Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
  • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/16—Dicarboxylic acids and dihydroxy compounds
  • C08G63/18—Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
  • C08G63/181—Acids containing aromatic rings
  • C08G63/183—Terephthalic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
  • C08G18/4018—Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
  • C08G18/4205—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
  • C08G18/4208—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
  • C08G18/4211—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols
  • C08G18/4213—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols from terephthalic acid and dialcohols
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
  • C08G18/4205—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
  • C08G18/4208—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
  • C08G18/4211—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols
  • C08G18/4219—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols from aromatic dicarboxylic acids and dialcohols in combination with polycarboxylic acids and/or polyhydroxy compounds which are at least trifunctional
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
  • C08G18/4244—Polycondensates having carboxylic or carbonic ester groups in the main chain containing oxygen in the form of ether groups
  • C08G18/4247—Polycondensates having carboxylic or carbonic ester groups in the main chain containing oxygen in the form of ether groups derived from polyols containing at least one ether group and polycarboxylic acids
  • C08G18/4252—Polycondensates having carboxylic or carbonic ester groups in the main chain containing oxygen in the form of ether groups derived from polyols containing at least one ether group and polycarboxylic acids derived from polyols containing polyether groups and polycarboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
  • C08G18/4288—Polycondensates having carboxylic or carbonic ester groups in the main chain modified by higher fatty oils or their acids or by resin acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
  • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/123—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
  • C08G63/127—Acids containing aromatic rings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
  • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/46—Polyesters chemically modified by esterification
  • C08G63/48—Polyesters chemically modified by esterification by unsaturated higher fatty oils or their acids; by resin acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G2110/00—Foam properties
  • C08G2110/0025—Foam properties rigid

Definitions

• the invention relates to polyester polyols based on terephthalic acid and their use for the production of rigid polyurethane foams.
• polyesterpolyols When polyesterpolyols are used, it is customary to use polycondensates of aromatic and / or aliphatic dicarboxylic acids and alkanediols and / or triols or ether diols.
• PET polyethylene terephthalate
• PBT polybutylene terephthalate
• a whole series of methods are known and described. The basis of some processes is the conversion of the polyester into a diester of terephthalic acid, e.g. in dimethyl terephthalate.
• DE-A 1003714 and US Pat. No. 5,051,528 describe such transesterifications using methanol and transesterification catalysts.
• terephthalic acid-based esters are superior in fire performance to phthalic acid-based esters.
• a disadvantage is the high crystallization tendency and thus low storage stability of terephthalic acid-based esters.
• the object of the invention is to provide polyester polyols based on terephthalic acid or terephthalic acid derivatives, which have improved storage stability.
• the object of the invention is also to provide polyester polyols having improved storage stability, which give polyurethane foams with improved fire behavior.
• the object is achieved by a polyester polyol containing the esterification of
• polyester polyol at least 200 mmol, preferably at least 500 mmol and more preferably at least 800 mmol of polyols d) are reacted with an OH functionality of ⁇ 2.9.
• the dicarboxylic acid composition a) contains more than 50 mol% of the terephthalic acid-based material a1), preferably more than 75 mol% and particularly preferably 100 mol% of the terephthalic acid-based material a1).
• the aliphatic diol is selected from the group consisting of ethylene glycol, diethylene glycol, polyethylene glycol, propylene glycol, 1, 3-propanediol, 1, 4-butanediol, 1, 5-pentanediol, 1, 6-hexanediol, 2-methyl-1, 3rd Propanediol, 3-methyl-1, 5-pentanediol and alkoxylates thereof, in particular ethoxylates thereof.
• the aliphatic diol is diethylene glycol.
