DE102011050220A1 - New isocyanate-terminated prepolymer obtained by reacting an isocyanate composition comprising monomeric and polymeric diphenylmethane diisocyanate with a polyester ether polyol, useful to prepare polyurethane/polyisocyanurate polymer - Google Patents

Abstract

Isocyanate-terminated prepolymer (C1) having an isocyanate content of 26-31 wt.% obtained by reacting an isocyanate composition (A) having a viscosity of 60-800 mPas at 25[deg] C with a polyester ether polyol (B) having an average functionality of 1.9-2.1 and hydroxyl number of 200-500 mg potassium hydroxide (KOH)/g, is new : Isocyanate-terminated prepolymer (C1) having an isocyanate content of 26-31 wt.% obtained by reacting an isocyanate composition (A) having a viscosity of 60-800 mPas at 25[deg] C with a polyester ether polyol (B) having an average functionality of 1.9-2.1 and hydroxyl number of 200-500 mg potassium hydroxide (KOH)/g, is new, where: (A) comprises 25-60 wt.% of monomeric diphenylmethane diisocyanate (A1) and 40-75 wt.% of polymeric diphenylmethane diisocyanate, (B) is obtained by reacting a dicarboxylic acid and/or its derivative (B1) with at least a polyol (B2) and/or an epoxide (B3), and the amount of (B) is 1.5-6 wt.%. Independent claims are included for: (1) polyurethane/polyisocyanurate polymer obtained by reacting (C1) with an isocyanate reactive component (D1); and (2) a composite element comprising a layer containing polyurethane/polyisocyanurate polymer and a top layer.

Description

The present invention relates to an isocyanate-terminated prepolymer having an NCO content of ≥ 26.0% by mass to ≤ 31.0% by mass, which is obtainable from the reaction of an isocyanate composition comprising ≥ 30% by mass to ≤ 60% by mass of 2-core MDI and ≥ 40% by mass to ≤ 70% by mass of polymeric MDI with a bifunctional polyester ether polyol obtained from the reaction of a dicarboxylic acid / dicarboxylic acid derivative with at least one polyol and with an epoxide. Further objects of the invention are a PUR / PIR polymer produced from this prepolymer, its use and composite elements based thereon.

In the field of application of the metal composite elements for industrial hall construction, a high and permanent adhesive strength of the insulating foam to the metallic cover layer is required. This applies in particular to polyisocyanurate foams. For this purpose can be used as starting materials isocyanate group-containing polyurethane prepolymers obtained by reacting a stoichiometric excess of an organic polyisocyanate with an organic polyol. Such prepolymers are well known in the field of polyurethanes and are used, for example, in the production of flexible and rigid foams as well as elastomers, coatings, adhesives and the like.

• – Kontinuierliche Anlieferung einer organischen Polyisocyanatzusammensetzung und einer isocyanatreaktiven Verbindung mit einem durchschnittlichen Molekulargewicht von mindestens 1000, und wahlweise eines Katalysators zu einem Reaktionsbereich, wobei das relative Verhältnis der Isocyanatzusammensetzung und der isocyanatreaktiven Verbindung für die Bildung eines Vorpolymers mit einem NCO-Gehalt im Bereich von 2 bis 15 Gewichts-% geeignet ist;
• – Umsetzung der Isocyanatzusammensetzung und der isocyanatreaktiven Verbindung im Reaktionsbereich unter Bildung eines isocyanat-terminierten Vorpolymers;
• – Kontinuierliche Entfernung des Reaktionsgemisches aus dem Reaktionsbereich;
• – falls notwendig, Ausreifenlassen des Reaktionsgemisches zur Bildung eines Vorpolymers mit einem NCO-Gehalt im Bereich von 2 bis 15 Gewichts-%,
• – Anliefern des Vorpolymers zu einem Schaumstoffbildungsbereich;
• – Umsetzung des Vorpolymers im Schaumstoffbildungsbereich mit einer Wasser umfassenden isocyanatreaktiven Komponente; und
• – Wiedergewinnung des derart gebildeten Schaumstoffs, wobei der Reaktionsbereich auch als Schaumstoffbildungsbereich verwendet wird.

The preparation of such NCO prepolymers has been described in numerous publications. For example, disclosed DE 69132613 T2 a process for producing flexible foams which comprises the following steps:

• Continuously supplying an organic polyisocyanate composition and an isocyanate-reactive compound having an average molecular weight of at least 1000, and optionally a catalyst to a reaction range, wherein the relative ratio of the isocyanate composition and the isocyanate-reactive compound for the formation of a prepolymer having an NCO content in the range of 2 to 15% by weight is suitable;
• Reaction of the isocyanate composition and the isocyanate-reactive compound in the reaction region to form an isocyanate-terminated prepolymer;
• - Continuous removal of the reaction mixture from the reaction area;
• If necessary, allowing the reaction mixture to mature to form a prepolymer having an NCO content in the range of 2 to 15% by weight,
• - supplying the prepolymer to a foam-forming region;
• Reaction of the prepolymer in the foam-forming region with an isocyanate-reactive component comprising water; and
• Recovery of the thus formed foam, the reaction area also being used as the foam-forming area.

In WO 94/2936 1A1 describes a process for producing flexible foam, in which a prepolymer having an NCO content of 5 to 10% by weight is used. The prepolymer is the reaction product of an excess of polyisocyanate with at least 85% by weight of 4,4'-diphenylmethane diisocyanate or a variant thereof with a polyol having a nominal hydroxyl functionality of 2.5 to 3.5, an average hydroxyl equivalent weight of 1000 to 3000 and has an oxyethylene content of 50 to 85% by weight. The prepolymer is reacted with water, the amount of water being at least 20 parts by weight per 100 parts by weight of the prepolymer.

