DE3029272A1 - Water-tight fine celled polyurethane elastomers - e.g. for automobile shock absorbers reacting poly isocyanate and poly:hydroxy cpd. in the presence of polysiloxane cpd. - Google Patents

Abstract

Water-tight, fine celled polyurethane elastomers with a density of 0.3-0.8 g/cm3 are made by (opt. stagewise) reaction of (A) organic polyisocyanates, (B) polyhydroxy cpds. with a mol. wt. of 400-5000; (C) water, (D) opt. organic chain lengthenings cpds. with at least 2 NCO-reactive H atoms and a mol. wt. of 32-400, (E) opt. catalysts and/or other adjuvants and aids, using an equiv. ratio NCO gps. to NCO-reactive gps. of 0.95:1 to 1.15: 1, and (F) with the addn. during one of the process stages of 0.1-3 wt.% esp. 0.3-2 wt.% of one or more polysiloxanes (I) in which m is 1-500, Z (same or different) are 1-5C alkyl, 6-15C aryl or siloxy gp., X is as for Z or H-Y-R- gp., Y is -NR'-, -O-, -CO-O- or -S-, R is 1-6C alkylene gp. opt. contg. a hetero atom, R' is H, 1-6C alkyl or 5-9C cycloalkyl gp., and if X is H-Y-R, the organo functional silicone may be converted into NCO or OH-functional silicone prepolymers with polyisocyanates and opt. further polyvalent chain lengthening agents. Presence of the (I) gives fine-celled, uniform cell structure with largely closed cell configuration. The foams are water- tight without the necessity for formation of a surface skin as with integral foams. Prods. are useful as components in automobile shock absorbers, dampers, bump rubbers and suspension parts.

Description

Process for the production of waterproof moldings

cellular polyurethane elastomers and their use as suspension elements The invention relates to an improved method for producing waterproof cellular polyurethane elastomers made from polyisocyanates, higher molecular weight polyhydroxyl compounds, Water as a chain extender and blowing agent, and optionally additional ones Chain extenders and is characterized by the use of certain silicone derivatives. The new process allows the production of waterproof, cellular moldings, without a skin having to be formed on the surface, as is the case, for example is known from integral skin foams.

Moldings made from cellular polyurethane elastomers are used in industry in a manner known per se from polyisocyanates, higher molecular weight polyhydroxyl compounds, Water as a chain extender and blowing agent and, if necessary, additional ones Chain extension means built up. Differentiate from polyurethane foams cellular polyurethane elastomers due to their significantly higher density (approx. 0.3 up to 0.8 g / cm3), better physical properties and the technical properties that result from them Possible applications. Particularly high-quality cellular polyurethane elastomers, such as one from 1, 5-naphthylene diisocyanate, a linear ethanediol polyadipate (Molecular weight approx. 2000) and the product made with water are becoming large-scale Used, among other things, as a buffer and damping material.

A large area of application is in the automotive industry, where such materials are primarily used as damping and stop buffers will.

Particularly in the case of strut constructions, it is advantageous to use the Additional springs made from rubber by those made from cellular polyurethane elastomers to replace, since this is from elastic compact materials by a substantially differentiate between higher deformability. Deformations of up to 80% are in practice (e.g. additional springs in automobiles) are quite possible.

The suspension elements made from cellular polyurethane elastomers are in automobiles within the overall strut construction, consisting of Shock absorber, spiral spring and the buffer made of cellular elastomer on the piston rod the shock absorber pushed. With this type of arrangement there is now often the Risk of contamination of the buffers, as in the damping buffers due to their predominantly open-cell pore structure splash water and dust can penetrate. Above all This can change the suspension behavior at low temperatures; apart become of it as a result of the influence of water and dirt too premature corrosion and abrasion on the piston rod of the shock absorber observed.

In the German patent application P 29 20 502.5 it is already proposed improved cellular polyurethanes with a density of 0.45-0.8 from aromatic Polyisocyanates, polyhydroxyl compounds with a molecular weight of 400 to 6000, water, optionally glycols with a molecular weight of 62 to 250, and with the addition of 0.1 to 0.8% by weight of aromatic, diprimary diamines. The addition of aromatic diamines allows molded parts to be obtained significantly improved heat resistance and under lower mold internal pressure manufacturing too. However, such cellular polyurethanes lack water tightness with flex loads. It has also been shown that the security of the achievement very uniform and at the same time very fine-cell structures thanks to the Process according to the invention is achieved, as well as easy demoldability without Risk of cracking due to bursting, as well as an even surface skin.

The object of the present invention was therefore to provide suspension elements to make available, while maintaining the usual recipes and by means of the processing equipment customary in practice can and at the same or even improved mechanical properties (e.g. suspension properties) are also waterproof. As low as possible Water absorption, even with multiple alternating loads, is an essential property for use as buffer and suspension elements in the automotive sector. Simultaneously should be a hydrophobic, cellular polyurethane elastomer that is as uniform as possible (preferably based on polyester urethane) in safe and simple process engineering will. The thermal stability and the dynamic property values should also be increased. In addition, a method was to be found with which the waterproof, very Even fine-cell polyurethane elastomers with a density of 0.3 to 0.8 g / cm3 also Safe, reproducible and easy to use on simpler machines of the agitator type can be made in molds.

Surprisingly, it has been found that the stated objectives can be achieved can, if one in the production of the cellular elastomers, preferably in the Prepolymer stage, small amount of substantially linear polysiloxanes, preferably organofunctional derivatives, optionally as NCO or OH silicone prepolymers, used. In addition, such additives increase the coefficient of sliding friction of cellular elastomers are reduced, so that under dynamic stress on the spring element the material abrasion on the piston rod is significantly reduced. As special cheap Such a waterproof, very fine-celled polyurethane elastomer has proven itself proved, in which during the polyurethane synthesis at the same time a small amount is used in aromatic diamines, as this increases the uniformity, heat resistance, dynamic properties and the reproducibility of production are essential improved and the handling of the polyurethane reaction mixture because of the lower Pressure, the easier demolding and the smoother surface is facilitated.

The invention thus provides a process for the production of a waterproof, fine-cell polyurethane elastomer with a density of 0.3 to 0.8 g / cm3 by optionally stepwise reaction of A) organic polyisocyanates, in particular aromatic polyisocyanates, particularly preferably diisocyanates, B) with polyhydroxyl compounds a molecular weight of 400 to 6000, preferably 800 to 4000, C) water, and optionally D) organic chain extenders, preferably glycols with a molecular weight of 62 to 250 and / or aromatic diamines with a molecular weight of 108 to 400, optionally in the presence of E. ) Catalysts and / or other auxiliaries and additives known per se, the equivalence ratio between isocyanate groups and isocyanate-reactive compounds in the overall formulation between 0.95: 1 and 1.15: 1, preferably between 1: 1 and 1.1: 1 is, which is characterized in that one of the method stages F) the reaction mixture 0.1 to 3 wt .-%, preferably 0.3 to 2 wt .-%, of one or more polysiloxanes of the general formula in which m is an integer between 1 and 500, preferably between 5 and 250, the radicals Z can be identical or different and for C1- to C5-alkyl, C6- to C15-aryl or siloxyl radicals, but preferably for methyl -and / or phenyl radicals and the radicals X have the same meaning as Z or represent HYR groups (however, the polysiloxane in total preferably contains at most 5, particularly preferably at most 2, HYR groups), where Y is -NR'-, -O-, or -S-, preferably -0-, R is a C1- to C6-alkylene radical containing heteroatoms, preferably a methylene radical, and R 'is hydrogen, a C1 to C6-alkyl radical or a C5- to Cg-cycloalkyl radical, where, in the case of X being HYR, these organofunctional silicones can be converted into NCO- or OH-functional silicone prepolymers with polyisocyanates and optionally excess chain extenders.

