WO2006066763A1 - Method for producing microcellular polyurethane elastomers - Google Patents

Method for producing microcellular polyurethane elastomers Download PDF

Info

Publication number
WO2006066763A1
WO2006066763A1 PCT/EP2005/013405 EP2005013405W WO2006066763A1 WO 2006066763 A1 WO2006066763 A1 WO 2006066763A1 EP 2005013405 W EP2005013405 W EP 2005013405W WO 2006066763 A1 WO2006066763 A1 WO 2006066763A1
Authority
WO
WIPO (PCT)
Prior art keywords
polyurethane elastomers
microcellular polyurethane
aii
elastomers according
phosphorus content
Prior art date
Application number
PCT/EP2005/013405
Other languages
German (de)
French (fr)
Inventor
Markus SCHÜTTE
Diane Terese Langer
Original Assignee
Basf Aktiengesellschaft
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Basf Aktiengesellschaft filed Critical Basf Aktiengesellschaft
Priority to CN2005800431336A priority Critical patent/CN101080428B/en
Publication of WO2006066763A1 publication Critical patent/WO2006066763A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/088Removal of water or carbon dioxide from the reaction mixture or reaction components
    • C08G18/0885Removal of water or carbon dioxide from the reaction mixture or reaction components using additives, e.g. absorbing agents
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4236Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
    • C08G18/4238Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/32Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof from compositions containing microballoons, e.g. syntactic foams
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • C08K5/524Esters of phosphorous acids, e.g. of H3PO3
    • C08K5/526Esters of phosphorous acids, e.g. of H3PO3 with hydroxyaryl compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/53Phosphorus bound to oxygen bound to oxygen and to carbon only
    • C08K5/5317Phosphonic compounds, e.g. R—P(:O)(OR')2
    • C08K5/5333Esters of phosphonic acids
    • C08K5/5353Esters of phosphonic acids containing also nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00Foam properties
    • C08G2110/0041Foam properties having specified density
    • C08G2110/0066≥ 150kg/m3
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2410/00Soles

Definitions

  • Polyurethane integral foams often referred to as microcellular polyurethane elastomers and hereinafter also referred to as MPE, have been known for a long time and are used, for example, for the production of shoe soles. They are described, for example, in the Kunststoffhandbuch, volume 7 "Polyurethane", 3rd edition, page 376 et seq., They are prepared by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms as compounds having at least two hydrogen atoms reactive with isocyanate groups These materials are often used to produce high performance materials such as high elasticity, high tensile and tear strength or low abrasion, while at the same time processing such systems with high process reliability, a disadvantage of microcellular polyester-based polyurethane elastomers The low resistance to hydrolysis is caused by the intrinsic susceptibility of the ester groups to hydrolytic degradation, and the cleavage of the ester groups causes a reduction in the molar mass e of the polymer and
  • polyester alcohols based on adipic acid 1,4-butanediol, 1,6-hexanediol and neopentyl glycol are used.
  • substitution or partial substitution of the polyester alcohols for hydrolysis-resistant polyether alcohols is described.
  • EP 965 582 describes the use of acid anhydrides
  • DE 19 710 978 describes the use of a combination of lactones and carbodiimides.
  • the solutions to be taken from the prior art usually have disadvantages. In some cases, higher hydrolysis resistances are achieved, but at the same time only insufficient use properties are obtained before aging. In addition, some solutions can not be realized in practice due to the higher input costs. This can be done, for example, in the case of the use of special len polyester alcohols or high amounts of certain additives occur. Another disadvantage of many of the prior art solutions to be taken is the reduction of the storage stability of the components. Furthermore, many solutions have too low an efficacy, especially if extremely high demands are made on the hydrolysis resistance.
  • phosphites generally in microcellular polyurethane elastomers is known and is described e.g. in Kunststoffhandbuch, volume 7 "Polyurethane", 3rd edition, page 120 ff.
  • phosphites are used as antioxidants, and their use in combination with typical antioxidants, such as sterically hindered phenols, leads to a synergistic effect Effect, combined with a significant increase in the effect of preventing thermal oxidation processes.
  • JP 61128904 describes the use of 4-14% by weight of phosphite esters in polyester-based microcellular polyurethane elastomers. Phosphites based on phenol and long-chain alkyl radicals are used as yellowing inhibitors. The phosphites are used in the prepolymer.
  • JP 63278962 describes UV-stable polyester-based MPE for shoe soles. Phosphites are used as antioxidant aids together with sterically hindered phenols as antioxidant. The proportion by weight is 1 wt .-%.
  • JP 63305162 describes a UV stabilization package for polyester alcohol-based MPE. Here is u.a.
  • the proportion by weight is 0.5% by weight.
  • JP 05214240 describes a UV protection for PUR shoe soles which i.a. Contains thiophosphites in amounts of about 1%.
  • JP 2003147057 describes the use of polycarbonate diols in shoe systems. The example mentions that about 2% by weight of TPP is added to the prepolymer.
  • JP 61128904, JP 63278962 and JP 05214240 generally describe the use of phosphites in polyester-based MPE as antioxidant aids.
  • the documents JP 63278962 and JP 63305162 mention that i.a. aromatic phosphites can be used as an antioxidant in the isocyanate-reactive component.
  • the document JP 2003147057 describes the use of aromatic phosphites in microcellular polyurethane elastomers based on polyether carbonate alcohols.
  • the object of the present application was to provide a hydrolysis protection agent for polyester alcohol-based MPE, which allows a high effect at low input and guarantees high efficiency regardless of the polyester alcohol used.
  • the object could be achieved by the use of a special hydrolysis protection agent a), consisting of a combination of ai) an aromatic phosphite with a phosphorus content of 9.00 to 11, 00 wt .-%, preferably 9.90 to 10 , 10 wt .-% and in particular 9.95 to 10.05 wt .-% and aii) an amine compound such as triethylenediamine, wherein the molar ratio between ai) and aii) preferably 0.005 to 4.0, particularly preferably. 0.1 to 3.0, and especially 0.5 to 2.0. is.
  • the component ai) is preferably used in the isocyanate-containing component (B component) and aii) in the isocyanate-reactive component (A component).
  • MPE can be prepared by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that it is a combination of a) consisting of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11 , 00 wt .-%, and aii) of an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
  • the invention furthermore relates to a process for the preparation of MPE by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that the reaction in the presence of a), which comprises a combination consisting of ai) an aromatic phosphite with phosphorus content of 9.00 to 11.00 wt%, and aii) an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
  • a which comprises a combination consisting of ai) an aromatic phosphite with phosphorus content of 9.00 to 11.00 wt%, and aii) an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
  • the invention also provides the use of a combination of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11, 00 wt .-%, and aii) an amine compound as a hydrolysis protection for MPE.
  • the invention also relates to shoe soles comprising the microcellular polyurethane elastomers according to the invention.
  • the molar ratio between ai) and aii) is preferably 0.1 to 3.0, and more preferably 0.5 to 2.0.
  • the phosphorus content of component ai) is preferably 9.90 to 10.10 wt .-% and in particular 9.95 to 10.05 wt .-%.
  • the component ai) used is preferably triphenyl phosphite (TPP). 4
  • amine compounds aii) primary, secondary and preferably tertiary amines can be used. These are preferably those amines which are customarily used as catalysts for the preparation of polyurethanes.
  • tertiary amines selected from the groups comprising triethylamine, triethylenediamine, tributylamine, dimethylbenzylamine, N, N 1 N ', N'-tetramethylethylenediamine, N, N, N', N'-tetramethylbutanediamine, N, N , N ', N'-tetramethylhexane-1,6-diamine, dimethylcyclohexylamine, pentamethyldipropylenetriamine, penta-methyldiethylenetriamine, 3-methyl-6-dimethylamino-3-azapentol, dimethylaminopropylamine, 1,3-bisdimethylaminobutane, bis ( 2-dimethylaminoethyl) ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, 2-dimethylaminoethoxyethanol, dimethylethanolamine, tetramethyl
  • the amount of tertiary amines used as a catalyst is sufficient to achieve the required stabilizing effect in combination with the aromatic phosphites ai).
  • additional amines when using other than amine catalysts or when using smaller amounts of amine catalysts than required for adequate stabilization. These will not be the tertiary amines used as catalysts in the process to exclude catalysis disturbances.
  • the hydrolysis protection agent a) in an amount of 0.0001 to 3, 0.0005 to 2 and 0.001 to 1, 6 wt .-%, based on the weight of the MPE used.
  • the polyisocyanates used in the process according to the invention include the known from the prior art aliphatic, cycloaliphatic and aromatic isocyanates and any mixtures thereof. Examples are diisocyanate 4,4 'diphenylmethane ⁇ , the mixtures of monomeric diphenylmethane diisocyanates and higher-nuclear homologues of diphenylmethane diisocyanate (polymeric MDI), tetramethylene 5 013405
  • O is diisocyanate, hexamethylene diisocyanate (HDI), tolylene diisocyanate (TDI) or mixtures thereof.
  • 4,4'-MDI and / or HDI is used.
  • the most preferred 4,4'-MDI may contain minor amounts, up to about 10% by weight, of allophanate- or urethane-onimine-modified polyisocyanates. It is also possible to use small amounts of polyphenylenepolymethylene polyisocyanate (crude MDI). The total amount of these high-functionality polyisocyanates should not exceed 5% by weight of the isocyanate used.
  • the 4,4'-MDI may contain small amounts, preferably at most 10% by weight, of 2,4'-MDI.
  • the polyisocyanates can also be used in the form of polyisocyanate prepolymers. These prepolymers are known in the art. The preparation is carried out in a manner known per se, by reacting polyisocyanates described above, for example at temperatures of about 8O 0 C, with the compounds described below with isocyanate-reactive hydrogen atoms to the prepolymer.
  • the polyol-polyisocyanate ratio is generally chosen so that the NCO content of the prepolymer 8 to 25 wt .-%, preferably 10 to 22 wt .-%, particularly preferably 13 to 20 wt .-% is.
  • polyester alcohols are used as compounds with isocyanate-reactive hydrogen atoms.
  • the polyester alcohols are generally obtained by condensation of polyfunctional alcohols, preferably diols, having 2 to 12 carbon atoms, preferably 2 to 6 carbon atoms, with polyfunctional carboxylic acids having 2 to 12 carbon atoms, for example succinic acid, glutaric acid, adipic acid, phthalic acid, isophthalic acid, and / or terephthalic acid and mixtures thereof.
  • polyfunctional alcohols preferably diols, having 2 to 12 carbon atoms, preferably 2 to 6 carbon atoms
  • polyfunctional carboxylic acids having 2 to 12 carbon atoms
  • suitable dihydric and polyhydric alcohols are ethylene glycol, diethylene glycol, 1,4-butanediol, 1, 5-pentanediol, and / or 1, 6-hexanediol and mixtures thereof.
  • the polyester alcohols may also be branched.
  • the branched polyester alcohols preferably have a functionality of more than 2 to 3, in particular from 2.2 to 2.8. Furthermore, the branched polyester alcohols preferably have a number-average molecular weight of from 500 to 5000 g / mol, more preferably from 2000 to 3000 g / mol.
  • the polyester alcohols used for the process according to the invention have an average theoretical functionality of 2 to 4, preferably of more than 2 to less than 3 and the above-mentioned number average molecular weights.
  • polyester alcohols used can in principle also be used in a mixture with polyether alcohols. However, since such mixtures often have insufficient phase stability, the use of such mixtures is not preferred.
  • the compounds having two active hydrogen atoms also include the optionally used chain extenders.
  • Suitable chain extenders are known in the art. Preference is given to using 2-functional alcohols having molecular weights below 400 g / mol, in particular in the range from 60 to 150 g / mol. Examples are ethylene glycol, 1,3-propanediol, diethylene glycol, butanediol-1, 4, glycerol or trimethylolpropane, and mixtures thereof. Preferably, ethylene glycol is used.
  • the chain extender if used, is usually present in an amount of from 1 to 15% by weight, preferably from 3 to 12% by weight, more preferably from 4 to 10% by weight, based on the total weight of the two compounds Isocyanatat phenomenon reactive hydrogen atoms used.
  • blowing agents it is possible to use generally known chemically or physically active compounds.
  • chemically acting blowing agent water can preferably be used.
  • physical blowing agents are inert (cyclo) aliphatic hydrocarbons having from 4 to 8 carbon atoms which evaporate under the conditions of polyurethane formation. The amount of blowing agent used depends on the desired density of the foams.
  • the reaction of the polyisocyanates with the compounds with two active hydrogen atoms is optionally carried out in the presence of catalysts and of auxiliaries and / or additives, such.
  • Catalysts for the preparation of the microcellular polyurethane elastomers according to the invention can be the customary and known polyurethane-forming catalysts, for example organic metal compounds, such as tin diacetate, tin dioctoate, dibutyltin dilaurate, and / or strongly basic amines, such as diazabicyclooctane, bis (N, N-dimethylaminoethyl) ether or the above-mentioned amines.
  • the catalysts are preferably used in an amount of from 0.01 to 10% by weight, preferably from 0.02 to 5% by weight, based on the reaction mixture.
  • amines in particular tertiary amines, are preferably used as catalysts.
  • the amines can, as described above, individually or as any mixtures with one another set. These act simultaneously in the microcellular polyurethane elastomers as component aii).
  • organic amines known from the prior art tertiary amines are useful.
  • suitable are organic amines, such as triethylamine, triethylenediamine, tributylamine, dimethylbenzylamine, N, N, N ', N'-tetramethylethylenediamine, N, N, N', N'-tetramethylbutanediamine, N, N, N ' , N'-tetramethylhexane-1,6-diamine, dimethylcyclohexylamine, pentamethyldipropylenetriamine, pentamethyldiethylenetriamine, 3-methyl-6-dimethylamino-3-azapentol, dimethylaminopropylamine, 1,3-bis-dimethylaminobutane, bis (2-dimethylaminoethyl) - ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, 2-dimethylamin
  • the catalysts which can be used in a mixture with the tertiary amines are, as described above, mainly organic metal compounds, in particular tin compounds, such as tin diacetate, tin dioctoate, dibutyltin dilaurate, and / or bismuth compound.
  • the catalysts are preferably mixed with the compounds having at least two isocyanate-reactive hydrogen atoms. In principle, it is also possible to mix at least the organic metal compounds with the polyisocyanates.
  • the polyisocyanates are referred to as the isocyanate component and the compounds having at least two isocyanate-reactive hydrogen atoms, which is usually used in admixture with the catalysts, optionally the blowing agents and additives, as a polyol component.
  • the isocyanate component and the polyol component are usually reacted in amounts such that the equivalent ratio of NCO groups to the sum of the reactive hydrogen atoms is 1: 0.8 to 1: 1, 25, preferably 1: 0.9 to 1 : 1, 15 is.
  • a ratio of 1: 1 corresponds to an NGO index of 100.
  • the reaction to the microcellular polyurethane elastomer is preferably carried out in densified forms.
  • the molds are preferably made of metal, for example steel or aluminum, or else of plastic, for example epoxy resin.
  • the starting components are mixed at temperatures of 15 to 90 ° C., preferably at 20 to 35 ° C., and if appropriate under elevated pressure, introduced into the preferably closed molding tool.
  • the mixing can be carried out during introduction by known in the art high or low pressure mixing heads.
  • the mold temperature is generally between 20 and 90 0 C, preferably between 30 and 60 ° C.
  • the amount of the reaction mixture introduced into the mold is such that the resulting molded articles have a density of from 250 to 600 g / l or from 800 to 1200 g / l, preferably from 400 to 600 g / l or from 820 to 1050 g / l , exhibit.
  • the degrees of compression of the resulting microcellular polyurethane elastomers are between 1, 1 and 8.5, preferably between 1.2 and 5, particularly preferably between 1, 5 and 4.
  • microcellular polyurethane elastomers according to the invention can be used for steering wheels, safety clothing and preferably for shoe soles.
  • 100 parts by weight of the polyol component and the specified in Table 1 parts by weight of the isocyanate component were thoroughly mixed at 23 ° C and the mixture in a tempered at 50 0 C, plate-shaped aluminum mold with dimensions of 20cm x 20 cm ⁇ 1 cm in such an amount that after foaming and curing in the closed mold, a microcellular polyurethane elastomer plate with a total density of 550 g / l resulted.
  • Amine catalyst 33% strength by weight solution of triethylenediamine in ethylene glycol (Lupragen ® N 202) BASF AG
  • Table 1 Composition of the systems V1-V3 (comparative examples) and 1-4 (examples according to the invention).
  • Table 2 Aging results of samples V1-V3 and 1-4.
  • a) residual tensile strength or residual strain in% of the initial value after 2 weeks of aging.

