POLYURETHANE ELASTOMER AND FOAM EXHIBITING IMPROVED ABRASION RESISTANCE

Abstract: A polyurethane elastomer having a density of from 100 to 1100 kg/m<3>, and an abrasion loss of less than 300 mg, as determined in accordance with Test Method A of ISO 4649. Such elastomer can be prepared by reacting a urethane-modified polyisocyanate with at least one polyol in the presence of from 1.1 to 10 parts per 100 parts by weight of polyol of a liquid polybutadiene comprising 1,2-butene, 2,3-(trans)butene and 2,3-(cis)-butene moieties, wherein the 1,2-butene content is less than 50 percent, based on total butene content, and the 2,3(cis)-butene content is greater than the 2,3-(trans)butene content.

Description: POLYURETHANE ELASTOMER AND FOAM EXHIBITING IMPROVED ABRASION RESISTANCE Background of Invention This invention relates to a polyurethane elastomer exhibiting an improved abrasion resistance performance, and a process for the preparation thereof requiring the use of a liquid polybutadiene. Polyurethane elastomer may be obtained by reaction of an isocyanate compound with an active hydrogen-containing compound such as, for example, a polyester or polyether polyol, optionally in the presence of a blowing agent. For processing convenience, the isocyanate compound is preferably an isocyanate-terminated prepolymer prepared by reaction of an excess of an aromatic diisocyanate with a low molecular weight diol such as, for example, dipropylene glycol and/or tripropylene glycol. The blowing agent may be an inert physical blowing agent such as, for example, trichiorofluoromethane or, alternatively, a reactive agent such as, for example, water. The preparation of polyurethane elastomer by such procedures is described in, for example, patent publications E.P. 235,888; E.P. 175,733; U.S. Patents 3,591,532; 3,901,959; 4,647,596 and 4,757,095. Current manufacturing trends for polyurethane elastomers are driven by two dominant factors, namely, cost and environmental concern. Consideration of cost stimulates polyurethane elastomer producers to select polyether polyols over polyester polyols; consideration of environmental concerns stimulates polyurethane elastomer producers to select, when required, water in preference to certain physical blowing agents. Selection of polyether polyols can have a negative implication for physical properties of the resulting elastomer, including abrasion resistance. Similarly, use of water as blowing agent can also have a negative implication for physical properties of the resulting elastomer, including abrasion resistance and low temperature durability. Some of these deficiencies, notably low temperature durability, can be reduced by use of an isocyanate-terminated prepolymer prepared by reaction of an excess of an aromatic diisocyanate with a high molecular weight polyether diol or triol. However, there still remains the need to find a general means of enhancing the abrasion resistance of a polyurethane elastomer, optionally prepared in the presence of a blowing agent and particularly water. Our investigations into the preparation of polyurethane elastomer has now revealed that selected liquid polybutadienes can significantly enhance the abrasion resistance of a polyurethane elastomer when prepared in the presence thereof. Such observation was unexpected in consideration of the open literature documenting the use of liquid polybutadienes when preparing a polyurethane elastomer. U.S. Patent 4,242,468 discloses the use of a monohydroxylated polybutadiene, in amounts of at least 30 parts per 100 parts by weight of polyol, as a nonmigratory plasticizer in polyurethanes; the- document is silent with respect to abrasion resistance. Plasticizers serve to soften material and it is generally appreciated that softer material has an inferior abrasion resistance. U.S. Patent 5,079,270 discloses the preparation of polyurethane articles in the presence of a liquid polybutadiene having a molecular weight of from 1500 to 6000 wherein the polybutadiene serves as an internal mold release agent; the document is silent with respect to abrasion resistance. In a