The invention also relates to the use of the waterproof, fine-cell polyurethane elastomers, which were produced using this process, in suspension and damping elements.

The cellular polyurethanes can be produced according to conventional methods Procedures and from starting materials A - E known per se.

As polyisocyanates A) are aliphatic, cycloaliphatic, araliphatic, aromatic and heterocyclic polyisocyanates into consideration, e.g. by W. Siefken in Justus Liebig's Annalen der Chemie, 562, Pages 75 to 136, for example those of the formula Q (NCO) n in which n is 2 to 4, preferably 2, and Q is an aliphatic hydrocarbon radical with 2 to 18, preferably 6 to 10, carbon atoms, a cycloaliphatic hydrocarbon radical with 4 to 15, preferably 5 to 10, carbon atoms, an aromatic hydrocarbon radical with 6 to 15, preferably 6 to 13, carbon atoms, or an araliphatic hydrocarbon radical with 8 to 15, preferably 8 to 13, carbon atoms, e.g. 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, 1,12-dodecane diisocyanate, furthermore cycloaliphatic Diisocyanates in any mixtures of their stereoisomers, e.g. cyclobutane-1,3-diisocyanate, Cyclohexane-1,3- and 1,4-diisocyanate, 1-isocyanato-3, 3, 5-trimethyl-5-isocyanatomethyl-cyclohexane (DE-Auslegeschrift 1 202 785, US Patent 3 401 190), 2,4- and 2,6-hexahydrotolylene diisocyanate, Hexahydro-1,3- and / or 1,4-phenylene diisocyanate, perhydro-2,4'- and / or -4,4'-diphenylmethane diisocyanate; In particular, however, aromatic diisocyanates are suitable, e.g. 1,3- and 1,4-phenylene diisocyanate, 2,4- and 2,6-tolylene diisocyanate, as well as any mixtures of these isomers, diphenylmethane-2,4'- and / or -4,4'-diisocyanate, including its alkyl- and chlorine-substituted ones Derivatives and naphthylene-1,5-diisocyanate.

Also possible are, for example: triphenylmethane-4,4'4 "-triisocyanate, Polyphenyl-polymethylene polyisocyanates, as produced by aniline-formaldehyde condensation and subsequent phosgenation and, for example, in GB patents 874 430 and 848 671 are described, m- and p-Isocyanatophenylsulfonyl-isocyanate U.S. Patent 3,454,606, perchlorinated aryl polyisocyanates such as them e.g.

in DE-Auslegeschrift 1 157 601 (US Pat. No. 3,277,138) are, carbodiimide-containing polyisocyanates, as they are in the DE patent 1 092 007 (US Pat. No. 3,152,162) and in German Offenlegungsschrift 2,504 400, 2,537,685 and 2,552,350, norbornane diisocyanates according to U.S. Patent 3,492,330, polyisocyanates containing allophanate groups, such as those described, for example, in the GB patent specification 994 890, BE patent specification 761 626 and NL patent application 7 102 524 are described, polyisocyanates containing isocyanurate groups, such as they are e.g. in US patent specification 3 001 973, in DE patent specifications 1 002 789, 1 222 067 and 1 027 394 as well as in DE-Offenlegungsschriften 1 929 034 and 2 004 048, polyisocyanates containing urethane groups, as e.g. in BE Patent 752 261 or in U.S. Patent Nos. 3,394,164 and 3,644 457 are described, polyisocyanates containing acylated urea groups according to DE Patent 1,230,778, polyisocyanates containing biuret groups, such as them e.g.

in U.S. Patents 3,124,605, 3,201,372, and 3,124,605, and in GB 889 050, by telomerization reactions polyisocyanates such as those described in U.S. Patent 3,654,106 , polyisocyanates containing ester groups, such as are e.g.

in GB patents 965,474 and 1,072,956, in US patent 3,567,763 and in DE patent specification 1,231,688 are reaction products of the above-mentioned isocyanates with acetals according to DE patent specification 1 072 385 and polyisocyanates containing polymeric fatty acid esters according to US Pat. No. 3 455 883.

It is also possible to use the technical isocyanate production resulting distillation residues containing isocyanate groups, if appropriate solved in one or more of the aforementioned polyisocyanates to be used. Furthermore is it is possible to use any mixtures of the aforementioned polyisocyanates.

Aromatic diisocyanates are preferred, such as 1,5-naphthylene diisocyanate, 4,4'-Diisocyanatodiphenylmethane, optionally with minor amounts of his 2,4'-isomers, also 2,4- and 2,6-toluylene diisocyanate and mixtures thereof are used.

4,4'-Diisocyanatodiphenylmethane and in particular 1, 5-naphthylene diisocyanate.

As higher molecular weight polyhydroxyl compounds B) are preferred compounds of molecular weight having an average of 2 to 3 hydroxyl groups 400 to 6000, in particular -800 to 4000, are used, e.g.

Polyesters, polyethers, polythioethers, polyacetals, polycarbonates and Polyester amides, such as those used for the production of homogeneous and cellular polyurethanes are known per se.

Such connections are e.g. in the German Offenlegungsschriften 2,550,796, 2,550,797, 2,624,527, 2,638,759, 2,302,564 (U.S. Patent 3,963,679), 2,402,840 (U.S. Patent 3,984,607), 2,457,387 (U.S. Patent 4,035,213), 2,829,670, 2,830,949 and 2,830,953 described in detail.

According to the invention, polyesters based on adipic acid are preferred and aliphatic diols or diol mixtures, e.g. ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol or neopentyl glycol, but polyethers are also available Well suited based on tetramethylene oxide diols.

In the process according to the invention, compounds can optionally also be used D) with at least 2 isocyanate-reactive hydrogen atoms and a molecular weight of 32 to 400 can also be used.

In this case too, this is understood to mean hydroxyl groups and / or Compounds containing amino groups and / or thiol groups and / or carboxyl groups, preferably hydroxyl-containing compounds, such as those used as chain extenders or crosslinking agents are known and are described in the above-mentioned publications will. These compounds generally have 2 to 4 isocyanate-reactive compounds Hydrogen atoms, preferably 2 or 3 reactive hydrogen atoms.

