Polyurethane reaction systems for pultrusion.

Abstract

The present invention relates to a polyurethane reaction system and its use for producing pultrusions containing reinforcing fibers.

Description

[Technical Field]

[0001] The present invention relates to a polyurethane reaction system and its use for producing pultrudates containing reinforcing fibers. [Background technology]

[0002] Pultrusion is a continuous process for producing fiber-reinforced profiles of constant cross-section. A pultrusion apparatus typically consists of an impregnation unit and a heated mold, as well as a take-off device that keeps the process running. Fiber impregnation is carried out in an open bath or in a closed injection box. For thermosetting reactive resins, such as polyurethanes, a closed injection box is preferred. The injection box may be mounted upstream of the actual mold as a separate unit, or may otherwise be integrated into the mold ("direct injection"). Molding and curing of the composite then take place in the heated mold. A take-off device pulls the final profile from the mold and finally cuts it to the desired length.

[0003] To make the pultrusion process as efficient as possible, high process speeds combined with very good mechanical properties and high surface quality of the pultrusions are required. Low take-off forces of less than 3 kN reflect the flow process in particular. Different patents offer different solutions for an effective pultrusion process with PU resins.

[0004] Patent Document 1 discloses a reaction system for producing fiber-reinforced composites by a pultrusion molding process, the system being composed of a continuous fiber reinforcement material and an immiscible polyurethane formulation containing a polyisocyanate component containing at least one polyisocyanate and an isocyanate-reactive component containing at least one isocyanate-reactive compound. It is stated that the incompatibility of the polyether polyol used in the isocyanate-reactive compound and / or the incompatibility between the isocyanate-reactive compound and the isocyanate makes it possible to achieve an improved pultrusion molding process.

[0005] It is common to add insoluble solids to isocyanate-reactive components as additives to achieve specific functions that cannot be achieved equally well with monophasic isocyanate-reactive components. These are therefore multiphase isocyanate-reactive components. Multiphasing is defined as the presence of two or more phases at room temperature over a six-month period. Additives used to control the reaction include, for example, solids as water binders (e.g., U.S. Patent Nos. 5,629,992 and 5,629,992), fillers such as chalk, silica sand, and gypsum (U.S. Patent No. 5,629,992), or encapsulated catalysts (U.S. Patent No. 5,629,992). In addition to the liquid / solid multiphase characteristics listed, liquid / liquid multiphase characteristics similar to those observable in oil / water mixtures are often also present. Various publications further state that this phase instability is necessary to achieve low take-off forces (e.g., U.S. Patent No. 5,629,992).

[0006] In addition to the advantages mentioned above, multiphase solid / liquid and / or liquid / liquid systems also have the following disadvantages. Thus, for example, the material handling of the filling and transport of the multiphasic isocyanate-reactive components presents significant challenges, since it is necessary to ensure the presence of a homogeneous mixture despite its multiphase nature. It is also necessary to ensure consistent and sufficient mixing in the pultrusion equipment, so that a consistent composition and therefore profile quality can be achieved in the pultrusion process. For example, filters are also installed in the metering units to separate impurities from the impregnating resin. These filters can become clogged with solids in the formulation, bringing the process to a halt. The pumps utilized are also sensitive to the use of solids. [Prior art documents] [Patent documents]

[0007] [Patent Document 1] U.S. Patent Application Publication No. 2008 / 090966 [Patent Document 2] International Publication No. 2011 / 067246 [Patent Document 3] International Application No. PCT / EP2018 / 059790 [Patent Document 4] European Patent Application Publication No. 3380539 [Patent Document 5] International Publication No. 2018 / 162519 Summary of the Invention [Problem to be solved by the invention]

[0008] It is therefore an object of the present invention to develop a pultrusion process that at least partially overcomes the disadvantages of known processes, such as the multiphase nature of the isocyanate reaction components and / or the only partially adequate mechanical properties of the resulting pultrusions, without excessively impairing the efficiency of the process. Furthermore, the transport of the reaction system to the pultrusion apparatus should be improved, and the processability of the reaction system should be simplified by avoiding exposure of pumps and filters to solids. This object has surprisingly been achieved by the process of the present invention, which makes it possible to obtain the polyurethane pultrusions of the present invention using the polyurethane reaction system of the present invention. [Means for solving the problem]