• the fatty acid or fatty acid derivative b) is a fatty acid or a fatty acid derivative based on renewable raw materials selected from the group consisting of castor oil, polyhydroxy fatty acids, ricinoleic acid, hydroxyl-modified oils, grape seed oil, black cumin oil, pumpkin seed oil, borage seed oil, soybean oil, wheat seed oil , Rapeseed oil, sunflower seed oil, peanut oil, apricot kernel oil, pistachio oil, almond oil, olive oil, macadamia nut oil, avocado oil, sea buckthorn oil, sesame oil, hemp oil, hazelnut oil, primrose oil, wild rose oil, thistle oil, walnut oil, hydroxyl modified fatty acids and fatty acid esters based on myristoleic acid, palmitoleic acid , Oleic acid, vaccenic acid, petroselinic acid, gadoleic acid, erucic acid, neruloic acid, linoleic acid, ⁇ - and
• esterification or transesterification takes place under customary esterification or transesterification conditions.
• the aromatic and aliphatic dicarboxylic acids or dicarboxylic acid esters and polyhydric alcohols are catalyst-free or preferably in the presence of esterification catalysts, conveniently in an atmosphere of inert gas such as nitrogen, carbon monoxide, helium, argon and others in the melt at temperatures of 150 to 26O 0 C, preferably 180 to 25O 0 C optionally reacted under reduced pressure, wherein the liberated by the transesterification low molecular weight alcohol (for example, methanol), preferably at reduced pressure, is distilled off.
• inert gas such as nitrogen, carbon monoxide, helium, argon and others
• Suitable 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.
• the transesterification can also be carried out in the presence of diluents and / or entrainers, such as benzene, toluene, xylene or chlorobenzene, for the azeotropic distillation of the water of condensation.
• the invention also relates to a process for the production of rigid polyurethane foams by reacting
• component B) the specific polyester polyols according to the invention, wherein component B) may have up to 50% by weight of further polyester polyols, C) optionally polyetherols and / or further compounds having at least two isocyanate-reactive groups and optionally chain extenders and / or crosslinking agents,
• Suitable organic and / or modified organic polyisocyanates A) are the per se known aliphatic, cycloaliphatic, araliphatic and preferably aromatic polyfunctional isocyanates.
• alkylenediisocyanates having 4 to 12 carbon atoms in the alkylene radical such as 1,12-dodecanediisocyanate, 2-ethyltetra methylene diisocyanate-1,4,2-methylpentamethylene-1,5-diisocyanate-1,1,5-tetramethylene diisocyanate-1,4 preferably hexamethylene diisocyanate-1, 6;
• Cycloaliphatic diisocyanates such as cyclohexane-1, 3- and 1, 4-diisocyanate and any mixtures of these isomers, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane (IPDI), 2,4- and 2,6 Hexahydrotoluylendiisocyanat and the corresponding isomer mixtures, 4,4'-, 2,2'- and 2,4'-dicyclohexylmethane diisocyanate and the corresponding isomer mixtures
• Preferred diisocyanates and polyisocyanates are tolylene diisocyanate (TDI), diphenylmethane diisocyanate (MDI) and, in particular, mixtures of diphenylmethane diisocyanate and polyphenylenepolymethylene polyisocyanates (polymeric MDI or PMDI).
• TDI tolylene diisocyanate
• MDI diphenylmethane diisocyanate
• PMDI polyphenylenepolymethylene polyisocyanates
• modified polyfunctional isocyanates ie products obtained by chemical reaction of organic di- and / or polyisocyanates.
• examples include ester, urea, biuret, allophanate, Carbodiimide, isocyanurate, uretdione, carbamate, and / or urethane groups-containing di- and / or polyisocyanates.
• isocyanurate groups into the polyisocyanate.
• D i e isocyanurate formation leads to flame-resistant polyisocyanurate foams (PIR foams), which are preferably used in engineering foam, for example in construction as an insulating board or sandwich panels.
• Suitable further polyester polyols can be prepared, for example, from organic dicarboxylic acids having 2 to 12 carbon atoms, preferably aliphatic dicarboxylic acids having 4 to 6 carbon atoms, and polyhydric alcohols, preferably diols, having 2 to 12 carbon atoms, 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.
