THE USE OF POLYESTER POLYOLS FOR PREPARING MICROCELLULAR POLYURETHANE ELASTOMERS

Abstract: The invention relates to a method for preparing micro­ cellular polyurethane elastomer by reacting an organic isocyanate, a polyester polyol, a difunctional chain extender and a blowing agent, wherein at least a part of the polyester polyol used consists of a polyester polyol having a hydroxyl number between 28 and 112 and comprising units derived from aliphatic and/or aromatic dicarboxylic acids and from aliphatic, cycloaliphatic and/or heterocyclic glycols, as well as between 0.02 and 11 mole percent of units derived from monoalkanolamine with respect to the total amount of glycol and monoalkanolamine present in the polyester polyol.

Description: It is well known to manufacture microcellular polyurethane elastomers, especially for shoe-soling applications, by the interaction of a number of difunctional components. Thus, in one type of formulation, an organic diisocyanate, which may be in the form of a prepolymer, is reacted with a polyester diol and a low molecular weight diol such as 1,4-butanediol as chain extender, the reaction being performed in the presence of catalysts, surface active agents and a blowing agent, for example water. It is appreciated by those skilled in the art that polyurethanes made from essentially difunctional components can, nevertheless, contain cross-links because of secondary reactions, for example the reaction of diisocyanates or isocyanate-terminated polymer chains with the urethane and urea groups formed in the primary reactions. The introduction of a higher cross-link density by the deliberate use of higher functionality components, for example branched polyesters, can at certain levels have a generally deleterious effect on elastomer properties, for example tear and tensile strengths and abrasion resistance. At a lower level, however, the introduction of higher functionality components into an otherwise difunctional system can have advantageous effects. Thus United Kingdom Patent Specification No 1478045 describes a process for the manufacture of moulded flexible cellular polyurethane articles, especially microcellular elastomers, from a reaction mixture in which at least one of the reactants has a functionality greater than two, the overall functionality being defined in terms of the additional degree of branching present in the final polyurethane. The higher functionality component can be a polyester polyol, a polyisocyanate or a non-polymeric cross-linking agent. Suitable polyesters are said to be obtained by including a branching component in the polyester-forming reaction mixture, the branching components mentioned being glycerol, trimethylolpropane, pentaerythritol and trimesic acid. The effect of the higher functionality component is to enable the elastomers to be removed from the moulds in a shorter time than is the case for elastomers made from wholly difunctional components. Additionally, the increased functionality generally improves the humid ageing resistance of the elastomer. It has now been found that a significant improvement in the flex fatigue properties of the elastomers over a wide NCO/OH mixing ratio range can be achieved by the use of from aliphatic and/or aromatic certain new polyester polyols containing amide (-CONH-) ester forming derivatives and linkages. The present invention is concerned with the use of polyester polyols in the preparation of microcellular polyurethane elastomers, said polyester polyols comprising units derived from aliphatic and/or aromatic dicarboxylic acids or their ester forming derivatives and from aliphatic,cycloaliphatic and/or heterocyclic glycols, and between 0.02 and 11.0 mole percent of units derived from monoalkanolamine, with respect to the total amount of glycol and monoalkanolamine present in the polyester polyol and the polyester polyol having an hydroxyl number between 28 and 112. The polyester polyols as such have been disclosed in GB 858 757 and US 3948 847. The preferred polyester polyols in accordance with the invention are more particularly those comprising between 3 and 6 mole percent of units derived from monoalkanolamine with respect to the total amount of glycol and monoalkanolamine present in the polyester polyol. The invention furthermore provides a method for preparing microcellular polyurethane elastomers by reacting an organic diisocyanate, a polyester polyol , a difunctional chain extender and a blowing agent, wherein at least part of the polyester polyol used has an hydroxyl number between 28 and 112 and comprises between 0.02 and 11 mole percent, preferably between 3 and 6 mole percent, of units derived from monoethanolamine with respect to the total amount of glycol and monethanol amine present in the polyester polyol. The organic diisocyanate is preferably an aromatic diisocyanate, for example 4,4′-diphenylmethane diisocyanate and its mixtures with the 2,4′-isomer. In making the elastomer, the diisocyanate, especially when solid at ambient temperatures, may be used in the form of a prepolymer obtained in known manner by reacting the diisocyanate with a