Examples of compounds containing hydroxyl groups are ethylene glycol, Propylene glycol, trimethylene glycol, butanediol-1,4 and -2,3, hexanediol-1,6, neopentylglycol, Diethylene glycol, dipropylene glycol, diethanolamine, triethanolamine, dipropanolamine and called N-methyl-diethanolamine. Other polyols with a molecular weight between preferably 62 to 250 can also be used.

Particularly advantageous results for the production of cellular polyurethane elastomers are achieved if one according to the German patent application P 29 20 502.5 in the reaction mixture from higher molecular weight Polyols, excess Polyisocyanates and optionally other low molecular weight chain extenders in addition to water, minor amounts, based on the NCO content of the NCO prepolymers or the reaction mixture, aromatic diamines are also used as compounds D). The aromatic diamines are those with a molecular weight of 108 to 400, preferably from 108 to 250, is used. In particular, an additive has an effect from 0.1 to 0.8% by weight, preferably 0.15 to 0.5% by weight, of aromatic diamines in the entire reaction mixture very favorably on a uniform cell structure and an improved thermal stability.

Examples of aromatic diamines are bisanthranilic acid esters according to DE-Offenlegungsschriften 2,040,644 and 2,160,590, 3,5- and 2,4-diaminobenzoic acid esters according to DE-Offenlegungsschrift 2 025 900, which in DE-Offenlegungsschriften 1 803 635 (U.S. Patents 3,681,290 and 3,736,350), 2,040,650 and 2,160,589 ester group-containing diamines, the ether group-containing diamines according to DE-Offenlegungsschriften 1,770,525 and 1,809,172 (U.S. Patents 3,654,364 and 3,736,295), optionally 2-halo-1,3-phenylenediamines substituted in the 5-position (DE-Offenlegungsschriften 2 001 772, 2 025 896 and 2 065 869), 3,3'-dichloro-4,4'-diamino-diphenylmethane, 2,4- and / or 2,6-toluenediamine and substituted by 1 or 2 C1-C3-alkyl groups Tolylenediamine, e.g.

3,5-diethyl-2,4- or -2,6-diaminotoluene, 4,4'-diaminodiphenylmethane and 2,4'-diaminodiphenylmethane and their substituted with 1 to 4 C1-C4-alkyl groups Derivatives, e.g. 3,3'-dimethyl-4,41-diaminodiphenylmethane, 3,3,5,5'-tetraethyl-4,4'-diaminodiphenylmethane, 3,3'-Diisopropyl-4,4'-diaminodiphenylmethane etc., whose substituted with 1-4 chlorine groups Derivatives, 4,4'-Diaminodiphenyldisulfide (DE-Offenlegungsschrift 2 404 976), Diaminodiphenyldithioether (DE-Offenlegungsschrift 2,509,404) and aromatic substituted by alkylthio groups Diamine (DE-Offenlegungsschrift 2 638 760) called. Preferred diamines are those used which are similar in structure to the diisocyanate used: Tolylenediamine and substituted tolylenediamines are preferred for the reaction applied with 2,4- and 2,6-tolylene diisocyanate, while prepolymers based on 4,4'-Diisocyantodiphenylmethane preferably with - optionally substituted -diaminodiphenylmethanes implemented. Naphthylene-1,5-diisocyanate is advantageous with 1,5-diaminonaphthalene combined, but also the combination of 1,5-diaminonaphthalene with 4,4'-diisocyanatodiphenylmethane makes valuable products. It is surprising that even very small amounts of diamine, preferably 0.15 to 0.5% by weight, based on total polyurethane, for the purposes of the present invention Invention work.

4,4'-Diaminodiphenylmethane and its methyl and chlorine substitution products are preferred, optionally in a mixture with 2,4'-diamino-diphenylmethane, 1,5-diaminonaphthalene and the 2,4- and / or 2,6-toluenediamines.

The combination of 1,5-naphthylene diisocyanate / 1,5-diamino-naphthalene is very particularly preferred.

The diprimary diamine can be used in any of the reaction batches Process stage - e.g. mixed with one of the starting components - can be added. It is generally most convenient to use the diamine in the form of a solution in the part of the higher molecular weight polyhydroxyl compound used in the 2nd process step to use. It is often advantageous in terms of process technology to use this diamine solution in a separate process step with a small amount of the aromatic used To put diisocyanate, the molar ratio diamine: diisocyanate between 2: 1 and 10: 9 and due to the practically selective reaction between NCO and NH2 groups in the polyol in situ amine ureas of the general formula NH2-Q'-NHiCO-NH-Q-NH-CO-NH-Q'-NH7nH are formed in an amount of about 0.2 to 1% by weight, based on polyurethane, in which n is an integer between 1 and 11, Q is the remainder which by removing the NCO groups from the diisocyanate and Q 'for the remainder which is formed when the amino groups are removed from the diamine.

A second preferred way of working is to have the diamine already the NCO prepolymer of the 1st process stage, possibly already during its production, to be added, an NCO prepolymer modified with small amounts of urea groups is obtained. According to a variant of this procedure, the diamine is set in situ in the prepolymer by replacing the diamine with an equivalent amount of Adds water, which converts the diisocyanate into the corresponding diamine with saponification converts.

In the process according to the invention, the under E) listed catalysts, other blowing agents, foam stabilizers, pigments, Stabilizers against aging and weathering, as well as others known per se Auxiliaries and additives are also used, as they are in the above-mentioned publications are described in detail and are generally known.

Surface-active additives such as emulsifiers and foam stabilizers can also be used.

The sodium salts of castor oil sulfonates, for example, are used as emulsifiers or salts of fatty acids with amines such as oleic diethylamine or stearic acid Diethanolamine is an option. Also alkali or ammonium salts of sulfonic acids such as of didecylbenzenesulfonic acid or dinaphthylmethanedisulfonic acid or of fatty acids such as ricinoleic acid or of polymeric fatty acids can be used as surface-active additives can also be used.

In the process according to the invention, preference is given to both water and Chain extenders as well as used as blowing agents. Besides water you can however, the chain extenders mentioned by way of example can also be used. The water is generally in an amount of 0.5 to 2 wt .-%, based on Total mixture of all other reactants, preferably in an amount of 0.7 up to 1.2% by weight, used. The water preferably arrives in the form of an aqueous one Solution of an emulsifier of the type exemplified above is used. Through this an intimate mixing of the water with the other reactants guaranteed.

Preferably, in the production of the cellular polyurethane elastomer moldings worked according to the known prepolymer process, i.e. it is made from the higher molecular weight Polyol and the diisocyanate in an NCO / OH equivalent ratio of 1.5: 1 to 3: 1, preferably 1.8: 1 to 2.2: 1 a prepolymer containing isocyanate groups is prepared, which is then reacted with the stated amount of water. A work the known one shot "process is possible, but by no means preferred. If organic chain extenders are also used, these come in in the amounts customary in the production of polyurethane elastomers or in only small amounts modifying amounts, as described for the aromatic diamines, are used.