• dicarboxylic acid derivatives e.g. Dicarboxylic acid esters of alcohols having 1 to 4 carbon atoms or dicarboxylic anhydrides are used.
• dicarboxylic acid mixtures of succinic, glutaric and adipic acid in proportions of, for example, 20 to 35: 35 to 50: 20 to 32 parts by weight, and in particular adipic acid.
• 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, trimethylolpropane and pentaerythritol.
• Polyester polyols may also be employed from lactones, e.g. ⁇ -caprolactone or hydroxycarboxylic acids, e.g. ⁇ -hydroxycaproic acid.
• the organic, for example aromatic and preferably aliphatic, polycarboxylic acids and / or derivatives and polyhydric alcohols may be free of catalyst or preferably in the presence of esterification catalysts, conveniently in an atmosphere of inert gas, such as nitrogen, carbon monoxide, helium, Argon, inter alia, in the melt at temperatures of 150 to 26O 0 C, preferably 180 to 25O 0 C optionally under reduced pressure to the desired acid number, which is advantageously less than 10, preferably less than 2, polycondensed.
• inert gas such as nitrogen, carbon monoxide, helium, Argon, inter alia
• the esterification mixture is polycondensed at the abovementioned temperatures to an acid number of 80 to 20, preferably 40 to 20, under atmospheric pressure and then under a pressure of less than 500 mbar, preferably 40 to 200 mbar.
• Suitable 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.
• 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, for the azeotropic distillation of the water of condensation.
• diluents and / or entrainers such as benzene, toluene, xylene or chlorobenzene
• the organic polycarboxylic acids and / or derivatives and polyhydric alcohols are advantageously in a molar ratio of 1: 1 to 2.1, preferably 1: 1, 05 to 1, 9, polycondensed.
• the polyesterpolyols obtained preferably have a functionality of 2 to 4, in particular 2 to 3, and a molecular weight of 300 to 3000, preferably 400 to 1000 and in particular 450 to 800.
• polyether polyols prepared by known methods, for example by anionic polymerization with alkali hydroxides, e.g. Sodium or potassium hydroxide or alkali alcoholates, e.g. Sodium methylate, sodium or potassium or potassium isopropoxide, as catalysts and with the addition of at least one starter molecule containing 2 to 8, preferably 2 to 6, bonded reactive hydrogen atoms, or by cationic polymerization with Lewis acids, such as antimony pentachloride, boron fluoride etherate among others or bleaching earth, are prepared as catalysts from one or more alkylene oxides having 2 to 4 carbon atoms in the alkylene radical.
• alkali hydroxides e.g. Sodium or potassium hydroxide or alkali alcoholates, e.g. Sodium methylate, sodium or potassium or potassium isopropoxide
• Lewis acids such as antimony pentachloride, boron fluoride etherate among others or bleaching earth
• 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.
• the alkylene oxides can be used individually, alternately one after another or as mixtures.
• Preferred alkylene oxides are propylene oxide and ethylene oxide, particularly preferred is ethylene 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 mono- and optionally dialkyl-substituted ethylenediamine, diethylenetriamine, triethylenetetramine, 1,3-propylenediamine, 1,3- or 1,4-butylenediamine, 1,2,3,1-, 4-, 1-, 5- and 1,6-hexamethylenediamine , Phenylenediamines, 2,3-, 2,4- and 2,6-toluenediamine and 4,4'-, 2,4'- and 2,2'-diaminodiphenylmethane.
• alkyl radical such as mono- and optionally dialkyl-substituted ethylenediamine, diethylenetriamine, triethylenetetramine, 1,3-propylenediamine, 1,3- or 1,4-butylenediamine, 1,2,3,1-, 4-, 1-, 5- and 1,6-hexamethylenediamine , Phenylenediamines, 2,3-,
• alkanolamines e.g. Ethanolamine, N-methyl and N-ethylethanolamine
• dialkanolamines e.g. Diethanolamine, N-methyl and N-ethyldiethanolamine
• trialkanolamines e.g. Triethanolamine, and ammonia.