[0009] The present invention provides a polyurethane reaction system comprising: an isocyanate component A), isocyanate-reactive component B), 3% to 13% by weight of a polyether polyol B1) having a hydroxyl number (OHN) of 20 mg KOH / g to 50 mg KOH / g, which can be obtained by reacting a first H-functional starter compound having a functionality f of ≧2 to ≦4 with ethylene oxide and propylene oxide; 15% to 37% by weight of a polyether polyol B2) having a hydroxyl number (OHN) of 900 mg KOH / g to 1100 mg KOH / g, which can be obtained by reacting a second H-functional starter compound having a functionality f of ≥ 2 to ≤ 4 with a second alkylene oxide; 50% to 72% by weight of a polyether polyol B3) having a hydroxyl number (OHN) of more than 50 mg KOH / g and less than 900 mg KOH / g, which can be obtained by reacting a third H-functional starter compound with a third alkylene oxide; one or more catalysts B4) Desiccant B5) and Including, the sum of the weight percentages of components B1) and B2) is 40% by weight or less relative to the sum of the amounts of B), C) and D), and the sum of the weight percentages of components B1), B2), B3), B4) and B5) is 90% by weight or more relative to the sum of the amounts of B), C) and D); an isocyanate-reactive component B); C) an internal mold release agent; Optionally further auxiliary and additional substances D), Including, the weight percent of components B), C) and optionally D) total 100 weight percent; The hydroxyl number (OHN) of the polyether polyols B1), B2) and B3) is determined using ISO 14900, A polyurethane reaction system is provided.

[0010] In one embodiment of the present invention, components A), B), C) and optionally D) are utilized in amounts such that the ratio of the number of NCO groups in (A) to the sum of the number of isocyanate reactive groups in (B), (C) and (D), multiplied by 100 (the so-called index), has a value of 100 to 150. DETAILED DESCRIPTION OF THE INVENTION

[0011] An isocyanate-reactive component in the context of this application is a compound capable of reacting with an isocyanate group, such as a component containing a hydroxyl group (-OH), an amine group (-NH or -NRH, where R is an organic residue), or a thio group (-SH).

[0012] Hydroxyl number (OHN) in the context of this application is the amount of potassium hydroxide in milligrams equivalent to the amount of acetic acid that binds in the acetylation of one gram of material. For this application, OHN was determined according to ISO 14900.

[0013] The polyisocyanate component A) preferably comprises at least one of monomeric methylene di(phenyl isocyanate) (MDI), oligomeric MDI, polymeric MDI, and mixtures thereof.

[0014] The NCO content of polyisocyanate component A) is preferably greater than 25% by weight, preferably greater than 30% by weight, particularly preferably greater than 31.5% by weight. Polyisocyanate component A) preferably has a functionality of 2.1 to 2.9. The viscosity of polyisocyanate component A) is preferably 500 mPas (25°C) or less, measured in accordance with DIN 53019-1.

[0015] Also available are the common aliphatic, cycloaliphatic, araliphatic di- and / or polyisocyanates, especially aromatic isocyanates, known from polyurethane chemistry. Examples of such suitable polyisocyanates are ethylene diisocyanate, 1,4-butylene diisocyanate, 1,5-pentane diisocyanate, 1,6-hexamethylene diisocyanate (HDI), 1,12-dodecane diisocyanate, cyclobutane-1,3-diisocyanate, cyclohexane-1,3- and -1,4-diisocyanate, and mixtures of these isomers, isophorone diisocyanate (IPDI), 2,4 - and 2,6-hexahydrotolylene diisocyanate and mixtures of these isomers, 2,2,4- and / or 2,4,4-trimethylhexamethylene diisocyanate, bis(4,4'-, 2,4'- and 2,2'-isocyanatocyclohexyl)methane or mixtures of these isomers, and aromatic isocyanates of the general formula R(NCO)z, where R is a polyvalent organic radical containing aromatic groups and z is an integer of at least 2.Examples thereof are 1,3-diisocyanato-o-xylene, 1,3-diisocyanato-p-xylene, 1,3-diisocyanato-m-xylene, 2,4-diisocyanato-1-chlorobenzene, 2,4-diisocyanato-1-nitrobenzene, 2,5-diisocyanato-1-nitrobenzene, m-phenylene diisocyanate, p-phenylene diisocyanate, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, mixtures of 2,4- and 2,6-tolylene diisocyanate, 1,5-naphthalene diisocyanate, 1-methoxy-2,4-phenylene diisocyanate, 4,4'-biphenyl diisocyanate, 1,5-diisocyanate, 1-methoxy-2,4-phenylene ... phenylene diisocyanate, 3,3'-dimethyl-4,4'-diphenylmethane diisocyanate, and 3,3'-dimethyldiphenylmethane-4,4'-diisocyanate, triisocyanates such as 4,4',4"-triphenylmethane triisocyanate and 2,4,6-toluene triisocyanate, and tetraisocyanates such as 4,4'-dimethyl-2,2'-5,5'-diphenylmethane tetraisocyanate and 1,3- and / or 1,4-bis(2-isocyanatoprop-2-yl)benzene (TMXDI), 1,3-bis(isocyanatomethyl)benzene (XDI).