first aspect, this invention relates to a polyurethane elastomer prepared by reacting (a) a urethane-modified polyisocyanate, with (b) a polyether polyol or polyester polyol, in the presence of (c) from 0.1 to 10 parts per 100 parts by weight of component (b) of a liquid polybutadiene, and optionally a blowing agent characterized in that when; i) the polybutadiene, based on its total butene content, comprises the 1 ,2-butene moiety in an amount of less than 50 percent, and the amount present of the 2,3-(cis)-butene moiety is greater than that of the 2,3-(trans)-butene moiety; and ii) the elastomer has a density of from 100 to 1100 kg/m 3 , and an abrasion loss of less than 300 mg, as determined in accordance with Test Method A of ISO 4649. In a second aspect, this invention relates to a process for preparing a polyurethane elastomer having a density of from 100 to 1100 kg/m and exhibiting an abrasion loss of less than 300 mg as determined in accordance with Test Method A of ISO 4649 which comprises reacting, optionally in the presence of a blowing agent: a) a urethane-modified polyisocyanate which has an isocyanate content of from 15 to 30 weight percent and is obtained by reacting a methylene diphenylisocyanate with a polyol; with b) a polyester or polyether polyol, being a diol or triol which has an average hydroxyl equivalent weight of from 500 to 5000; in the presence of (c) from 0.1 to 10 parts per 100 parts by weight of (b) of a liquid polybutadiene having a molecular weight of from 1000 to 10000 and which, based on its total butene content, comprises the 1 ,2-butene moiety in an amount of less than 50 percent, and wherein the 2,3- (cis)-butene moiety is present in an amount greater than that of the 2,3-(trans)-butene moiety, wherein component (a) is present in an amount sufficient to provide an isocyanate reaction index of from 80 to 120. In a third aspect, this invention relates to the use of a liquid polybutadiene to improve the abrasion resistance of a polyurethane elastomer prepared by reacting a urethane-modified polyisocyanate with a polyether polyol or polyester polyol in the presence of the liquid polybutadiene, characterized in that the polybutadiene is present in an amount of from 0.1 to 10 parts per 100 parts by weight of polyol, and, based on its total butene content, comprises the 1 ,2-butene moiety in an amount of less than 50 percent, and the amount of the 2,3-(cis)-butene moiety present is greater than that of the 2,3-(trans)butene moiety. In a fourth aspect, this invention relates to an isocyanate-reactive composition for use in the manufacture of a polyurethane elastomer, as above mentioned, which comprises, a) from 90 to 99.9 weight percent based on the total amount of component (a) and component (b), of a polyester or polyether polyol having an average hydroxyl equivalent weight of from 500 to 5000; and b) from 0.1 to 10 weight percent of a liquid polybutadiene which, based on its total butene content, comprises the 1 ,2-butene moiety in an amount of less than 50 percent, and the amount present of the 2,3-(cis)-butene moiety is greater than that of the 2,3-(trans)butene moiety. The polyurethane elastomer disclosed of the invention generally has a density of from 100 to 1100, preferably from 200 to 1000, and more preferably from 300 to 800 kg/m 3 , and exhibits an improved abrasion resistance. The abrasion resistance performance of the elastomer is generally such that it exhibits a material loss of less than 300, preferably less than 250, and more preferably less than 200, and yet more preferably less than 150 mg, as determined in accordance with Test Method A of ISO 4649. The polyurethane elastomer is prepared by reacting a urethane-modified polyisocyanate with a polyester polyol or polyether polyol in the presence of a polybutadiene, which is a liquid at room temperature (25°C). The applicants have found that the use of a selected polybutadiene is important for obtaining a product that exhibits the improved abrasion resistance performance. Polybutadiene, prepared by polymerization of butadiene, in general is constituted by