• polyhydric alcohols such as ethanediol, propanediol-1, 2 and -1, 3, diethylene glycol, dipropylene glycol, butanediol-1, 4, hexanediol-1, 6, glycerol, trimethylolpropane, pentaerythritol, ethylenediamine, sorbitol and sucrose.
• Polyether polyols preferably polyoxypropylene and polyoxypropylene polyoxyethylene polyols, have a functionality of preferably 2 to 6 and in particular 2 to 5 and molecular weights of 300 to 3000, preferably 300 to 2000 and in particular 400 to 1000.
• 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, e.g.
• polyetherpolyol dispersions which are used as disperse phase, usually in an amount of 1 to 50% by weight, preferably 2 to 25% by weight.
• polyureas include: eg Polyureas, polyhydrazides, polyurethanes containing tertiary amino groups bound and / or melamine and the e.g. are described in EP-B 011 752 (US 4,304,708), US-A, 4,374,209 and DE-A, 32 31 497.
• the polyether polyols can be used singly or in the form of mixtures. Furthermore, they can be mixed with the graft polyether polyols or polyester polyols and with the hydroxyl-containing polyester amides, polyacetals, polycarbonates and / or polyether polyamines.
• Suitable hydroxyl-containing polyacetals are the compounds which can be prepared from glycols, such as diethylene glycol, triethylene glycol, 4,4'-dihydroxyethoxydiphenyldimethylmethane, hexanediol and formaldehyde. It is also possible to prepare suitable polyacetals by polymerization of cyclic acetals.
• Hydroxyl-containing polycarbonates are those of the type known per se, for example, by reacting diols, such as propanediol 1, 3, butanediol-1, 4 and / or hexanediol-1, 6, diethylene glycol, triethylene glycol or tetraethylenglykol with Diaryl carbonates, such as diphenyl carbonate, or phosgene can be produced.
• diols such as propanediol 1, 3, butanediol-1, 4 and / or hexanediol-1, 6, diethylene glycol, triethylene glycol or tetraethylenglykol
• Diaryl carbonates such as diphenyl carbonate, or phosgene can be produced.
• the polyester amides include e.g. the predominantly linear condensates obtained from polybasic, saturated and / or unsaturated carboxylic acids or their anhydrides and polybasic saturated and / or unsaturated aminoalcohols or mixtures of polyhydric alcohols and aminoalcohols and / or polyamines.
• Suitable polyether polyamines can be prepared from the above polyether polyols by known methods. Examples include the cyanoalkylation of polyoxyalkylene polyols and subsequent hydrogenation of the nitrile formed (US Pat. No. 3,267,050) or the partial or complete amination of polyoxyalkylene polyols with amines or ammonia in the presence of hydrogen and catalysts (DE 12 15 373).
• the rigid polyurethane foams can be prepared by using chain extenders and / or crosslinking agents C).
• chain extenders and / or crosslinking agents C To modify the mechanical properties, e.g. However, the hardness, the addition of chain extenders, crosslinking agents or optionally mixtures thereof may prove advantageous.
• chain extenders and / or crosslinking agents are used diols and / or triols having molecular weights less than 400, preferably from 60 to 300.
• Suitable examples are aliphatic, cycloaliphatic and / or araliphatic diols having 2 to 14, preferably 4 to 10 carbon atoms, such as eg Ethylene glycol, propanediol 1, 3, decanediol 1, 10, o-, m-, p-dihydroxycyclohexane, diethylene glycol, dipropylene glycol and preferably butanediol-1, 4, hexanediol-1, 6 and bis- (2-hydroxy-ethyl) hydroquinone, triols, such as 1, 2,4-, 1, 3,5-trihydroxycyclohexane, glycerol and trimethylolpropane and low molecular weight hydroxyl-containing polyalkylene oxides based on ethylene and / or 1,2-propylene oxide and the abovementioned diols and / or triplets as starter molecules.
