Blends of block copolymers and metallocene polyolefins

Abstract: The invention provides an elastomeric composition comprising i) one or more block copolymers having at least two monoalkenyl arene blocks separated by a saturated conjugated diene block and ii) a metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3.

Description: The present invention relates to block copolymer compositions containing a polyolefin. Extrudable elastomeric compositions which can be easily compression molded or melt blown are typically prepared by blending a styrenic block copolymer and a crystalline polyolefin. Such blends have been used to make a variety of products including automotive molding and elastic films. WO 94/18263 discloses an elastomeric film comprising a monoalkenyl arene-diene elastomeric block copolymer (preferably S-B-S: KRATON D 2104) and a metallocene polyolefin of ethylene and 7-35 mole% of a comonomer (e.g. octene). Styrene-poly(ethylene-butylene)-styrene elastomeric block copolymers and styrene-poly(ethylene-propylene)-styrene elastomeric block copolymers have been blended with other materials such as, for example, polyolefins and tackifying resins to form extrudable elastomeric compositions which can be more easily extruded into elastic sheets having improved processing and/or bonding properties. While the additives improve the extrusion properties of the compositions and the processing and/or bonding properties of the elastic sheet, such additives may, in certain situations, have an adverse affect on the elastic properties of the resulting sheet. For example, such elastomeric block copolymers blended with large amounts of a polyolefin and/or hydrocarbon resin may have poor stress relaxation properties and stress-strain tests of such materials show significant hysteresis. The present invention provides an elastomeric composition comprising i) one or more block copolymers having good elastomeric properties and ii) a metallocene polyolefin of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, having a density from 0.86 to 0.91 and a molecular weight distribution (Mw/Mn) less than 3. The polyolefin has a good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. WO 95/33006, which is Art 54(3) EPC art for Contracting States BE, DE, ES, FR, GB and IT, discloses a blend of a metallocene polyolefin and one block copolymer having at least two mono-alkenyl arene blocks separated by a saturated conjugated diene block. The present compositions suitably have a recoverable energy greater than 60%. Other compounds which the present compositions may include comprise crystalline polyolefins and tackifying resins. The metallocene polyolefins are polyolefins produced with a metallocene catalyst such as those described in United States Patents Nos. 5,322,728 and 5,272,236. Such metallocene polyolefins are available from Dow Chemical Company under the trademark AFFINITY or ENGAGE (ethylene/octene copolymers) and from Exxon Chemical Company under the trademark EXACT (ethylene/butene copolymers). The metallocene polyolefins have low crystallinity when ethylene is copolymerised with from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. Such polyolefins have a good distribution of ethylene and the comonomer (as further explained in the references). The block copolymers have at least two monoalkenyl arene blocks, preferably two polystyrene blocks, separated by a block of saturated conjugated diene comprising less than 20% residual ethylenic unsaturation, prefererably a saturated polybutadiene block. The preferred styrenic block copolymers have a linear structure although branched or radial polymers or functionalised block copolymers make useful compounds. Polystyrene-saturated polybutadiene-polystyrene (S-EB-S) and polystyrene-saturated polyisoprene-polystyrene (S-EP-S) block copolymers comprise polystyrene endblocks having a number average molecular weight from 5,000 to 35,000 and saturated polybutadiene or saturated polyisoprene midblocks having a number average molecular weight from 20,000 to 170,000. The saturated polybutadiene blocks preferably have from 35% to 55% 1,2-configuration and the saturated polyisoprene blocks preferably have greater than 85% 1,4-configuration. The total number average molecular weight of the styrenic block copolymer is preferably from 30,000 to 250,000 if the copolymer has a linear structure. Such block copolymers may have an average polystyrene content from 10% by weight to 35% by weight. A S-EB-S block copolymer useful in the present invention is available from the Shell Chemical Company and has a number average molecular weight of 50,000 with polystyrene endblocks each having a number average molecular weight of 7,200 and polystyrene content of 30% by weight. These polymers may be prepared using free-radical, cationic and anionic initiators or polymerisation catalysts. Such polymers may be prepared using bulk, solution or emulsion techniques. In any case, the polymer containing at least ethylenic unsaturation will, generally, be recovered as a solid such as a crumb, a powder, a pellet, or the like. In general, when solution anionic techniques are used, conjugated diolefin polymers and copolymers of conjugated diolefins and alkenyl aromatic hydrocarbons are prepared by contacting the monomer or monomers to be polymerised simultaneously or sequentially with an organoalkali metal compound in a suitable solvent at a temperature within the range from -150°C to 300°C, preferably at a temperature within the range from 0°C to 