The polyurethane elastomers are also produced under Use of such amounts of the individual reactants that an isocyanate number from 100 to 115. This applies both to the preferred conversion of NCO prepolymers with water as well as for the proportions of the individual reactants according to the invention less preferred "one shot" method.

The amount of the reaction mixture to be charged into the mold becomes so dimensioned so that the above-mentioned density of 0.3 to 0.8 g / cm results. For the production The reaction mixtures and the filling of the mold can be done using mechanical equipment such as those described in U.S. Patent 2,764,565.

Details of processing facilities that are also in accordance with the invention are in the Kunststoff-Handbuch, Volume VII, published by Vieweg and Höchtlen, Carl-Hanser-Verlag, Munich 1966, e.g. on pages 121 to 205 described.

Metal, e.g. aluminum, or plastic, e.g. Epoxy resin, in question. The foamable reaction mixture foams up in the mold forms the shaped body.

Essential to the invention is the use of 0.1 to 3% by weight, preferably 0.3 to 2% by weight, based on the total reaction mixture, of one or more polysiloxanes (F) of the general formula (I) defined above. The polysiloxanes can be used at any point during the manufacture of the cellular polyurethane elastomer They are preferably added - if by the "one shot" process is worked - together with the polyol component. In the prepolymer process they are preferably either the NCO prepolymer of the 1st process stage or the Polyol components used in the 2nd process stage are mixed in.

Polysiloxanes of the general formula (I) in which X has the same meaning like Z has long been known as chemically inert silicone oils. Your manufacture and physicochemical properties of these products are described in W. Noll, "Chemie and Technologie der Silicones ", 2nd edition 1968, Verlag Chemie, Weinheim / Bergstrasse, BRD, described in detail. For the purposes of the present invention, this includes especially those silicone oils that have an average of about 5 to 400, particularly preferably 20 to 250 siloxane units and in which X and Z for methyl groups or proportionally (up to approx.

50%) also stand for phenyl groups. Special polysiloxanes of these Art are also described in DE-OS 2 232 525, for example. Silicone oils are in the invention Process preferably only in amounts of 0.1 to 2% by weight, in particular 0.3 to 1% by weight, based on the total reaction mixture, added, since higher proportions a deterioration in the mechanical properties of the moldings can occur.

According to the invention, however, those polysiloxanes are preferred which at least one, preferably 1 to 5, particularly preferably 2 against isocyanates reactive, "organofunctional" groups, in particular hydroxyl or amino groups, have ("organopolysiloxanes").

Connections of this type are in the German Auslegeschriften 1 114 632, 1 190 176 and 1 248 287, as well as the French patent specification 1 291 937.

They contain at least two silicon-bonded carbofunctional Groups with isocyanate-reactive hydrogen atoms. The carbofunctional Groups are preferably aliphatic hydrocarbon radicals, optionally containing heteroatoms with 1 to 6 carbon atoms, the at least one hydroxyl, carboxyl, mercapto or primary or have secondary amino groups - Such carbofunctional radicals are for example Hydroxymethyl -CH20H Hydroxylbutyl - (CH2) 4OH B-Hydroxyethyloxymethyl -CH2-O-CH2-CH2-OH ß-Hydroxyethylmercaptomethyl -CH2-S-CH2-CH2-OH ß, -dihydroxypropylmercaptomethyl -CH2-S-CH2-CHOH-CH2OH mercaptomethyl -CH2SH ß-mercaptoethyl mercaptomethyl -CH2-S-CH2-CH2-SH B-carboxylethyl -CH2-CH2-COOH aminomethyl -CH2-NH2 -aminobutyl - (CH2) 4-NH2 n-butylaminomethyl -CH2-NH-C4H9 or Cyc lohexylaminomethyl -CH2-NH-C6H11 The organopolysiloxanes are accessible by known methods. For example, the particularly suitable Hydroxymethylpolysiloxanes by direct reaction of bromomethylpolysiloxanes with alcoholic potassium hydroxide solution can be represented. 4-aminobutylpolysiloxanes are about the hydrogenation of the easily accessible nitriles produced, corresponding carboxyl derivatives by saponification of the cyanoalkyl silicon compounds. Aminomethylsiloxanes are by amination of the halomethylsilicon compounds with ammonia or primary Obtained amines.

In many cases, the functional groups are initially attached to low molecular weight Siloxanes introduced; the products obtained in this way are then used by the well-known Equilibration reaction converted into higher molecular weight polysiloxanes.

Organopolysiloxanes with at least 2, in particular 5 to 100, siloxane groups and having a molecular weight of 194 to 8000, particularly preferably between 800 and 3000. Also preferred are essentially linear organofunctional polysiloxanes and those with terminal hydroxyl or Amino groups.

For example, the following organofunctional polysiloxanes are suitable for the process according to the invention: HO-CH2-Si (CH3) 2-O [Si (CH3) 2-O] n-Si (CH3) 2-CH2OH n = 1 to 100 n = 1 to 100 n = 5 to 60 or The organopolysiloxanes particularly preferred according to the invention correspond to the general formula n = 5 to 30 They are obtained in a manner known per se by equilibrating 1,1,3,3-tetramethyl-1,3-hydroxymethyldisiloxane of the formula with octamethylcyclotetrasiloxane in the presence of sulfuric acid or by the process of DE-AS 1,236,505.

The organopolysiloxanes can be used directly in the process according to the invention are used as such. However, it is preferred to have them in an upstream First to convert the process step into a prepolymer. Be for this purpose it with one of the above-mentioned polyisocyanates in an equivalent ratio of NCO / active H from about 1.5: 1 to 3: 1, preferably about 2: 1, prepolymerized. Particularly preferred is to convert the NCO prepolymer thus obtained in a further step with a low molecular weight and / or higher molecular weight polyol into an OH prepolymer and only this the reaction mixture for the production of cellular To add moldings.

The reaction between the organofunctional polysiloxane and the Polyisocyanate is preferably carried out in the temperature range between 30 and 100 ° C., if appropriate using suitable catalysts such as organotin compounds such as tin (II) acetate, tin (II) octoate, tin (II) alkyl hexoate or dibutyl tin diacetate.

If appropriate, excess amounts of polyisocyanate used can if appropriate, removed by thin-film distillation before the next reaction stage will.

However, it is also possible to use any excess to leave unreacted polyisocyanate in the reaction mixture and this mixture to be fed to the next reaction stage.