[0016] In addition to the above-mentioned isocyanates, modified isocyanates, such as those containing uretdione, isocyanurate, carbodiimide, uretonimine, allophanate or biuret structures, and also modified isocyanates in the form of prepolymers obtainable from the reaction of one or more polyisocyanates with one or more polyols. The isocyanates may optionally be prepolymers obtainable from the reaction of an isocyanate having an NCO functionality of 2 or more with a polyol having a molecular weight of 62 g / mol to 8000 g / mol and an OH functionality of 1.5 to 6.

[0017] The polyisocyanate building block A) particularly preferably consists of monomeric, oligomeric, polymeric MDI or mixtures thereof.

[0018] The polyether polyols B1) according to the invention having a hydroxyl number (OHN) of 20 mg KOH / g to 50 mg KOH / g can be obtained by reacting a first H-functional starter compound having a functionality f of ≧2 to ≦4 with ethylene oxide and propylene oxide.

[0019] The polyether polyol B1) may be one or more polyols.

[0020] The first H-functional starter compound is preferably one or more compounds selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, triethylene glycol, tripropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane, pentaerythritol, ethylenediamine and triethanolamine, particularly preferably 1,2- and 1,3-propylene glycol, diethylene glycol, glycerol, trimethylolpropane, very particularly preferably glycerol and trimethylolpropane.

[0021] In one embodiment of the present invention, for the polyether polyol B1), the mass fraction of propylene oxide is 60% to 90% by weight, preferably 70% to 85% by weight, based on the total of ethylene oxide and propylene oxide used.

[0022] In a preferred embodiment of the present invention, the polyether polyol B1) is i) reacting a first H-functional starter compound with propylene oxide in the presence of a first catalyst to form a first intermediate; ii) reacting the first intermediate with ethylene oxide to form a block copolymer; It is possible to obtain it by

[0023] In an alternative, less preferred embodiment of the present invention, the polyether polyol B1) can be obtained by copolymerizing ethylene oxide and propylene oxide onto a first H-functional starter compound in the presence of a first catalyst to form a copolymer.

[0024] In one embodiment of the invention, the first catalyst is potassium hydroxide, sodium hydroxide, cesium hydroxide, a double metal cyanide (DMC) catalyst and / or an amine, preferably potassium hydroxide.

[0025] The polyether polyols B2) according to the invention having a hydroxyl number (OHN) of 900 mg KOH / g to 1100 mg KOH / g can be obtained by reacting a second H-functional starter compound having a functionality f of ≧2 to ≦4 with a second alkylene oxide.

[0026] The polyether polyol B2) may be one or more polyols.

[0027] The second H-functional starter compound is preferably one or more compounds selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, triethylene glycol, tripropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane, pentaerythritol, ethylenediamine and triethanolamine, particularly preferably 1,2- and 1,3-propylene glycol, diethylene glycol, glycerol, trimethylolpropane, very particularly preferably glycerol and trimethylolpropane.

[0028] In one embodiment of the present invention, the polyether polyol B2) is obtainable by copolymerizing a second alkylene oxide onto a second H-functional starter compound in the presence of a second catalyst.

[0029] In one embodiment of the invention, the second catalyst is potassium hydroxide, sodium hydroxide, cesium hydroxide, a double metal cyanide (DMC) catalyst and / or an amine, preferably potassium hydroxide.

[0030] In one embodiment of the present invention, the second alkylene oxide is propylene oxide and / or ethylene oxide, preferably propylene oxide.

[0031] The polyether polyols B3) according to the invention having a hydroxyl number (OHN) of more than 50 mg KOH / g and less than 900 mg KOH / g can be obtained by reacting a third H-functional starter compound with propylene oxide.