Abstract

The invention relates to microcellular polyurethane elastomers which can be produced by reacting polyisocyanates with compounds having at least two hydrogen atoms which are reactive with isocyanate groups. Said elastomers are characterised in that they contains a combination a) made of ai) an aromatic phosphite having a phosphorus content of between 9,00 - 11,00 wt.- %, and aii) an amine compound. The molar ratio between ai) and aii) is between 0,005 - 4,0.

Description

Verfahren zur Herstellung von Mikrozellulären Polyurethan-ElastomerenProcess for the preparation of microcellular polyurethane elastomers
Polyurethan-Integralschaumstoffe, häufig als mikrozelluläre Polyurethan-Elastomere und im folgenden auch als MPE bezeichnet, sind seit langem bekannt und werden bei- spielsweise zur Herstellung von Schuhsohlen verwendet. Sie sind beispielsweise im Kunststoffhandbuch, Band 7 „Polyurethane", 3. Auflage, Seite 376 ff., beschrieben. Ihre Herstellung erfolgt durch Umsetzung von Polyisocyanaten mit Verbindungen mit mindestens zwei mit Isocyanatgruppen reaktiven Wasserstoffatomen. Als Verbindungen mit mindestens zwei mit Isocyanatgruppen reaktiven Wasserstoffatomen werden hier- bei häufig Polyesteralkohole eingesetzt. Dabei werden Materialien mit hervorragenden Gebrauchseigenschaften wie hohe Elastizität, hohe Zug- und Weiterreißfestigkeit oder geringer Abrieb erhalten. Gleichzeitig können solche Systeme mit hoher Prozess- Sicherheit verarbeitet werden. Ein Nachteil von mikrozellulären Polyurethan-Elastomeren auf Polyesteralkohol-Basis besteht in der geringen Hydrolysebeständigkeit der Materialien. Die geringe Hydrolysebeständigkeit wird durch die intrinsisch bedingte Anfälligkeit der Estergruppen gegen hydrolytischen Abbau verursacht. Die Spaltung der Estergruppen verursacht einen Abbau der Molmasse des Polymers und führt zu einer Verschlechterung der Gebrauchseigenschaften, die im Extremfall zu totalem Materialversagen führen kann.Polyurethane integral foams, often referred to as microcellular polyurethane elastomers and hereinafter also referred to as MPE, have been known for a long time and are used, for example, for the production of shoe soles. They are described, for example, in the Kunststoffhandbuch, volume 7 "Polyurethane", 3rd edition, page 376 et seq., They are prepared by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms as compounds having at least two hydrogen atoms reactive with isocyanate groups These materials are often used to produce high performance materials such as high elasticity, high tensile and tear strength or low abrasion, while at the same time processing such systems with high process reliability, a disadvantage of microcellular polyester-based polyurethane elastomers The low resistance to hydrolysis is caused by the intrinsic susceptibility of the ester groups to hydrolytic degradation, and the cleavage of the ester groups causes a reduction in the molar mass e of the polymer and leads to a deterioration of the performance, which can lead to total material failure in extreme cases.
Daher gab es in der Vergangenheit zahlreiche Bemühungen, die Hydrolysebeständigkeit solcher Materialien zu erhöhen.Therefore, there have been many attempts in the past to increase the hydrolysis resistance of such materials.
Als eine Möglichkeit zur Verbesserung der Hydrolysebeständigkeit von Polyesteralko- hol-basierten mikrozellulären Polyurethan-Elastomeren wird die Verwendung von speziellen Polyesteralkoholen vorgeschlagen. Beispielhaft sei hier die DE 3 144 968 erwähnt, in der Polyesteralkohole auf Basis von Adipinsäure, 1 ,4-Butandiol, 1 ,6-Hexan- diol und Neopentylglykol eingesetzt werden. Daneben wird die Substitution oder Teilsubstitution der Polyesteralkohole gegen hydrolysebeständigere Polyetheralkohole beschrieben.As a way to improve the hydrolysis resistance of polyester-based microcellular polyurethane elastomers, the use of special polyester alcohols is suggested. By way of example, mention may be made of DE 3 144 968, in which polyester alcohols based on adipic acid, 1,4-butanediol, 1,6-hexanediol and neopentyl glycol are used. In addition, the substitution or partial substitution of the polyester alcohols for hydrolysis-resistant polyether alcohols is described.
Eine andere Möglichkeit zur Verbesserung der Hydrolysebeständigkeit ist die Verwendung von bestimmten Additiven, die meist in Mengen kleiner 10 Gew.-% eingesetzt werden. So beschreibt EP 965 582 die Verwendung von Säureanhydriden, während DE 19 710 978 die Verwendung einer Kombinationen aus Lactonen und Carbodiimiden beschreibt.Another possibility for improving the hydrolysis resistance is the use of certain additives, which are usually used in amounts of less than 10 wt .-%. For example, EP 965 582 describes the use of acid anhydrides, while DE 19 710 978 describes the use of a combination of lactones and carbodiimides.
Die dem Stand der Technik zu entnehmenden Lösungen besitzen jedoch meist Nachteile. In einigen Fällen werden zwar höhere Hydrolysebeständigkeiten erreicht, jedoch werden gleichzeitig nur unzureichende Gebrauchseigenschaften vor Alterung erhalten. Daneben lassen sich einige Lösungen aufgrund der höheren Einsatzstoffkosten nicht in der Praxis realisieren. Dies kann z.B. im Falle der Verwendung von speziel- len Polyesteralkoholen bzw. hoher Einsatzmengen bestimmter Additive auftreten. Ein weiterer Nachteil vieler dem Stand der Technik zu entnehmenden Lösungen ist die Verringerung der Lagerstabilität der Komponenten. Weiterhin weisen viele Lösungen eine zu geringe Wirksamkeit auf, insbesondere, wenn extrem hohe Anforderungen an die Hydrolysebeständigkeit benötigt werden.However, the solutions to be taken from the prior art usually have disadvantages. In some cases, higher hydrolysis resistances are achieved, but at the same time only insufficient use properties are obtained before aging. In addition, some solutions can not be realized in practice due to the higher input costs. This can be done, for example, in the case of the use of special len polyester alcohols or high amounts of certain additives occur. Another disadvantage of many of the prior art solutions to be taken is the reduction of the storage stability of the components. Furthermore, many solutions have too low an efficacy, especially if extremely high demands are made on the hydrolysis resistance.
Die Verwendung von Phosphiten allgemein in mikrozellulären Polyurethan-Elastomeren ist bekannt und wird z.B. in Kunststoffhandbuch, Band 7 „Polyurethane", 3. Auflage, Seite 120 ff. beschrieben. Phosphite werden dabei als Antioxidant-Hilfsmittel ein- gesetzt. Der gemeinsame Einsatz mit typischen Vertretern von Antioxidantien, wie ste- risch gehinderten Phenolen, führt zu einer synergistischen Wirkung, verbunden mit einer erheblichen Steigerung des Effekts der Verhinderung von Thermooxidationspro- zessen.The use of phosphites generally in microcellular polyurethane elastomers is known and is described e.g. in Kunststoffhandbuch, volume 7 "Polyurethane", 3rd edition, page 120 ff., phosphites are used as antioxidants, and their use in combination with typical antioxidants, such as sterically hindered phenols, leads to a synergistic effect Effect, combined with a significant increase in the effect of preventing thermal oxidation processes.
JP 61128904 beschreibt den Einsatz von 4-14 Gew.-% an Phosphitestern in mikrozellulären Polyurethan-Elastomeren auf Polyesteralkohol-Basis. Phosphite auf Basis von Phenol und langkettigen Alkylresten werden als Vergilbungsinhibitoren eingesetzt. Die Phosphite werden im Prepolymer eingesetzt. JP 63278962 beschreibt UV-stabile MPE auf Polyester-Basis für Schuhsohlen. Phosphite werden als Antioxidant-Hilfsmittel ge- meinsam mit sterisch gehinderten Phenolen als Antioxidant eingesetzt. Der Gewichtsanteil beträgt 1 Gew.-%. JP 63305162 beschreibt ein UV-Stabilisierungspaket für PoIy- esteralkohol-basierte MPE. Hier wird u.a. Triphenylphosphit (TPP) als Antioxidant- Hilfsmittel in Verbindung mit sterisch gehinderten Phenolen erwähnt. Der Gewichtsanteil beträgt 0,5 Gew.-%. JP 05214240 beschreibt einen UV-Schutz für PUR- Schuhsohlen, der u.a. Thiophosphite in Einsatzmengen von ca. 1 % enthält.JP 61128904 describes the use of 4-14% by weight of phosphite esters in polyester-based microcellular polyurethane elastomers. Phosphites based on phenol and long-chain alkyl radicals are used as yellowing inhibitors. The phosphites are used in the prepolymer. JP 63278962 describes UV-stable polyester-based MPE for shoe soles. Phosphites are used as antioxidant aids together with sterically hindered phenols as antioxidant. The proportion by weight is 1 wt .-%. JP 63305162 describes a UV stabilization package for polyester alcohol-based MPE. Here is u.a. Triphenyl phosphite (TPP) as an antioxidant aid in connection with sterically hindered phenols mentioned. The proportion by weight is 0.5% by weight. JP 05214240 describes a UV protection for PUR shoe soles which i.a. Contains thiophosphites in amounts of about 1%.