100°C. Particularly effective anionic polymerisation initiators are organolithium compounds having the general formula: RLi n wherein R is an aliphatic, cycloaliphatic, aromatic, or alkyl-substituted aromatic hydrocarbon radical having from 1 to 20 carbon atoms; and n is an integer of 1 to 4. In addition to sequential techniques to obtain triblocks, tetrablocks, and higher orders of repeating structures, at least anionic initiators can be used to prepare diblocks of styrene-polydiene having a reactive ("live") chain end on the diene block which can be reacted through a coupling agent to create, for example, (S-I) x Y or (S-B) x Y structures wherein x is an integer from 2 to 30, Y is a coupling agent, I is isoprene, B is butadiene and greater than 65 percent of S-I or S-B diblocks are chemically attached to the coupling agent. Y usually has a molecular weight which is low compared to the polymers being prepared and can be any of a number of materials known in the art, including halogenated organic compounds; halogenated alkyl silanes; alkoxy silanes; various esters such as alkyl and aryl benzoates, difunctional aliphatic esters such as dialkyl adipates and the like; polyfunctional agents such as divinyl benzene (DVB) and low molecular weight polymers of DVB. Depending on the selected coupling agent the final polymer can be a fully or partially coupled linear triblock polymer (x=2), i.e., SIYIS; or branched, radial or star configurations. The coupling agent, being of low molecular weight, does not materially affect the properties of the final polymer. DVB oligomer is commonly used to create star polymers, wherein the number of diene arms can be 7 to 20 or even higher. It is not required in coupled polymers that the diblock units all be identical. In fact, diverse "living" diblock units can be brought together during the coupling reaction giving a variety of unsymmetrical structures, i.e., the total diblock chain lengths can be different, as well as the sequential block lengths of styrene and diene. Since the number of S-EB or S-IB polymeric arms in a star polymer can be large, the number average molecular weights of star polymers within the invention can be much larger than those of linear S-EB-S or S-EP-S polymers, i.e., up to 500,000 or higher. Such higher molecular weight polymers have the viscosity of lower molecular weight linear polymers and thus are processable in spite of the high molecular weight. The blockcopolymers are hydrogenated to improve weatherability and oxidation stability. In general, the hydrogenation or selective hydrogenation of the polymer may be accomplished using any of the several hydrogenation processes known in the prior art. For example the hydrogenation may be accomplished using methods such as those taught, for example, in U.S. Patent Nos. 3,494,942; 3,634,594; 3,670,054; 3,700,633; and Re. 27,145. The methods known in the prior art and useful in the present invention for hydrogenating polymers containing ethylenic unsaturation and for hydrogenating or selectively hydrogenating polymers containing aromatic and ethylenic unsaturation, involve the use of a suitable catalyst, particularly a catalyst or catalyst precursor comprising an iron group metal atom, particularly nickel or cobalt, and a suitable reducing agent such as an aluminium alkyl. In general, the hydrogenation will be accomplished in a suitable solvent at a temperature within the range from 20°C to 100°C and at a hydrogen partial pressure within the range from 7 atm (10 5 Pa) to 340 atm (10 5 Pa), preferably 7 atm (10 5 Pa) to 70 atm (10 5 Pa). Catalyst concentrations within the range from 10 ppm (wt) to 500 ppm (wt) of iron group metal based on total solution are generally used and contacting at hydrogenation conditions is generally continued for a period of time within the range from 60 to 240 minutes. After the hydrogenation is completed, the hydrogenation catalyst and catalyst residue will, generally, be separated from the polymer. Various tackifying resins can be used in the present invention. In particular, the purpose of the tackifying resin is to provide an elastomeric web that can act as a pressure sensitive adhesive, e.g., to bond the elastomeric sheet to another web or layer of material. Of course, various tackifying resins are known, and are discussed, e.g., in U.S Patent Nos. 4,789,699; 4,294,936; and 3,783,072. Any tackifier resin can be used which is compatible with the elastomeric polymer and the polyolefin, and can withstand the high processing (e.g., extrusion) temperatures. Generally, hydrogenated hydrocarbon resins are preferred tackifying resins, because of their better temperature stability. The following paragraphs disclose information on three specific tackifying resins, two of which (REGALREZ and ARKON P series tackifiers (REGALREZ and ARKON are trademarks)) are examples of hydrogenated hydrocarbon resins, and the ZONATAC 501 lite being a terpene hydrocarbon (ZONATAC is a trademark). Of course, while the three tackifying resins are specifically discussed, the present invention is not limited to use of such three tackifying resins, and other tackifying resins which are compatible with the other components of the composition and can withstand the high processing temperatures, and can achieve the objectives of the present invention, can also be used. REGALREZ hydrocarbon resins, a product of Hercules, Incorporated, are fully hydrogenated α-methyl styrene-type low molecular weight hydrocarbon resins, produced by polymerisation and