structural moieties that can be described as being equivalent to 1 ,2-butene, and 2,3-butene in both the cis- and trans- configuration. Formula I depicts schematically these moieties in a part of a polybutadiene polymer chain: the cis-2,3-butene moiety is represented by part A; the 1,2-butene moiety by part B; and the trans-2,3-butene moiety by part C. CH l = CH roraula I To provide the polyurethane elastomer with improved abrasion resistance performance, it has been found that the 1,2-butene content of the polybutadiene should be less than 50, preferably less than 35, and more preferably less than 25, and yet more preferably less than 15 weight percent of the total A, B and C content. For the same purpose, it is found advantageous to employ a polybutadiene which contains a greater proportion of cis-2,3-butene moieties than trans-2,3-butene moieties. The cis-2,3-butene content of the polybutadiene advantageously is at least 50, preferably at least 60, and more preferably at least 70 percent of the total A, B, and C content. To facilitate mixing with the polyisocyanate and polyol reactants used to prepare the polyurethane, the viscosity of the liquid polybutadiene advantageously does not exceed 50000, and preferably does not exceed 20000, and more preferably does not exceed 15000 mPa.s at 25°C. Typically a polybutadiene with a number average molecular weight of up to 10000, preferably from 1000 to 10000 is employed. In particular, the number average molecular weight may be from greater than 6000, preferably from 6500, to 10000. In a further preferred embodiment, the molecular weight is from 1500 to 8000, preferably from 3000 to 8000 and more preferably about 8000. If the polybutadiene has a high 1,2-butene content, it is of advantage for the said polybutadiene to have a high molecular weight. In a preferred embodiment of this invention, the polybutadiene has a 1,2-butene content of less than 25 percent, and has a cis-2,3-butene content of at least 60 percent of the total A, B, and C content. Optionally, and to enhance the compatibility of the liquid polybutadiene with polyol, a hydroxylated polybutadiene can be used. Such a hydroxylated polybutadiene typically will have a hydroxyl number of less than 40, preferably less than 25, and more preferably less than 15; and normally will have a hydroxyl functionality of less than 2, preferably less than 1.5 hydroxyl units/polybutadiene molecule. The techniques for preparing such liquid polybutadienes are well-known to those skilled in the art and will not be discussed in detail. It will be understood in particular by one skilled in the art that the A, B, and C butene contents of the polybutadiene can be influenced by the polymerization catalyst and polymerization conditions employed. Examples of commercially available polybutadienes suitable for use in the present invention are given in Table I, along with an indication of their general characteristics. Table I Total 2,3- Viscosity Molecular 1,2-butene butene Product Supplier (centipoise weight content content at 25°C) (cis - content) 99 POLYOL 110 Huls (De) 1800 860 1 (72) 99 POLYOL 130 Hϋls (De) 3000 3300 1 (75) LITHENE 80 Revertex (UK) 5000 4000 20 N4-5000 ( / ) LITHENE 87 Revertex (UK) 8000 14000 13 N4-9000 ( / ) LITHENE 80 Revertex (UK) 5000 3500 20 HFN4-9000 © ( / ) ICON 154 ® Ricon (USA) 2800 8090000 90 10 ® Understood to be a monohydroxylated polybutadiene, OH Number of about 7. © A comparative liquid polybutadiene for the purpose of this invention due to its 1,2-butene content. in preparing the elastomer of this invention the liquid polybutadiene is used in an amount of from 0.1 , pre erably from 0.5, more preferably from 1 , and yet more preferably from 2.5; and up to 10, preferably up to 5 parts per 100 parts by weight of polyol. The polyisocyanate component used to prepare the elastomer of this invention is a urethane-modified polyisocyanate, and especially a urethane-modified aromatic polyisocyanate. The isocyanate content of the urethane-modified polyisocyanate advantageously is from 15 to 30 weight percent. When the elastomer to be produced is