JP 2003147057 beschreibt die Verwendung von Polycarbonat-Diolen in Schuhsystemen. Im Beispiel wird erwähnt, dass ca. 2 Gew.-% an TPP dem Prepolymer zugefügt werden.JP 2003147057 describes the use of polycarbonate diols in shoe systems. The example mentions that about 2% by weight of TPP is added to the prepolymer.
Die Schriften JP 61128904, JP 63278962 und JP 05214240 beschreiben allgemein die Verwendung von Phosphiten in Polyester-basierten MPE als Antioxidant-Hilfsmittel. Die Schriften JP 63278962 und JP 63305162 erwähnen, dass u.a. aromatische Phosphite als Antioxidant in der Isocyanat-reaktiven Komponente eingesetzt werden können. Die Schrift JP 2003147057 beschreibt die Verwendung von aromatischen Phos- phiten in mikrozellulären Polyurethan-Elastomeren auf Basis von Polyethercarbonat- alkoholen.JP 61128904, JP 63278962 and JP 05214240 generally describe the use of phosphites in polyester-based MPE as antioxidant aids. The documents JP 63278962 and JP 63305162 mention that i.a. aromatic phosphites can be used as an antioxidant in the isocyanate-reactive component. The document JP 2003147057 describes the use of aromatic phosphites in microcellular polyurethane elastomers based on polyether carbonate alcohols.
Die Aufgabe der vorliegenden Anmeldung bestand in der Bereitstellung eines Hydrolyseschutzmittels für Polyesteralkohol-basierte MPE, das einen hohen Effekt bei geringer Einsatzmenge ermöglicht und unabhängig vom verwendeten Polyesteralkohol eine hohe Wirksamkeit garantiert. Die Aufgabe konnte gelöst werden durch die Verwendung eines speziellen Hydrolyseschutzmittels a), bestehend aus einer Kombination aus ai) einem aromatischem Phos- phit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, vorzugsweise 9,90 bis 10,10 Gew.-% und insbesondere 9,95 bis 10,05 Gew.-% und aii) einer Aminverbindung wie z.B. Triethylendiamin, wobei das molare Verhältnis zwischen ai) und aii) vorzugsweise 0,005 bis 4,0, besonders bevorzugt. 0,1 bis 3,0, und insbesondere 0,5 bis 2,0. beträgt. Bevorzugt wird die Komponente ai) in der Isocyanat-haltigen Komponente (B-Komponente) und aii) in der Isocyanat-reaktiven Komponente (A-Komponente) eingesetzt.The object of the present application was to provide a hydrolysis protection agent for polyester alcohol-based MPE, which allows a high effect at low input and guarantees high efficiency regardless of the polyester alcohol used. The object could be achieved by the use of a special hydrolysis protection agent a), consisting of a combination of ai) an aromatic phosphite with a phosphorus content of 9.00 to 11, 00 wt .-%, preferably 9.90 to 10 , 10 wt .-% and in particular 9.95 to 10.05 wt .-% and aii) an amine compound such as triethylenediamine, wherein the molar ratio between ai) and aii) preferably 0.005 to 4.0, particularly preferably. 0.1 to 3.0, and especially 0.5 to 2.0. is. The component ai) is preferably used in the isocyanate-containing component (B component) and aii) in the isocyanate-reactive component (A component).
Gegenstand der Erfindung sind demzufolge MPE, herstellbar durch Umsetzung von Polyisocyanaten mit Verbindungen mit mindestens zwei mit Isocyanatgruppen reaktiven Wasserstoffatomen, dadurch gekennzeichnet, dass sie eine Kombination a), bestehend aus ai) einem aromatischem Phosphit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung enthält, wobei das molare Verhältnis zwischen ai) und aii) 0,005 bis 4,0 beträgt.The invention accordingly MPE, can be prepared by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that it is a combination of a) consisting of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11 , 00 wt .-%, and aii) of an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
Gegenstand der Erfindung ist weiterhin ein Verfahren zur Herstellung von MPE durch Umsetzung von Polyisocyanaten mit Verbindungen mit mindestens zwei mit Isocya- natgruppen reaktiven Wasserstoffatomen, dadurch gekennzeichnet, dass die Umsetzung in Anwesenheit a), das eine Kombination, bestehend aus ai) einem aromatischem Phosphit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung ist, durchgeführt wird, wobei das molare Verhältnis zwischen ai) und aii) 0,005 bis 4,0 beträgt.The invention furthermore relates to a process for the preparation of MPE by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that the reaction in the presence of a), which comprises a combination consisting of ai) an aromatic phosphite with phosphorus content of 9.00 to 11.00 wt%, and aii) an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
Gegenstand der Erfindung ist auch die Verwendung einer Kombination aus ai) einem aromatischem Phosphit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung als Hydrolyseschutzmittel für MPE.The invention also provides the use of a combination of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11, 00 wt .-%, and aii) an amine compound as a hydrolysis protection for MPE.
Gegenstand der Erfindung sind auch Schuhsohlen, enthaltend die erfindungsgemäßen mikrozellulären Polyurethan-Elastomere.The invention also relates to shoe soles comprising the microcellular polyurethane elastomers according to the invention.
Das molare Verhältnis zwischen ai) und aii) beträgt vorzugsweise 0,1 bis 3,0 und insbesondere 0,5 bis 2,0.The molar ratio between ai) and aii) is preferably 0.1 to 3.0, and more preferably 0.5 to 2.0.
Der Phosphor-Gehalt der Komponente ai) beträgt vorzugsweise 9,90 bis 10,10 Gew.-% und insbesondere 9,95 bis 10,05 Gew.-%.The phosphorus content of component ai) is preferably 9.90 to 10.10 wt .-% and in particular 9.95 to 10.05 wt .-%.
Bevorzugt wird als Komponente ai) Triphenylphosphit (TPP) eingesetzt. 4The component ai) used is preferably triphenyl phosphite (TPP). 4
Als Aminverbindungen aii) können primäre, sekundäre und bevorzugt tertiäre Amine eingesetzt werden. Vorzugsweise handelt es sich um solche Amine, wie sie üblicherweise als Katalysatoren für die Herstellung von Polyurethanen eingesetzt werden.As amine compounds aii) primary, secondary and preferably tertiary amines can be used. These are preferably those amines which are customarily used as catalysts for the preparation of polyurethanes.
Vorzugsweise handelt es sich um tertiäre Amine, ausgewählt aus der Gruppen enthaltend Triethylamin, Triethylendiamin, Tributylamin, Dimethylbenzylamin, N, N1N', N'- Tetramethylethylendiamin, N,N,N',N'-Tetramethyl-butandiamin, N,N,N',N'-Tetramethyl- hexan-1 ,6-diamin, Dimethylcyclohexylamin, Pentamethyldipropylentriamin, Penta- methyldiethylentriamin, 3-Methyl-6-dimethylamino-3-azapentol, Dimethylaminopropyl- amin, 1,3-Bisdimethylaminobutan, Bis-(2-dimethylaminoethyl)-ether, N-Ethylmorpholin, N-Methylmorpholin, N-Cyclohexylmorpholin, 2-Dimethylamino-ethoxy-ethanol, Di- methylethanolamin, Tetramethylhexamethylendiamin, Dimethylamino-N-methyl- ethanolamin, N-Methylimidazol, N-(3-Aminopropyl)imidazol, N-(3-Aminopropyl)-2- Methylimidazol, 1-(2-Hydroxyethyl)imidazol, N-Formyl-N,N'-dimethylbutylendiamin, N-Dimethylaminoethylmorpholin, 3,3'-Bis-dimethylamino-di-n-propylamin und/oder 2,2'-Dipiparazin-diisopropylether, Dimethylpiparazin, N,N'-Bis-(3-aminopropyl)- ethylendiamin und/oder Tris-(N,N-dimethylaminopropyl)-s-hexahydrotriazin, oder Mischungen enthaltend mindestens zwei der genannten Amine, wobei auch höhermolekulare tertiäre Amine, wie sie beispielsweise in DE-A 28 12 256 beschrieben sind, ein- gesetzt werden können. Besonders bevorzugt wird Triethylendiamin eingesetzt.Preference is given to tertiary amines selected from the groups comprising triethylamine, triethylenediamine, tributylamine, dimethylbenzylamine, N, N 1 N ', N'-tetramethylethylenediamine, N, N, N', N'-tetramethylbutanediamine, N, N , N ', N'-tetramethylhexane-1,6-diamine, dimethylcyclohexylamine, pentamethyldipropylenetriamine, penta-methyldiethylenetriamine, 3-methyl-6-dimethylamino-3-azapentol, dimethylaminopropylamine, 1,3-bisdimethylaminobutane, bis ( 2-dimethylaminoethyl) ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, 2-dimethylaminoethoxyethanol, dimethylethanolamine, tetramethylhexamethylenediamine, dimethylamino-N-methylethanolamine, N-methylimidazole, N- Aminopropyl) imidazole, N- (3-aminopropyl) -2-methylimidazole, 1- (2-hydroxyethyl) imidazole, N-formyl-N, N'-dimethylbutylenediamine, N-dimethylaminoethylmorpholine, 3,3'-bis-dimethylamino-di n-propylamine and / or 2,2'-dipiparazin diisopropyl ether, dimethylpiparazine, N, N'-bis (3-aminopropyl) ethylenediamine and / or tris (N, N-dimethylaminopropyl) -s-hexahydrotriazine, or mixtures containing at least two of said amines, wherein higher molecular weight tertiary amines, as described for example in DE-A 28 12 256, can be used. Triethylenediamine is particularly preferably used.