This next reaction stage consists in the reaction of the NCO-polysiloxane prepolymers with alcohols or amino alcohols which are at least difunctional in the sense of the isocyanate polyaddition reaction. As already mentioned, these reaction components are at least difunctional, preferably trifunctional, compounds of the molecular weight range 62 to 5000, preferably 105 to 300, preferably apart from alcoholic, ie aliphatically bound, hydroxyl groups, as well as primary or secondary, in the sense of the isocyanate addition reaction non-aromatically bonded amino groups do not have any other isocyanate-reactive groups. However, in the sense of the isocyanate addition reaction, the compounds can contain indifferent heteroatoms, for example in the form of ether bridges, tertiary nitrogen atoms, amide or ester groups. Particularly preferred compounds of the type mentioned are those which have isocyanate-reactive groups of different reactivity, such as, in particular, amino alcohols with one primary or secondary amino group and two alcoholic hydroxyl groups. Typical examples are The alkoxylation products of these compounds mentioned by way of example can also be used, but are less preferred. Also suitable are, for example, the amino alcohols described in German patent application P 29 36 239.8 or the hydrogenation products listed in DE-OS 2 756 270, as well as hydroxy- and / or aminopolyhydroxy-functional compounds based on carbohydrates, for example glucosamine and galactosamine; however, the use of these compounds is less preferred than the starting materials mentioned by way of example at the beginning.

In the production of the reaction products from the NCO-polysiloxane prepolymer and the polyol, the starting materials are generally in an equivalent ratio between isocyanate groups and active hydrogen atoms from 1: 1.5 to 1: 6, preferably 1: 2 to 1: 4 used.

An NCO / NH ratio of about 1: 1 is particularly preferred. The reaction is generally carried out in the temperature range between 30 to 100 ° C, optionally with the use of those already mentioned above by way of example Isocyanate addition reaction accelerating catalysts. The OH prepolymers thus obtained preferably have a hydroxyl functionality of 2 to 4, a content of terminal Hydroxyl groups from 0.8 to 5 and a content of structural units of the formula -O-Si (R) 2 from 30 to 90% by weight.

Particularly good results are obtained when one in the invention Process organopolysiloxanes (which if necessary modified in the manner described were used in combination with the above-mentioned inert silicone oils (X = z), the weight ratio of the two polysiloxane components being between 4: 1 and 1: 4, particularly preferably between 2: 1 and 1: 2.

A further improvement in the properties of the invention manufactured Shaped body is achieved if you have it on the surface with a continuous, dense, non-porous skin with a thickness of 0.05 to 1 mm, preferably 0.1 up to 0.5 mm, particularly preferably 0.2 to 0.3 mm, made of polyurethane or polyurethane urea as a seal.

The production of the skin on the surface of the molded body can be done by Dipping or spraying the molded part, but preferably by spraying the mold itself, in the so-called in-mold coating process. Everyone is eligible known 1 or. 2-component polyurethane paints based on the above Starting compounds, but consisting of aliphatic or cycloaliphatic compounds existing compositions are preferred. For ecological considerations and reasons To protect the environment, aqueous solutions or dispersions of polyurethane or Polyurethane ureas preferred, with ionic and emulsifier-free products Reasons of liability are particularly preferred.

Those to be used in the method according to the invention for surface sealing One- and two-component polyurethanes are used in paint and coating technology known per se. The so-called "two-component polyurethanes" are reactive systems which, for example, from a pre-adduct containing isocyanate groups and one suitable chain extender (usually an aromatic diamine), which separately or together, diluted with a solvent, on the to be sealed Shaped bodies are applied by dipping or spraying.

Paints of this type are for example in the German patents 838 826, 872 268, DE-AS 1 023 449, DE-AS 1 240 656 (US patent 3,281,396) and in particular DE-OS 1 570 524 (US Pat. No. 3,475,266).

Conversely, it is of course also possible to use two-component polyurethanes from a low molecular weight polyisocyanate and a relatively high molecular weight pre-adduct build up which still has isocyanate-reactive groups. Such a thing The system is described, for example, in DE-OS 2 221 756 (US Pat. No. 3,904,796).

In contrast to the two-component polyurethanes that have been known for a long time The so-called one-component polyurethanes are the newer state of the art.

These high molecular weight products are already fully reacted by converting polyhydroxyl compounds, in practice mainly dihydroxypolyesters or dihydroxy polyethers, mixed with glycols, preferably ethylene glycol or Butanediol, with aromatic diisocyanates, preferably 4,4'-diphenylmethane diisocyanate, obtain. These are essentially linear and can be produced both in the melt and in solution Polyurethanes are used in the form of solutions or solvent mixtures, which contain dimethylformamide and / or other highly polar compounds. An advantage of one-component polyurethanes is their practically unlimited pot life. In addition to the So-called aromatic one-component polyurethanes composed of aromatic diisocyanates The state of the art also includes the so-called aliphatic one-component polyurethanes; these are polyurethane ureas made from higher molecular weight dihydroxy compounds, aliphatic diisocyanates and aliphatic diamines or

Bishydrazides, bissemicarbazides and bis-carbazic acid esters as chain extenders. These aliphatic one-component polyurethanes are made from solvent mixtures, which contain secondary or primary alcohols in addition to aromatic hydrocarbons, applied.

According to the invention, however, it is preferred for surface sealing aqueous solutions and especially film-forming aqueous dispersions of polyurethanes or polyurethane ureas, as they are also used in the coating industry are known per se.

The polyurethane dispersions can be anionic, cationic and / or Contain nonionic dispersion centers, possibly also external emulsifiers.

Suitable aqueous polyurethane dispersions and solutions are, for example by D. Dieterich et al. in J. Oil Col. Chem. Assoc. 1970, 53, pp. 363-379, in Die Angewandte Makromolekulare Chemie, 1972, 26, pages 85-106, in Angewandte Chemie 1970, 82, pages 53-63, in US Pat. No. 4,086,193 (ionic dispersions), and in US Pat German Offenlegungsschrift 2,550,860, 1,495,745 (U.S. Patent 3,479,310), 1,495,770 (U.S. Patent 3,535,274), 1,495,847 (Can. Patent 764,009), 1,770,068 (U.S. Patent 3,756 992), 2,314,512, 2,141,807, 2,314,513, and 2,343,294 (U.S. Patent 3,989,869).

Aqueous polyurethane solutions are also used in the French Patents 2,308,646 and 2,331,581 and in DE-OS 2,730,514.

Preferred polyurethane dispersions are those made from polyhydroxypolyesters, Hexane and / or isophorone di isocyanate and ethylenediamine ethylsulfonate of the formula H2N-CH2 -CH2-NH-CH2-CH2 -S03Na According to the invention, it is often preferred to use such aqueous Use polyurethane dispersions or solutions that are subsequently crosslinkable are. This can e.g.

by introducing N-methylol groups (e.g. by treatment with Formaldehyde) happen, which - preferably in the presence of acidic catalysts - Crosslink in a known manner with the formation of methylene groups.

The surface sealing of the moldings is produced by subsequent application of the coating agents or Dispersions on the prefabricated shaped body or preferably by coating the inside of the mold before filling the mold with one of the examples mentioned Coating agents or with one of the dispersions mentioned by way of example. To This coating of the inner wall of the mold is first the skin by reacting respectively.

Drying of the coating produced. Generally they come Coating agents or dispersions are used in such amounts that a dense Skin with a thickness of 0.05 to 1 mm, preferably 0.1 to 0.5 mm, particularly preferred 0.2 to 0.3 mm results.

