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US4323658A Expired / Lapsed US ⏱️ 0.0 years remaining

Polyisocyanurates from diols modified with epoxy resins

Assignee: Dow Chemical Co
•
Filing: 1980-09-02
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Granted: 1982-04-06
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Expires: 2000-09-02
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Abstract

Abstract A method of preparing polyether polyols in the 200-1000 molecular weight range by modifying a polyol initiator with an epoxy resin and one or more alkylene oxides is described. The modified polyols may be used in preparing rigid isocyanurate foams with improved compressability and flammability properties.

Inventors

  • 👤 George P. Speranza
  • 👤 Robert L. Zimmerman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 15:33
CPC Classifications
C; C08; C08G; C08G59/00; C08G59/14; C08G59/1433; C08G59/1438; C08G59/145; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/48; C08G18/4895; C08G65/00; C08G65/02; C08G65/26; C08G2115/00; C08G2115/02; Y; Y10; Y10S; Y10S521/00; Y10S521/902; Y10S521/914

Claims Analysis

Total Claims: 28
Claim 1
Independent Claim 66 words
A modified polyether polyol being produced by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 2
Dependent Claim 66 words
A modified polyether polyol being produced by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 3
Dependent Claim 27 words
The modified polyether polyol as described in claim 1 in which the resulting modified polyol has a molecular weight in the range of about 200 to 1,000.
Claim 4
Dependent Claim 37 words
The modified polyether polyol as described in claim 1 in which the epoxy resin is selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins, and aliphatic epoxy resins.
Claim 5
Dependent Claim 28 words
The modified polyether polyol as described in claim 1 in which the alkylene oxides are taken from the group consisting of ethylene oxide, propylene oxide and butylene oxide.
Claim 6
Dependent Claim 34 words
The modified polyether polyol as described in claim 1 in which the components are reacted in the pressure range between about 20 psi and about 60 psi during the preparation of the modified polyol.
Claim 7
Dependent Claim 27 words
The modified polyether polyol as described in claim 1 in which the resulting modified polyol has an OH number in the range of about 200 to 600.
Claim 8
Dependent Claim 99 words
A modified polyether polyol having a molecular weight in the range of about 200 to 1,000 and being produced by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of two with an epoxy resin selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins and aliphatic epoxy resins, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 9
Dependent Claim 99 words
A modified polyether polyol having a molecular weight in the range of about 200 to 1,000 and being produced by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of two with an epoxy resin selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins and aliphatic epoxy resins, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 10
Independent Claim 65 words
A method of preparing a modified polyether polyol comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 11
Independent Claim 65 words
A method of preparing a modified polyether polyol comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 12
Dependent Claim 31 words
A method of preparing a modified polyether polyol as described in claim 8 in which the resulting modified polyol has a molecular weight in the range of about 200 to 1,000.
Claim 13
Dependent Claim 41 words
A method of preparing a modified polyether polyol as described in claim 8 in which the epoxy resin is selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins, and aliphatic epoxy resins.
Claim 14
Dependent Claim 32 words
A method of preparing a modified polyether polyol as described in claim 8 in which the alkylene oxides are taken from the group consisting of ethylene oxide, propylene oxide and butylene oxide.
Claim 15
Dependent Claim 38 words
A method of preparing a modified polyether polyol as described in claim 8 in which the components are reacted in the pressure range between about 20 psi and about 60 psi during the preparation of the modified polyol.
Claim 16
Dependent Claim 31 words
A method of preparing a modified polyether polyol as described in claim 8 in which the resulting modified polyol has an OH number in the range of about 200 to 600.
Claim 17
Independent Claim 85 words
A method of preparing a modified polyether polyol comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of two with an epoxy resin selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins, and aliphatic epoxy resins, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 18
Independent Claim 85 words
A method of preparing a modified polyether polyol comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of two with an epoxy resin selected from the group of epoxy resins consisting of the diglycidyl ether of Bisphenol A, epoxy novolak resins, and aliphatic epoxy resins, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 19
Dependent Claim 88 words
An improved rigid polyisocyanurate foam produced by the reaction of a modified polyol, an organic polyisocyanate and a foam catalyst wherein the improvement comprises making the modified polyol by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 20
Dependent Claim 88 words
An improved rigid polyisocyanurate foam produced by the reaction of a modified polyol, an organic polyisocyanate and a foam catalyst wherein the improvement comprises making the modified polyol by a method comprising the following steps (a) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (b) heating the mixture in (a) to a temperature between about 70° C. to 115° C. for a period of time and (c) adding to the heated mixture one or more alkylene oxides.
Claim 21
Independent Claim 93 words
A method for producing an improved rigid polyisocyanurate foam which comprises (a) making a modified polyol by a method comprising the following steps (1) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (2) heating the mixture in (1) to a temperature between about 70° C. to 115° C. for a period of time and (3) adding to the heated mixture one or more alkylene oxides, and (b) reacting said modified polyol with an organic polyisocyanate and one or more suitable foam catalysts.
Claim 22
Independent Claim 93 words
A method for producing an improved rigid polyisocyanurate foam which comprises (a) making a modified polyol by a method comprising the following steps (1) mixing a low molecular weight polyol initiator having a hydroxyl functionality of less than three with an epoxy resin, (2) heating the mixture in (1) to a temperature between about 70° C. to 115° C. for a period of time and (3) adding to the heated mixture one or more alkylene oxides, and (b) reacting said modified polyol with an organic polyisocyanate and one or more suitable foam catalysts.
Claim 23
Dependent Claim 69 words
The modified polyol of claim 1 in which heating step (b) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.
Claim 24
Dependent Claim 68 words
The modified polyol of claim 7 in which heat-step (b) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.
Claim 25
Dependent Claim 68 words
The method of claim 8 in which heating step (b) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.
Claim 26
Dependent Claim 68 words
The method of claim 14 in which heating step (b) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.
Claim 27
Dependent Claim 69 words
The improved foam of claim 15 in which heating step (b) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.
Claim 28
Dependent Claim 68 words
The method of claim 16 in which heating step (2) occurs for at least fifteen minutes and in which the reaction mass containing initiator, epoxy resin and alkylene oxide is continued to be heated in the range between about 70° C. and 115° C. after the alkylene oxide is added for about one hour or more before the modified polyol is stripped out in a final separation step.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-04-05 1985-10-05 1986-04-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-04-05 1989-10-05 1990-04-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-04-05 1993-10-05 1994-04-06 $7700.00 Window Closed / Lapsed

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