In den meisten Fällen genügt die als Katalysator eingesetzte Menge an tertiären Aminen, um in Kombination mit den aromatischen Phosphiten ai) die erforderliche stabilisierende Wirkung zu erzielen. Es ist jedoch auch möglich, bei Verwendung von ande- ren als aminischen Katalysatoren oder bei der Verwendung von geringeren Mengen an aminischen Katalysatoren, als für eine ausreichende Stabilisierung erforderlich, zusätzliche Amine einzusetzen. Dies werden dann nicht die in dem Verfahren als Katalysatoren verwendeten tertiären Amine sein, um Störungen bei der Katalyse auszuschließen.In most cases, the amount of tertiary amines used as a catalyst is sufficient to achieve the required stabilizing effect in combination with the aromatic phosphites ai). However, it is also possible to use additional amines when using other than amine catalysts or when using smaller amounts of amine catalysts than required for adequate stabilization. These will not be the tertiary amines used as catalysts in the process to exclude catalysis disturbances.
Vorzugsweise wird das Hydrolyseschutzmittel a) in einer Menge von 0.0001 bis 3, 0,0005 bis 2 und 0,001 bis 1 ,6 Gew.-%, bezogen auf das Gewicht des MPE, eingesetzt.Preferably, the hydrolysis protection agent a) in an amount of 0.0001 to 3, 0.0005 to 2 and 0.001 to 1, 6 wt .-%, based on the weight of the MPE used.
Zu den zur Herstellung der erfindungsgemäßen MPE eingesetzten Ausgangsprodukten ist im einzelnen folgendes zu sagen.The following can be said in detail about the starting materials used to prepare the MPE according to the invention.
Die im erfindungsgemäßen Verfahren verwendeten Polyisocyanate umfassen die aus dem Stand der Technik bekannten aliphatischen, cycloaliphatischen und aromatischen Isocyanate sowie beliebige Mischungen daraus. Beispiele sind 4,4'-Diphenylmethan~ diisocyanat, die Mischungen aus monomeren Diphenylmethandiisocyanaten und höherkernigen Homologen des Diphenylmethandiisocyanats (Polymer-MDI), Tetramethy- 5 013405The polyisocyanates used in the process according to the invention include the known from the prior art aliphatic, cycloaliphatic and aromatic isocyanates and any mixtures thereof. Examples are diisocyanate 4,4 'diphenylmethane ~, the mixtures of monomeric diphenylmethane diisocyanates and higher-nuclear homologues of diphenylmethane diisocyanate (polymeric MDI), tetramethylene 5 013405
O lendiisocyanat, Hexamethylendiisocyanat (HDI), Toluylendiisocyanat (TDI) oder Mischungen daraus.O is diisocyanate, hexamethylene diisocyanate (HDI), tolylene diisocyanate (TDI) or mixtures thereof.
Bevorzugt wird 4,4'-MDI und/oder HDI verwendet. Das besonders bevorzugt verwen- dete 4,4'-MDI kann geringe Mengen, bis etwa 10 Gew.-%, allophanat- oder uret- oniminmodifizierte Polyisocyanate enthalten. Es können auch geringe Mengen PoIy- phenylenpolymethylenpolyisocyanat (Roh-MDI) mit eingesetzt werden. Die Gesamtmenge dieser hochfunktionellen Polyisocyanate sollte 5 Gew.-% des eingesetzten Isocyanats nicht überschreiten. Weiterhin kann das 4,4'-MDI geringe Mengen, vor- zugsweise maximal 10 Gew.-%, 2,4'-MDI enthalten.Preferably, 4,4'-MDI and / or HDI is used. The most preferred 4,4'-MDI may contain minor amounts, up to about 10% by weight, of allophanate- or urethane-onimine-modified polyisocyanates. It is also possible to use small amounts of polyphenylenepolymethylene polyisocyanate (crude MDI). The total amount of these high-functionality polyisocyanates should not exceed 5% by weight of the isocyanate used. Furthermore, the 4,4'-MDI may contain small amounts, preferably at most 10% by weight, of 2,4'-MDI.
Die Polyisocyanate können auch in Form von Polyisocyanatprepolymeren eingesetzt werden. Diese Prepolymere sind im Stand der Technik bekannt. Die Herstellung erfolgt auf an sich bekannte Weise, indem vorstehend beschriebene Polyisocyanate, bei- spielsweise bei Temperaturen von etwa 8O0C, mit nachstehend beschriebenen Verbindungen mit gegenüber Isocyanaten reaktiven Wasserstoffatomen zum Prepolymer umgesetzt werden. Das Polyol-Polyisocyanat-Verhältnis wird im allgemeinen so gewählt, dass der NCO-Gehalt des Prepolymeren 8 bis 25 Gew.-%, vorzugsweise 10 bis 22 Gew.-%, besonders bevorzugt 13 bis 20 Gew.-% beträgt.The polyisocyanates can also be used in the form of polyisocyanate prepolymers. These prepolymers are known in the art. The preparation is carried out in a manner known per se, by reacting polyisocyanates described above, for example at temperatures of about 8O 0 C, with the compounds described below with isocyanate-reactive hydrogen atoms to the prepolymer. The polyol-polyisocyanate ratio is generally chosen so that the NCO content of the prepolymer 8 to 25 wt .-%, preferably 10 to 22 wt .-%, particularly preferably 13 to 20 wt .-% is.
Als Verbindungen mit gegenüber Isocyanaten reaktiven Wasserstoffatomen kommen, wie beschrieben, Polyesteralkohole zum Einsatz.As compounds with isocyanate-reactive hydrogen atoms, as described, polyester alcohols are used.
Die Polyesteralkohole werden im allgemeinen durch Kondensation von mehrfunktionel- len Alkoholen, vorzugsweise Diolen, mit 2 bis 12 Kohlenstoffatomen, vorzugsweise 2 bis 6 Kohlenstoffatomen, mit mehrfunktionellen Carbonsäuren mit 2 bis 12 Kohlenstoffatomen, beispielsweise Bernsteinsäure, Glutarsäure, Adipinsäure, Phthalsäure, Iso- phthalsäure, und/oder Terephthalsäure und Gemischen hiervon hergestellt. Beispiele für geeignete zwei- und mehrwertige Alkohole sind Ethylenglykol, Diethylenglykol, 1,4-Butandiol, 1 ,5-Pentandiol, und/oder 1 ,6-Hexandiol und Gemische hiervon.The polyester alcohols are generally obtained by condensation of polyfunctional alcohols, preferably diols, having 2 to 12 carbon atoms, preferably 2 to 6 carbon atoms, with polyfunctional carboxylic acids having 2 to 12 carbon atoms, for example succinic acid, glutaric acid, adipic acid, phthalic acid, isophthalic acid, and / or terephthalic acid and mixtures thereof. Examples of suitable dihydric and polyhydric alcohols are ethylene glycol, diethylene glycol, 1,4-butanediol, 1, 5-pentanediol, and / or 1, 6-hexanediol and mixtures thereof.
Die Polyesteralkohole können auch verzweigt sein. Die verzweigten Polyesteralkohole weisen bevorzugt eine Funktionalität von mehr als 2 bis 3, insbesondere von 2,2 bis 2,8 auf. Des weiteren weisen die verzweigten Polyesteralkohole bevorzugt ein zahlen- mittleres Molekulargewicht von 500 bis 5000 g/mol, besonders bevorzugt von 2000 bis 3000 g/mol auf.The polyester alcohols may also be branched. The branched polyester alcohols preferably have a functionality of more than 2 to 3, in particular from 2.2 to 2.8. Furthermore, the branched polyester alcohols preferably have a number-average molecular weight of from 500 to 5000 g / mol, more preferably from 2000 to 3000 g / mol.
Im allgemeinen weisen die für das erfindungsgemäße Verfahren eingesetzten Polyesteralkohole eine mittlere theoretische Funktionalität von 2 bis 4, bevorzugt von mehr als 2 bis weniger als 3 und die oben genannten zahlenmittleren Molekulargewichte auf. bIn general, the polyester alcohols used for the process according to the invention have an average theoretical functionality of 2 to 4, preferably of more than 2 to less than 3 and the above-mentioned number average molecular weights. b
Die eingesetzten Polyesteralkohole können prinzipiell auch im Gemisch mit Polyether- alkoholen eingesetzt werden. Da derartiger Mischungen jedoch häufig eine unzureichende Phasenstabilität aufweisen, ist die Verwendung derartiger Mischungen nicht bevorzugt.The polyester alcohols used can in principle also be used in a mixture with polyether alcohols. However, since such mixtures often have insufficient phase stability, the use of such mixtures is not preferred.