DE 2823762 A1 relates to a process for the continuous production of thermoplastic polyurethanes from polyhydroxy compounds, diisocyanates and low molecular weight chain extenders, in which the starting components are passed through a mixing zone and then through a reaction zone. The starting components are mixed in a mixing zone in which a sufficient for the subsequent polyaddition reaction, virtually complete mixing takes place. The product temperature is so low that a reaction of the components is largely avoided. The mixture is then fed by means of a precision pump in a static mixer of such a length and diameter that at a flow rate preventing the preparation of polymers, the reaction components remain in the static mixer so long that the polyaddition occurs.

DE 19823392 A1 discloses a process for the preparation of isocyanate group-containing prepolymers by reacting organic isocyanates with H-acidic compounds, which is characterized in that the reaction takes place to prepolymer directly in the process stream of the isocyanate-generating plant. Articles of the publication are also the isocyanate group-containing prepolymers thus prepared, their use for the production of PUR and a process for the preparation of PUR by Reaction of at least one prepolymer containing isocyanate groups, optionally in admixture with other organic and / or modified organic isocyanates with compounds having at least two reactive hydrogen atoms in the presence of optionally blowing agents, catalysts and optionally further auxiliaries and / or additives.

EP 0 497 131 A2 discloses ether and ester group-containing isocyanate prepolymers having an NCO content of 1.9 to 25% by weight based on A) a polyisocyanate component consisting of at least one organic polyisocyanate having an average molecular weight of 168 to 1000, B) esterification products of polyether polyols an average hydroxyl number of 200 to 600 with monocarboxylic acids, optionally in admixture with minor amounts of polybasic carboxylic acids and optionally C) organic polyhydroxyl compounds in the molecular weight range from 62 to 200 in an amount of up to 25 hydroxyl equivalent%, based on component B), a process for the preparation of such isocyanate prepolymers by reacting said starting materials while maintaining an NCO / OH equivalent ratio of 1.7: 1 to 20: 1 and the use of isocyanate prepolymers as a binder or binder component in polyurethane coating compositions, sealants or -Vergussmass s.

DE 196 01 410 A1 deals with a process for producing flexible polyurethane foams by reacting a) organic and / or modified organic NCO group-containing compounds with b) higher molecular weight compounds having at least two reactive hydrogen atoms and c) optionally low molecular weight chain extenders and / or crosslinking agents in the presence of d) Blowing agents, e) catalysts, f) flame retardants and optionally g) further auxiliaries and / or additives. NCO group-containing prepolymers which are reaction products of polyester polyols and / or polyester ether polyols and aromatic diisocyanates and are subjected to a special aftertreatment are used as organic and / or modified organic NCO group-containing compounds.

WO 2009/055436 A1 relates to polyester-ether polyols and their use in urethane prepolymers, urethane foams and non-foamed urethane coatings, adhesives, sealants and / or elastomers. Methods for preparing such polyesterether polyols by double metal cyanide catalysis and for preparing urethane prepolymers are described. The polyester ether polyols described therein are preferably the reaction product of phthalic anhydride, diethylene glycol and propylene oxide. The polyester-ether polyols have improved solubility and compatibility in blends of either polyether polyols and / or polyester polyols. The polyester-ether polyols are preferably less viscous than the polyester-polyol intermediates and are typically soluble in either polyester and / or polyether polyols. In addition, the polyesterether polyols improve the hydrolytic stability of coatings, adhesives, sealants and elastomers in which they are used.

The processes described in the prior art for the preparation of NCO prepolymers therefore require a reaction of an isocyanate group-containing component with an isocyanate-reactive component in a reactor and in particular under controlled mixing and temperature conditions.

The object of the present invention is therefore to provide NCO prepolymers which can be prepared in a simple and rapid manner, the PUR or PUR / PIR foams produced from the prepolymers having a very good adhesion of at least 0.2 N / mm ² to metallic ones Have cover layers in metal composite elements.

• (i) einer Isocyanat-Zusammensetzung A mit einer Viskosität bei 25 °C von ≥ 60 mPas bis ≤ 800 mPas, umfassend ≥ 25 Massen-% bis ≤ 60 Massen-% monomeres Diphenylmethandiisocyanat (MDI) A1 und ≥ 40 Massen-% bis ≤ 75 Massen-% polymeres Diphenylmethandiisocyanat (pMDI) A2, wobei die Summe der Anteile der Komponenten A1 und A2 ≤ 100 Massen-% beträgt, mit
• (ii) einem Polyesteretherpolyol B mit einer durchschnittlichen Funktionalität von ≥1,9 bis ≤ 2,1 und einer OH-Zahl von ≥ 200 mg(KOH) / g bis ≤ 500 mg(KOH) / g, erhalten aus der Reaktion von einer Dicarbonsäure und/oder einem Dicarbonsäurederivat B1 mit mindestens einem Polyol B2 sowie mit einem Epoxid B3,

wobei das Polyesteretherpolyol B in Gehalten von ≥ 1,5 Massen-% bis ≤ 6,0 Massen-%, bezogen auf die Summe der Massen von A und B, eingesetzt wird.This object is achieved by an isocyanate-terminated prepolymer C having an NCO content of ≥ 26.0% by mass to ≤ 31.0% by mass, based on the mass of the prepolymer C, obtainable from the reaction of

• (I) an isocyanate composition A having a viscosity at 25 ° C of ≥ 60 mPas to ≤ 800 mPas, comprising ≥ 25% by mass to ≤ 60% by mass of monomeric diphenylmethane diisocyanate (MDI) A1 and ≥ 40% by mass to ≤ 75 mass% of polymeric diphenylmethane diisocyanate (pMDI) A2, wherein the sum of the proportions of the components A1 and A2 ≤ 100 mass%, with
• (ii) a polyester ether polyol B having an average functionality of ≥ 1.9 to ≤ 2.1 and an OH number of ≥ 200 mg (KOH) / g to ≤ 500 mg (KOH) / g, obtained from the reaction of one Dicarboxylic acid and / or a dicarboxylic acid derivative B1 with at least one polyol B2 and with an epoxide B3,

wherein the polyester ether polyol B in amounts of ≥ 1.5% by mass to ≤ 6.0% by mass, based on the sum of the masses of A and B, is used.