hydrogenation of pure monomer hydrocarbon feed stocks. Grades 1094, 3102, 6108, and 1126 are highly stable, light-colored low molecular weight, nonpolar resins suggested for use in plastics modification, adhesives, coatings, sealants, and caulks. The resins are compatible with a wide variety of oils, waxes, alkyds, plastics, and elastomers and are soluble in common organic solvents. ZONATAC 501 lite resin, a product of Arizona Chemical Co., has a softening point of 105°C, a Gardner colour (50% in heptane) of 1 and a Gardner colour neat (pure) of 2+; (a Gardner colour of 1(50% in heptane) is approximately equal to APHA colour = 70) a specific gravity (25°/25°C) of 1.02 and a flash point (closed cup,°C) of 250°C. Extending oils which may be used in the extrudable elastomeric composition should be capable of being melt-processed with the other components of the extrudable elastomeric composition without degrading. An exemplary extending oil is a white mineral oil available under the trade designation Drakeol 34 from the Pennzoil Company Pennreco Division. Drakeol 34 has a specific gravity of 0.864-.878 at 15°C, a flash point of 238°C, and viscosity of 370-420 SUS at 38°C. Suitable vegetable oils and animal oils or their derivatives may also be used as the extending oil. The additional components of the extrudable elastomeric composition can be utilized over broad ranges of the amounts of each components. As a guide, the best results for elastomeric films have been obtained when utilizing a five component extrudable elastomeric composition of an elastomeric block copolymer, a metallocene polyolefin, a crystaline polyolefin, a tackifying resin, and an extending oil. The following ranges, as shown in Table 1, are exemplary. It is emphasized that these ranges are merely illustrative, serving as a guide for amounts of the various components in the composition. Weight % Elastomeric block copolymer, e.g S-EB-S or S-EP-S 25-70 Metallocene Polyolefin 15-60 Tackifier 15-28 Crystalline Polyolefin 0-25 Extending Oil 0-15 The present invention, therefore, also relates to an elastomeric composition comprising i) from 25% to 70% by weight of a block copolymer having at least two monoalkenyl arene blocks separated by a hydrogenated conjugated diene block, ii) from 15% to 60% by weight of the polymer components of an elastomeric polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, and good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, iii)from 0% to 25% by weight of a crystalline polyolefin, and iv) from 15% to 28% by weight of a tackifying resin. Preferably, the present composition comprises in addition an extending oil. While the extrudable elastomeric composition used to form the elastic film has been discussed in terms of a five-component extrudable composition (see Table 1), the crystalline polyolefin, which functions as a flow-promoter for the composition can be substituetd by other compatible flow promoters or processing aids, or can be eliminated altogether where the tackifying resin can also act as the flow promoter and/or extending oil. The extending oil, which functions as a processing aid, may also be substituted by other compatible processing aids or can be eliminated altogether where the tackifying resin can also act as the extending oil. For example, low molecular weight hydrocarbon resins such as REGALREZ tackifier can also act as the viscosity reducer and/or the extending oil, whereby the extrudable composition may contain the elastomeric polymer(s) and the tackifying resin (e.g. REGALREZ tackifier). While the principal components of the extrudable elastomeric composition used to form the elastic sheet have been described in the foregoing, such extrudable elastomeric composition is not limited thereto, and can include other components not adversely affecting the extrudable elastomeric composition attaining the stated objectives. Exemplary materials which could be used as additional components would include, without limitation, pigments, antioxidants, stabilizers, surfactants, waxes, flow promoters, solvents, particulates, and materials added to enhance processability and pellet handling of the composition. A suitable extrudable elastomeric composition of the present invention comprises 90 parts by weight of a linear styrenic block coplymer having two monoalkenyl arene blocks separated by a saturated conjugated diene block and from 10 to 70 parts by weight of a metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, and a good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. Such blends have a surprising balance of elasticity, tensile strength, tensile set at break, and solvent resistance in comparison to conventional blends of styrenic block copolymer and conventional polyolefins. Extrudable elastic compositions were prepared by blending varying amounts of styrenic block copolymers, available from the Shell Chemical Company, with a metallocene polyolefin available from Dow Chemical Company or Exxon Chemical Company. Additional components when used include a crystalline polyolefin (Petrothene NA 601 polyethylene), a tackifying resin (REGALREZ 1126 hydrocarbon resin), and an extending oil (Drakeol 34 white mineral oil). The term "elastic" is used herein to mean any material which, upon application of a biasing force, is stretchable, that is, elongatable at least 60 percent (i.e., to a stretched, biased length which is at least 160 percent of its relaxed unbiased length) and which, will recover at least 55 percent of its elongation