• Ethylene glycol propanediol 1, 3, decanedi
• Further compounds C) having at least two isocyanate-reactive groups are in particular those which have two or more reactive groups selected from OH groups, SH groups, NH groups, NH 2 groups and CH-acidic groups such as .beta.-diketo groups.
• chain extenders, crosslinking agents or mixtures thereof are used for the production of the rigid polyurethane foams, these are suitable for use. in an amount of from 0 to 20% by weight, preferably from 0.5 to 5% by weight, based on the weight of component B).
• Propellants D which are used for producing the rigid polyurethane foams preferably include water, formic acid and mixtures thereof. These react with isocyanate groups to form carbon dioxide and in the case of formic acid to carbon dioxide and carbon monoxide.
• physical blowing agents such as low-boiling hydrocarbons can be used.
• Suitable liquids are those which are inert toward the organic, modified or unmodified polyisocyanates and have boiling points below 100 0 C, preferably below 50 0 C at atmospheric pressure so that they lyadditionsretress evaporate under the influence of the exothermic Po.
• alkanes such as heptane, hexane, n- and iso-pentane, preferably technical mixtures of n- and iso-pentanes, n- and iso-butane and propane, cycloalkanes, such as cyclopentane and / or cyclohexane, Ethers, such as furan, dimethyl ether and diethyl ether, ketones, such as acetone and methyl ethyl ketone, alkyl carboxylates, such as methyl formate, dimethyl oxalate and ethyl acetate, and halogenated hydrocarbons, such as methylene chloride, dichloromonofluoromethane, difluoromethane, trifluoromethane, difluoroethane, tetrafluoroethane, chlorodifluoroethanes, 1,1 Dichloro-2,2,
• low-boiling liquids with one another and / or with other substituted or unsubstituted hydrocarbons.
• organic carboxylic acids such as, for example, formic acid, acetic acid, oxalic acid, ricinoleic acid and carboxyl group-containing compounds.
• these blowing agents e.g. Mixtures of water and cyclohexane, mixtures of chlorodifluoromethane and 1-chloro-2,2-difluoroethane and optionally water.
• blowing agents are either completely or partially dissolved in the polyol component (i.e., B + C + E + F + G), or are metered in just prior to foaming the polyol component via a static mixer.
• water or formic acid is completely or partially dissolved in the polyol component and the physical blowing agent (for example pentane) and optionally the remainder of the chemical blowing agent are metered "online”.
• the amount of blowing agent or propellant mixture used is 1 to 45 wt .-%, preferably 1 to 30 wt .-%, particularly preferably 1, 5 to 20 wt .-%, each based on the sum of components B) to G). If water is used as the blowing agent, it is preferably added to the synthesis component B) in an amount of from 0.2 to 5% by weight, based on the synthesis component B). The addition of water can be done in combination with the use of the other blowing agents described.
• catalysts E) for the production of rigid polyurethane foams in particular compounds are used which greatly accelerate the reaction of the reactive hydrogen atoms, in particular hydroxyl groups, containing compounds of component B) and optionally C) with the organic, optionally modified polyisocyanates A).
• basic polyurethane catalysts for example tertiary amines, such as triethylamine, tributylamine, dimethylbenzylamine, dicyclohexylmethylamine, dimethylcyclohexylamine, N, N, N ', N'-tetramethyldiaminodiethyl ether, bis (dimethylaminopropyl) urea, N-methyl or N Ethylmorpholine, N-cyclohexylmorpholine, N, N, N ', N'-tetramethylethylenediamine, N, N, N', N'-tetramethylbutanediamine, N, N, N ', N'-tetramethylhexanediamine-1, 6, pentamethyldiethylenetriamine Dimethylpiperazine, N-dimethylaminoethylpiperidine, 1, 2-dimethylimidazole, 1-azabicyclo- (2,2,0) -oct
• metal salts are also suitable, such as iron (II) chloride, zinc chloride, lead octoate and preferably tin salts, such as tin dioctoate, tin diethylhexanoate and dibutyltin dilaurate, and in particular mixtures of tertiary amines and organic tin salts.