[0032] The polyether polyol B3) may be one or more polyols.

[0033] In one embodiment, the third H-functional starter compound has a functionality f of 2 or more and 4 or less.

[0034] The third H-functional starter compound is preferably one or more compounds selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, triethylene glycol, tripropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane, pentaerythritol, ethylenediamine and triethanolamine, particularly preferably 1,2- and 1,3-propylene glycol, diethylene glycol, glycerol, trimethylolpropane, very particularly preferably 1,2-propylene glycol, glycerol and trimethylolpropane.

[0035] In one embodiment of the present invention, the polyether polyol B3) is obtainable by copolymerizing a third alkylene oxide onto a third H-functional starter compound in the presence of a third catalyst.

[0036] In one embodiment of the invention, the third catalyst is potassium hydroxide, sodium hydroxide, cesium hydroxide, a double metal cyanide (DMC) catalyst and / or an amine, preferably potassium hydroxide.

[0037] In one embodiment of the present invention, the third alkylene oxide is propylene oxide and / or ethylene oxide, preferably propylene oxide.

[0038] According to the invention, in the isocyanate-reactive component B), not only the polyols B1), B2) and B3) used according to the invention can be used, but also further polyether polyols, further polyester polyols, further polyetherester polyols and / or further polycarbonate polyols. It is preferred if further polyether polyols and / or further polyester polyols, particularly preferably further polyether polyols, are used in B).

[0039] In addition to OH functional groups, the further polyols utilized in the isocyanate-reactive component B) may also contain further isocyanate-reactive hydrogen atoms (i.e., active hydrogen atoms), such as NH and NH groups. To the extent that such further active hydrogen atoms are present, preferably more than 90%, in particular more than 95%, particularly preferably more than 99%, and very particularly preferably 100% of all isocyanate-reactive hydrogen atoms in the isocyanate-reactive component are derived from OH functional groups.

[0040] Such polyols are described, for example, in Ionescu, "Chemistry and Technology of Polyols for Polyurethanes", Rapra Technology Limited, Shawbury 2005, on pages 31 ff (Chapter 3: The General Characteristics of Oligo-Polyols), 55 ff (Chapter 4: Oligo-Polyols for Elastic Polyurethanes), 263 ff (Chapter 8: Polyester Polyols for Elastic Polyurethanes), in particular on pages 321 ff (Chapter 13: Polyether Polyols for Rigid Polyurethane Foams), and 419 ff (Chapter 16: Polyester Polyols for Rigid Polyurethane Foams).

[0041] Preferably, polyols are used in the isocyanate-reactive component B) which can be produced by polyaddition of alkylene oxides, such as propylene oxide and / or ethylene oxide, to H-functional starter compounds in the presence of a catalyst in a manner known per se. Polyhydroxyl polyethers are preferably produced from H-functional starter compounds having an average of 2 to 8 active hydrogen atoms and one or more alkylene oxides, such as ethylene oxide, butylene oxide, and / or propylene oxide. Preferred starter compounds are molecules having 2 to 8 hydroxyl groups per molecule, such as water, ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, triethylene glycol, tripropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane, pentaerythritol, sorbitol, and sucrose, as well as amine-based starter compounds, such as ethylenediamine and triethanolamine. The starter compounds can be used alone or in mixtures. Particularly preferred are 1,2-propylene glycol and 1,3-propylene glycol, diethylene glycol, sorbitol, glycerol, trimethylolpropane, sucrose, and mixtures of the products listed. Representative examples of isocyanate-reactive components B) are described, for example, in "Kunststoff-Handbuch, volume VII "Polyurethane", 3rd edition, Carl Hanser Verlag, Munich / Vienna, 1993, pages 57-67 and 88-90.

[0042] Polyester polyols are polyhydroxyl compounds having ester groups, such as castor oil or polyhydroxyl polyesters, such as can be obtained by polycondensation of a surplus of simple polyhydric alcohols of the type listed herein above by way of example, with preferably dibasic carboxylic acids or their anhydrides, such as adipic acid, phthalic acid, or phthalic anhydride.