Zu den Verbindungen mit zwei aktiven Wasserstoffatomen gehören auch die gegebenenfalls eingesetzten Kettenverlängerungsmittel. Geeignete Kettenverlängerungsmittel sind im Stand der Technik bekannt. Bevorzugt werden 2-funktionelle Alkohole mit Molekulargewichten unter 400 g/mol, insbesondere im Bereich von 60 bis 150 g/mol, ver- wendet. Beispiele sind Ethylenglykol, 1,3-Propandiol, Diethylenglykol, Butandiol-1 ,4, Glycerin oder Trimethylolpropan, sowie Gemische davon. Bevorzugt wird Ethylenglykol verwendet.The compounds having two active hydrogen atoms also include the optionally used chain extenders. Suitable chain extenders are known in the art. Preference is given to using 2-functional alcohols having molecular weights below 400 g / mol, in particular in the range from 60 to 150 g / mol. Examples are ethylene glycol, 1,3-propanediol, diethylene glycol, butanediol-1, 4, glycerol or trimethylolpropane, and mixtures thereof. Preferably, ethylene glycol is used.
Das Kettenverlängerungsmittel wird, sofern eingesetzt, üblicherweise in einer Menge von 1 bis 15 Gew.-%, bevorzugt von 3 bis 12 Gew.-%, besonders bevorzugt von 4 bis 10 Gew.-%, bezogen auf das Gesamtgewicht der Verbindungen mit zwei mit Isocya- natgruppen reaktiven Wasserstoffatomen verwendet.The chain extender, if used, is usually present in an amount of from 1 to 15% by weight, preferably from 3 to 12% by weight, more preferably from 4 to 10% by weight, based on the total weight of the two compounds Isocyanatatgruppen reactive hydrogen atoms used.
Die Umsetzung der Polyisocyanate mit den Verbindungen mit zwei aktiven Wasser- stoffatomen erfolgt üblicherweise in Gegenwart von Treibmitteln. Als Treibmittel können allgemein bekannte chemisch oder physikalisch wirkende Verbindungen eingesetzt werden. Als chemisch wirkendes Treibmittel kann bevorzugt Wasser eingesetzt werden. Beispiele für physikalische Treibmittel sind inerte (cyclo)aliphatische Kohlenwasserstoffe mit 4 bis 8 Kohlenstoffatomen, die unter den Bedingungen der PoIy- urethanbildung verdampfen. Die Menge der eingesetzten Treibmittel richtet sich nach der angestrebten Dichte der Schaumstoffe.The reaction of the polyisocyanates with the compounds having two active hydrogen atoms is usually carried out in the presence of blowing agents. As blowing agents it is possible to use generally known chemically or physically active compounds. As the chemically acting blowing agent, water can preferably be used. Examples of physical blowing agents are inert (cyclo) aliphatic hydrocarbons having from 4 to 8 carbon atoms which evaporate under the conditions of polyurethane formation. The amount of blowing agent used depends on the desired density of the foams.
Die Umsetzung der Polyisocyanate mit den Verbindungen mit zwei aktiven Wasserstoffatomen erfolgt gegebenenfalls in Anwesenheit von Katalysatoren sowie von Hilfs- und/oder Zusatzstoffen, wie z.B. Zellreglern, Trennmitteln, Pigmenten, Verstärkungsstoffen wie Glasfasern, oberflächenaktiven Verbindungen und/oder Stabilisatoren gegen oxidativen, thermischen, oder mikrobiellen Abbau oder Alterung.The reaction of the polyisocyanates with the compounds with two active hydrogen atoms is optionally carried out in the presence of catalysts and of auxiliaries and / or additives, such. Cell regulators, release agents, pigments, reinforcing agents such as glass fibers, surface-active compounds and / or stabilizers against oxidative, thermal or microbial degradation or aging.
Als Katalysatoren für die Herstellung der erfindungsgemäßen mikrozellulären PoIy- urethan-Elastomere können die üblichen und bekannten Polyurethanbildungskatalysatoren eingesetzt werden, beispielsweise organische Metallverbindungen, wie Zinndi- acetat, Zinndioctoat, Dibutylzinndilaurat, und/oder stark basische Amine wie Diazabi- cyclooctan, Bis(N,N-Dimethylaminoethyl)ether oder die oben genannten Amine. Die Katalysatoren werden vorzugsweise in einer Menge von 0,01 bis 10 Gew.-%, vorzugs- weise 0,02 bis 5 Gew.-%, bezogen auf die Reaktionsmischung, eingesetzt. Wie oben beschrieben, werden bevorzugt Amine, insbesondere tertiäre Amine, als Katalysatoren eingesetzt. Die Amine können, wie oben beschrieben, einzeln oder als beliebige Gemische untereinander ein gesetzt werden. Diese wirken in den mikrozellulären Polyurethan-Elastomeren gleichzeitig als Komponente aii). Dazu ist es bevorzugt, nur die genannten Amine in den für die Wirkung als Stabilisator erforderlichen Mengen einzusetzen. Falls dies für die katalytische Wirkung nicht ausreichend ist, können die tertiären Amine in Kombination mit anderen Katalysatoren eingesetzt werden.Catalysts for the preparation of the microcellular polyurethane elastomers according to the invention can be the customary and known polyurethane-forming catalysts, for example organic metal compounds, such as tin diacetate, tin dioctoate, dibutyltin dilaurate, and / or strongly basic amines, such as diazabicyclooctane, bis (N, N-dimethylaminoethyl) ether or the above-mentioned amines. The catalysts are preferably used in an amount of from 0.01 to 10% by weight, preferably from 0.02 to 5% by weight, based on the reaction mixture. As described above, amines, in particular tertiary amines, are preferably used as catalysts. The amines can, as described above, individually or as any mixtures with one another set. These act simultaneously in the microcellular polyurethane elastomers as component aii). For this purpose, it is preferred to use only the amines mentioned in the amounts required for the action as a stabilizer. If this is not sufficient for the catalytic effect, the tertiary amines can be used in combination with other catalysts.
Als organische Amine sind die aus dem Stand der Technik bekannten tertiären Amine verwendbar. In Betracht kommen beispielsweise organische Amine, wie Triethylamin, Triethylendiamin, Tributylamin, Dimethylbenzylamin, N,N,N',N'-Tetramethylethylen- diamin, N,N,N',N'-Tetramethyl-butandiamin, N,N,N',N'-Tetramethyl-hexan-1 ,6-diamin, Dimethylcyclohexylamin, Pentamethyldipropylentriamin, Pentamethyldiethylentriamin, 3-Methyl-6-dimethylamino-3-azapentol, Dimethylaminopropylamin, 1 ,3-Bisdimethyl- aminobutan, Bis-(2-dimethylaminoethyl)-ether, N-Ethylmorpholin, N-Methylmorpholin, N-Cyclohexylmorpholin, 2-Dimethylamino-ethoxy-ethanol, Dimethylethanolamin, Tetramethylhexamethylendiamin, Dimethylamino-N-methyl-ethanolamin, N-Methyl- imidazol, N-(3-Aminopropyl)imidazol, N-(3-Aminopropyl)-2-Methylimidazol, 1-(2- Hydroxyethyl)imidazol, N-Formyl-N,N'-dimethylbutylendiamin, N-Dimethylamino- ethylmorpholin, 3,3'-Bis-dimethylamino-di-n-propylamin und/oder 2,2'-Dipiparazin- diisopropylether, Dimethylpiparazin, N,N'-Bis-(3-aminopropyl)-ethylendiamin und/oder Tris-(N,N-dimethylaminopropyl)-s-hexahydrotriazin, oder Mischungen enthaltend mindestens zwei der genannten Amine, wobei auch höhermolekulare tertiäre Amine, wie sie beispielsweise in DE-A 28 12 256 beschrieben sind, möglich sind. Besonders be- vorzugt ist der Einsatz von Triethylendiamin.As organic amines known from the prior art tertiary amines are useful. For example, suitable are organic amines, such as triethylamine, triethylenediamine, tributylamine, dimethylbenzylamine, N, N, N ', N'-tetramethylethylenediamine, N, N, N', N'-tetramethylbutanediamine, N, N, N ' , N'-tetramethylhexane-1,6-diamine, dimethylcyclohexylamine, pentamethyldipropylenetriamine, pentamethyldiethylenetriamine, 3-methyl-6-dimethylamino-3-azapentol, dimethylaminopropylamine, 1,3-bis-dimethylaminobutane, bis (2-dimethylaminoethyl) - ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, 2-dimethylaminoethoxyethanol, dimethylethanolamine, tetramethylhexamethylenediamine, dimethylamino-N-methylethanolamine, N-methylimidazole, N- (3-aminopropyl) imidazole, N - (3-aminopropyl) -2-methylimidazole, 1- (2-hydroxyethyl) imidazole, N-formyl-N, N'-dimethylbutylenediamine, N-dimethylamino-ethylmorpholine, 3,3'-bis-dimethylamino-di-n- propylamine and / or 2,2'-dipiparazin diisopropyl ether, dimethyl piparazine, N, N'-bis (3-aminopropyl) ethylenediamine and / or tris (N, N-dimethylaminopropyl) -s-hexahydr otriazine, or mixtures containing at least two of said amines, wherein higher molecular weight tertiary amines, as described for example in DE-A 28 12 256, are possible. Particularly preferred is the use of triethylenediamine.