intended, for example, for a shoe sole application, it is advantageous to use a urethane- modified polyisocyanate having an isocyanate content of from 17 to 24 weight percent. When the elastomer to be produced is intended, for example, for a semirigid integral skin application, it is advantageous to use a urethane-modified polyisocyanate having an isocyanate content of more than 25 and up to 30, preferably from 27 to 30, weight percent Use of a non modified polyisocyanate in combination with the liquid polybutadiene has, to date, not been found to provide forthe improved abrasion resistance of polyurethane elastomer. The preferred urethane-modified aromatic polyisocyanates are those obtained by reacting an excess of a methylene diphenyiisocyanate with a polyol which is a polyester or preferably a polyether polyol and notably a diol or triol. Applicants have found that methylene diphenyiisocyanate modified by reaction with low moiecuiar weight glycol or high molecular weight polyol are equally suitable for this invention. By the term "high molecular weight" it is meant polyols having a moiecuiar weight of 1000 or more. The techniques for preparing such urethane-modified polyisocyanates are well documented in the open literature and will not be further reported herein. In preparing the elastomer of this invention, the urethane-modified polyisocyanate is used in an amount to provide for an isocyanate reaction index of advantageously from 80 to 120, preferably from 90 to 110, and more preferably from 95 to 105. By the tenn "isocyanate index" it is understood that at an index of 100, one equivalent of isocyanate is present for each isocyanate reactive hydrogen atom present from the polyol, or other active hydrogen atom bearing substance able to react with the urethane-modified polyisocyanate. The polyol component suitable for use in preparing the elastomer of this invention is a polyester polyoi, preferably a polyether polyol which has an average of from 2 to 4, preferably from 2 to 3, and more preferably from 2 to 2.S hydroxyl groups/molecule; and an average hydroxyl equivalent weight of from 500 to 5000, preferably from 1000 to 3500, and more preferably from 1500 to 3000. Optionally and advantageously, such polyether polyoi may also have a primary hydroxyl content of from at least 75, preferably from at least 80, and more preferably from at least 85 percent based on total hydroxyl content of the polyol. Typically, such polyether polyols may be obtained by reaction of an active hydrogen-containing initiator with a quantity of one or more alkylene oxides to give a product of desired hydroxyl nature and equivalent weight. Generally, such alkylene oxides are C M alkylene oxides and include 1,4- butylene oxide, 2,3-butyiene oxide, and especially propylene oxide and ethylene oxide. Exemplary of suitable active hydrogen-containing initiators are polyols, polyether adducts of polyols, polyamines and other compounds having a plurality of active hydrogen atoms per molecule, such as those described in U.S. Patent 4,500,422. Preferred initiators for use in preparing polyether polyols suitable for employment in the process of preparing the polyurethane elastomer include ethylene giycol, propylene glycol, butylene glycol, glycerine, 1 ,1,1 -trimethylolpropane, 1,1 ,1-trimethylolethane, σ-methylgiucoside, C 2 .8 alkylene diamines such as, for example, ethylenediamine and hexamethylenediamine, and mixtures thereof. Espe ally preferred are the glycol initiators or alkoxylated adducts of such glycols. Exemplary of commercially available and preferred polyether polyols for use in manufacturing a polyurethane elastomer by the process of this invention are those polyether polyols identified by the trademark "VORANOL" and indude products designated as VORANOL EP 1900 and VORANOL CP 6055, sold by The Dow Chemical Company. In addition to the polyols described hereinabove other suitable polyols which may be present in the process of preparing the polyurethane elastomer include the so-called polymer polyols based on polyether polyols such as those described in U.S. Patent 4,394,491. Among