Surprisingly, it has been found that the isocyanate group-containing component A can be continuously brought together in a stoichiometric excess and an isocyanate-reactive component B in a stoichiometric deficit at room temperature or elevated temperatures of up to 100 ° C in a mixing device and reproducibly react to an isocyanate group-containing prepolymer. Alternatively, component A can be introduced into a reaction vessel and reacted at room temperature to 100 ° C. with component B for reaction. The isocyanate group-containing prepolymer is also formed.

Surprisingly, it has furthermore been found that the PUR / PIR foams produced from the slightly modified isocyanate according to the invention have improved adhesion in metal composite elements compared to the foams produced with unmodified isocyanates.

The excess of NCO component A gives a prepolymer with free NCO end groups. The NCO content is preferably ≥ 27.0% by mass to ≤ 30.0% by mass, more preferably ≥ 27.5% by mass to ≤ 29.5% by mass, and can be calculated from ISO 14896 be determined.

Preferably, the polyester-ether polyol B is in contents of ≥ 2.0 mass% to ≤ 5 mass%, and more preferably ≥ 2.5 mass% to ≤ 4 mass%, based on the sum of the masses of A and B, used.

Commercially available mixtures of monomeric MDI and polymeric MDI can be used as polyisocyanate A. The viscosity at 25 ° C can be determined by DIN 53019 part 1 and is preferably ≥ 80 mPas to ≤ 500 mPas, more preferably ≥ 90 mPas to ≤ 300 mPas.

For the purposes of the present invention, the terms "monomeric MDI" and "2-core MDI" are used synonymously. Furthermore, "polymeric MDI" denotes di- and trimeric adducts and higher homologues of the monomeric MDI.

Their composition is preferably ≥ 35% by mass to ≦ 55% by mass of monomeric MDI and ≥ 45% by mass to ≦ 65% by mass of polymeric MDI, the sum of these proportions again being ≦ 100% by mass. Even more preferred are ≥40 mass% to ≤50 mass% monomeric MDI and ≥50 mass% to ≤60 mass% polymeric MDI.

Suitable polyester ether polyols B are preferably alkoxylation products of oligo- and polyesters of aromatic and aliphatic dicarboxylic acids and dicarboxylic acid derivatives B1 such as, for example, anhydrides with isocyanate-reactive end groups. Polyester ether polyols can be prepared by targeted construction, for example by alkoxylation of carboxylic acids or carboxylic anhydrides or polyesters, or by molecule-doubling condensation of OH-terminated polyesters. These compounds can also be reacted with epoxides by known methods.

The OH number of the polyester ether polyol B is preferably ≥ 250 mg (KOH) / g to ≦ 380 mg (KOH) / g, more preferably ≥ 280 mg (KOH) / g to ≦ 350 mg (KOH) / g, and most preferably ≥ 300 mg (KOH) / g to ≤ 320 mg (KOH) / g. She relaxes DIN 53240 ("Determination of hydroxyl number") determine.

The average functionality F _N of polyol B is 1.9 to 2.1, preferably 1.95 to 2.05, and most preferably 2.0.

The polyester ether polyols B used may contain, for example, adipic acid, maleic acid, fumaric acid, phthalic acid, terephthalic acid, isophthalic acid, tetrahydrophthalic acid, halogenated phthalic and tetrahydrophthalic acids and derivatives thereof as starter molecules B1. Preferred carboxylic acids are adipic acid, maleic acid, fumaric acid or their derivatives, particular preference is given to phthalic acid, terephthalic acid and isophthalic acid or their derivatives. In particular, preferred carboxylic acid derivatives are their carboxylic acid anhydrides.

The starter molecules B2 used in addition to the carboxylic acids or carboxylic acid derivatives are secondary products of ethylene oxide and propylene oxide such as ethylene glycol, diethylene glycol, triethylene glycol, 1,2-propylene glycol, dipropylene glycol or the primary alcohols such as 1,4-butanediol, 1,6-hexanediol, Neopentyl glycol, 1,3-butanediol or branching triol components such as trimethylolpropane, trimethylolethane or glycerol.

Preferred epoxides B3 are ethylene oxide and / or propylene oxide.

Embodiments of the present invention will be described below, wherein the individual embodiments can be freely combined with each other, unless the context clearly reveals the opposite,

In one embodiment of the prepolymer according to the invention this has a viscosity at 25 ° C of ≥ 300 mPas to ≤ 1600 mPas. This viscosity is preferably in a range from ≥ 350 mPas to ≦ 1400 mPas, particularly preferably from ≥ 500 mPas to ≦ 1000 mPas. It can be based on DIN 53019 part 1 determine.

In a further embodiment of the prepolymer according to the invention, the component A has a viscosity at 25 ° C. of ≥ 90 mPas to ≤ 300 mPas and an NCO content of ≥ 30 mass% to ≤ 33 mass%. This viscosity ( DIN 53019 part 1 ) is preferably in a range of ≥ 160 mPas to ≦ 240 mPas, more preferably 170 mPas to ≦ 230 mPas. The NCO content ( ISO 14896 ) may preferably be from ≥ 30.5 mass% to ≦ 32.5 mass%.

