in a copolymerizable monomer containing 30-80% non-volatile matter on a weight basis, at least one urethane reaction catalyst, at least one polyisocyanate trimerization catalyst, at least one organic compound functional as a peroxide decomposition catalyst, at least one low molecular weight polyol, at least one silicone surface active agent, a polyisocyanate, at least one organic peroxide functional as an unsaturated polyester resin curing catalyst, at least one urethane reaction catalyst, and a blowing agent, and allowing said mixture to cream and foam as a result of heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyol and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the copolymerizable monomer.
Claim 13
Dependent Claim 157 words
A process of producing a modified polyester foam having a density of 0.5 to 40 pounds per cubic foot comprising mixing unsaturated polyester resin dissolved in a copolymerizable monomer containing 30-80% non-volatile matter on a weight basis, at least one urethane reaction catalyst, at least one polyisocyanate trimerization catalyst, at least one organic compound functional as a peroxide decomposition catalyst, at least one low molecular weight polyol, at least one silicone surface active agent, a polyisocyanate, at least one organic peroxide functional as an unsaturated polyester resin curing catalyst, at least one urethane reaction catalyst, and a blowing agent, and allowing said mixture to cream and foam as a result of heat generated by the trimerization of the polyisocyanate and the urethane reaction between isocyanate groups and hydroxyl groups in the polyol and unsaturated polyester, said heat being sufficient to cause gas generation from the blowing agent and cross-linking of the unsaturated polyester with the copolymerizable monomer.

References Cited (Backward Citations)

US3886229A Cited
US3860537A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-05-30 1986-11-29 1987-05-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-05-30 1990-11-29 1991-05-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-05-30 1994-11-29 1995-05-31 $7700.00 Window Closed / Lapsed

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