the useful polymer polyols are included dispersions of vinyl polymers, particularly styrene/acrylonitrile copolymers, in a continuous polyether polyol phase. Also useful are the so-called polyisocyanate polyaddition (PIPA) polyols (dispersions of polyurea-polyurethane particles in a polyoi) and the polyurea dispersions in polyol such as, for example, PHD polyols. o Copolymer polyols of the vinyl type are described in, for example, U.S. Patents 4,390,645; 4,463,107; 4,148,840 and 4,574,137. Suitable polyester polyols may, for instance, be produced from dicarboxylic acids, preferably aliphatic dicarboxylic acids, having 2 to 12 carbon atoms in the alkylene radical, and multifunctional alcohols, preferably diols. These acids include, for instance, aliphatic dicarboxylic acids such as glutaric acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, and preferably, succinic and adipic acids; cycloaliphatic dicarboxylic acids sud. as 1 ,3- and 1 ,4-cyclohexane dicarboxylic acid; and aromatic dicarboxylic acids such as phthalic acid and terephthalic acid. Examples of di- and multifunctional, particulariy difunctional, alcohols are: ethylene glycol, diethylene glycol, 0 propylene glycol, dipropylene glycol, 1 ,3-propanediol, 1 ,10-decanedioi, glycerine, trimethylolpropane, and preferably, 1,4-butanediol, and 1,6-hexanediol. When preparing a polyurethane elastomer as disclosed herein, optionally and advantageously the polyether or polyester polyoi is used in admixture with a chain extending agent. The presence of a chain extending agent provides desirable physical properties, 5 especially hardness, of the resulting elastomer. Typically polyurethane elastomers prepared according to this invention, in the presence of a chain extending agent, will have a Shore A Hardness of from 20A to 80A, preferably from 35A to 75A, and more preferably from 45A to 70A. To provide elastomers with such hardness, the chain-extending agent advantageously is used in an amount of from 2 to 20, preferably from 5 to 15, and more preferably from 6 to 12 0 percent based on total weight of the polyether polyol and chain extending agent. The chain-extending agent is characterized in that it is an isocyanate-reactive substance, especially an organic difunctionai isocyanate-reactive substance that has an equivalent weight of less than or equal to 150 and preferably less than or equal to 100. Representative of suitable chain-extending agents include polyhydric alcohols, aliphatic 5 diamines including polyoxyalkyienediamines, aromatic diamines and mixtures thereof. Preferred chain extending agents are dihydroxyl compounds, especially glycols. Illustrative of suitable chain-extending agents include 1,2-ethanediol, 1,3-propanediol, 1,5-pentanedioI, 1,6-hexaπediol, 1,2-propanediol, 1,3-butanediol, 1 ,4-butanediol, 1,6-hexanediol, 1 ,4-cydohexanediol, 1 ,4-cyclohexanedimethanol, ethylenediamine 1 ,4-butylenediamine and 1 ,6-hexamethylenediamine. Compounds such as ethoxylated hydroquinone can also be employed as a chain-extending agent. The above- -mentioned chain extending agents can be used singularly or combined or in admixture with other compounds induding diethylene glycol, dipropylene glycol, tripropyieπe glycol, ethanolamine, diethanolamine, triethanolamine and N-methyidiethanolamine, and N-ethyldiethaπolamine, as well as adducts obtained by esterification of aliphatic carboxyiic acids with aliphatic diols or triols such as those exemplified above utilizing from 0.01 to 1.08 0 mole of acid per mole of diol/triol. While any of the chain extending agents exemplified above can be employed in the process of preparing the polyurethane elastomer, it is particularly preferred to use 1,4-butanediol, 1 ,6-hexanediol, neopentyl giycol, 1,4-cyclohexane diol, ethylene glycol, bishydroxyethoxybenzene, ethoxylated hydroquinone glycerine, and diethylene glycol either alone or in admixture. Especially preferred as chain-extending agent is 5 1 ,4-butanediol. As mentioned hereinabove, the polyurethane elastomer is optionally prepared in the presence of a blowing agent which comprises carbon dioxide, an aliphatic or alicyclic C.