NPE-free emulsifiers for water-blown polyurethane spray foam

Patent metadata

Field	Value
Publication number	US-9290604-B2
Application number	US-201113206545-A
Country	US
Kind code	B2
Filing date	Aug 10, 2011
Priority date	Aug 13, 2010
Publication date	Mar 22, 2016
Grant date	Mar 22, 2016

Abstract

Alkylethoxylate alcohols or mixtures of alkyl alcohol ethoxylate with an average HLB value between 10 and 15 as compatibilizers for water blown polyurethane foam formulations that are substantially free of nonylphenol ethoxylates are disclosed. The HLB is defined as the mass percent of average structure of the compatibilizer that is hydrophilic, divided by 5. The compatibilizer is mixed into the B-side of the polyurethane formulation. The B-side of the spray foam formulations comprise polyol, water, amine catalyst, and the compatibilizer of the invention such that the water is present at about 2% to about 30% by weight of the B-side formulation, and the compatibilizer is present at about 1% to about 30% by weight of the B-side formulation. The B-side of the formulation may further comprise metal catalysts, flame retardants, silicone surfactants, cell openers, antioxidants, as well as other additives.

First claim

The invention claimed is:

1. A method for making a polyurethane foam, the method comprising contacting at least one isocyanate with an isocyanate-reactive mixture comprising at least one polyether polyol, at least one silicone surfactant, a blowing agent comprising water, at least one amine catalyst, and an emulsifier wherein the emulsifier comprises at least two alkyl alcohol ethoxylates having an amount of propylene oxide that is not more than about 10% by mass of the overall average molecular weight of the emulsifier and has an average HLB value between about 10 to about 15, and wherein the isocyanate-reactive mixture contains about 0% by mass of nonylphenol ethoxylates; wherein the mixture is at least 90% phase stable for at least three days at 45 C, and the foam comprises an open cell foam having a density of 6 to 16 kg/m3.

2. The method of claim 1 where the emulsifier comprises at least one alcohol ethoxylate with renewable carbon content derived from soy, palm, canola, or other natural oil seed.

3. The method of claim 1 where the mixture of alkyl alcohol ethoxylates comprises at least about 5% by mass of one of more structure with a calculated HLB below about 10.

4. The method of claim 1 where the alkyl alcohol ethoxylates consists essentially of alkyl alcohol ethoxylates having the molecular formula R—(OCH2CH2)xOH, where R is a linear, branched, saturated or partially unsaturated hydrocarbon with between 5 and 20 carbon atoms, and x is 1 to 40.

5. The method of claim 1 wherein the mixture of alkylethoxylate alcohols that has a bimodal distribution of HLBs.

6. The method of claim 1 where the emulsifier contains renewable carbon content derived from non-seed sources.

7. The method of claim 6 wherein the non-seed source comprises one or more of biomass and sucrose.

8. The method of claim 1 where the emulsifier further comprises about 5 to about 50 mass % water wherein the amount of water is sufficient to suppress the freeze point of the emulsifier such that it is a liquid at about 20 C.

9. The method of claim 1 where the catalyst comprises at least one tertiary amine.

10. The method of claim 1 further comprising spraying a contact product of the at least one isocyanate with an isocyanate-reactive mixture.

11. A method for making a polyurethane foam comprising contacting at least one isocyanate with an isocyanate-reactive mixture comprising at least one polyol, at least one blowing agent comprising about 2 to about 30 wt % water, at least one catalyst, and an emulsifier comprising at least two alky alcohol ethoxylates wherein the emulsifier has a HLB value between about 10 and about 15 and an amount of propylene oxide that is not more than about 10% by mass of the overall average molecular weight of the emulsifier and wherein the isocyanate-reactive mixture is substantially free of nonylphenol ethoxylates.

12. The composition of claim 11 wherein the composition is free of NPE.

13. The composition of claim 11 wherein the emulsifier consists essentially of emulsifiers having a chemical structure:

Where x is 4 to 19 and y is 1 to 20.