The moldings produced according to the invention are particularly suitable as suspension elements, including damping and stop buffers of all kinds, as well as Seals for motor vehicles, in particular automobiles.

The following examples explain the process according to the invention. Unless otherwise stated, the quantities given are parts by weight or percentages by weight to understand.

The experiments were carried out on agitator machines such as those used for processing of liquid polyurethane systems are common (SK or EZ-AB machines from Hennecke).

Buffer elements with a density of approx. 500 were used as molded parts g / dm3 in appropriate forms, the filling openings through a lid over toggle levers were closed. On the coated or uncoated buffer elements was the water absorption according to different degrees of deformation, partly before and determined after dynamic testing under water.

The test specimens for determining the dynamic properties were Taken from cuboid shaped parts.

The steel mold had a square plan of 120 x 120 mm, a height of 100 mm and was closed at the top by a steel plate, which was pressed onto the 1 cm wide edge of the mold by toggle levers.

The silicone oil used in Example 1 corresponds to the general formula where m has an average value of about 200.

The organopolysiloxane used in Examples 1, 2 and 3 has the general formula where m has an average value of 10 to 13.

This organopolysiloxane is also used in the production of the Organopolysiloxane prepolymers used in other examples.

Example 1 a) Comparative experiment: A prepolymer composed of 100 parts was obtained of a linear ethanediol polyadipate (molecular weight 2000) and 24 parts of 1,5-naphthylene diisocyanate manufactured.

Then 2.15 parts of a 50% strength aqueous solution of a fatty acid sulfonate were added intensively mixed with 124 parts of the prepolymer and filled into the 70 "C warm mold. The molded part obtained after a heating time of 30 minutes at 90.degree. C. showed im Pressure test under water after several deformations showed considerable water absorption. The measured values determined are compiled in Table 1.

b) Process according to the invention: First, 100 parts of the said linear ethanediol polyadipate with the amount of organopolysiloxane given in Table 1 and / or silicone oil added.

With this mixture and 24 parts of 1,5-naphthylene diisocyanate was then made the prepolymer.

Then 2.12 parts of a 50% strength aqueous solution of the Fatty acid sulfonates are intensively mixed with 125.25 parts of the prepolymer and put in the 700C warm mold is filled. The one obtained after demolding Molded part showed a significantly reduced water absorption in the pressure test under water the comparison experiment.

Table 1 Water absorption after 55% deformation of the molding under Water (15 cycles; deformation speed: 100 mm / min).

Polysiloxane zero weight water absorption (parts) (s) (g) (%) - 107.44 71.88 66.9 0.75 silicone oil 106.99 1.29 1.21 0.75 organopoly- 105.10 0.71 0.68 siloxane 0.50 silicone oil + 103.11 0.52 0.5 0.25 organopolysiloxane Example 2 Example 1 b) was repeated, but using 0.75 parts of a polysiloxane prepolymer, which by reacting 2 moles of the organopolysiloxane with 3 moles of tolylene diisocyanate (80% 2,4-isomer) and then one to the number of free NCO groups equimolar amount of diethanolamine had been obtained.

The printing test was tightened compared to Example 1 insofar as the molded part both in the compressed and in the relaxed state for 2 minutes each was left before starting the next cycle.

Nevertheless, the water absorption is extremely low: Table 2 Zero weight (g) Water absorption (g) (%) 109.77 0.56 0.51 Example 3 Example 1 b was detailed below using 0.75 parts each described OH-polysiloxane prepolymers repeated. The results are in below Table 3 compiled.

a) Preparation of modified organopolysiloxanes A to J A) In 1400 g of an Ot-hydroxymethyl-polydimethylsiloxane with an OH number of 80 are 252 g Hexamethylene diisocyanate added dropwise; it is heated to 50 ° C. until the prepolymer has a Has reached an NCO content of 2.54%, then add at 500C while stirring 105 g of diethanolamine are added and left at this temperature until NCO can no longer be detected is.

A modified polysiloxane is obtained with a viscosity of 550 mPas / 250C, a hydroxyl functionality of 4, a content of terminal Hydroxyl groups of 2% and a content of dimethylsiloxane units of 71% by weight.

B) In 1400 g of an α, # - hydroxymethyl-polydimethylsiloxane the OH number 80, 252 g of hexamethylene diisocyanate are added dropwise; it is heated to 500C, until the prepolymer has reached an NCO content of 2.54%, then adds at 500C 281 g of Tris-z2- (2-hydroxyethoxy) -ethyI7-amine are added and left at this temperature, until NCO is no longer detectable. A modified organopolysiloxane is obtained the viscosity 920 mpas / 250C, the hydroxyl functionality 4, with a content of terminal hydroxyl groups of 1.6% by weight and a content of dimethylsiloxane units of 65% by weight.

C) In 1400 g of an α, # - hydroxymethyl-polydimethylsiloxane the OH number 80, 252 g of hexamethylene diisocyanate are added dropwise; it is heated to 500C, until the prepolymer has reached an NCO content of 2.54%, then adds at 50.degree 133 g of diisopropanolamine are added and left at this temperature until NCO can no longer be detected is.

A modified organopolysiloxane having a viscosity of 35 is obtained 950 mPas / 250C, the hydroxyl functionality 4, with a salary of terminal hydroxyl groups of 1.9% by weight and a content of dimethylsiloxane units of 76% by weight.

D) In 570 g of a J hydroxymethyl polydimethylsiloxane with an OH number 200 g of hexamethylene diisocyanate are added dropwise; it is heated to 500C until the Prepolymer has reached an NCO content of 5.12%, then adds 133 g of diisopropanolamine at 500C and leaves at this temperature until NCO is no longer detectable.

A modified organopolysiloxane with a viscosity of 31 is obtained 500 mPas / 250C, the hydroxyl functionality 4, with a content of terminal hydroxyl groups of 1.7% by weight and a content of dimethylsiloxane units of 70% by weight.

E) 1100 g of an α, # - hydroxymethyl-polydimethylsiloxane with the OH number 80 are heated to 90 ° C. with 60 g of hexamethylene diisocyanate and 0.2 g of tin (II) ethylhexoate heated until NCO is no longer detectable.

The advanced polysiloxane is made with 99 g of hexamethylene diisocyanate reacted at a temperature of 500C up to an NCO content of 1.3%, then 40 g of diethanolamine are added and the reaction mixture is at this temperature leave until NCO is no longer detectable.

A paste-like, modified organopolysiloxane is obtained Hydroxyl functionality 4, with a terminal hydroxyl content of 0.99 % By weight and a content of dimethylsiloxane units of 87% by weight.

F) 1400 g of a ß,,. -Hydroxymethyl-polydimethylsiloxane of the OH number 56 and 212 g of hexamethylene diisocyanate are heated to 50 ° C. until there is an NCO content of 2.54% is reached. 1970 g of one started on isopropanol / water are then used Polypropylene oxide with OH number 56 and holds at 500C until NCO is no longer detectable is.

A modified organopolysiloxane having a viscosity of 360 is obtained mPas / 250C, the hydroxyl functionality 2, with a content of terminal hydroxyl groups of 0.94% by weight and a content of dimethylsiloxane units of 37% by weight.