• amidines such as 2,3-dimethyl-3,4,5,6-tetrahydropyrimidine
• tetraalkylammonium hydroxides such as tetramethylammonium hydroxide
• alkali metal hydroxides such as sodium hydroxide and alkali metal alkoxides, such as sodium methylate and potassium isopropylate
• alkali metal salts of long-chain fatty acids with 10 to 20 carbon atoms and optionally pendant OH groups Preferably used are 0.001 to 5 wt .-%, in particular 0.05 to 2 wt .-%, catalyst or catalyst lysatorkombination, based on the weight of component B).
• Isocyanurate group-forming catalysts for example ammonium ion or alkali metal salts, are used for this purpose alone or in combination with tertiary amines. Isocyanurate formation leads to flame-retardant PIR Foams, which are preferably used in technical foam, for example in construction as insulation board or sandwich panels.
• auxiliaries and / or additives F may also be added to the reaction mixture for the preparation of the rigid polyurethane foams. Mention may be made, for example, of surface-active substances, foam stabilizers, cell regulators, fillers, dyes, pigments, flame retardants, hydrolysis protectants, fungistatic and bacteriostatic substances.
• surface-active substances are e.g. Compounds which serve to assist the homogenization of the starting materials and, if appropriate, are also suitable for regulating the cell structure of the plastics.
• emulsifiers such as the sodium salts of castor oil sulfates or fatty acids, and salts of fatty acids with amines, e.g. diethylamine, stearic diethanolamine, ricinoleic diethanolamine, salts of sulfonic acids, e.g.
• Alkali metal ammonium salts of dodecylbenzene or dinaphthylmethanedisulfonic acid and ricinoleic acid Alkali metal ammonium salts of dodecylbenzene or dinaphthylmethanedisulfonic acid and ricinoleic acid;
• Foam stabilizers such as siloxane-oxalkylene copolymers and other organopolysiloxanes, ethoxylated alkylphenols, ethoxylated fatty alcohols, paraffin oils, castor oil or ricinoleic acid esters, turkey red oil and peanut oil, and cell regulators, such as paraffins, fatty alcohols and dimethylpolysiloxanes.
• the above-described oligomeric acrylates having polyoxyalkylene and fluoroalkane radicals are also suitable as side groups.
• the surface-active substances are usually used in amounts of from 0.01 to 10% by weight, based on 100% by weight of component B).
• Fillers are the usual conventional organic and inorganic fillers, reinforcing agents, weighting agents, agents for improving the abrasion behavior in paints, coating agents, etc., to be understood.
• inorganic fillers such as silicate minerals, for example phyllosilicates such as antigorite, serpentine, hornblende, amphiboles, chrysotile and talc, metal oxides such as kaolin, aluminas, titanium oxides and iron oxides, metal salts such as chalk, barite and inorganic pigments such as cadmium sulfide and zinc sulfide, as well as glass and others.
• kaolin China Clay
• aluminum silicate and coprecipitates of barium sulfate and aluminum silicate and natural and synthetic fibrous minerals such as wollastonite, metal fibers and in particular glass fibers of various lengths, which may optionally be sized.
• suitable organic fillers are: carbon, melamine, rosin, cyclopentadienyl resins and graft polymers, as well as cellulose fibers, polyamide, polyacrylonitrile, polyurethane, polyester fibers based on aromatic and / or aliphatic dicarboxylic esters and in particular carbon fibers.