14. A method for making a polyurethane foam, the method comprising contacting at least one isocyanate with an isocyanate-reactive mixture comprising at least one polyol, a blowing agent comprising water, at least one catalyst, and at least one emulsifier, wherein the isocyanate-reactive mixture is at least 90% phase stable for at least three days at 45 C and comprises about 2 to about 30% by mass water, about 1 to about 30% by mass emulsifier, and is substantially free of nonylphenol ethoxylates and wherein the emulsifier comprises at least two alkyl alcohol ethoxylates and has an average calculated HLB value between about 10 to about 15 and an amount of propylene oxide that is not more than about 10% by mass of the overall average molecular weight of the emulsifier, and spraying a contact product of the at least one isocyanate and the isocyanate-reactive mixture thereby making a foam comprising an open-cell foam having a density of about 6 to about 16 Kg/m3.

15. A method of claim 1 where the isocyanate-reactive mixture further comprises a metal catalyst of tin, potassium, or bismuth.

16. The method of claim 1 where the mixture of alkyl alcohol ethoxylates comprises at least about 5% by mass of one of more structure with a calculated HLB above 15.

17. A foam made by the method of claim 14 .

18. The method of claim 10 wherein the spraying comprising spraying between wall studs.

19. A method for making a water-blown polyurethane foam, the method comprising contacting at least one isocyanate with an isocyanate-reactive mixture comprising at least one polyol, a blowing agent comprising consisting water, at least one catalyst, and at least one emulsifier wherein the emulsifier comprises at least two alkyl alcohol ethoxylates and having an average HLB of about 10 to about 15 and an amount of propylene oxide that is not more than about 10% by mass of the overall average molecular weight of the emulsifier and wherein the amount of emulsifier is sufficient to provide the mixture that is at least 90% phase stable for at least three days at 45 C, and the foam comprises an open cell foam having a density of 6 to 16 kg/m3.

20. A method for making a water-blown polyurethane foam, the method comprising: i) contacting at least one isocyanate with an isocyanate-reactive mixture comprising at least one polyol, a blowing agent water, at least one catalyst, and at least one emulsifier wherein the emulsifier comprises at least two alkyl alcohol ethoxylates having an amount of propylene oxide that is not more than about 10% by mass of the overall average molecular weight of the emulsifier and an average HLB value between about 10 to about 15, and wherein the amount of emulsifier is sufficient to provide the mixture that is at least 90% phase stable for at least three days at 45 C, and ii) spraying a contact product of the at least one isocyanate and isocyanate-reactive mixture between wall studs thereby providing an open cell foam between the wall studs having a density of 6 to 16 kg/m3.

21. The method of claim 1 wherein the emulsifier contains an ethylene oxide portion containing between 1 and 40 ethylene oxide units that is terminated in a hydroxyl group.

22. The method of claim 20 wherein the emulsifier is pre-mixed with water prior to incorporation into the mixture.

23. The method of claim 20 wherein the mixture further comprises at least one silicone polyether copolymer.

24. The method of claim 20 wherein the polyol comprises a triol.

25. A foam made by the method of claim 1 .

26. A foam made by the method of claim 19 .

27. A foam made by the method of claim 20 .

Assignees

• Andrew Gary Dale
• Vincent Jean Louise
• Miller Timothy J
• Zarkov Goran
• Air Prod & Chem

Inventors

• Andrew Gary Dale
• Vincent Jean Louise
• Miller Timothy J
• Zarkov Goran

Classifications

• C08G2101/00

  Manufacture of cellular products · CPC title

• C08G18/10

  Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step · CPC title

• C08G18/12

  using two or more compounds having active hydrogen in the first polymerisation step · CPC title

• C08G18/283 Primary

  Compounds containing ether groups, e.g. oxyalkylated monohydroxy compounds · CPC title

• C08G18/2835

  having less than 5 ether groups · CPC title