-C. alkane, or a chlorine-free halogenated alkane, or mixtures thereof. Carbon dioxide may be used in a gaseous or liquid form, or generated insitu by the presence of water which reacts with o the polyisocyanate to provide the carbon dioxide. The amount of water present is typically from 0.05 to 2, preferably from 0.1 to 1.5 and more preferably from 0.2 to 1 weight percent, based on the total weight of the polyol and optional chain-extending agent present. Examples of suitable aliphatic or alicyclic C 3 -C 8 alkanes include butane, n-pentane, i- pentane, hexane, cyclopentane and cyclohexane. Examples of suitable chlorine-free 5 halogenated alkanes include di-, tri-, and tetrafluoroethane. When preparing the polyurethane elastomer, optionally but advantageously present are additional additives induding catalysts, surfactants, fillers, pigments, fire retardants, antioxidants, and antistatic agents. The use of such additives is well-known in the art and reference is made thereto for this purpose. 0 Suitable catalysts indude the tertiary amine and organometallic compounds such as those desσibed in U.S. Patent 4,495,081. When using an amine catalyst advantageously it is present in an amount of from 0.1 to 3, preferably from 0.1 to 1.5 and more preferably from 0.3 to 1 weight percent by total weight of polyoi and optional chain extending agent When the catalyst is an organometallic catalyst, advantageously it is present in an amount of from 0.001 5 to 0.2, preferably from 0.002 to 0.1 and more preferably from 0.01 to 0.05 weight percent by total weight of polyol and optional chain extending agent Particularly useful catalysts include triethylenediamine, bis(N,N-dimethylaminoethyl)ether and di(N,N-dimethylaminoethyl)amine, dialkyl tiπdicarboxylate substances including dimethyltin dilaurate, dibutyltin dilaurate, dioctyltin dilaurate, dibutyltin diacetate; and stannous octoate. Combinations of amine and organometallic catalysts advantageously may be employed. Suitable surfactants include the diverse silicone surfactants, preferably those which are block copoiymers of a polysiloxane and a polyoxyalkylene. Exemplary of such surfactants are the products DC-193 and Q4-3657 available from Dow Corning and TEGOSTAB B41 13 available from Goldschmidt When present, the amount of surfactants advantageously employed is from 0.1 to 2, and preferably from 0.2 to 1.3 percent by total weight of the polyol and optional chain extending agent. Other suitable surfactants also include non-silicone containing surfactants, such as poly(alkyleneoxides). Suitable pigments and fillers include for example calcium carbonate, graphite, carbon black, titanium dioxide, iron oxide, alumina trihydrate, wollastonite, prepared glass fibers dropped or continuous, polyesters and other polymeric fibers. Suitable methods of intimately mixing the urethane-modified polyisocyanate with the polyoi indude molding techniques such as described in, for example, "Polyurethanes Handbook" by G unter Oertel Hanser Publishes Munich ISBN 0-02-948920-2 (1985). Other suitable methods for preparing microcellular and elastomeric polyurethane polymers are described, for example, in U.S. Patents 4,297,444; 4,218,543; 4,444,910; 4,530,941 and 4,269,945. The polyurethane elastomer disclosed herein is preferably a microcellular polyurethane elastomer. Such a elastomer is typically prepared by intimately mixing the reaction components at room temperature or a slightly elevated temperature for a short period and then pouring the resulting mixture into an open mold, or injecting the resulting mixture into a closed mold, which in either case is heated. Upon completion of the reaction, the mixture takes the shape of the mold to produce a polyurethane elastomer of a predefined structure, which can then be sufficiently cured and removed from the mold with a minimum risk of incurring deformation greater than that permitted for its intended end application. Suitable conditions for promoting the curing of the elastomer include a mold temperature of typically from 20°C to 150°C, preferably from 35°C to 75 β