upon release of the stretching, elongating force. A hypothetical example would be a 2.54 cm sample of a material which is elongatable to at least 4.1 cm and which, upon being elongated to 4.06 cm and released, will recover to a length of not more than 3.23 cm. Many elastic materials may be elongated by much more than 60 percent (i.e., much more than 160 percent of their relaxed length), for example, elongated 100 percent or more, and many of these will recover to substantially their initial relaxed length, for example, to within 105 percent of their initial relaxed length, upon release of the stretching force. As used herein, the terms "recover" and "recovery" refer to a contraction of a stretched material upon termination of a biasing force following stretching of the material by application of the biasing force. For example, if a material having a relaxed, unbiased length of 2.54 cm is elongated 50 percent by stretching to a length of one and 3.81 cm the material would be elongated 50 percent 1.27 cm and would have a stretched length that is 150 percent of its relaxed length. If this exemplary stretched material contracted, that is recovered to a length of one and 2.79 cm after release of the biasing and stretching force, the material would have recovered 80 percent (1.02 cm) of its 1.27 cm elongation. Recovery may be expressed as [(maximum stretch length - final sample length)/(maximum stretch length - initial sample length)] X 100. As used herein, the term "stress relaxation" refers to the percent loss of tension or load between the maximum load or force encountered after elongating an elastic material at a specified rate of extension to a predetermined length (or the load or force measured at some initial length) and the remaining load or force measured after the sample has been held at that length for a specified period of time, for example, from 0 minutes to 30 minutes. Except where otherwise noted for the present invention, stress relaxation is expressed as a percentage loss of the initial load encountered at a specified extension of an elastic material. The stress relaxation is determined by calculating the difference between the initial maximum load measured after elongating an elastic material at a rate of 50.8 cm per minute to an elongation of 160 percent (i.e., to 260 percent of the material's initial length) and the remaining load measured after that sample was held at that length for 30 minutes divided by the initial maximum load at that length. Testing may be performed on an Instron Model 1122 Universal Test Machine using a 100 mm by 7.62 cm sample attached to jaw faces that have a width of 7.62 cm and a height of 2.54 cm. Stress relaxation after 30 minutes at, for example, an elongation of 160 percent (i.e., to 260 percent of the material's initial length - from 100 mm to 260 mm) may be expressed as a percentage utilizing the following equation: stress relaxation = (peak load 160% - load 160% @30 min)/(peak load 160% )*100. As used herein, the term "tensile strength" refers to the resistance of an elastic material to being elongated as determined in accordance with ASTM D-412 using 3mm wide and 0.15 cm thick dumbbell samples that are cut from films. Films formed from a blend of an elastomeric block copolymer and other materials such as, for example, a polyolefin (metallocene and/or crystalline), a tackifier, and/or an extending oil were compression molded. Tensile testing may be performed on an Instron Model 1122 Universal Test Machine. An alternative tensile test specimen is a 100 mm by 7.62 cm sample attached to jaw faces that have a width of 7.62 cm and a height of 2.54 cm. As used herein, the term "recoverable energy" refers to the energy stored by an elastic material when it is elongated to a specified length. Recoverable energy is measured utilizing a tensile testing apparatus such as, for example, an Instron Model 1122 Universal Test Machine by elongating a sample of an elastic material sample at 2.54 cm/minute to 150 percent elongation (i.e., to 250 percent of the material's initial relaxed length) and cycling back to zero load for 1 hysteresis loop. The percent recoverable energy is determined by dividing the area under the retraction curve of the first hysteresis loop by the area under the elongation curve of the first hysteresis loop and then multiplying by 100. As used herein, the term "loss" refers to the decrease in resistance to elongation of an elastic material after that elastic material has been elongated to a specified length and then allowed to recover. The loss is measured utilizing a tensile testing apparatus such as, for example, an Instron Model 1122 Universal Test Machine by elongating a sample of an elastic material sample at 2.54cm/minute to 150 percent elongation (i.e., to 250 percent of the material's initial relaxed length), cycling back to zero load for 1 hysteresis loop and then elongating the material again at 2.54 cm/minute to 150 percent elongation. The percent loss is determined by dividing the area under the elongation curve of the second hysteresis loop by the area under the elongation curve of the first hysteresis loop, subtracting that value from one (1), and then multiplying by 100. As used herein, the terms "set" or "percent set" refer to the deformation of an elastic material measured while the material is in a relaxed condition immediately after the material was released from a specified elongation, without allowing the material to snap back. The percent set is determined by dividing