[0043] Suitable catalysts B4) include, for example, known polyurethane catalysts, such as organometallic compounds, for example potassium or sodium salts of organic carboxylic acids, for example potassium acetate; as well as tin(II) salts of organic carboxylic acids, for example tin(II) acetate, tin(II) octoate, ethyltin(II) hexanoate and tin(II) laurate, and dialkyltin(IV) salts of organic carboxylic acids, for example dibutyltin diacetate, dibutyltin dilaurate, dimethyltin dilaurate, dibutyltin maleate and dioctyltin diacetate, and also, for example, diisooctyl-2,2'-[(dioctylstannylene)bis(thio)]diacetate, di-n-butyl-bis(dodecylthio)tin, monooctyltin isooctylthioglycolate, isooctyl Examples of suitable latent catalysts include mercaptoacetate, 2-ethylhexyl-4,4'-dibutyl-10-ethyl-7-oxo-8-oxa-3,5-dithia-4-stannatetradecanoate, dimethyltin dithioglycolate, and / or strong basic amines such as 2,2,2-diazabicyclooctane, N,N-dimethylaminopropylamine, N,N-bis(3-dimethylaminopropyl)-N-isopropanolamine, triethylamine, triethylenediamine, tetramethylhexamethylenediamine, pentamethyldiethylenetriamine, N,N-dimethylcyclohexylamine or bis(N,N-dimethylaminoethyl)ether, N,N-dimethylbenzylamine, N,N-methyldibenzylamine, and N-methylimidazole, as well as latent catalysts. Latent catalysts and their mechanisms of action are described, for example, in EP 2 531 538, pages 1 to 4 and page 9, line 26 to page 10, line 2. Typical latent catalysts include blocked amine and amidine catalysts such as those from Air Products (e.g., Polycat™ SA-1 / 10, Dabco KTM60) and those from Tosoh Corporation (e.g., Toyocat™ DB2, DB30, DB31, DB40, DB41, DB42, DB60, DB70).Further representative examples of catalysts and details regarding the mechanism of action of catalysts are described in Kunststoff-Handbuch, volume VII "Polyurethane", 3rd edition, Carl Hanser Verlag, Munich / Vienna, 1993, pp. 104-110.

[0044] In one embodiment of the present invention, the amount of catalyst B4) is 0.05% by weight to 5% by weight, preferably 0.05% by weight to 2% by weight, based on the total of B), C) and D).

[0045] The desiccant B5) used is preferably a liquid or dissolved desiccant (water-binding agent) at room temperature, i.e., 25° C. In the context of the present invention, the terms “desiccant” and “water-binding agent” are used synonymously.

[0046] In one embodiment of the invention, the amount of desiccant B5) is in each case not more than 5% by weight, preferably not more than 2% by weight, relative to the sum of the amounts of B), C) and D).

[0047] In one embodiment of the invention, the amount of desiccant B5) is in each case from 0.05% to 5% by weight, preferably from 0.05% to 2% by weight, relative to the sum of the amounts of B), C) and D).

[0048] In one embodiment of the invention, the drying agent B5) is a trialkyl orthoformate, p-toluenesulfonyl isocyanate, oxazolidine or a mixture thereof, preferably oxazolidine.

[0049] In a preferred embodiment, the drying agent B5) is an oxazolidine, which is 3-ethyl-2-methyl-2-(3-methylbutyl)-1,3-oxazolidine and / or N-butyl-2-(1-ethylpentyl)-1,3-oxazolidine, particularly preferably N-butyl-2-(1-ethylpentyl)-1,3-oxazolidine.

[0050] Usable internal mold release agents C) include all release agents customary in polyurethane production, such as long-chain monocarboxylic acids, especially fatty acids such as stearic acid, amines of long-chain carboxylic acids such as stearamide, fatty acid esters, and metal salts of long-chain fatty acids such as zinc stearate or silicones. Particularly suitable are internal mold release agents available for pultrusion molding, such as MOLD WIZ INT-1948 MCH, MOLD WIZ INT-1947 MCH, and MOLD WIZ-1960 MCH available from Axel Plastics, or Luvotrent TL HB 550-D and Luvotrent TL HB 550 available from Lehmann & Voss. The internal mold release agent is used in an amount of 0.1 to 8% by weight, preferably 0.1 to 6% by weight, and particularly preferably 0.1 to 4% by weight, based on the total weight of B).