In a further embodiment of the prepolymer according to the invention, the polyester-ether polyol B is obtained from the reaction of phthalic anhydride as component B1, diethylene glycol as component B2 and ethylene oxide as component B3. As catalysts ethoxylated amines can be used. These catalysts may remain in the polyester-ether polyol without adverse effect in prepolymer preparation.

A further subject of the present invention is a polyurethane / polyisocyanurate polymer obtainable from the reaction of a prepolymer C according to the invention with an isocyanate-reactive component D. Such a polymer can be used as insulation foam and / or adhesion promoter, in particular in the production of metal composite elements. It is possible to add the customary additives known to the person skilled in the art, such as surfactants, flame retardants, fillers and the like. With regard to details of the prepolymer, to avoid repetition, reference is made in full to the above statements.

Examples of the isocyanate-reactive component D are polyetherpolyamines and / or preferably polyols selected from the group of polyetherpolyols, polyesterpolyols, polythioetherpolyols, polyesteramides, hydroxyl-containing polyacetals and hydroxyl-containing aliphatic polycarbonates or mixtures of at least two of said polyols. Preferably used polyester polyols and / or polyether polyols.

Suitable polyester polyols may be prepared, for example, from organic dicarboxylic acids having 2 to 12 carbon atoms, preferably dicarboxylic acids having 4 to 6 carbon atoms, and polyhydric alcohols, preferably diols, having 2 to 12, preferably 2 to 6, carbon atoms. Suitable dicarboxylic acids are, for example: succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, maleic acid, fumaric acid, phthalic acid, isophthalic acid and terephthalic acid. The dicarboxylic acids can be used both individually and in admixture with each other. Instead of the free dicarboxylic acids, it is also possible to use the corresponding dicarboxylic acid derivatives, for example dicarboxylic acid esters of alcohols having 1 to 4 carbon atoms or dicarboxylic acid anhydrides. Examples of dihydric and polyhydric alcohols, in particular diols, are: ethanediol, diethylene glycol, 1,2- or 1,3-propanediol, dipropylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1 , 10-decanediol, glycerol and trimethylolpropane. Preferably used are ethanediol, diethylene glycol, 1,4-butanediol, 1,5-pentanediol and 1,6-hexanediol. It is also possible to use polyester polyols from lactones, for example ε-caprolactone or hydroxycarboxylic acids, for example ω-hydroxycaproic acid.

For the preparation of the polyester polyols, the organic, for example. aromatic and preferably aliphatic, polycarboxylic acids and / or derivatives and polyhydric alcohols catalyst-free or preferably in the presence of esterification catalysts, suitably in an atmosphere of inert gas, such as. Nitrogen, carbon monoxide, helium, argon and others, in the melt at temperatures of 150 to 250 ° C, preferably 180 to 220 ° C, optionally under reduced pressure to the desired acid number, which is advantageously less than 10, preferably less than 2, is , polycondensed. According to a preferred embodiment, the esterification mixture is polycondensed at the abovementioned temperatures to an acid number of 80 to 30, preferably 40 to 30, mg KOH / g under normal pressure and then under a pressure of less than 500 mbar, preferably 50 to 150 mbar , As esterification catalysts are, for example, iron, cadmium, cobalt, lead, zinc, antimony, Magnesium, titanium and tin catalysts in the form of metals, metal oxides or metal salts into consideration. However, the polycondensation can also be carried out in the liquid phase in the presence of diluents and / or entrainers, such as. Benzene, toluene, xylene or chlorobenzene, be carried out for the azeotropic distillation of the condensation water.

To prepare the polyesterpolyols, the organic polycarboxylic acids and / or derivatives and polyhydric alcohols are advantageously polycondensed in a molar ratio of 1: 1 to 1.8, preferably 1: 1.05 to 1.2.

The polyesterpolyols obtained preferably have a functionality of 2 to 4, in particular 2 to 3, and a molecular weight of 480 to 3000, in particular 600 to 2000 g / mol.

The polyether polyols are prepared by known methods, for example by anionic polymerization with alkali metal hydroxides, such as. Sodium or potassium hydroxide, or alkali alcoholates, such as. Sodium methylate, sodium or potassium or potassium isopropoxide, as catalysts and with the addition of at least one starter molecule containing 2 to 4, preferably 2 to 3, bonded reactive hydrogen atoms, or by cationic polymerization with Lewis acids, such as antimony pentachloride, boron fluoride etherate u. a., Or bleaching earth, prepared as catalysts from one or more alkylene oxides having 2 to 4 carbon atoms in the alkylene radical.

Suitable alkylene oxides are, for example, tetrahydrofuran, 1,3-propylene oxide, 1,2- or 2,3-butylene oxide, styrene oxide and preferably ethylene oxide and 1,2-propylene oxide. Suitable starter molecules are, for example: water, organic dicarboxylic acids such as succinic acid, adipic acid, phthalic acid and terephthalic acid, aliphatic and aromatic, optionally N-mono-, N, N- and N, N'-dialkyl-substituted diamines having 1 to 4 carbon atoms in the alkyl radical , such as optionally mono- and dialkyl-substituted ethylenediamine, diethylenetriamine, triethylenetetramine, 1,3-propylenediamine, 1,3- or 1,4-butylenediamine, 1,2-, 1,3-, 1,4-, 1,5- and 1,6-hexamethylenediamine, phenylenediamine, 2,3-, 2,4- and 2,6-toluenediamine, and 4,4'-, 2,4'- and 2,2'-diaminodiphenylmethane. Other suitable starter molecules are: alkanolamines, such as, for example. Ethanolamine, N-methyl and N-ethylethanolamine, dialkanolamines, such as. Diethanolamine, N-methyl and N-ethyldiethanolamine, and trialkanolamines, such as. Triethanolamine, and ammonia. preferably used are polyhydric, especially dihydric and / or trihydric alcohols, such as ethanediol, 1,2-propanediol and 2,3, diethylene glycol, dipropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane and pentaerythritol, while for Hartschaumpolyetherole predominantly higher functional starters, such as. Sorbitol and sucrose, are used.