C, and more preferably from 45°C to 55°C Such temperatures generally permit the sufficiently cured elastomer to be removed from the mold typically in 1 to 10 minutes and more typically in 1 to 5 minutes after intimately mixing the reactants. Optimum cure conditions will depend on the particular components induding catalysts and quantities used in preparing the elastomer and also the size and shape of the article manufactured. The polyurethane elastomer disclosed herein is useful in the preparation of artides such as, for example, carpet, rollers, door seals, coatings, tires, wiper blades, steering wheels, gaskets, belts, and particularly shoe soles. The following examples are provided to illustrate the invention but are not intended to limit the scope thereof. All parts and percentages are given by weight unless otherwise indicated. The reactants and the components present when preparing the polyurethane elastomers are identified as follows: Polyol 1 - a poly(oxypropylene-oxyethylene) diol having a hydroxyl equivalent weight of 2000 and a primary hydroxyl content of at least 85%. Polyol 2 - a 2000 equivalent weight poly(oxypropylene-oxyethylene) triol having a primary hydroxyl content of at least 75%. TEDA - triethylenediamine D8TDL - dibutyltin dilaurate Polybutadiene A - Polyol 110, as described in Table I. Polybutadiene B - Polyol 130, as described in Table I. Polybutadiene C - LITHENE N4-5000, as described in Table I. Polybutadiene D - LITHENE N4-9000, as described in Table I. Isocyanate 1 - a urethane-modified polyisocyanate having an isocyanate content of 18 weight percent obtained by reacting an excess of 4,4'-methylene diphenyiisocyanate with a polyol mixture having an average equivalent weight of 1000 and comprising Polyol 2 and a 1000 moiecuiar weight polyoxypropylene giycol. Isocyanate 2 - a urethane-modified polyisocyanate having an isocyanate content of 18.5 weight percent obtained by reacting an excess of 4,4'-methylene diphenyiisocyanate with a polyol mixture having an average equivalent weight of 1770 and comprising Polyol 1 , Polyol 2 and dipropylene glycol. Isocyanate 3 - a urethane-modified polyisocyanate having an isocyanate content of 23.2 weight percent obtained by reacting an excess of 4,4'-methylene diphenyiisocyanate with dipropylene giycol. Example 1 Elastomers 1 to 4 are prepared according to the formulation given in Table II employing a low pressure mixer dispensing unit and a mold with dimensions of 200 X 200 x 6 mm thermostated to a temperature of from 45 to 55°C Elastomers 5 to 11 are prepared in a similar manner only in this case the mold has as dimensions 200 X 200 X 10 mm. The physical properties, as observed, of the resulting elastomers are also reported in Table II. Examples 1 to 4 illustrate the abrasion resistance improvement of polyurethane elastomers obtained by use of a greater amount of a liquid polybutadiene. Examples 5 to 9 illustrate the abrasion resistance improvement of a water-blown polyurethane elastomer obtained by use of the same amount of a liquid polybutadiene having a different moiecuiar weight Use of a higher molecular weight polybutadiene favoring a better abrasion resistance. Example 10 and 11 illustrate the dramatic improvement of abrasion resistance of a water- blown polyurethane elastomer prepared from an alternative isocyanate and in the presence a liquid polybutadiene. Examples 1, 5 and 10 do not contain a polybutadiene and are not an example of this invention. Example 2 (Comparative Example) An elastomer, Elastomer 12, is prepared according to the procedure as described for Elastomer 7 of Example 1 except that the 3.5 pbw of Polybutadiene B is substituted by 3.5 o pbw of Polybutadiene E. Polybutadiene E being the product RICON 154 as disclosed in Table I of the description. The abrasion resistance of the Elastomer 12 is observed as being a weight loss of 340 mg, compared to 140 mg of Elastomer 7. Both polybutadienes have a similar molecular weight, but Polybutadiene E has a significantly higher 1 ,2-butene content which is beiieved to 5 lead to the inferior abrasion resistance. 0 5 0 35

