Thermoplastic polyurethane for seal applications
US-2016333134-A1 · Nov 17, 2016 · US
US11267926B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11267926-B2 |
| Application number | US-201716346715-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 14, 2017 |
| Priority date | Nov 14, 2016 |
| Publication date | Mar 8, 2022 |
| Grant date | Mar 8, 2022 |
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The present invention relates to a method of preparing a polyurethane elastomer, said method comprising the step of reacting at least one isocyanate composition (ZI) and one polyol composition (ZP) comprising a poly-ε-caprolactone polyol and an α-hydro-ω-hydroxy-poly(oxytetramethylene) polyol to obtain an isocyanate-functional prepolymer and the step of reacting the prepolymer obtained as per step (i) with at least one chain extender (KV). The present invention further relates to a polyurethane elastomer obtained or obtainable according to a method of the invention and also to the method of using a polyurethane elastomer according to the invention or a polyurethane elastomer obtained or obtainable according to a method of the invention in the manufacture of a shaped article, especially a damping element, a shock absorber or a stop buffer or part of a shoe or of a shoe sole, for example part of an insert sole or of a midsole.
Opening claim text (preview).
We claim: 1. A method of preparing a polyurethane elastomer, comprising (i) and (ii): (i) reacting at least one isocyanate composition (ZI) and one polyol composition (ZP) comprising a poly-ε-caprolactone polyol and an α-hydro-ω-hydroxypoly(oxytetramethylene) polyol to obtain an isocyanate-functional prepolymer, and (ii) reacting the prepolymer obtained in (i) with at least one chain extender (KV) in the presence of a blowing agent. 2. The method according to claim 1 , wherein the reacting in (i) is performed such that the prepolymer obtained in (i) has an isocyanate (NCO) content in the range from 2% to 8%. 3. The method according to claim 1 , wherein the reacting in (i) is effected at a temperature in the range from 110° C. to 180° C. 4. The method according to claim 1 , wherein the reacting in (i) is performed such that the prepolymer obtained in (i) has an isocyanate (NCO) content in the range from 8% to 22%. 5. The method according to claim 1 , wherein the reacting in (i) is effected at a temperature in the range from 40° C. to 110° C. 6. The method according to claim 1 , wherein the reacting in (ii) is performed in the presence of at least further component selected from the group consisting of a polyol, water, a chain-extending agent, a crosslinking agent, a catalyst, and an auxiliary. 7. The method according to claim 1 , wherein the poly-ε-caprolactone polyol is obtained by reacting ε-caprolactone and a starter molecule that is a diol having a number average molecular weight in the range from 80 to 1500 g/mol. 8. The method according to claim 1 , wherein the poly-ε-caprolactone polyol is obtained by reacting ε-caprolactone and at least one starter molecule selected from the group consisting of an α-hydro-ω-hydroxypoly(oxytetramethylene)diol, a polyethylene glycol and a polypropylene glycol. 9. The method according to claim 1 , wherein the polyol composition comprises the α-hydro-ω-hydroxypoly(oxytetramethylene) polyol in an amount in the range from 0.1 to 50 wt %, based on the polyol composition. 10. The method according to claim 1 , wherein the isocyanate composition comprises at least one isocyanate selected from the group consisting of 1,5-naphthylene diisocyanate (NDI), 4,4′-diphenylmethane diisocyanate (MDI), p-phenyl diisocyanate (PPDI) and o-tolidine diisocyanate (TODI). 11. The method according to claim 1 , wherein the isocyanate composition comprises 1,5-naphthylene diisocyanate (NDI) in an amount ranging from 90 to 100 wt % based on the entire isocyanate composition. 12. The method according to claim 1 , wherein the chain extender (KV) is at least one selected from the group consisting of water, a diol having a molecular weight in the range from 50 to 500 g/mol, a triol having a molecular weight in the range from 50 to 500 g/mol and a diamine having a molecular weight in the range from 50 to 500 g/mol. 13. The method according to claim 1 , wherein the poly-ε-caprolactone polyol and/or the α-hydro-ω-hydroxypoly(oxytetramethylene) polyol have a number average molecular weight in the range from 1500 to 2500 g/mol. 14. A polyurethane elastomer obtained by a method that comprises (i) and (ii): (i) reacting at least one isocyanate composition (ZI) and one polyol composition (ZP) comprising a poly-ε-caprolactone polyol and an α-hydro-ω-hydroxypoly(oxytetramethylene) polyol to obtain an isocyanate-functional prepolymer, and (ii) reacting the prepolymer obtained in (i) with at least one chain extender (KV) in the presence of a blowing agent. 15. The polyurethane elastomer according to claim 14 wherein the polyurethane elastomer is microcellular. 16. The polyurethane elastomer according to claim 14 having a density in the range from 0.12 to 0.8 g/cm 3 according to DIN EN ISO 845. 17. A shaped article comprising the polyurethane elastomer according to claim 14 . 18. The shaped article according to claim 17 , which is a damping element, a shock absorber, a stop buffer, or part of a shoe. 19. The method according to claim 1 , wherein the (Z1) component consists of 1,5-napththylene diisocyanate and the polyol component (ZP) consists of poly-ε-caprolactone polyol and α-hydro-ω-hydroxypoly(oxytetramethylene) polyol. 20. The method according to claim 19 , wherein the polyol component (ZP) comprises 15-25% by weight of α-hydro-ω-hydroxy-poly(oxytetramethylene).
Caprolactone and/or substituted caprolactone · CPC title
Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group · CPC title
Soles · CPC title
flexible · CPC title
prepared using water as the sole blowing agent · CPC title
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