the zero load extension after 1 cycle by the initial sample gauge length, and then multiplying by 100. The zero load extension is the distance that the jaws of the tensile test equipment move at the beginning of the second cycle before a load is registered by the tensile test equipment. The set may be measured utilizing a tensile testing apparatus such as, for example, an Instron Model 1122 Universal Test Machine by elongating a sample of an elastic material at 2.54 cm/minute to 150 percent elongation and cycling back to zero load for 1 hysteresis loop. As used herein, the term "set at break" refers to the deformation of an elastic material measured after the material has been elongated to break. The set at break is measured in accordance with ASTM D 412 in which, ten minutes after the sample is broken, the two pieces of the sample are fitted together so they substantially match up over the full area of the break. The percent set at break is determined by subtracting the original distance between the bench marks from the distance between the joined pieces, dividing by the original distance between the bench marks and then multiplying by 100. As used herein, the "number average molecular weight" was determined utilizing conventional gel permeation chromatography techniques with a polystyrene standard. All molecular weights are measured prior to hydrogenation which will increase them by a small amount. The present invention further relates to an elastomeric composition which comprises more than one block copolymer. Accordingly, the present invention also relates to an elastomeric composition which comprises a mixture of a high molecular weight styrenic block copolymer, a low molecular weight styrenic block copolymer, and a metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, and good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. Such compositions are improved extension blowing compositions. Compositions having from 10% to 30% by weight of the metallocene polyolefin have improved elasticity while maintaining excellent properties for film extrusion processes. Such an extrudable composition suitably comprises i) from 20% to 35% by weight of a first hydrogenated block copolymer having a high molecular weight, ii) from 8% to 33% by weight of a second hydrogenated block copolymer having a low molecular weight, wherein the ratio of the molecular weight of the first hydrogenated block copolymer to the molecular weight of the second hydrogenated block copolymer is greater than 1.1:1, iii) from 10% to 30% by weight of a metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, and good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, iv) from 10% to 30% by weight of a non-aromatic processing oil, and v) from 5% to 15% by weight of a polymer which is compatible with the hydrogenated block copolymers. The first hydrogenated block copolymer comprises at least two blocks A which are predominantly polymerised alkenyl arene, and at least one block B which is predominantly polymerised conjugated diene, wherein the first hydrogenated block copolymer comprises from 1 to 60 percent by weight polymerised alkenyl arene, a number average molecular weight within the range of 55,000 to 200,000, preferably between 60,000 and 110,000, and less than 20% residual ethylenic unsaturation in the conjugated diene block. The second hydrogenated block copolymer comprises at least two blocks A which are predominantly polymerised alkenyl arene, and at least one block B which is predominantly polymerised conjugated diene, wherein the second hydrogenated block copolymer comprises from 1 to 60 percent by weight polymerized alkenyl arene, a number average molecular weight within the range of 15,000 to 85,000, preferably between 30,000 and 60,000, and less than 20% residual ethylenic unsaturation of the conjugated diene block. The elastomeric films which can be produced from the above compositions are films of 0.0025 to 0.0125 cm in thickness and are preferably produced by extrusion casting or extrusion blowing the composition described above using extrusion equipment, conditions, and techniques known in the art. The process for producing an elastomeric film of this invention comprises the steps of providing a polymeric composition as described above; extruding the polymeric composition through a die, the die having a gap greater than 0.0125 cm and less than 0.305 cm; expanding the extruded film to a thickness of between 0.00125 cm and 0.0254 cm by application of differential pressure by a gas; and rapidly cooling the expanded extruded film. The hydrogenated block copolymers have at least two alkenyl arene polymer blocks A, which may be selected independently and at least one elastomeric conjugated diene polymer block B. A preferred structure of the block copolymer is (A-B) n -A where n is an integer of 1 to 20. Blocks A and B may be either homopolymer, random or tapered copolymer blocks as long as each block is predominantly the class of the monomer characterizing the block. For example, the block copolymer may contain A blocks which are styrene/alpha-methylstyrene copolymer blocks or styrene/butadiene random or tapered copolymer blocks as long as the blocks individually predominate in alkenyl arenes. The A blocks are preferably monoalkenyl arene homopolymer blocks. The term "monoalkenyl arene" will be taken to include particularly those of the benzene series such as styrene and its analogs and homologs including o-methylstyrene, p-methylstyrene, p-tert-butylstyrene, 