The polyether polyols, preferably polyoxypropylene and polyoxypropylene polyoxyethylene polyols, have for example a functionality of preferably 2 to 4 and in particular 2 to 3 and molecular weights of 300 g / mol to 8000 g / mol, preferably 300 g / mol to 6000 g / mol and in particular 1000 g / mol to 5000 g / mol, and suitable polyoxytetramethylene glycols have a molecular weight of up to about 3500 g / mol, while in the case of rigid foam polyetherols molecular weights of 300 g / mol to 1000 g / mol are the rule.

Also suitable as polyether polyols are polymer-modified polyether polyols, preferably graft polyether polyols, in particular those based on styrene and / or acrylonitrile, which are obtained by in situ polymerization of acrylonitrile, styrene or preferably mixtures of styrene and acrylonitrile, for example. in the weight ratio 90:10 to 10:90, preferably 70:30 to 30:70, in expediently the abovementioned polyether polyols analogously to the statements in DE 11 11 394 . DE 12 22 669 ( US-A-3,304,273 . US-A-3,383,351 . US-A-3,523,093 ) DE 11 52 536 ( GB 1040452 ) and DE 11 52 537 ( GB 987618 ) and polyetherpolyol dispersions containing as disperse phase, usually in an amount of 1 to 50% by weight, preferably 2 to 25% by weight: for example. Polyureas, polyhydrazides, tertiary amino groups bound polyurethanes and / or melamine and the example. be described in the EP-B-011 752 ( US-A-4,304,708 ) US-A-4,374,209 and DE-A-32 31 497 ,

In one embodiment of the polyurethane / polyisocyanurate polymer according to the invention, the molar ratio of isocyanate groups to hydroxyl groups in the reaction mixture of components C and D is ≥ 1: 1 to ≦ 5: 1. In other words, the index of this reaction mixture is 100 to 500. The index may also be ≥ 120 to ≦ 450, and preferably ≥ 180 to ≦ 420. With such ratios, predominantly polyisocyanurate foams are obtained, which manage with smaller amounts of flame retardants and yet can be firmly attached to cover layers, in particular aluminum cover layers.

In a further embodiment of the polyurethane / polyisocyanurate polymer according to the invention, the reaction of the prepolymer C with the isocyanate-reactive component D takes place in the presence of a blowing agent E. Preferred blowing agents are CO ₂ , n-pentane, iso-pentane and / or cyclopentane. The foam thus obtained is preferably a rigid polyisocyanurate foam, defined by its compressive stress at 10% compression or from ≥ 100 kPa to ≦ 300 kPa. This compressive stress or compressive strength can according to DIN 53421 / DIN EN ISO 604 be determined. It can also be in a range of ≥ 150 kPa to ≤ 250 kPa or from ≥ 180 kPa to ≤ 280 kPa.

In a further embodiment of the polyurethane / polyisocyanurate polymer according to the invention, the isocyanate-reactive component D comprises ≥50 mass% to ≤95 mass% of a polyester polyol D1 and ≥5 mass% to ≤50 mass% of a polyether polyol D2, in each case based on the total mass of the component D, and the sum of the proportions of the components D1 and D2 is still ≤ 100 mass%. Included in the invention are mixtures of several polyester polyols D1 and polyether polyols D2. Preferred ranges for the proportion of the polyester polyol D1 are ≥ 85% by mass to ≦ 92% by mass and, for the proportion of the polyether polyol D 2, ≥ 6% by mass to ≦ 10% by mass.

• a) wenigstens ein Carbonsäureanhydrid (A') und Diethylenglykol (B') vermischt werden, wobei das Molverhältnis der Komponenten (B') zu (A') im Bereich von 1,5 zu 1,0 bis 0,7 zu 1,0 liegt und der Gewichtsanteil der Komponenten (A') und (B') bezogen auf das Gewicht aller Komponenten der Mischung im Bereich zwischen 66 bis 90 Gew.- % liegt, und in einem Schritt
• b) zu dem Polyesterpolyol aus Schritt a) Diethylenglykol (B') zugesetzt wird,

wobei das Polyesterpolyol aus Schritt a) eine höhere Molmasse als das Polyesterpolyol aus Schritt b) aufweist.The polyester polyol D1 may preferably be obtained by a method in which

• a) at least one carboxylic acid anhydride (A ') and diethylene glycol (B') are mixed, the molar ratio of components (B ') to (A') ranging from 1.5 to 1.0 to 0.7 to 1.0 and the weight proportion of the components (A ') and (B') based on the weight of all components of the mixture in the range between 66 to 90% by weight, and in one step
• b) adding diethylene glycol (B ') to the polyester polyol from step a),

wherein the polyester polyol from step a) has a higher molecular weight than the polyester polyol from step b).

In step a) at least one C ₂ -C ₄ glycol (C ') and at least one aliphatic C ₅ -C ₁₂ dicarboxylic acid (D') or at least one C ₅ -C ₁₀ glycol (E ') and at least one C ₄ dicarboxylic acid (F ') added.