[0051] Suitable auxiliary and additional substances D) include all auxiliary and additional substances known for polyurethane production. Such substances are known and are described, for example, in "Kunststoffhandbuch, Volume 7, Polyurethane", Carl Hanser Verlag, 3rd Edition 1993, Chapters 3.4.4, 3.4.6 to 3.4.11. These include, for example, surface-active substances, antifoaming agents, emulsifiers, viscosity reducers, dyes, pigments, flame retardants, and adhesion promoters.

[0052] The present invention further provides a polyurethane composite material comprising a polyurethane obtainable from the polyurethane reaction system according to the present invention and a fiber material.

[0053] The fibrous material is preferably at least one of inorganic fibrous material, organic fibrous material, metal fibrous material, natural fibrous material and combinations thereof, in particular glass fibrous material and carbon fibrous material or combinations thereof, particularly preferably carbon fibrous material.

[0054] The present invention provides a process for producing a polyurethane pultrusion according to the present invention, comprising the steps of: i) mixing components A), B), C) and optionally D) to obtain a polyurethane reaction system; ii) conveying the polyurethane reaction system from step i) into an injection box; iii) simultaneously with process step ii), introducing the fibrous material through an injection box to obtain the fibrous material impregnated in the polyurethane reaction system; iv) introducing the fibrous material impregnated with the polyurethane reaction system into a heated curing mold; v) curing the fibrous material impregnated with the polyurethane reaction system in a curing mold to obtain a polyurethane pultrusion; vi) extracting the polyurethane pultrusion from step v) out of the curing mold using an extraction mechanism; vii) removing the polyurethane pultrusion from the cured mold and cutting it to a desired length; The present invention further provides a process comprising:

[0055] The mixing of components A), B), C), and optionally D) may be accomplished in a manner conventional for the preparation of polyurethane reaction mixtures, for example, by high-pressure or low-pressure processes. It is preferred if components B), C), and optionally D) are premixed and the resulting mixture is mixed with component A).

[0056] The temperature during impregnation of the fibrous material in process step iii) is preferably between 0° C. and 75° C., particularly preferably between 10° C. and 50° C., very particularly preferably between 15° C. and 35° C. Curing step v) is preferably carried out at a curing mould temperature of between 140° C. and 220° C., the curing mould preferably comprising several zones with different temperatures, preferably three or four zones.

[0057] The fibrous material is in the form of continuous fibers. In the context of the present application, the term "continuous fibers" should be understood to mean fibers known to those skilled in the art, such as inorganic fibers, organic fibers, metal fibers, and natural fibers, preferably glass fibers and carbon fibers, and particularly preferably carbon fibers. The term "continuous fibers" should be understood to mean fibrous materials having a length of at least several meters. The fibers are, for example, unwound from a roll or spool. Fibre materials that can be used herein include individual fibers known as fibrous rovings, braided fibers, fibrous mats, laid fibrous scrims, and woven fibrous fabrics. In particular, in the case of fibrous composites, such as braided fibers, twisted fibers, or woven fibrous fabrics, shorter individual fibers may also be present among the individual fibers present in these fibrous composites. However, the fibrous composite itself must be in the form of a continuous material. In a preferred embodiment of the present invention, glass fibers are used in the form of fibrous rovings.

[0058] In a further preferred embodiment of the invention, process step iii) comprises passing not only the fibrous material but also so-called release layers through the injection box, these release layers preferably coming to form at least two outer sides of the final polyurethane pultrusion. In further processing of the polyurethane pultrusion according to the invention, this release layer may be removed from the outer sides to form at least two roughened surfaces, thus facilitating, for example, adhesive bonding of the polyurethane pultrusion.

[0059] The polyurethane pultrusions according to the invention may be used, for example, to manufacture reinforcing profiles or structural elements in vehicle construction, aircraft construction or in wind power plants. Such lightweight reinforcing profiles may be used, for example, to manufacture so-called "spar flanges" in the rotor blades of wind power plants.