Die im Gemisch mit den tertiären Aminen einsetzbaren Katalysatoren sind, wie oben beschrieben, hauptsächlich organische Metallverbindungen, insbesondere Zinnverbindungen, wie Zinndiacetat, Zinndioctoat, Dibutylzinndilaurat, und/oder Bismuthverbin- düngen.The catalysts which can be used in a mixture with the tertiary amines are, as described above, mainly organic metal compounds, in particular tin compounds, such as tin diacetate, tin dioctoate, dibutyltin dilaurate, and / or bismuth compound.
Die Katalysatoren werden vorzugsweise mit den Verbindungen mit mindestens zwei mit Isocyanatgruppen reaktiven Wasserstoffatomen vermischt. Prinzipiell ist es auch möglich, zumindest die organischen Metallverbindungen auch mit den Polyisocyanaten zu vermischen.The catalysts are preferably mixed with the compounds having at least two isocyanate-reactive hydrogen atoms. In principle, it is also possible to mix at least the organic metal compounds with the polyisocyanates.
Im allgemeinen werden die Polyisocyanate als Isocyanatkomponente und die Verbindungen mit mindestens zwei mit Isocyanatgruppen reaktiven Wasserstoffatomen, die zumeist im Gemisch mit den Katalysatoren, gegebenenfalls den Treibmitteln und Zu- satzstoffen eingesetzt wird, als Polyolkomponente bezeichnet. Zur Herstellung von Polyurethanschaumstoffen werden die Isocyanatkomponente und die Polyolkomponente zumeist in solchen Mengen zur Umsetzung gebracht, dass das Äquivalenzverhältnis von NCO-Gruppen zur Summe der reaktiven Wasserstoffatome 1:0,8 bis 1 :1 ,25, vorzugsweise 1 :0,9 bis 1:1 ,15 beträgt. Ein Verhältnis von 1 :1 ent- spricht hierbei einem NGO-Index von 100.In general, the polyisocyanates are referred to as the isocyanate component and the compounds having at least two isocyanate-reactive hydrogen atoms, which is usually used in admixture with the catalysts, optionally the blowing agents and additives, as a polyol component. For the preparation of polyurethane foams, the isocyanate component and the polyol component are usually reacted in amounts such that the equivalent ratio of NCO groups to the sum of the reactive hydrogen atoms is 1: 0.8 to 1: 1, 25, preferably 1: 0.9 to 1 : 1, 15 is. A ratio of 1: 1 corresponds to an NGO index of 100.
Die Umsetzung zum mikrozellulären Polyurethan-Elastomer wird bevorzugt in Formen unter Verdichtung durchgeführt. Die Formen bestehen bevorzugt aus Metall, z.B. Stahl oder Aluminium, oder auch aus Kunststoff, z.B. Epoxyharz. Die Ausgangskomponen- ten werden bei Temperaturen von 15 bis 900C, vorzugsweise bei 20 bis 350C gemischt, und gegebenenfalls unter erhöhtem Druck, in das bevorzugt geschlossene Formwerkzeug eingebracht. Die Vermischung kann beim Einbringen durch im Stand der Technik bekannte Hoch- oder Niederdruckmischköpfe erfolgen. Die Temperatur der Form beträgt im allgemeinen zwischen 20 und 900C, bevorzugt zwischen 30 und 60°C.The reaction to the microcellular polyurethane elastomer is preferably carried out in densified forms. The molds are preferably made of metal, for example steel or aluminum, or else of plastic, for example epoxy resin. The starting components are mixed at temperatures of 15 to 90 ° C., preferably at 20 to 35 ° C., and if appropriate under elevated pressure, introduced into the preferably closed molding tool. The mixing can be carried out during introduction by known in the art high or low pressure mixing heads. The mold temperature is generally between 20 and 90 0 C, preferably between 30 and 60 ° C.
Die Menge des in die Form eingebrachten Reaktionsgemisches wird so bemessen, dass die erhaltenen Formkörper eine Dichte von 250 bis 600 g/l oder von 800 bis 1200 g/l, bevorzugt von 400 bis 600 g/l oder von 820 bis 1050 g/l, aufweisen. Die Ver- dichtungsgrade der resultierenden mikrozellulären Polyurethan-Elastomere, liegen zwischen 1 ,1 und 8,5, bevorzugt zwischen 1,2 und 5, besonders bevorzugt zwischen 1 ,5 und 4.The amount of the reaction mixture introduced into the mold is such that the resulting molded articles have a density of from 250 to 600 g / l or from 800 to 1200 g / l, preferably from 400 to 600 g / l or from 820 to 1050 g / l , exhibit. The degrees of compression of the resulting microcellular polyurethane elastomers are between 1, 1 and 8.5, preferably between 1.2 and 5, particularly preferably between 1, 5 and 4.
Die erfindungsgemäßen mikrozellulären Polyurethan-Elastomere können für Lenk- räder, Sicherheitsbekleidung und bevorzugt für Schuhsohlen verwendet werden.The microcellular polyurethane elastomers according to the invention can be used for steering wheels, safety clothing and preferably for shoe soles.
Die Erfindung soll an den nachfolgenden Beispielen näher erläutert werden.The invention will be explained in more detail in the following examples.
Vergleichsbeispiele V1 bis V3 und Beispiele 1 bis 4Comparative Examples V1 to V3 and Examples 1 to 4
100 Gew.-Teile der Polyol-Komponente und die in Tabelle 1 angegebenen Gew.-Teile der Isocyanat-Komponente wurden bei 23°C intensiv gemischt und die Mischung in ein auf 500C temperiertes, plattenförmiges Formwerkzeug aus Aluminium mit den Abmessungen 20cm x 20cm x 1cm in einer solchen Menge eingebracht, dass nach dem Auf- schäumen und Aushärten lassen im geschlossenen Formwerkzeug eine Platte aus mikrozellulärem Polyurethan-Elastomer mit einer Gesamtdichte von 550 g/l resultierte.100 parts by weight of the polyol component and the specified in Table 1 parts by weight of the isocyanate component were thoroughly mixed at 23 ° C and the mixture in a tempered at 50 0 C, plate-shaped aluminum mold with dimensions of 20cm x 20 cm × 1 cm in such an amount that after foaming and curing in the closed mold, a microcellular polyurethane elastomer plate with a total density of 550 g / l resulted.
Aus den so hergestellten Elastomer-Platten wurden nach 24 h Lagerung mit einem Stanzwerkzeug Schulterstäbe als Prüfkörper ausgestanzt. Vor Beginn der Alterungs- versuche wurden die Ausgangswerte der Zugfestigkeit nach DIN 53543 bestimmt. Die Probekörper wurden danach einem Alterungstest bei 700C unter Wasser nach DIN 53543 unterzogen. Die Probennahme erfolgt nach 14 Tagen. Die Ergebnisse der Tests sind in Tabelle 2 zusammengefasst.From the elastomer plates produced in this way, shoulder bars were punched out as test specimens after 24 hours of storage with a punching tool. Before the beginning of the aging tests, the initial values of the tensile strength according to DIN 53543 were determined. The specimens were then after an aging test at 70 0 C under water after DIN 53543 subjected. Sampling takes place after 14 days. The results of the tests are summarized in Table 2.
Die Restzugfestigkeit und -dehnung nach 2 Wochen Hydrolysealterung der Proben 1-4 ist deutlich höher als die der Vergleichsproben V1 -V3.The residual tensile strength and elongation after 2 weeks hydrolysis aging of samples 1-4 is significantly higher than that of comparative samples V1 -V3.
Verwendete Einsatzstoffe:Used ingredients:
PESOL 1 : Polyesteralkohol aus Adipinsäure, 1 ,4-Butandiol und Ethylenglykol (Lupraphen® 8108) der Elastogran GmbH, OHZ=56 mg KOH/g, Funktionalität=2PESOL 1: polyester alcohol prepared from adipic acid, 1, 4-butanediol and ethylene glycol (Lupraphen ® 8108) Elastogran GmbH, OHN = 56 mg KOH / g, functionality = 2
Aminkatalysator: 33 %gew.-ige Lösung von Triethylendiamin in Ethylenglykol (Lupragen® N 202) der BASF AGAmine catalyst: 33% strength by weight solution of triethylenediamine in ethylene glycol (Lupragen ® N 202) BASF AG
Zellstabilisator: Dabco® DC 193 von Air ProductsCell stabilizer: Dabco ® DC 193 from Air Products
Isocyanat-Prepolymer: Prepoymer auf Basis von 4,4'-MDI und PESOL1 , NCO-Gehalt=17,4 %Isocyanate prepolymer: prepolymer based on 4,4'-MDI and PESOL1, NCO content = 17.4%
Hydrolyseschutzmittel ai): TriphenylphosphitHydrolysis protection agent ai): triphenyl phosphite
Hydrolyseschutzmittel aii): TriethylendiaminHydrolysis protection agent aii): triethylenediamine
Tabelle 1 : Zusammensetzung der Systeme V1-V3 (Vergleichsbeispiele) sowie 1-4 (erfindungsgemäße Beispiele).Table 1: Composition of the systems V1-V3 (comparative examples) and 1-4 (examples according to the invention).
Figure imgf000010_0001
Tabelle 2: Alterungsergebnisse der Proben V1-V3 sowie 1-4.
Figure imgf000010_0001
Table 2: Aging results of samples V1-V3 and 1-4.
Figure imgf000011_0001
a) = Restzugfestigkeit bzw. Restdehnung in % vom Ausgangswert nach 2 Wochen Alterung.
Figure imgf000011_0001
a) = residual tensile strength or residual strain in% of the initial value after 2 weeks of aging.
n.m. = nicht messbar (Probe zerstört)n.m. = not measurable (sample destroyed)
t = Alterungsintervall in Tagen t = aging interval in days