stoichiometric deficiency of a polyester polyol or one or more low molecular weight diols. The polyester polyol may be prepared in conventional manner by reacting one or more aliphatic and/or aromatic dicarboxylic acids, for example adipic, glutaric, succinic, phthalic, isophthalic and terephthalic acids, or their ester-forming derivatives, for example their dimethyl esters, with one or more aliphatic, cycloaliphatic or heterocyclic glycols, for example ethylene glycol, propylene glycol, diethylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,4-cyclohexanedimethanol and 2,5 bis-hydroxymethylfuran and with a mono-alkanolamine such as ethanolamine (2-aminoethanol). The melting point of the polyester should not exceed 50 deg. Celsius and the viscosity at 100 deg. Celsius should not exceed 10 poises. The polyester polyol containing -CONH- linkages may be the sole polyester in the formulation or, alternatively, it may be used in conjunction with a polyester polyol containing no -CONH- linkages. Furthermore, as indicated above, a portion of polyester, which may or may not contain -CONH-linkages, may be pre-polymerised with the diisocyanate. The overall polyester hydroxyl number is preferably in the range 45 - 65. Whilst the polyester polyols containing -CONH- linkages are essentially unbranched in structure unlike, for example, polyesters containing trimethylolpropane or pentaerythritol residues, the presence of the -CONH- linkages introduces the possibility of cross-links being formed during reaction with the diisocyanate, the level of cross-linking being dependent upon the -CONH- content and the isocyanate index. It is preferred that the -CONH- content of the polyester and the isocyanate index should be such that the polyurethane product contains from 0.008 to 0.20 branch point per 1000 units of molecular weight additional to the branching present when wholly difunctional components are used. The difunctional chain extender is suitably a low molecular weight aliphatic, cycloaliphatic or heterocyclic diol, for example ethylene glycol, 1,4- butanediol or a low molecular weight diamine. Suitable blowing agents include water and inert volatile liquids such as trichlorofluoromethane, the amount being selected in known manner to provide an elastomer of the desired density. In addition to the components already mentioned, the elastomer-forming reaction mixture may also contain other conventional ingredients of such systems. In particular, it may contain catalysts, for example tertiary amines and tin compounds, surfactants, for example siloxane-oxyalkylene copolymers and oxyethylated alkylphenols, flame-retardants, fillers and pigments. The components of the reaction mixture may be mixed together in any convenient manner, for example by using any of the equipment described in the prior art for the purpose. If desired some of the individual components may be pre-blended so as to reduce the number of component streams requiring to be brought together in the final mixing step. It is often convenient to have a two-stream system whereby one stream comprises a prepolymer and the second stream comprises all the other components of the reaction mixture. In preferred formulations, one stream comprises a prepolymer of diphenylmethane diisocyanate and a polyester diol, the other stream comprising a polyester containing ethanolamine residues, 1,4-butanediol and/or ethylene glycol as chain extender, water as blowing agent together with catalyst and surfactant. The method of the invention is particularly useful for the production of shoe soles. For that purpose, the reaction mixture may be introduced into moulds corresponding in size and shape with the desired products, the overall density being varied in known manner by varying the amount of blowing agent and the degree of overpacking. The microcellular products may have densities in the range 0.3 -1.0 g/cm³. A further useful feature of the polyester diols containing -CONH- linkages is that they yield polyurethanes having some of the advantageous properties associated with branched polyesters whilst retaining the lower viscosities associated with linear polyesters. The invention is illustrated but not limited by the following Example in which all parts and percentages are by weight unless otherwise indicated. Examples 1. Preparation of Polyesters The following polyesters were prepared in a conventional manner by reacting the reactants in the molar quantities listed below, in the presence of tetrabutyl-o-titanate sufficient to give 6 ppm Ti in final product, and in a nitrogen atmosphere at temperatures up to 210 Deg. C. 2. Preparation of Prepolymers Prepolymer X having an NCO content of 18.52 % was prepared by reacting 60.11 parts of 4,4′-diphenylmethane diisocyanate with 39.84 parts of Polyester A. Prepolymer Y having an NCO content of 18.70 % was prepared by reacting 59.21 parts of 4,4′-diphenylmethane diisocyanate and 1.50 parts of crude MDI (NCO content 29.2 %) containing approximately 55% of diphenylmethane diisocyanate, the bulk of the remainder being polymethylene polyphenyl polyisocyanates of functionality greater than two with 39.29 parts of Polyester A. 3. Preparation of Elastomers from polyester A, B and E Microcellular elastomers were prepared under conventional conditions from the formulations 1-9 described in Table II. Quantities are quoted in parts by weight. The formulations were designed to give elastomers having one theoretical branch point per 81000 units of molecular weight (theoretical number of branch points based on polyol plus prepolymer). Physical properties of the elastomers obtained are given in Table III. Testing was carried out under uniform conditions. The formulations 4-9 are comparative. The cream time, gel time, tack free time, tear resistance time, free rise density and moulding resilience were substantially comparable for all formulations. 