[0060] The present invention will be elucidated in more detail in the following examples. [Example]

[0061] A pultrusion molding machine with a heatable mold with internal dimensions of 60 mm x 5 mm and an injection box connected upstream of the mold was used. Thus, right-angle profiles with a width of 60 mm and a wall thickness of 5 mm were produced. Carbon fiber roving (Pyrofil™ TRW 40 50L KNA, Mitsubishi Rayon Co., Ltd.) was used as the fiber material and pulled through the injection box and mold. The carbon fiber concentration in the final profile was approximately 65% ​​by volume. The polyol mixtures reported in Table 1 were mixed in each case with a specific amount of internal mold release agent and subjected to intensive stirring. These mixtures were mixed in each case with sufficient isocyanate at 23 °C using a low-pressure mixing device including a static mixer to achieve the respective NCO index reported in Table 1, and the resulting polyurethane reaction system was continuously injected into the injection box. The impregnated reinforcing fibers were continuously pulled from the heated mold by the pull-off mechanism of the pultrusion machine and cured. The temperature control of the mold was divided into three zones: Zone 1 (mold entrance in the take-off direction) had a temperature of 170°C, Zone 2 (mold center) had a temperature of 200°C, and Zone 3 (mold exit) had a temperature of 220°C. The final profiles were then cut to the desired length in a continuous fashion.

[0062] The following starting materials were utilized: Isocyanate building block A) MDI 1: Polymeric MDI with an NCO content of 32.4% by weight and a monomeric MDI content of 80% by weight. The total content of 2,4'-MDI and 2,2'-MDI is 25% by weight. Covestro Deutschland AG. Isocyanate Reactive Component B) Polyether polyol B1) Polyol 6: A polyether polyol obtainable by reacting glycerol (F=3) with propylene oxide in the presence of a KOH catalyst, followed by reacting the propoxylated intermediate with ethylene oxide to form a polyether polyol block copolymer, having an OHN=29 mg KOH / g and a propylene oxide (PO) content of 78.1 wt. % based on the mass of PO and EO employed, and an ethylene oxide (EO) content of 21.9 wt. % based on the mass of PO and EO employed. Polyether polyol B2) Polyol 2: Glycerol-started triol, propoxylated. OHN=1050 mg KOH / g Polyether polyol B3) Polyol 1: Glycerol-started triol, propoxylated. OHN=235 mg KOH / g Polyol 3: Glycerol-started triol, propoxylated. OHN=400 mg KOH / g Polyol 5: Propylene glycol-started diol, propoxylated. OHN=515 mg KOH / g Further polyether polyols Polyol 4: Propylene glycol-started diol, propoxylated. OHN=28 mg KOH / g Polyol 7: A polyether monol obtainable by reacting butyl diglycol (F=1) with propylene oxide and ethylene oxide in the presence of a KOH catalyst, followed by reacting this intermediate with propylene oxide to form a polyether monol block copolymer, having an OHN=33 mg KOH / g and a propylene oxide (PO) content of 52.9 wt.% based on the mass of PO and EO employed, and an ethylene oxide (EO) content of 47.1 wt.% based on the mass of PO and EO employed. Catalyst B4) Catalyst: Diisooctyl 2,2'-[(dioctylstannylene)bis(thio)]diacetate Desiccant B5) as a water binding agent Water Binder 1: UOP's MOLSIV™ L Powder Water binding agent 2: Incozol-2 (N-butyl-2(1-ethylpentyl)-1,3-oxazolidine) from Incorez Release agent C) Internal mold release agent (IMR): Luvotrent™ TL HB 550 from Lehmann & Voss for pultrusion.

[0063] All amounts in Table 1 are reported in parts by weight. Mechanical parameters were determined by the following methods. Transverse bending stress: DIN EN ISO 14125 Axial bending stress: DIN EN ISO 178 Lateral interlaminar shear strength (ILSS): DIN EN ISO 14130 Axial ILSS: DIN EN ISO 14130

[0064] Furthermore, the take-off force and take-off speed were determined in the pultrusion machine during the production of polyurethane pultrusions, and the fiber impregnation, surface quality and wear occurrence were visually evaluated.

[0065] The single-phase nature of the utilized isocyanate-reactive components was also examined visually. To this end, the isocyanate-reactive components utilized in Examples 1-6 were stored in clear plastic containers at room temperature for six months and visually inspected at regular intervals. Multiphase nature indicates the occurrence of any inhomogeneity, such as phase separation, turbidity, and droplet formation. Thus, the monophasic isocyanate-reactive components do not exhibit any of these effects over six months at room temperature. The monophasic isocyanate-reactive components are homogeneous, transparent liquids. Furthermore, the monophasic isocyanate-reactive components also do not exhibit any of the aforementioned effects of multiphase nature after centrifugation at 6000 rpm for 30 minutes.

[0066] [Table 1]

[0067] Example 1 corresponds to an inventive composition: the isocyanate-reactive component is solids-free and monophasic, and the pultrusion has good processability and good mechanical properties.