The amounts of components (C '), (D'), (E ') and (F') in step a) are chosen so that the amounts of all components (A '), (B'), (C ' ) and (D ') or (E') and (F ') in the mixture add to ≤ 100% by weight.

In a preferred embodiment, the carboxylic acid anhydride (A ') is aromatic.

Preferably, the carboxylic acid anhydride (A ') is selected from the group consisting of phthalic anhydride, trimellitic anhydride and pyromellitic anhydride. The carboxylic acid anhydride is particularly preferably phthalic anhydride.

By replacing small amounts of aromatic dicarboxylic acids with an equivalent amount of an aliphatic dicarboxylic acid (D 'or F') and replacing small amounts of diethylene glycol with equivalent amounts of glycols (C ') or (E'), the amount of dioxane waste decreases Preparation of the polyester polyols far beyond what is expected by the dilution effect addition. The properties of the polyesterpolyol produced remain virtually the same, that is to say polyesterpolyols which are prepared by the process according to the invention have the same properties as corresponding polyesterpolyols which are obtained without the addition of aliphatic dicarboxylic acids (D 'or F') and without the addition of glycols ( C ') or (E').

Preferably, the C ₂ -C ₄ glycol (C ') is selected from the group consisting of ethylene glycol, 1,3-propanediol, 2-methyl-1,3-propanediol, 1,2-propanediol. Particularly preferred is the C ₂ -C ₄ glycol (C ') ethylene glycol.

Preferably, the aliphatic C ₅ -C ₁₂ dicarboxylic acid (D ') is selected from the group consisting of glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid and dodecanedioic acid. Particularly preferred as C ₅ -C ₁₂ dicarboxylic acid (D ') is adipic acid or sebacic acid.

Preferably, the C ₅ -C ₁₀ glycol (E ') is selected from the group consisting of 1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,6-hexanediol and 1,8-octanediol. Particularly preferred is the C ₅ -C ₁₀ glycol (E ') 3-methyl-1,5-pentanediol or 1,6-hexanediol.

Preferably, the C ₄ dicarboxylic acid (F ') is selected from the group consisting of succinic acid, fumaric acid and maleic acid. Particularly preferred is the C ₄ dicarboxylic acid (F ') succinic acid.

In one embodiment of the polyurethane / polyisocyanurate polymer of the invention, the polyester polyol D1 has an average functionality of ≥ 1.9 to ≤ 2.1 and an OH number of ≥ 220 mg (KOH) / g to ≤ 270 mg (KOH) / g and is further obtained from the reaction of phthalic acid and / or phthalic anhydride and adipic acid, diethylene glycol and ethylene glycol. The preparation can be carried out as described above.

In one embodiment of the polyurethane / polyisocyanurate polymer according to the invention, the polyether polyol D2 is a trimethylolpropane-initiated polyoxyethylene and / or polyoxypropylene polyol having the OH number of ≥ 200 mg (KOH) / g to ≦ 300 mg (KOH) / g. The OH number relaxes DIN 53240 determine. Preference is given to OH numbers of ≥ 225 mg (KOH) / g to ≦ 275 mg (KOH) / g. The preparation can be carried out as described above.

The present invention also relates to a composite element comprising a layer comprising a polyurethane / polyisocyanurate polymer according to the invention and a cover layer. The cover layer is in this case at least partially contacted by the layer comprising a polyurethane / polyisocyanurate polymer according to the invention. Preferably, the polyurethane / polyisocyanurate polymer is present as a rigid foam. Such composite elements are suitable for example for industrial hall construction. With regard to details of the prepolymer or the polymer, reference is made in full to the above statements to avoid repetition.

Preferably, the material of the cover layer is aluminum, steel, bitumen, paper, a mineral nonwoven fabric, a nonwoven comprising organic fibers, a plastic sheet, a plastic sheet and / or a wood sheet. It is particularly preferred if the cover layer is aluminum-metal or steel. The aluminum or the steel can be coated. The modified isocyanates used according to the invention lead to particularly good adhesion, in particular between polyurethane / polyisocyanurate foam and aluminum cover layer or steel cover layer.

In a foam composite element according to the invention, the adhesion between the layer comprising a polyurethane / polyisocyanurate polymer according to the invention and the cover layer may be ≥ 0.20 N / mm ² . This adhesive strength is preferably ≥ 0.20 N / mm ² to ≦ 0.50 N / mm ² , particularly preferably ≥ 0.22 N / mm ² to ≦ 0.45 N / mm ² , very particularly preferably ≥ 0.25 N. / mm ² to ≤ 0.40 N / mm ² . The adhesive strength is advantageously based on this DIN 53292 measured as described below.

A further subject of the invention is therefore the use of a polyurethane / polyisocyanurate polymer according to the invention as insulation foam and / or as adhesion promoter in composite elements, wherein the composite elements comprise a layer comprising a polyurethane / polyisocyanurate polymer according to the invention and a cover layer. The cover layer is in this case at least partially contacted by the layer comprising a polyurethane / polyisocyanurate polymer according to the invention.

The invention will be further explained with reference to the following examples, but without being limited thereto. Glossary: 44V20L: Desmodur ^® 44 V 20 L, mixture of 4,4'-diphenylmethane diisocyanate (MDI) and higher functional homologues (pMDI) with a viscosity at 25 ° C of ≥ 160 mPas to ≤ 240 mPas; Bayer MaterialScience AG. The product contains about 45% 2-core MDI. 44V70L: Desmodur ^® 44 V 70 L, mixture of 4,4'-diphenylmethane diisocyanate (MDI) and higher functional homologues (pMDI) with a viscosity at 25 ° C of ≥ 610 mPas to ≤ 750 mPas; Bayer MaterialScience AG. The product contains about 34% 2-core MDI. Polyol 1: Polyesterpolyol based on adipic acid, phthalic acid and diethylene glycol having an OH number of about 210 mg (KOH) / g and a viscosity of 10.4 Pa s at 20 ° C .; Bayer MaterialScience AG. Polyol 2: bifunctional polyester ether polyol, EO adduct to a mixture of phthalic anhydride, diethylene glycol and ethylenediamine having an OH number of 275 to 325 mg (KOH) / g and a viscosity of 6.5 +/- 1.3 Pa s at 25 ° C; Bayer MaterialScience AG. Polyol 3: Diethylene glycol, OH number 1055 mg (KOH) / g, viscosity 38 mPa s at 20 ° C.