1,3-dimethylstyrene, alpha-methylstyrene and other ring alkylated styrenes, particularly ring-methylated styrenes, and other monoalkenyl polycyclic aromatic compounds such as vinyl naphthalene, vinyl anthracene and the like. The preferred monoalkenyl arenes are monovinyl monocyclic arenes such as styrene and alpha-methylstyrene, and styrene is particularly preferred. By predominantly being the class of the monomer characterizing the block, it is meant that more than 75% by weight of the A blocks are alkenyl arene monomer units, and more than 75% by weight of the B blocks are conjugated diene monomer units. The blocks B may comprise homopolymers of conjugated diene monomers, copolymers of two or more conjugated dienes, and copolymers of one or more of the dienes with a monoalkenyl arene as long as the blocks B are predominantly conjugated diene units. The conjugated dienes preferably contain from 4 to 8 carbon atoms. Examples of such suitable conjugated diene monomers include: 1, 3-butadiene (butadiene), 2-methyl-1,3-butadiene (isoprene), 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene (piperylene), 1,3-hexadiene, and the like. Preferably, the block copolymers of conjugated dienes and alkenyl arene hydrocarbons which may be utilized include those butadiene derived elastomers which have 1,2-microstructure contents prior to hydrogenation of from 7 to 100 percent, more preferably from 25 to 65 percent, and most preferably from 35 to 55 percent. The proportion of the copolymer which is alkenyl arene monomer units is between 1 and 60 percent by weight of the block copolymer, preferably between 5 and 50 percent, more preferably between 15 and 45 percent by weight and most preferably between 20 and 40 percent by weight. The block copolymers may be produced by any block polymerisation or copolymerisation procedures including the well known sequential addition of monomer technique, incremental addition of monomer technique or coupling technique as illustrated in, for example, U.S. Patent Nos. 3,251,905; 3,390,207; 3,598,887 and 4,219,627. As is well known in the block copolymer art, tapered copolymer blocks can be incorporated in the multiblock copolymer by copolymerising a mixture of conjugated diene and alkenyl arene monomers utilizing the difference in their copolymerisation reactivity rates. Various patents describe the preparation of multiblock copolymers containing tapered copolymer blocks including U.S. Patent Nos. 3,251,905; 3,265,765; 3,639,521 and 4,208,356. It should be observed that the above-described polymers and copolymers may, if desired, be readily prepared by the methods set forth above. However, since many of these polymers and copolymers are commercially available, it is usually preferred to employ the commercially available polymer as this serves to reduce the number of processing steps involved in the overall process. The second block copolymer of the present invention has a lower molecular weight than the first, and has been found to lower the melt temperatures and improve processability of the composition. But as opposed to other methods of lowering the melt temperatures, adding a lower molecular weight block copolymer was found to be significantly less detrimental to film forming ability. The non-aromatic processing oil component of the invention composition preferably contains less than about 10% by weight aromatics as determined by clay-gel analysis. Acceptable softening oils are also referred to in the industry as softening oils, mineral oils, and extender oils. These oils are commonly incorporated in rubber compositions to decrease the cost of the composition and to lower the modulus of the composition. Non-aromatic processing oils of the present invention will preferably have a flash temperature between 170°C and 300°C. Synthetic extender oils, such as low molecular weight liquid polybutadiene, may also be used as the non-aromatic processing oil. The amount of non-aromatic processing oil required is preferably between 10% and 30% by weight and most preferably between 15% and 25% by weight of the composition. The elastic film compositions of the present invention may be manufactured using polymer blending techniques currently practiced in the art, such as batch and continuous mixing methods employing mixing equipment like Banbury batch mixers, Farrell continuous mixers and twin-screw extruders. Well mixed compositions are obtainable when mixing is carried out at a melt temperature in the range between 200 to about 230°C. Films extruded with inadequately mixed compositions usually would show a high intensity of gels or a fish eye appearance as well as a tendency to block. Extrusion blown films may be prepared from the compositions of this invention using standard extrusion equipment, standard techniques and typical conditions. Standard techniques include, but are not limited to extrusion blown and extrusion casting processes. For the extrusion blown process, a polyolefin type extruder screw is preferred, but other designs are also acceptable. A die gap of 0.0127 to 0.305 cm is acceptable, a gap of 0.0254 to 0.203 cm is preferred, and a gap of 0.051 to 0.102 cm is most preferred. Die temperatures of 200°C to 230°C are acceptable and between 204°C and 226°C are preferred. A blow up ratio of 2 to 1 is preferred. Rapid cooling of the extruder blown film is preferably performed by a dual lip cooling ring. Due to the low modulus of the film produced from the composition of this invention, a rollered collapsing frame is