4. Preparation of Elastomers from polyester A, B, C and D Elastomers were prepared by hand mixing technique from the formulations 1-4 described in table IV. Prepolymer Z is a commercially available product having a NCO content of 19 %, marketed by Imperial Chemical Industries Ltd. under the trade name "Uropol DP 980". Formulation 1 is comparative. Quantities used in the formulations are quoted in parts by weight. The cream time, gel time, tack free time, tear resistance time, free rise density and moulding resilience were substantially comparable for all formulations. The physical properties of the obtained elastomers are given in table V. 5. Preparation of Elastomers from Polyester A, F and G Elastomers were prepared by machine mixing technique from the formulations 1 - 9 described in table VI. Quantities are quoted in parts by weight. Physical properties of the obtained elastomers are given in table VII. Formulations 1 to 3 are comparative. The cream time, gel time, tack free time, tear resistance time, free rise density and moulding rsilience are substantially comparable for all formulations.

Claims: The use of a polyester polyol in the preparation of microcellular polyurethane elastomers comprising units derived from aliphatic and/or aromatic dicarboxylic acids or their ester forming derivatives and aliphatic, cycloaliphatic and/or heterocyclic glycols and between 0.02 and 11.0 mole percent of units derived from monoalkanolamine with respect to the total amount of glycol and monoalkanolamine present in the polyester polyol, and the polyester polyol having an hydroxyl number between 28 and 112. The use according to claim 1 characterized in that the polyester polyol comprises between 3 and 6 mole percent of units derived from monoalkanolamine. The use according to claim 1 or 2 characterized in that the monoalkanolamine is monoethanolamine. A method for preparing microcellular polyurethane elastomer by reacting an organic isocyanate, a polyester polyol, a difunctional chain extender and a blowing agent, characterized in that at least a part of the polyester polyol used consists of a polyester polyol having a hydroxyl number between 28 and 112 and comprising units derived from aliphatic and/or aromatic dicarboxylic acids and from aliphatic, cycloaliphatic and/or heterocyclic glycols, as well as between 0.02 and 11 mole percent of units derived from monoalkanolamine with respect to the total amount of glycol and monoalkanolamine present in the polyester polyol. A method according to claim 4 characterized in that a polyester polyol is used comprising between 3 and 6 mole percent of units derived from monoalkanolamine. A method according to claim 4 or 5 characterized in that a polyester polyol comprising monoethanolamine is used. A method according to claim 4 or 5 characterized in that a prepolymer of an excess of diphenylmethane diisocyanate and a polyester polyol is reacted with 1,4-butanediol and/or ethylene glycol as chain extender and with a polyester polyol composition comprising at least one polyester polyol containing ethanolamine residues, in the presence of water as a blowing agent and of catalyst and surfactant. The use of a polyester polyol blend in the preparation of microcellular polyurethane elastomers, characterised in that it consists of a mixture of one or more polyester polyols comprising units derived from aliphatic and/or aromatic dicarboxylic acids and aliphatic, cycloaliphatic and/or heterocyclic glycols and not comprising - COHN - linkages, with at least one polyester glycol having a hydroxyl number between 28 and 112 and consisting of units derived from aliphatic and/or aromatic dicarboxylic acids, aliphatic, cycloaliphatic and/or heterocyclic glycols, and between 0.02 and 11.0 mole percent of monoalkanolamine with respect to the total amount of glycol and monoalkanolamine present in said polyester glycol. The use of a blend according to claim 8, characterized in that said polyester glycol comprises between 3 and 6 mole percent of units derived from monoalkanolamine. The use of a blend according to claim 8 or 9 characterized in that said polyester glycol comprises units derived from monethanolamine.

Inventors: BAGAGLIO, GIAN CARLO, BENTLEY, JAMES MARTIN, BROWN, JAMES PETER
Applicants: IMPERIAL CHEMICAL INDUSTRIES PLC
Application year: 1987
Main classification: C08G18
IPC codes: C08G101, C09J9, C08G18, C08G69