• the inorganic and organic fillers can be used individually or as mixtures and are advantageously added to the reaction mixture in amounts of 0.5 to 50% by weight, preferably 1 to 40% by weight, based on the weight of components A) to C). , but the content of mats, nonwovens and woven fabrics of natural and synthetic fibers can reach values of up to 80% by weight.
• Suitable flame retardants are, for example, non-incorporable brominated substances, brominated esters, brominated ethers (Ixol), or brominated alcohols such as dibromoneopentyl alcohol, tribromoneopentyl alcohol and PHT-4-diol, and also chlorinated phosphates, e.g.
• phosphates or phosphonates such as diethyl ethane phosphonate (DEEP), triethyl phosphate (TEP), dimethyl propyl phosphonate (DMPP), diphenyl cresyl phosphate (DPK) and others.
• DEEP diethyl ethane phosphonate
• TEP triethyl phosphate
• DMPP dimethyl propyl phosphonate
• DPK diphenyl cresyl phosphate
• inorganic or organic flame retardants such as red phosphorus, red phosphorus-containing finishes, alumina hydrate, antimony trioxide, arsenic oxide, ammonium polyphosphate and calcium sulfate, expandable graphite or cyanuric acid derivatives, e.g. Melamine, or mixtures of at least two flame retardants, e.g. Ammonium polyphosphates and melamine and optionally corn starch or ammonium polyphosphate, melamine and expandable graphite and / or optionally aromatic polyester for flame retardancy of the rigid polyurethane foams can be used.
• flame retardants e.g. Ammonium polyphosphates and melamine and optionally corn starch or ammonium polyphosphate, melamine and expandable graphite and / or optionally aromatic polyester for flame retardancy of the rigid polyurethane foams
• the organic and / or modified organic polyisocyanates A), the special polyester polyols B) and optionally polyetherol and / or further compounds having at least two isocyanate-reactive groups and optionally chain extenders and / or crosslinking agents C) such amounts are reacted, that the equivalence ratio of NCO groups of the polyisocyanates A) to the sum of the reactive hydrogen atoms of the components B), optionally C) and D) to G) 1 to 6: 1, preferably 1, 1 to 5: 1 and in particular 1.2 to 3.5: 1.
• the rigid polyurethane foams are advantageously produced by the one-shot process, for example by means of the high-pressure or low-pressure technique in open or closed molds, for example metallic molds. Also common is the continuous application of the reaction mixture on suitable conveyor belts for the production of panels.
• the starting components are at a temperature of 15 to 9O 0 C, preferably from 20 to 60 0 C and in particular from 20 to 35 0 C, mixed and introduced into the open or optionally under increased pressure in the closed mold or in a continuous workstation a tape which absorbs the reaction mass is applied.
• the mixing can, as already stated, be carried out mechanically by means of a stirrer or a stirring screw.
• the mold temperature is expediently 20 to 11 O 0 C, preferably 30 to 7O 0 C and in particular 40 to 6O 0 C.
• the rigid polyurethane foams produced by the process according to the invention have a density of from 15 to 300 g / l, preferably from 20 to 100 g / l and in particular from 25 to 60 g / l.
• Table 1 shows that the polyesterols prepared by the process according to the invention are stable in storage for more than 3 months.
• the isocyanates as well as the isocyanate-reactive components were foamed together with the blowing agents, catalysts and all other additives at a constant mixing ratio of polyol component to isocyanate component of 100: 190. In each case, a constant setting time of 49 +/- 1 seconds and a total raw density of 33 +/- 0.5 g / L was set.
• polyetherol consisting of the ether of ethylene glycol and ethylene oxide having a hydroxyl functionality of 2 and a hydroxyl value of 200 mg KOH / g
• polymer MDI (Lupranat® M50 from BASF SE, Ludwigshafen, DE).
• the adjustment of the bulk density to 33 +/- 1 g / L was made on the water content, the setting time was adjusted by means of variation of the bis (2-dimethylaminoethyl) ether content to 49 +/- 1 s.