preferred to avoid bubble chatter. A film which is extrusion blown from the composition of this invention is between 0.00127 cm and 0.0254 cm in thickness, and is preferably between 0.0254 and 0.0152 in thickness and is most preferably between 0.00254 and 0.0127 cm in thickness. The composition of this invention may be formed to a film with a low modulus, and excellent tensile strength and high ultimate elongation in both machine and transverse directions, low permanent set and high recoverable energy. This composition is also made of less expensive components than alternative elastomeric film compositions. Films having 100% modulus of less than 13.6 atm (10 5 Pa) in both the machine and transverse directions are obtainable with the composition of this invention. Films made from the composition of this invention have recoverable energy of greater than about 70% and permanent set less than 12% Comparative Examples A and B In Comparative Example A, the S-EB-S elastomer described above was compounded in a preferred formulation for making elastomeric films wherein the formulation contained 63% by weight of the S-EB-S elastomer, 20% by weight of a polyethylene resin, and 17% by weight of a tackifying resin. Comparative Examples B demonstrates complete replacement of the S-EB-S elastomer with Dow's ENGAGE EG 8100 elastomer (ENGAGE is trademark), an elastomeric polyolefin having a molecular weight distribution less than 3, good dispersion of 76% by weight of ethylene and 24% by weight of octene, and a density of 0.87. Example 1-3 Examples 1, 2, and 3 represent replacement of the crystalline polyolefin in Comparative Example A with a metallocene polyolefin having a molecular weight distribution less than 3, a good dispersion of ethylene and an α-olefin comonomer having from 4 to 8 carbon atoms, and a density from 0.86 to 0.91. The weight % of each component for Comparative Examples A and B and Examples 1-3 is shown in Table 2. Extrudable compositions for each Example were pressed from pellets into films using heat and pressure according to conventional compression molding techniques. The films were cut into dumbbell shaped samples that were 3mm wide and 0.15 cm thick. The stress-strain properties of the pressed films were determined in accordance with ASTM D-412 utilizing a Constant Rate of Extension Tester, Instron Model 1122 Universal Testing Instrument. Each sample was placed lengthwise in jaw faces, 7.62 cm wide x 2.54 cm height, with a jaw span or separation of 5.08 cm. The Instron Model 1122 Universal Test Instrument crosshead speed was set at 25.4 cm per minute for the first series of tests measuring the Stress-Strain properties reported in Table 3. Measurements were taken of the sample's tensile strength, elongation at break, set, and modulus or load at 100% elongation (i.e., at 200% of the materials initial relaxed length) and 300% elongation (i.e., at 400% of the materials initial relaxed length). Hysteresis properties were measured using the Instron Model 1122 Universal Test Machine with the crosshead speed set at 2.54 cm per minute. The loss, dynamic, recoverable energy and set were determined as previously described in the "Definition" section and are reported in Table 3. The results show that Comparative Example B has significantly reduced recoverable energy and is thus has poor elastomeric properties in comparison to Comparative Example A. Examples 1-3 have improved tensile strength and improved recoverable energy in comparison to Comparative Example A. Example A B 1 2 3 S-EB-S block copolymer 63 63 63 63 Metallocene polyolefin 1 63 20 2 20 3 20 Crystalline Polyolefin 20 20 Tackifying resin 17 17 17 17 17 Example A B 1 2 3 Melt flow, g/10' 190C/2.16 Kg 16 4.2 4.9 5.9 5 Stress-strain Properties: (25.4 cm/min crosshead speed) 100% modulus, atm (10 5 Pa) 12.9 24.4 7.2 12.3 12.3 300% modulus, atm (10 5 Pa) 18.7 35.5 16.0 22.5 22.5 500% modulus, atm (10 5 Pa) 28.6 49.0 25.9 38.8 38.1 Tensile strength, atm (10 5 Pa) 94.0 105.5 96.0 117.1 122.6 Elongation at break, % 58.6 58.0 61.3 59.2 59.9 Hysteresis Properties: (Loop 1, 2.54 cm/min crosshead speed) Recovery energy, % 66 47 78 74 75 Hysteresis set, % 14 23 11 14 14 Unloading stress, @ 100% elongation, atm (10 5 Pa) First loading 9.1 12.4 8.5 9.5 9.5 Second loading 8.8 12.1 8.2 9.2 9.2 Examples 4 and 5 Examples 4 and 5 represent replacement of a portion of the block copolymer in Comparative Example A with a metallocene polyolefin having a molecular weight distribution less than 3, a good dispersion of ethylene and an α-olefin comonomer having from 4 to 8 carbon atoms, and a density from 0.86 to 0.91. The weight % of each component for Comparative Example A and Examples 4 and 5 is shown in Table 4. Extrudable compositions for each Example were used to compression mold films as described for Comparative Example A. The sample were tested for properties as described for Comparative Example A and the results are shown in Table 5. In addition, stress relaxation was measured for Examples 4 and 5 and Comparative Example A using the Instron Model 1122 Universal Test Machine and determined as previously described. The results are reported in Table 5. The compositions of Examples 4 and 5 have improved modulus and stress relaxation in comparison to Comparative Example A. Examples 6, C and D A blend of 90 parts by weight of styrenic block copolymer and 10 parts by weight of a metallocene polyolefin were dissolved in toluene at 90°C and coagulated with 3 volumes of methanol, then dried in a vacuum oven. The block