G) 1400 g of a ,, c, -Hydroxymethylpolydimethylsiloxans the OH number 56 and 375 g of 4,4'-diisocyanatodiphenylmethane become an NCO prepolymer at 50 ° C. implemented with an NCO content of 2.4 wt .-%.

Then 105 g of diethanolamine are added and the temperature held at 500C until NCO is no longer detectable. A modified one is obtained Organopolysiloxane with viscosity 26,500 mPas / 50 ° C, hydroxyl functionality 4, with a terminal hydroxyl group content of 1.8% by weight and a content of polydimethylsiloxane units of 72% by weight.

H) 840 g of a hydroxymethylpolydimethylsiloxane with an OH number of 80 and 156 g of a mixture of 2,4- and 2,6-tolylene diisocyanate (80:20) heated to 50 ° C. up to an NCO number of 1.26%; the prepolymer 32 g of diethanolamine are then added and the reaction mixture is at this temperature held until NCO is no longer detectable.

A modified organopolysiloxane with a viscosity is obtained of 1530 mPas / 250C, the hydroxyl functionality 4, a content of terminal hydroxyl groups of 1.0% by weight and a content of dimethylsiloxane units of 83% by weight.

I) 570 g of an α, # - hydroxymethylpolydimethylsiloxane with the OH number 197 and 252 g of hexamethylene diisocyanate are added up to an NCO number of 5.2% 500C heated, then 133 g of diisopropanolamine added and kept at this temperature, until NCO is no longer detectable. A modified organopolysiloxane is obtained the viscosity 60 300 mPas / 250C, the hydroxyl functionality 4, with a content of terminal hydroxyl groups of 3.6% by weight and a content of dimethylsiloxane units of 58% by weight.

J) To 770 g of α, # - bis (hydroxymethyl) polydimethylsiloxane With an OH number of 80, 0.5 g of methyl p-toluenesulfonate are added at room temperature. The mixture is heated to 70 ° C. under a nitrogen atmosphere. At this temperature 220 g of a mixture of 2,4- and 2,6-tolylene diisocyanate (80:20) are added. The batch is heated to 1500 ° C. and left at this temperature for 6 hours. Volatile components are then drawn off in a water jet vacuum. That The prepolymer obtained has an NCO content of 6.6%.

In 209 g of diisopropanolamine in 200 ml of dimethylformamide are briskly 1000 g of the above-mentioned prepolymer are stirred in.

When the reaction is complete, the solvent is drawn off. Man receives a modified organopolysiloxane with a viscosity of 66 100 mPas / 250C with a Terminal hydroxyl group content of 4.2% and a content of dimethylsiloxane units of 61%.

The results of the water absorption tests on cellular elastomers, which which contain polysiloxanes A - J are shown in Table 3): Table 3 Polysiloxane zero weight water absorption (g) (g) (g) A 109.77 0.54 0.49 B 105.33 0.53 0.50 C 103.20 0.57 0.55 D 107.31 0.51 0.47 E 106.48 0.56 0.52 F 107.55 0.52 0.48 G 108.33 0.59 0.54 H 104.88 0.58 0.55 I 107.27 0.57 0.53 J 108.45 0.56 0.51 An important criterion for assessing elastomers for an application as a damping and stop buffer is the damping maximum (tangent c) determined by torsional vibration test according to DIN 53 445. In all of the invention Examples were elastomers with the same damping maximum of -350C as obtained in comparative example 1a.

In addition, the moldings produced according to the invention show a significantly reduced abrasion compared to Example 1a.

Example 4 a) Comparative experiment: (without silicone, without aromatic Diamine) It became a prepolymer of 100 parts of a linear ethanediol polyadipate (Molecular weight 2000) and 24 parts of 1,5-naphthylene diisocyanate.

Then 2.15 parts of a 50% strength aqueous solution of a fatty acid sulfonate were added intensively mixed with 124 parts of the NCO prepolymer and placed in the 700C warm form filled. After the mold was closed, significant amounts of the reactive foam were released driven out between the mold and the mold lid.

The molded part obtained after a heating time of 30 minutes at 90.degree showed in a pressure test under water after several deformations a considerable water uptake. The measured values determined are in the table 4 and the results from the dynamic test are compiled in Tables 5 and 6.

b) Method according to the invention (silicone plus diamine) First of all 100 parts of said linear ethanediol polyadipate with 0.75 parts of a polysiloxane prepolymer, which by reacting 2 moles of organopolysiloxane with 3 moles of tolylene diisocyanate (80% 2,4-isomer) and then with an equimolar to the number of free NCO groups Amount of diethanolamine had been obtained, and 0.2 parts of 1,5-naphthylenediamine offset.

With this mixture and 24 parts of 1,5-naphthylene diisocyanate was then the NCO prepolymer is produced.

Then 2.15 parts of the 50% strength aqueous solution were Fatty acid sulfonate mixed with 124.95 parts of the prepolymer and poured into the 70 "C warm shape filled.

The molded part could be produced without any sprouting and showed in the pressure test under water, it was considerably reduced compared to the comparison test Water absorption that only increased slightly after dynamic exposure. the The structure of the cellular polyurethane elastomer was extremely uniform and fine cell structure. The molded part was easy to remove from the mold, the surface of the molded part was very even.

As can be seen from Tables 5 and 6, the material also has a improved dynamic behavior.

The one in the rotational flexometer test after 30 minutes The higher temperature determined is due to the greater possible transverse deflection with this quality SD attributed.

c) Method according to the invention (only with silicone) 100 parts of the above linear ethanediol polyadipate with 0.75 parts of the described under 4b) Organopolysiloxane derivatives added. With this mixture and 24 parts of 1,5-naphthylene diisocyanate the NCO prepolymer was then produced. Then 2.15 parts of a 50% strength aqueous solution of the fatty acid sulfonate with 124.75 parts of the NCO prepolymer intensively mixed and filled into 700C warm molds. The molding could only with clear buds are produced and showed a pressure test under water reduced water absorption, which, however, was higher than in the dynamic load Example 4b).

Example 5 Example 4b) was repeated, but using of 0.2 part of 4,4'-diaminodiphenylmethane and 0.75 part of a polysiloxane prepolymer, which by reacting 2 moles of organopolysiloxane with 3 moles of hexamethylene diisocyanate and subsequent reaction with diisopropanolamine in one to Number of free NCO groups in an equimolar amount, based on the NH groups of the diisopropanolamine, had been received. The results are shown in Tables 4, 5 and 6 below.

Example 6 Example 4b) was repeated, but using of 0.5 part of 3,3'-dicarbethoxy-4,4'-diamino-diphenylmethane and 0.75 part of a Polysiloxane prepolymer, which by reacting 2 moles of organopolysiloxane with 3 moles of hexamethylene diisocyanate had been obtained. The results are in the tables 4, 5 and 6 put together.