• the hardening was determined with the bolt test. For this purpose, 2.5, 3, 4, 5, 6 and 7 minutes after mixing the components in a polystyrene cup, a steel bolt with a spherical calotte of 10 mm radius was pressed 10 mm deep into the foam mushroom formed using a tensile / compression testing machine.
• the required maximum force in N is a measure of the hardening of the foam.
• the time was determined at which the surface of the rigid foam had visible fracture zones during the bolt test.
• the flame height was measured according to EN ISO 1 1925-2. The results are shown in Table 2.
• the rigid polyurethane foams produced by the process according to the invention have an improved curing behavior and an improved fire behavior.
• the isocyanates and the isocyanate-reactive components were foamed together with the blowing agents, catalysts and all other additives at a constant mixing ratio of polyol to isocyanate of 100: 190. In each case, a constant setting time of 49 +/- 1 seconds and a total raw density of 41 +/- 1 g / L was set.
• polyesterol according to Examples 1 and 2 or Comparative Examples 2 20 parts by weight of polyetherol, with an OHN of - 490 mg KOH / g prepared by polyaddition of propylene oxide on a sucrose / glycerol mixture as a starter molecule
• polyetherol consisting of the ether of ethylene glycol and ethylene oxide having a hydroxyl functionality of 2 and a hydroxyl value of 200 mg KOH / g 25 parts by weight of flame retardant trichloroisopropyl phosphate (TCPP) 2.5 parts by weight stabilizer Niax Silicone L 6635 (silicone-containing stabilizer) 7, 5 parts by weight pentane S 80:20 2.0 parts by weight water
• polymer MDI (Lupranat® M50 from BASF SE, Ludwigshafen, DE)
• the adjustment of the bulk density to 41 +/- 1 g / L was about the pentane content, the setting time was adjusted by means of variation of the proportion of 1: 1 mixture of bis (2-dimethylaminoethyl) ether and tetramethylhexanediamine to 49 +/- 1 s.
• sandwich panels were made by the double belt method.
• the bulk density was adjusted by raising the water content to 2.6 parts instead of 2 parts and using 11 parts of pentane instead of 7.5 parts to 30 +/- 1 g / L.
• the setting time was further adjusted by varying the proportion of 1: 1 mixture of bis (2-dimethylaminoethyl) ether and tetramethylhexanediamine to 49 +/- 1 s.
• the specimens for the assessment of the frequency of surface defects were prepared by the double-band method.
• the surface defects were determined by the method described above. For this purpose, a 20 cm x 30 cm large foam sample is pretreated and illuminated as described above and then photographed. The foams were then binarized and placed one on top of the other. The integrated area of the black areas of the binary images was set in relation to the total area of the images and thus represents a measure of the frequency of surface defects.
• Table 4 shows that the rigid polyurethane foams produced by the process of the invention are easier to produce trouble-free.
• test plates were produced by the double belt method according to the following production of a rigid polyurethane foam (variant 3).
• the isocyanates and the isocyanate-reactive components were foamed together with the blowing agents, catalysts and all other additives at a constant mixing ratio of polyol to isocyanate of 100: 170. In each case, a constant setting time of 28 +/- 1 seconds and a total raw density of 37 +/- 1 g / L was set.
• polyetherol consisting of the ether of ethylene glycol and ethylene oxide having a hydroxyl functionality of 2 and a hydroxyl value of 200 mg
• the adjustment of the bulk density to 37 +/- 1 g / L was made by adjusting the pentane content, the setting time was adjusted by means of variation of the bis (2-dimethylamino- ethyl) ether content to 28 +/- 1 s.
• Table 5 shows that the polyisocyanurate rigid foams produced by the process according to the invention are easier to produce trouble-free.

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• Chemical & Material Sciences (AREA)
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• Medicinal Chemistry (AREA)
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