Method for producing a mixture of alkoxylated polyphenols and use of said mixture
US-2024409679-A1 · Dec 12, 2024 · US
US10519273B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10519273-B2 |
| Application number | US-201715834127-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 7, 2017 |
| Priority date | Dec 7, 2017 |
| Publication date | Dec 31, 2019 |
| Grant date | Dec 31, 2019 |
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Disclosed are processes for producing molded polyurethane elastomers and products, such as filter end caps, that include such elastomers. The elastomers are the reaction product of a non-foaming reaction mixture comprising an isocyanate-reactive composition and an organic polyisocyanate prepolymer with an internal mold release agent.
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What is claimed is: 1. A process of making a filter cartridge assembly comprising an end member and a body comprising a filter medium, comprising affixing the end member to an end of the body, wherein the end member is a polyurethane elastomer that is a reaction product of a non-foaming reaction mixture comprising an isocyanate-reactive composition and an organic polyisocyanate prepolymer having an internal mold release agent, wherein the isocyanate-reactive composition comprises 1% to 10% by weight, based on the total weight of isocyanate-reactive ingredients in the isocyanate-reactive composition, of a polyether tetrol that is an alkylene diamine-alkylene oxide adduct having a number average molecular weight of 150 to 500 gram/mole. 2. The process of claim 1 , wherein the organic polyisocyanate prepolymer comprises a reaction product of a fatty acid ester and an organic polyisocyanate. 3. The process of claim 2 , wherein the fatty acid ester is a condensate of oleic acid with a dicarboxylic acid and a polyfunctional alcohol that has a number average molecular weight of 900 to 2500 gram/mole and a hydroxyl number of 30 to 70 mg KOH/gram. 4. The process of claim 1 , wherein the polyether tetrol has a number average molecular weight 340 to 380 gram/mole. 5. The process of claim 1 , wherein the polyether tetrol is present in an amount of 2% to 6% by weight, based on the total weight of isocyanate-reactive ingredients in the isocyanate-reactive composition. 6. The process of claim 1 , wherein the isocyanate-reactive composition further comprises a polyether that has a hydroxyl functionality of greater than 2 and a number average molecular weight of 150 to 450 gram/mole, wherein the polyether polyol is prepared from an initiator which is not an amine. 7. The process of claim 6 , wherein the polyether polyol prepared from an initiator which is not an amine has a functionality of 3 and a hydroxyl number of 640 to 660 mg KOH/g. 8. The process of claim 6 , wherein the polyether polyol prepared from an initiator which is not an amine (A) and the alkylene diamine-alkylene oxide adduct (B) are present in the isocyanate-reactive composition in a relative weight ratio of (A):(B) of at least 1:1. 9. The process of claim 8 , wherein the relative weight ratio of (A):(B) is 2:1 to 4:1. 10. The process of claim 8 , wherein the isocyanate-reactive composition further comprises a polyether polyol having a hydroxyl functionality of greater than 2 and a number average molecular weight of 600 to 800 gram/mole. 11. The process of claim 10 , wherein the polyether polyol having a hydroxyl functionality of greater than 2 and a number average molecular weight of 600 to 800 gram/mole is present in an amount of 40 to 80 percent by weight, based on the total weight of the isocyanate-reactive composition. 12. The process of claim 1 , wherein the isocyanate-reactive composition comprises less than 0.1% by weight of carboxylic acid. 13. The process of claim 1 , wherein the isocyanate-reactive composition comprises less than 0.5% by weight of zinc carboxylate. 14. The process of claim 1 , wherein the isocyanate-reactive composition does not include an internal mold release agent. 15. A process of making a filter cartridge assembly comprising an end member and a body comprising a filter medium, comprising affixing the end member to an end of the body, wherein the end member is a polyurethane elastomer that is a reaction product of a non-foaming reaction mixture comprising an isocyanate-reactive composition and an organic polyisocyanate prepolymer having an internal mold release agent, wherein the isocyanate-reactive composition comprises a mixture of polyols formulated to provide a polyurethane elastomer having a Shore D hardness, measured according to ASTM D2240-15, within 10 minutes after production that is at least 60% of the Shore D hardness of the polyurethane elastomer measured 16 hours after production, wherein the mixture of polyols comprises 1% to 10% by weight, based on the total weight of isocyanate-reactive ingredients in the isocyanate-reactive composition, of a polyether tetrol that is an alkylene diamine-alkylene oxide adduct having a number average molecular weight of 150 to 500 gram/mole. 16. The process of claim 15 , wherein the elastomer has a Shore D hardness of at least 80 measured 16 hours after production and the Shore D hardness within 10 minutes after production that is at least 80% of the Shore D hardness of the polyurethane elastomer measured 16 hours after production.
Mixtures of polyethers containing at least one polyether containing nitrogen · CPC title
having nitrogen · CPC title
mixtures of two or more polyetherpolyols having at least three hydroxy groups · CPC title
Mixtures of two or more polyetherdiols · CPC title
Polyethers containing two hydroxy groups (C08G18/4833 - C08G18/5096 take precedence) · CPC title
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