Claims: CLAIMS 1. A polyurethane elastomer prepared by reacting (a) a urethane-modified polyisocyanate, with (b) a polyether polyol or polyester polyol, in the presence of (c) from 0.1 to 10 parts per 100 parts by weight of (b) of a liquid polybutadiene, and optionally a blowing agent characterized in that; 0 the polybutadiene, based on its total butene content, comprises the 1 ,2- butene moiety in an amount of less than 50 percent, ii) the amount of the 2,3-(cis)-butene moiety present in the polybutadiene is greater than the amount of the 2,3-(trans)butene moiety; and iii) the elastomer has a density of from 100 to 1100kg/m 3 , and an abrasion loss of less than 300 mg, as determined in accordance with Test Method A of ISO 4649. 2. An elastomer as claimed in Ciaim 1 wherein the polybutadiene has a 1,2-butene content of less than 25 percent, and a 2-3-(cis)-butene content of at least 50 percent. 3. An elastomer as claimed in Claim 1 or 2 wherein the polybutadiene has a number average moiecuiar weight of from 1000 to 10000. 4. An elastomer as claimed in Ciaim 1 or 2 wherein the polybutadiene is a hydroxylated polybutadiene. 5. An elastomer as claimed in Claim 1 or 2 prepared in the presence of a blowing agent which comprises carbon dioxide, an aliphatic or alicyclic C 3 -C 8 alkane, or a chlorine-free halogenated alkane. 6. An elastomer as claimed in Claim 5 wherein the blowing agent consists essentially of carbon dioxide produced by the reaction of water with the polyisocyanate. 7. A process for preparing a polyurethane elastomer having a density of from 100 to 1100 kg/m 3 and exhibiting an abrasion loss of less than 300 mg as determined in accordance with Test Method A of ISO 4649 which comprises reacting, optionally in the presence of a blowing agent: (a) a urethane-modified polyisocyanate which has an isocyanate content of from 15 to 30 weight percent and is obtained by reacting a methylene diphenyiisocyanate with a polyol; with (b) a polyester or polyether polyol, being a diol or triol which has an average hydroxyl equivalent weight of from 500 to 5000; in the presence of (c) from 0.1 to 10 parts per 100 parts by weight of (b) of a liquid polybutadiene having a molecular weight of from 1000 to 10000 and which, based on its total butene content, comprises the 1 ,2 butene moiety in an amount of less than 50 percent, and wherein the 2,3 (cis)-butene moiety is present in an amount greater than that of the 2,3-(trans)butene moiety, wherein (a) is present in an amount sufficient to provide an isocyanate reaction index of frorr 80 to 120. 8. A process according to Claim 7 wherein the polybutadiene is present in an amount of from 0.5 to 5 parts by weight and has a number average molecular weight of from 3000 to 8000. 9. Use of a liquid polybutadiene to improve the abrasion resistance of a polyurethane elastomer prepared by reacting, a urethane-modified polyisocyanate with a polyether polyol or polyester polyol in the presence of the liquid polybutadiene, characterized in that the polybutadiene is present in an amount of from 0.1 to 10 parts per 100 parts by (3 weight of polyol, and, based on its total butene content, comprises the 1,2-butene moiety in an amount of less than 50 percent, and the amount of the 2,3-(cis)-butene moiety present is greater than that of the 2,3-(trans)butene moiety. 10. An isocyanate-reactive composition for use in the manufacture of a polyurethane elastomer, according to the process of Claim 7, which comprises: 5 a) from 90 to 99.9 weight percent based on total amounts by weight of (a) and (b), of a polyester or polyether polyol having an average hydroxyl equivalent weight of from 500 to 5000; and b) from 0.1 to 10 weight percent of a liquid polybutadiene which, based on its total butene content, comprises the 1 ,2-butene moiety in an amount of less 0 than 50 percent, and the amount of the 2,3-(cis)-butene moiety present is greater than that of the 2,3-(trans)butene moiety. 5 0 5

Inventors: MUSSINI STEFANO, MUSSINI, STEFANO
Applicants: DOW ITALIA, DOW ITALIA S.P.A.
Application year: 1996
Main classification: C08G18
IPC codes: C08G18