[0068] Example 2 shows a known system composition based on zeolite (Water Binding Agent 1), i.e., a solid-containing, and therefore phase-unstable, isocyanate-reactive component. The reaction system of the present invention has advantages over this known composition in that pumps and filters are not exposed to any solids, and transport and processability are easier / better.

[0069] Examples 3 and 4 show that System 1 and System 2 without the use of a water binder have poorer processability and poorer mechanical properties, demonstrating that a solids-free single-phase reaction system is not sufficient by itself to combine excellent processability with excellent mechanical properties of the resulting pultrusions.

[0070] Example 5 shows that the simple substitution of Water Binding Agent 1 for Water Binding Agent 2 (otherwise identical in composition to the isocyanate-reactive component of Example 2) results in a solids-free system, but this still does not ensure good processability and mechanical properties of the pultrusion. The system still remained multiphasic, with the aforementioned disadvantages during processing due to the polyether composition.

[0071] Example 6 similarly shows a solids-free single-phase system, but it is clear that only the inventive composition of component B) produces a pultrusion with excellent mechanical properties.

Claims

1. 1. A polyurethane reaction system comprising: an isocyanate component A), and Isocyanate-reactive components B) 3% to 13% by weight of a polyether polyol B1) having a hydroxyl number (OHN) of 20 mg KOH / g to 50 mg KOH / g, which polyether polyol B1) can be obtained by reacting a first H-functional starter compound having a functionality f of ≧2 to ≦4 with propylene oxide to form a first intermediate, and reacting said first intermediate with ethylene oxide to form a block copolymer, the mass fraction of propylene oxide being 60% to 90% by weight, based on the total of the ethylene oxide and polypropylene oxide used; 15% to 37% by weight of a polyether polyol B2) having a hydroxyl number (OHN) of 900 mg KOH / g to 1100 mg KOH / g, which can be obtained by reacting a second H-functional starter compound having a functionality f of ≧2 to ≦4 with a second alkylene oxide, 50% to 72% by weight of a polyether polyol B3) having a hydroxyl number (OHN) of more than 50 mg KOH / g and less than 900 mg KOH / g, which can be obtained by reacting a third H-functional starter compound with a third alkylene oxide; one or more catalysts B4), Desiccant B5), Including, the sum of the weight percentages of components B1) and B2) is 40% by weight or less relative to the sum of the amounts of B), C) and D), and the sum of the weight percentages of components B1), B2), B3), B4) and B5) is 90% by weight or more relative to the sum of the amounts of B), C) and D); an isocyanate-reactive component B); C) an internal mold release agent; Optionally further auxiliary and additional substances D), Including, the weight percent of components B), C) and optionally D) add up to 100 weight percent; The hydroxyl number (OHN) of the polyether polyols B1), B2) and B3) is determined using ISO 14900; Polyurethane reactive system.

2. 10. The polyurethane reaction system of claim 1, wherein said drying agent B5) is a trialkyl orthoformate, p-toluenesulfonyl isocyanate, oxazolidine, or a mixture thereof.

3. 3. The polyurethane reaction system according to claim 1 or 2, wherein the drying agent B5) is an oxazolidine, and the oxazolidine is 3-ethyl-2-methyl-2-(3-methylbutyl)-1,3-oxazolidine and / or N-butyl-2-(1-ethylpentyl)-1,3-oxazolidine.

4. A polyurethane composite material comprising a polyurethane obtainable from the polyurethane reaction system according to any one of claims 1 to 3 and a fibrous material.

5. 5. A pultrusion process for producing the polyurethane composite of claim 4, comprising: i) mixing said components A), B), C) and optionally D) to obtain the polyurethane reaction system of any one of claims 1 to 3; ii) conveying the polyurethane reaction system from step i) into an injection box; iii) simultaneously with process step ii), introducing a fibrous material through the injection box to obtain a fibrous material impregnated in the polyurethane reaction system; iv) introducing the fibrous material impregnated with the polyurethane reaction system into a heated curing mold; v) curing the fibrous material impregnated with the polyurethane reaction system in the curing mold to obtain a polyurethane pultrusion; vi) extracting the polyurethane pultrusion from step v) out of the curing mold using an extraction mechanism; vii) removing the polyurethane pultrusion from the cured mold and cutting it to a desired length; The pultrusion process includes:

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