Example 1: General description of the preparation of the prepolymers

19.0 t 44V20L with 200 mPa s viscosity at 25 ° C and an NCO content of 31.2% were metered into a stirred tank reactor with external heat exchanger and pumped circulation in 2 h. The isocyanate was heated to 70 ° C. Subsequently, the polyol addition of 1.0 t over one hour. The reaction temperature was kept constant at 70 ° C during the addition. After a post-reaction time of 30 minutes, a sample was taken and checked in the laboratory. The released reaction mixture was cooled and could now be pumped into a tank truck.

Example 2:

With reference to Example 1, the general preparation procedure, the syntheses shown in the table below were carried out. The terminology of the present invention is the syntheses of isocyanate-terminated prepolymers C.

Syntheses according to the invention are those with polyol 2 (in the terminology of the present invention, polyester ether polyol B), not those of the invention with polyol 1 and polyol 3 as polyol components. In all cases, the isocyanate component was 44V20L (in the terminology of the present invention, isocyanate component A).

The viscosity was according to DIN 53019 part 1 at 25 ° C and the NCO content according to ISO 14896 certainly.

Example 3: Production of metal composite elements with PUR / PIR foam

• – 71 Massen-% einer Polyolmischung (in der Terminologie der vorliegenden Erfindung Isocyanatreaktive Komponente D): aus: 64 Gewichtsteilen eines Polyesterpolyols aus Phthalsäureanhydrid, Adipinsäure, Diethylenglykol und Ethylenglykol mit einer OH-Zahl von 240 mg(KOH) / g (in der Terminologie der vorliegenden Erfindung Polyesterpolyol D1); 5 Gewichtsteilen eines Polyetherpolyols basierend auf TMP (Trimethylolpropan) und Ethylenoxid mit einer Funktionalität von 2 und einer OH-Zahl 240 mg(KOH) / g (in der Terminologie der vorliegenden Erfindung Polyetherpolyol D2); und 2,2 Gewichtsteilen Polyesterpolyol aus Phthalsäureanhydrid und Diethylenglykol, OH-Zahl 795 mg(KOH) / g

A PUR / PIR foam was obtained in the usual manner on a double conveyor belt using two steel topcoats according to the following recipe:

• - 71% by mass of a polyol mixture (in the terminology of the present invention isocyanate-reactive component D): from: 64 parts by weight of a polyester polyol of phthalic anhydride, adipic acid, diethylene glycol and ethylene glycol having an OH number of 240 mg (KOH) / g (in terminology the present invention polyester polyol D1); 5 parts by weight of a polyether polyol based on TMP (trimethylolpropane) and ethylene oxide having a functionality of 2 and an OH number of 240 mg (KOH) / g (in the terminology of the present invention, polyether polyol D2); and 2.2 parts by weight of polyester polyol of phthalic anhydride and diethylene glycol, OH number 795 mg (KOH) / g

Additional components:

• - 20% by mass of flame retardant TCPP (tris (chloropropyl) phosphate)
• 5 mass% flame retardant TEP (triethyl phosphate)
• 4% by mass silicone-containing stabilizer

This was reacted with 5 parts by weight of carboxylic acid salt (PIR catalyst) and 13 parts by weight of n-pentane propellant (in the terminology of the present invention, Component E) in the reaction to the PUR / PIR foam.

Furthermore, an isocyanate component was used. In the case of Comparative Example 3-1, the 44V70L already mentioned above and in Example 3-2 according to the invention the prepolymer of Example 2-4 (in the terminology of the present invention prepolymer C).

The isocyanate component and the isocyanate-reactive component were reacted in Comparative Example 3-1 in a mixing ratio of 100 parts by weight of the isocyanate-reactive component to 190 parts by weight of the isocyanate component and in Example 3-2 according to the invention in a mixing ratio of 100 parts by weight of the isocyanate reactive component to 220 parts by weight of the isocyanate component. The experiment was carried out on a continuous processing plant for the production of metal composite elements.

It was the adhesive strength based on the Standard DIN 53292 checked. The procedure differed from the tensile test perpendicular to the cover layer DIN 53292-82 due to the different sample thickness and number of cover layers.

When trying to DIN 53292-82 the total thickness of the cover layers is taken as the basis. The weakest area of the total sample determines the location of the break. In contrast, the detention attempt in the modification described here allowed a page-related assessment of liability.

For sampling, therefore, a composite element was cut perpendicular to the outer layers. In the measurement, square samples were used whose side length was 50 mm and whose sample height was 15 mm (including the cover layer).

For the comparison of the results from Example 3-1 with Example 3-2, in each case 3 comparative measurements were carried out. While average adhesion strengths of 0.15 MPa were measured for Example 3-1, they were in the range of 0.37 MPa for Example 3-2. In a reproduction of this result even slightly higher adhesion strengths of> 0.40 MPa could be determined for experiment 3-2.

The blistering after annealing at 105 ° C was also checked for 1 h. Here, for test 3-2, a trouble-free boundary region between foam and metallic cover layer was found.

