Polyisocyanate polyaddition polyol manufacturing process and product

Patent metadata

Field	Value
Publication number	US-9840578-B2
Application number	US-201414912075-A
Country	US
Kind code	B2
Filing date	Sep 11, 2014
Priority date	Sep 13, 2013
Publication date	Dec 12, 2017
Grant date	Dec 12, 2017

Abstract

PIPA polyols are made in a two-step process. In the first step, a base polyether polyol and a polyisocyanate are reacted to form a mixture that contains unreacted base polyol, unreacted polyisocyanate and adducts of the base polyol and polyisocyanate. A low equivalent weight polyol is then added and reacted in a second step to form the dispersion. The process unexpectedly produces a stable dispersion of the fine PIPA particles in the base polyol, even when the base polyol contains mostly secondary hydroxyl groups. The process also permits the tuning of product viscosity by increasing or decreasing the extent of reaction in the first step.

First claim

What is claimed is:

1. A process for preparing a dispersion of polyisocyanate polyaddition particles in a base polyol, comprising
a) combining (1) 1 to 50 parts by weight of a polyisocyanate having an isocyanate equivalent weight of up to 300 and (2) 100 parts by weight of one or more liquid base polyether polyols, the base polyether polyol(s) having an average hydroxyl equivalent weight of at least 200, a nominal hydroxyl functionality of at least 2.5, wherein at least 75% of the hydroxyl groups of the base polyol are secondary hydroxyl groups, and reacting the polyisocyanate with the polyether polyol while mixing to produce a mixture containing unreacted base polyol, unreacted polyisocyanate compound and one or more isocyanate group-containing adducts of the base polyol with the polyisocyanate;
b) then dispersing (3) a low equivalent weight polyol having an equivalent weight of up to 80 and 2 to 6 hydroxyl groups per molecule and optionally additional polyisocyanate into the mixture formed in step a), wherein 1.05 to 1.75 equivalents of the low equivalent weight polyol are provided per equivalent of isocyanate groups provided by the mixture formed in step a) and said additional polyisocyanate if any, and reacting the low equivalent weight polyol with the isocyanate groups to form polyisocyanate polyaddition particles dispersed in the base polyether polyol.

2. The process of claim 1 wherein at least 85% of the hydroxyl groups of the base polyol are secondary hydroxyl groups.

3. The process of claim 1 wherein the base polyol is at least one polyol selected from i) a nominally trifunctional poly(propylene oxide) homopolymer having a hydroxyl equivalent weight of 900 to 1350, and ii) a nominally trifunctional random copolymer of 80 to 99.5% by weight propylene oxide and 0.5 to 20% by weight ethylene oxide, based on the combined weight of the propylene oxide and ethylene oxide, the random copolymer having a hydroxyl equivalent weight of 900 to 1350, wherein 92 to 100% of the hydroxyl groups of the base polyol are secondary hydroxyl groups.

4. The process of claim 1 , wherein the low equivalent weight polyol is triethanolamine or a mixture containing at least 75% by weight of triethanolamine by weight of the mixture.

5. The process of claim 1 , wherein the polyisocyanate includes toluene diisocyanate or diphenylmethanediisocyanate.

6. A process for preparing a dispersion of polyisocyanate polyaddition particles in a base polyol, comprising
a) combining (1) 1 to 50 parts by weight of toluene diisocyanate and (2) 100 parts by weight of a liquid base polyether polyol, wherein the base polyol is at least one polyol selected from i) a nominally trifunctional polypropylene oxide) homopolymer having a hydroxyl equivalent weight of 900 to 1350, and ii) a nominally trifunctional random copolymer of 80 to 99.5% by weight propylene oxide and 0.5 to 20% by weight ethylene oxide, based on the combined weight of the propylene oxide and ethylene oxide, the random copolymer having a hydroxyl equivalent weight of 900 to 1350, wherein 85 to 100% of the hydroxyl groups of the base polyol are secondary hydroxyl groups, and reacting the toluene diisocyanate with the base polyether polyol while mixing to produce a mixture containing unreacted base polyol, unreacted toluene diisocyanate and one or more isocyanate group-containing adducts of the base polyol with the toluene diisocyanate;
b) then dispersing (3) triethanolamine or a mixture of 75 to 99.9% by weight triethanolamine and 0.1 to 25% by weight, based on the weight of the mixture, of one or more other polyols having a hydroxyl equivalent weight of up to 80 and 2 to 6 hydroxyl groups per molecule and optionally additional toluene diisocyanate into the mixture formed in step a), wherein 1.05 to 1.75 equivalents of the triethanolamine or mixture are provided per equivalent of isocyanate groups provided by the mixture formed in step a) and said additional toluene diisocyanate if any, and reacting the triethanolamine or mixture with the isocyanate groups to form polyisocyanate polyaddition particles dispersed in the base polyether polyol.

7. The process of claim 6 , wherein in step a), 1 to 30% of the hydroxyl groups of the base polyether polyol react with isocyanate groups.

8. The process of claim 6 , wherein steps a) and b) each are performed in the absence of a tin catalyst.

9. The process of claim 6 wherein in step (a), the base polyol and polyisocyanate are reacted for 5 seconds to 5 minutes before performing step (b).

10. The process of claim 6 wherein steps (a) and (b) are performed in the absence of an ionic surfactant, a silicone surfactant or a nonionic surfactant compound having one or more hydrophilic, internal or terminal poly(ethylene oxide) chains.

11. The process of claim 6 , wherein steps (a) and (b) are performed in the presence of up to 2 weight percent water, based on the combined weights of base polyol, polyisocyanate, low equivalent weight polyol and water.

12. The process of claim 6 , wherein step (b) is performed in the presence of a preformed PIPA polyol.

13. The process of claim 6 , wherein step (a) is performed by continuously bringing the base polyol and toluene diisocyanate together in a mixhead to form a mixture which is continuously introduced into a tubular reactor where the base polyol and toluene diisocyanate react as the mixture passes through an initial portion of the tubular reactor to form a base polyol mixture, and step (b) is performed by introducing the low equivalent weight polyol and optionally an additional toluene diisocyanate into a downstream section of the tubular reactor and mixing it with the base polyol mixture formed in step (a), and then completing the reaction of the low equivalent weight polyol.

14. The process of claim 6 , wherein the dispersion has a solids content of 8 to 25% by weight.

15. The process of claim 6 , wherein at least 90 volume-% of the particles have a particle size of 0.1 to 5 μm.

16. The process of claim 6 , wherein the dispersion has a viscosity of 750 to 20,000 mPa·s at 20° C. with a solid content of at least 10% weight percent.

17. A dispersion of polyisocyanate polyaddition particles in a base polyether polyol made in accordance with the process of claim 1 .

18. A dispersion of polyisocyanate polyaddition particles in a base polyether polyol made in accordance with the process of claim 6 .

Assignees

• Dow Global Technologies Llc

Inventors

• Cookson Paul
• Casati Francois
• Borella Ricco
• Hoehener Daniel
• Amici-Kroutilova Irena

Classifications

• C08G18/246

  containing also tin-carbon bonds · CPC title

• C08G18/7621

  being toluene diisocyanate including isomer mixtures · CPC title

• C08G18/3281

  containing three hydroxy groups · CPC title

• C08G18/7664

  containing alkylene polyphenyl groups · CPC title

• C08G18/4866

  having a low unsaturation value · CPC title