Laminated pane for a head-up display system with p-polarized radiation
US-2024399718-A1 · Dec 5, 2024 · US
US10293586B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10293586-B2 |
| Application number | US-201013514523-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 6, 2010 |
| Priority date | Dec 12, 2009 |
| Publication date | May 21, 2019 |
| Grant date | May 21, 2019 |
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The invention relates to the use of layer structures in the production of rotor blades for wind power plants, and to rotor blades for wind power plants.
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The invention claimed is: 1. A process for the production of rotor blades for wind power plants comprising providing a layer structure, wherein the layer structure comprises a) a release agent layer b) a fiber layer treated with a polyurethane, c) a fiber layer provided with the polyurethane wherein at least one of the treatment of the fiber layer b) and the providing of the fiber layer c) comprises injection of a polyurethane reaction mixture through a vacuum-assisted resin transfer moulding process into a mould comprising the fiber layer b) and the fiber layer c), and wherein the polyurethane reaction mixture has a viscosity of 5000 mPas at 25° C., 30 minutes after a mixing of the polyurethane reaction mixture. 2. Process for the production of rotor blades according to claim 1 for wind power plants, comprising providing rotor blades comprising a casing comprising the layer structure. 3. Process according to claim 2 , wherein the reaction mixture comprises an isocyanate diphenylmethane diisocyanate and/or polyphenylenepolymethylene polyisocyanate having an NCO content of more than 25 wt. %. 4. Process according to claim 2 , wherein the reaction mixture contains a compound having at least two hydrogen atoms reactive towards isocyanate a polyether polyol in which at least 60% of the OH groups are secondary OH groups and which has an OH number of from 200 to 1830 mg KOH/g. 5. Process according to claim 2 , wherein the reaction mixture is applied to the fiber layers at a temperature of from 20 to 80° C. 6. Process according to claim 2 , wherein the reaction mixture is cured at a temperature of from 40 to 160° C. 7. Process according to claim 2 , wherein the reaction mixture has a viscosity of ≤5000 mPas 30 minutes after a mixing of the reaction mixture. 8. The process according to claim 2 , wherein the reaction mixture comprises an isocyanate diphenylmethane diisocyanate and/or polyphenylenepolymethylene polyisocyanate having an NCO content of more than 25 wt. %, wherein the reaction mixture contains as the compound having at least two hydrogen atoms reactive towards isocyanate a polyether polyol in which at least 60% of the OH groups are secondary OH groups and which has an OH number of from 200 to 1830 mg KOH/g, and wherein the reaction mixture has a viscosity of ≤5000 mPas 30 minutes after a mixing of the reaction mixture. 9. The process according to claim 8 , wherein the reaction mixture has a viscosity of ≤2000 mPas 30 minutes after the mixing of the reaction mixture.
hollow blades · CPC title
Cross-Sectional Technologies · mapped topic
Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as mould material · CPC title
comprising polyurethanes · CPC title
Cross-Sectional Technologies · mapped topic
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