Claims

Patentansprüche claims
1. Mikrozelluläre Polyurethan-Elastomere, herstellbar durch Umsetzung von PoIy- isocyanaten mit Verbindungen mit mindestens zwei mit Isocyanatgruppen reak- tiven Wasserstoffatomen, dadurch gekennzeichnet, dass sie eine Kombination a), bestehend aus ai) einem aromatischem Phosphit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung enthält, wobei das molare Verhältnis zwischen ai) und aii) 0,005 bis 4,0 beträgt.1. Microcellular polyurethane elastomers obtainable by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that they contain a combination a) consisting of ai) an aromatic phosphite having a phosphorus content of 9 , 00 to 11, 00 wt .-%, and aii) of an amine compound, wherein the molar ratio between ai) and aii) is 0.005 to 4.0.
2. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass das molare Verhältnis zwischen ai) und aii) 0,1 bis 3,0 beträgt.2. Microcellular polyurethane elastomers according to claim 1, characterized in that the molar ratio between ai) and aii) is 0.1 to 3.0.
3. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1, dadurch gekennzeichnet, dass das molare Verhältnis zwischen ai) und aii) 0,5 bis 2,0 beträgt.3. Microcellular polyurethane elastomers according to claim 1, characterized in that the molar ratio between ai) and aii) is 0.5 to 2.0.
4. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass das aromatische Phosphit einen Phosphor-Gehalt von 9,90 bis 10,10 Gew.-% aufweist.4. Microcellular polyurethane elastomers according to claim 1, characterized in that the aromatic phosphite has a phosphorus content of 9.90 to 10.10 wt .-%.
5. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass das aromatische Phosphit einen Phosphor-Gehalt von 9,95 bis 10,05 Gew.-% aufweist.5. Microcellular polyurethane elastomers according to claim 1, characterized in that the aromatic phosphite has a phosphorus content of 9.95 to 10.05 wt .-%.
6. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeich- net, dass das aromatische Phosphit Triphenylphosphit ist.6. Microcellular polyurethane elastomers according to claim 1, characterized in that the aromatic phosphite is triphenyl phosphite.
7. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass als Amine aii) tertiäre Amine eingesetzt werden.7. Microcellular polyurethane elastomers according to claim 1, characterized in that tertiary amines are used as amines aii).
8. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass die tertiären Amine ausgewählt sind aus der Gruppe, enthaltend Triethylamin, Triethylendiamin, Tributylamin, Dimethylbenzylamin, N, N, N', N'- Tetramethylethylendiamin, N,N,N',N'-Tetramethyl-butandiamin, N, N, N', N'- Tetramethyl-hexan-1 ,6-diamin, Dimethylcyclohexylamin, Pentamethyldipropy- lentriamin, Pentamethyldiethylentriamin, 3-Methyl-6-dimethylamino-3-azapentol,8. Microcellular polyurethane elastomers according to claim 1, characterized in that the tertiary amines are selected from the group comprising triethylamine, triethylenediamine, tributylamine, dimethylbenzylamine, N, N, N ', N'-tetramethylethylenediamine, N, N, N' , N'-tetramethylbutanediamine, N, N, N ', N'-tetramethylhexane-1,6-diamine, dimethylcyclohexylamine, pentamethyldipropylenetriamine, pentamethyldiethylenetriamine, 3-methyl-6-dimethylamino-3-azapentol,
Dimethylaminopropylamin, 1 ,3-Bisdimethylaminobutan, Bis-(2-dimethyl- aminoethyl)-ether, N-Ethylmorpholin, N-Methylmorpholin, N-Cyclohexyl- morpholin, 2-Dimethylamino-ethoxy-ethanol, Dimethylethanolamin, Tetramethyl- hexamethylendiamin, Dimethylamino-N-methyl-ethanolamin, N-Methylimidazol, N-(3-Aminopropyl)imidazol, N-(3-Aminopropyl)-2-Methylimidazol, 1 -(2-Hydroxy- ethyl)imidazol, N-Formyl-N.N'-dimethylbutylendiamin, N-Dimethylaminoethyl- momholin. 3,3'-Bis-dimethylamino-di-n-propylamin und/oder 2,2'-Dipiparazin- diisopropylether, Dimethylpiparazin, N,N'-Bis-(3-aminopropyl)-ethylendiamin und/oder Tris-(N,N-dimethylaminopropyl)-s-hexahydrotriazin, oder Mischungen enthaltend mindestens zwei der genannten Amine.Dimethylaminopropylamine, 1, 3-bisdimethylaminobutane, bis (2-dimethylaminoethyl) ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, 2-dimethylaminoethoxyethanol, dimethylethanolamine, tetramethylhexamethylenediamine, dimethylamino N-methylethanolamine, N-methylimidazole, N- (3-aminopropyl) imidazole, N- (3-aminopropyl) -2-methylimidazole, 1- (2-hydroxyethyl) imidazole, N-formyl-N, N ' dimethylbutylenediamine, N-dimethylaminoethylmomholin. 3,3'-bis-dimethylamino-di-n-propylamine and / or 2,2'-dipiparazinone diisopropyl ether, dimethyl piparazine, N, N'-bis (3-aminopropyl) ethylenediamine and / or tris (N, N-dimethylaminopropyl) -s-hexahydrotriazine, or mixtures containing at least two of said amines.
9. Mikrozelluläre Polyurethan-Elastomere nach Anspruch 1 , dadurch gekennzeichnet, dass das tertiäre Amin Triethylendiamin ist.9. Microcellular polyurethane elastomers according to claim 1, characterized in that the tertiary amine is triethylenediamine.
10. Verfahren zur Herstellung von mikrozellulären Polyurethan-Elastomeren durch Umsetzung von Polyisocyanaten mit Verbindungen mit mindestens zwei mit Iso- cyanatgruppen reaktiven Wasserstoffatomen, dadurch gekennzeichnet, dass die10. A process for the preparation of microcellular polyurethane elastomers by reacting polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms, characterized in that the
Umsetzung in Anwesenheit eines Hydrolyseschutzmittels a), das eine Kombination, bestehend aus ai) einem aromatischem Phosphit mit einem Phosphor- Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung ist, durchgeführt wird, wobei das molare Verhältnis zwischen ai) und aii) 0,005 bis 4,0 be- trägt.Reacting in the presence of a hydrolysis protection agent a), which is a combination consisting of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11, 00 wt .-%, and aii) an amine compound, wherein the molar Ratio between ai) and aii) is 0.005 to 4.0.
11. Verwendung von mikrozellulären Polyurethan-Elastomeren nach einem der Ansprüche 1-9 zur Herstellung Schuhsohlen.11. Use of microcellular polyurethane elastomers according to any one of claims 1-9 for the production of shoe soles.
12. Verwendung von ai) einem aromatischem Phosphit mit einem Phosphor-Gehalt von 9,00 bis 11 ,00 Gew.-%, und aii) einer Aminverbindung als Hydrolyseschutzmittel für mikrozelluläre Polyurethan-Elastomere.12. Use of ai) an aromatic phosphite having a phosphorus content of 9.00 to 11.00% by weight, and aii) an amine compound as a hydrolysis protection agent for microcellular polyurethane elastomers.
13. Schuhsohlen, enthaltend mikrozelluläre Polyurethan-Elastomere nach einem der Ansprüche 1 bis 9. 13. shoe soles containing microcellular polyurethane elastomers according to any one of claims 1 to 9.
PCT/EP2005/013405 2004-12-17 2005-12-14 Method for producing microcellular polyurethane elastomers WO2006066763A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2005800431336A CN101080428B (en) 2004-12-17 2005-12-14 Method for producing microcellular polyurethane elastomers