QUOTES INCLUDE IN THE DESCRIPTION

This list of the documents listed by the applicant has been generated automatically and is included solely for the better information of the reader. The list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions.

Cited patent literature

• DE 69132613 T2 [0003]
• WO 94/29361 A1 [0004]
• DE 2823762 A1 [0005]
• DE 19823392 A1 [0006]
• EP 0497131 A2 [0007]
• DE 19601410 A1 [0008]
• WO 2009/055436 A1 [0009]
• DE 1111394 [0039]
• DE 1222669 [0039]
• US 3304273 A [0039]
• US 3383351 A [0039]
• US Pat. No. 3,523,093 A [0039]
• DE 1152536 [0039]
• GB 1040452 [0039]
• DE 1152537 [0039]
• GB 987618 [0039]
• EP 011752 B [0039]
• US 4304708 A [0039]
• US 4374209 A [0039]
• DE 3231497A [0039]

Cited non-patent literature

• ISO 14896 [0015]
• DIN 53019 Part 1 [0017]
• DIN 53240 ("Determination of the Hydroxyl Number ") [0021]
• DIN 53019 Part 1 [0027]
• DIN 53019 Part 1 [0028]
• ISO 14896 [0028]
• DIN 53421 [0041]
• DIN EN ISO 604 [0041]
• DIN 53240 [0054]
• DIN 53292 [0057]
• DIN 53019 Part 1 [0063]
• ISO 14896 [0063]
• Standard DIN 53292 [0068]
• DIN 53292-82 [0068]
• DIN 53292-82 [0069]

Claims (14)

Isocyanate-terminated prepolymer C having an NCO content of ≥ 26.0% by mass to ≦ 31.0% by mass, based on the mass of the prepolymer C, available from the reaction of (i) an isocyanate composition A having a viscosity at 25 ° C of ≥ 60 mPas to ≤ 800 mPas, comprising ≥ 25% by mass to ≤ 60% by mass of monomeric diphenylmethane diisocyanate A1 and ≥ 40% by mass to ≤ 75% by mass of polymeric diphenylmethane diisocyanate A2, the sum of the proportions of components A1 and A2 being ≦ 100 mass%, With (ii) a polyester ether polyol B having an average functionality of ≥ 1.9 to ≤ 2.1 and an OH number of ≥ 200 mg (KOH) / g to ≤ 500 mg (KOH) / g, obtained from the reaction of a dicarboxylic acid and / or a dicarboxylic acid derivative B1 with at least one polyol B2 and with an epoxide B3, wherein the polyester ether polyol B in amounts of ≥ 1.5% by mass to ≤ 6.0% by mass, based on the sum of the masses of A and B, is used. A prepolymer according to claim 1 having a viscosity at 25 ° C of ≥ 300 mPas to ≤ 1600 mPas. The prepolymer according to claim 1, wherein the component A has a viscosity at 25 ° C of ≥ 90 mPas to ≤ 300 mPas and an NCO content of ≥ 30 mass% to ≤ 33 mass%. A prepolymer according to claim 1, wherein the polyester-ether polyol B is obtained from the reaction of phthalic anhydride as component B1, diethylene glycol as component B2 and ethylene oxide as component B3. A polyurethane / polyisocyanurate polymer obtainable from the reaction of a prepolymer C according to any one of claims 1 to 4 with an isocyanate-reactive component D. Polyurethane / polyisocyanurate according to claim 5, wherein in the reaction mixture of the components C and D, the molar ratio of isocyanate groups to hydroxyl groups ≥ 1: 1 to ≤ 5: 1. Polyurethane / polyisocyanurate polymer according to claim 5, wherein the reaction of the prepolymer C with the isocyanate-reactive component D takes place in the presence of a blowing agent E. Polyurethane / polyisocyanurate according to claim 5, wherein the isocyanate-reactive component D ≥ 50% by mass to ≤ 95% by mass of a polyester polyol D1 and ≥ 5% by mass to ≤ 50% by mass of a polyether polyol D2, each based on the total mass component D, and further wherein the sum of the proportions of the components D1 and D2 ≤ 100 mass%. The polyurethane / polyisocyanurate polymer according to claim 8, wherein the polyester polyol D1 has an average functionality of ≥ 1.9 to ≤ 2.1 and an OH number of ≥ 220 mg (KOH) / g to ≤ 270 mg (KOH) / g, and is further obtained from the reaction of phthalic acid and / or phthalic anhydride and adipic acid, diethylene glycol and ethylene glycol. The polyurethane / polyisocyanurate polymer according to claim 8, wherein the polyether polyol D2 is a trimethylolpropane-initiated polyoxyethylene and / or polyoxypropylene polyol having an OH number of ≥ 200 mg (KOH) / g to ≤ 300 mg (KOH) / g. Composite element comprising a layer comprising a polyurethane / polyisocyanurate polymer according to one or more of claims 5 to 10 and a cover layer. A composite member according to claim 11, wherein the material of the cover layer is aluminum, steel, bitumen, paper, a mineral nonwoven fabric, a nonwoven fabric comprising organic fibers, a plastic sheet, a plastic sheet and / or a wood sheet. A composite member according to claim 11, wherein the adhesive strength between the layer comprising a polyurethane / polyisocyanurate polymer according to one or more of claims 5 to 9 and the cover layer is ≥ 0.20 N / mm ² . Use of a polyurethane / polyisocyanurate polymer according to one or more of claims 5 to 10 as insulation foam and / or as adhesion promoter in composite elements, wherein the composite elements comprise a layer comprising a polyurethane / polyisocyanurate polymer according to one or more of claims 5 to 10 and a cover layer.