Table 4 Water absorption after 55% deformation of the molding under Water test conditions: 15 cycles with a deformation rate of 100 mm / min., wherein the molded part both in the compressed and in the relaxed state, respectively 2 minutes before starting the next cycle.

The water absorption was determined before and after dynamic loading (55% deformation, 2 HZ, 500,000 cycles). Table 4 At zero weight Water absorption (wt .-%) compressive forces (N) play (g) before and after before and after dynamic load 10% 30% 50% 10% 30% 50% dynamic load Burden # # Load. # # Discharge # # discharge. # # 4a 107.1 34 - 162.5 342.5 845 - - - 152.5 297.5 735 - - - 4b 109.8 0.5 0.9 210 530 1370 145 340 1000 170 417 1140 115 310 895 4c 107.3 1.2 24.4 160 430 1130 155 375 1090 150 370 1005 130 285 900 5 102.2 0.6 5.2 175 405 1075 150 350 1020 155 345 955 145 285 865 6 110 0.5 4.2 210 540 1385 140 325 1150 165 415 1140 100 315 980 7 107 0.45 0.7 205 530 1240 145 330 1080 150 400 1080 105 320 1010 (Example 4a represents a comparison test to 4b and 4c) Measurement of the dynamic properties (according to DIN 53 533, sheets 1 to 3).

1. Compression flexometer (see table 5 for measurement results) Medium tension: 1.0 MPa, f = 24 Hz Ambient temperature: room temperature (23 + 2) OC, running time = '1 Hour.

Sample dimensions: 17.8 mm diameter x 25 mm high. Table 5 Example RG stroke = 4.45 mm stroke = 6.35 mm g / cm³ #T flow permanent flow #T flow permanent flow (° C) (%) forming (° C) (%) forming (%) (%) 4 a ** 483 19.7 -4.5 6.0 24.5 -6.0 10.7 4 b 475 13.7 -3.8 4.0 20.2 -4.0 6 4 c 480 16 -5.8 6.5 28 * -8 13 5,486 12.0 -3.0 3.8 18.2 -4.1 5.8 6,472 10.0 -3.3 4.1 17.8 -3.7 5.3 * Sample discolored inside. RG = volume weight ** Comparative example 2. Rotation flexometer (for measurement results see Table 6) Test specimen: d = 20.0 mm h0 = 20.0 mm; Ao = 314 mm2 frequency = 25 Hz, ambient temperature: room temperature (23 + 2) ° C, constant: axial deformation #h = 6.0 mm test parameters: transverse deflection Sa.

Table 6 Example R.G # T-Messg. Final run time = 30 minutes (g / dm³) Sa = 2.0 mm SD #D #T γD = SD / (h0 / minus) t = 20 min (mm) (MPa) (° C) [1] (° C) 4 a +) 483 52 2.4 0.16 69 0.17 4 b 475 33 3.8 0.097 92 0.27 4 c 480 56 2.0 0.089 72 0.14 5 486 32 3.5 0.08 63 0.25 6 472 36 3.7 0.085 64 0.26 Sa = amplitude of the Transverse deflection SD = permanent transverse deflection Sa with ND γD = permanent deformability SD / ho- # h #D = fatigue strength QD / A0 #T = temperature increase QD = force to apply the permanent transverse deflection SD RG = volume weight +) = comparative example example 7 Example 4b was repeated, but before the reactive mixture was poured in the inner walls of the 700C mold with a 40% aqueous PU dispersion sprayed with a spray gun, the water evaporating instantly and a uniform film (0.2 mm) remained on the mold wall. Then became the reactive mixture from Example 4b in the prepared in this way Shape filled. The molded part obtained after demolding had on its entire Surface adopted the polyurethane film with good adhesion. With the corresponding Compared to the comparative experiment, the buffer showed a pressure tests under water Significantly reduced water absorption, which is only slightly after dynamic load got bigger.

Claims (10)

Claims 1) Process for the production of a waterproof, fine-cell polyurethane elastomer with a density of 0.3 to 0.8 g / cm3 by optionally stepwise reaction of A) organic polyisocyanates, B) polyhydroxyl compounds with a molecular weight of 400 to 6000, C) water and optionally D) organic chain extenders with at least 2 isocyanate-reactive hydrogen atoms and a molecular weight of 32 to 400, optionally in the presence of E) catalysts and / or other auxiliaries and additives known per se, the equivalence ratio between isocyanate groups and isocyanate-reactive compounds in the overall formulation is between 0.95: 1 and 1.15: 1, which is characterized in that 0.1 to 3% by weight, preferably 0.3 to 2% by weight, are added to the reaction mixture in one of the process stages F) %, one or more polysiloxanes of the general formula in which is an integer between 1 and 500, the radicals Z can be identical or different and represent C1- to C5-alkyl, C6- to C15-aryl or siloxyl radicals and the radicals X have the same meaning as Z or Represent HYR groups, where Y is -NR'-, -O-, or -S-, R is a C1- to C6-alkylene radical optionally containing heteroatoms and R 'is hydrogen, a C1- to C6-alkyl radical or a C5- to Cg-cycloalkyl radical, where in the case of X being HYR these organofunctional silicones can also be converted into NCO- or OH-functional silicone prepolymers with polyisocyanates and, if appropriate, excess polyvalent chain extenders. 2) Method according to claim 1, characterized in that one polysiloxanes is used, in which m is an integer between 1 and 100 and 1 to 5 of the radicals X stands for a group H-Y-R-. 3) Method according to claim 2, characterized in that one polysiloxanes is used, in which m for an integer between 5 and 30, Z for methyl groups and two of the radicals X stand for a group H-Y-R-. 4) Method according to claim 2 or 3, characterized in that one Polysiloxanes are used in which Y stands for an oxygen atom. 5) Process according to claim 1 to 4, characterized in that one Mixtures of a) polysiloxanes in which X stands for H-Y-R-, and b) polysiloxanes, in which X = Z and all groups X = Z for methyl and optionally phenyl groups are used in a weight ratio of 4: 1 to 1: 4. 6) Process according to claim 1 to 5, characterized in that one Polysiloxane uses that through Implementation of the groups H-Y-R- with an excess of polyisocyanate and optionally then with an amino-polyol have been prepolymerized. 7) Method according to claim 1 to 6, characterized in that one in a first stage from component A) and the total or partial amount of B) produces a prepolymer and this in a second stage with the components C) and optionally D) and the remainder of B), the polysiloxanes F) are added to the prepolymer or to component B). 8) Process according to claim 1 to 7, characterized in that one as organic chain extenders D) aromatic diamines with a molecular weight from 108 to 400 in an amount of 0.1 to 0.8% by weight, based on the total mixture, used. 9) Process according to claim 1 to 8, characterized in that one the cellular polyurethane elastomers on the surface with a continuous, dense, non-porous skin with a thickness of 0.05 to 1 mm made of polyurethane and / or polyurethaneurea provides. 10) use of waterproof, fine-cell polyurethane elastomers, which were produced by the method of claims 1 to 9, in suspension and Damping elements.