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004061609.4 2004-12-17
DE102004061609.4A DE102004061609B4 (en) 2004-12-17 2004-12-17 Microcellular polyurethane elastomers preparable by reaction of polyisocyanates containing 4,4'-diphenylmethane diisocyanate, process for the preparation of such microcellular polyurethane elastomers and their use

Publications (1)

Publication Number Publication Date
WO2006066763A1 true WO2006066763A1 (en) 2006-06-29

Family

ID=36072021

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2005/013405 WO2006066763A1 (en) 2004-12-17 2005-12-14 Method for producing microcellular polyurethane elastomers

Country Status (4)

Country Link
KR (1) KR20070100937A (en)
CN (1) CN101080428B (en)
DE (1) DE102004061609B4 (en)
WO (1) WO2006066763A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008074701A1 (en) * 2006-12-20 2008-06-26 Basf Se Anisotropic cellular elastomers
WO2008074705A1 (en) * 2006-12-20 2008-06-26 Basf Se Anisotropic cellular elastomers
US7985780B2 (en) 2005-02-22 2011-07-26 Basf Se Cylindrical mouldings based on cellular polyurethane elastomers

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2710901A1 (en) * 1976-03-12 1977-09-15 Prb Sa INTEGRATED SKIN POLYURETHANE AND METHOD FOR MANUFACTURING THE SAME
DE3008811A1 (en) * 1979-03-09 1980-09-18 Prb Sa METHOD FOR MANUFACTURING POLYURETHANE WITH INTEGRAL SKIN AND POLYURETHANE
US4477600A (en) * 1983-09-23 1984-10-16 Stauffer Chemical Company Polyurethane foams having low scorch discoloration

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2710901A1 (en) * 1976-03-12 1977-09-15 Prb Sa INTEGRATED SKIN POLYURETHANE AND METHOD FOR MANUFACTURING THE SAME
DE3008811A1 (en) * 1979-03-09 1980-09-18 Prb Sa METHOD FOR MANUFACTURING POLYURETHANE WITH INTEGRAL SKIN AND POLYURETHANE
US4477600A (en) * 1983-09-23 1984-10-16 Stauffer Chemical Company Polyurethane foams having low scorch discoloration

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7985780B2 (en) 2005-02-22 2011-07-26 Basf Se Cylindrical mouldings based on cellular polyurethane elastomers
WO2008074701A1 (en) * 2006-12-20 2008-06-26 Basf Se Anisotropic cellular elastomers
WO2008074705A1 (en) * 2006-12-20 2008-06-26 Basf Se Anisotropic cellular elastomers
US8282851B2 (en) 2006-12-20 2012-10-09 Basf Se Anisotropic cellular elastomers

Also Published As

Publication number Publication date
DE102004061609B4 (en) 2014-06-26
KR20070100937A (en) 2007-10-15
CN101080428A (en) 2007-11-28
CN101080428B (en) 2011-02-02
DE102004061609A1 (en) 2006-07-06

Similar Documents

Publication Publication Date Title
EP2013258B1 (en) Process for preparing polyurethanes
EP0296449B1 (en) Process for the preparation of room-temperature curing soft polyurethene foams
EP1650240B1 (en) Flexible polyurethane foams of low density and low hardness
EP1720927B1 (en) Shoe soles made from tin and transition metal free polyurethane foams
WO2014064130A1 (en) Method for producing soft polyurethane foam based on polyester polyols
EP1861446B1 (en) Polyurethane shoe soles
DE102004033849A1 (en) Process for the preparation of liquid, storage-stable carbodiimide and / or uretonimine containing organic isocyanates having a low color number
EP0499053A2 (en) Process for the production of polyurethane elastomers and mixtures of polyoxybutylene-polyoxyalkylene glycols and glycidyl compounds suitable therefore
EP2877511B2 (en) Phosphorous compounds containing polyurethane foams
EP1024156A1 (en) Polyurethane casting elastomers based on durol diisocyanate
EP1345974B1 (en) Method for producing polyurethane elastomers having high heat resistance
WO2006066763A1 (en) Method for producing microcellular polyurethane elastomers
EP3268408A1 (en) Molded polyurethane bodies with excellent flexibility at low temperatures
WO2019201953A1 (en) High-elasticity shoe sole material and use thereof
EP1471109B1 (en) Composition containing an oxalic acid dialkyl ester and a sterically hindered carbodiimide
EP1446436B1 (en) Method for producing polyurethanes
DE10359024A1 (en) Tin-free polyurethane foam, e.g. for production of shoe soles, obtained by reacting polyisocyanate with isocyanate-reactive compounds in presence of alkali metal carboxylate as catalyst, e.g. potassium acetate
EP1170314A1 (en) Polyisocyanate polyaddition products based on polyols with low unsaturation
EP3492505A1 (en) Reaction system for a 1k polyurethane rigid foam
DE3842220A1 (en) PROCESS FOR PRODUCING OPEN CELL HYDROPHILIC POLYURETHANE FOAMS
DE102008030940A1 (en) Soft polyurethane foam comprises a content of a hydroxyl group containing oil, grease or resin, which are chemically bounded in polyurethane
DE10000494B4 (en) Process for the preparation of soft polyurethane block or molded foams
EP1162230B1 (en) Cellular polyisocyanate-polyaddition products
DE10227187A1 (en) Polyurethane for use e.g. in shoe sole production, based on a prepolymer obtained by reacting polyisocyanate with an alkoxylated triol and a polyether-ol obtained by alkoxylating a diol
EP1041098A2 (en) Preparation process for polyurethanes

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KN KP KR KZ LC LK LR LS LT LU LV LY MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
DPE1 Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101)
WWE Wipo information: entry into national phase

Ref document number: 1200701141

Country of ref document: VN

WWE Wipo information: entry into national phase

Ref document number: 200580043133.6

Country of ref document: CN

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 1020077015957

Country of ref document: KR

WWE Wipo information: entry into national phase

Ref document number: 3139/CHENP/2007

Country of ref document: IN

122 Ep: pct application non-entry in european phase

Ref document number: 05850265

Country of ref document: EP

Kind code of ref document: A1

WWW Wipo information: withdrawn in national office

Ref document number: 5850265

Country of ref document: EP