copolymer was an S-EB-S block copolymer having number average molecular weights of 7,200 for the polystyrene blocks and 35,300 for the saturated butadiene blocks and having 40% 1,2-addition. The metallocene polyolefin was EXACT 4011 polymer (available from Exxon Chemical) which is a copolymer of ethylene and 17% by weight of 1-butene. Example A 4 5 S-EB-S block copolymer 63 41.5 41.5 Metallocene polyolefin 1 41.5 2 41.5 Tackifying resin 17 17 17 Crystalline Polyolefin 20 0 0 Example A 4 5 Melt flow, 190C/2.16 KG 16 2.3 27 Hysteresis Recoverable energy, % 67 67 63 Stress @150 % extension 198 225 247 Hysteresis set, % 14 15 16 Unloading stress, atm (10 5 Pa) Cycle 1 9.1 9.9 10.4 Cycle 2 8.8 9.7 10.1 Tensile properties Tensile strength, atm (10 5 Pa) 94.0 97.9 89.0 Ultimate elongation, % 64.7 66.1 77.6 100 % modulus, atm (10 5 Pa) 12.9 13.3 15.1 300 % modulus, atm (10 5 Pa) 18.7 21.8 23.2 500 % modulus, atm (10 5 Pa) 28.6 36.2 33.4 Stress relaxation, % (after 30 min at 160% elongation and at 50.8 cm/min crosshead speed) 34 30 32 Compression molded films were then prepared at 140°C and 0.05 cm thickness of the blend and the components and measured for comparison properties as shown in Table 6. Example 6 C D Components, parts by weight S-EB-S Block Copolymer 90 90 0 Metallocene Polyolefin 10 0 10 Tensile properties Tensile strength, atm (10 5 Pa) 456.3 347.3 422.2 Elongation @ Break, % 810 720 1060 Tensile Set @ Break 0 50 400 As shown in Table 6, the blend had greater tensile strength and lower tensile set than either of the components. Examples 7-10, C, E Blends of 90 parts by weight of a styrenic block copolymer and various amounts of a metallocene polyolefin were dissolved in toluene at 90°C and coagulated with 3 volumes of methanol, then dried in a vacuum oven. The block copolymer was an S-EB-S block copolymer having number average molecular weights of 7,200 for the polystyrene blocks and 35,300 for the saturated butadiene blocks and having 40% 1,2-addition. The metallocene polyolefin was ENGAGE 8100 polymer (available from Dow Chemical) which is a copolymer of ethylene and 24% by weight of 1-octene and has a density of 0.87. Compression molded films were then prepared at 140°C and 0.05cm thickness of the blend and the components and measured for comparison properties as shown in Tables 7 and 8. Example C 7 8 Components, parts by weight S-EB-S Block Copolymer 90 90 90 Metallocene Polyolefin 0 60 135 Tensile properties Tensile strength, atm (10 5 Pa) 347.3 333.7 252.0 Elongation @ Break, % 720 850 870 Tensile Set @ Break 50 75 100 Example 9 10 E Components, parts by weight S-EB-S Block Copolymer 90 90 0 Metallocene Polyolefin 270 810 10 Tensile properties Tensile strength, atm (10 5 Pa) 204.3 136.2 204.3 Elongation @ Break, % 920 910 1090 Tensile Set @ Break 100 150 200 Examples 11 and D A blend of 90 parts by weigh of a styrenic block copolymer and a metallocene polyolefin were dissolved in toluene at 90°C and coagulated with 3 volumes of methanol, then dried in a vacuum oven. The block copolymer was an S-EB-S block copolymer having number average molecular weights of 19,000 for the polystyrene blocks and 88,000 for the saturated butadiene blocks and having 40% 1,2-addition. The metallocene polyolefin was EXACT 4011 polymer (available from Exxon Chemical) which is a copolymer of ethylene and 17% by wieght of 1-butene. Compression molded films were then prepared at 140°C and 0.05 cm thickness of the blend and the components and measured for comparison properties as shown in Table 9. Example D 11 Components, parts by weight Styrenic Block Copolymer 0 90 Metallocene Polyolefin 10 60 Tensile properties Tensile strength, atm (10 5 Pa) 422.2 408.6 Elongation @ Break, % 1060 890 Tensile Set @ Break 400 75 EXAMPLES 12, 13 and F The low molecular weight hydrogenated block copolymer used in the following examples was a hydrogenated styrene-butadiene-styrene block copolymer with a total molecular weight of 49700 as measured by GPC with a polystyrene standard and 30% by weight polystyrene endblocks. The 1,2-microstructure content of the midblock segment prior to hydrogenation is 40%. Hydrogenation had saturated more than 95% of the original midblock ethylenic unsaturation. The high molecular weight block copolymer was also a hydrogenated styrene-butadiene styrene block copolymer. The high molecular weight block copolymer had 32% by weight of polystyrene endblocks and a total molecular weight of 68000 measured by GPC with a polystyrene standard. The 1,2-microstructure content of the midblock segment prior to hydrogenation was 40%, and hydrogenation had saturated more than 95% of the original midblock ethylenic unsaturation. The metallocene polyolefin was XU-58320, an experimental copolymer of ethylene and 1-octene, manufactured by Dow Chemical Co. The metallocene polyolefin has a density from 0.86 to 0.91, a molecular weight distribution less than 3, and good distribution of ethylene and from 8% to 30% by weight of the octene. The endblock compatible resin employed was a high-softening-point pure monomer hydrocarbon resin derived from a styrene monomer, Piccolastic D125. This resin was manufactured by Hercules Inc. The resin has a ring ball softening point of 125°C and a melt viscosity of 100 poises (10 -1 Pa.s) at 185°C. A non-aromatic processing oil, Penreco 4434 oil, manufactured by Pennzoil Company was employed. The processing oil exhibits the following typical properties: viscosity by ASTM D-445 at 38°C of 370 to 410 SUS; specific gravity of 0.864 to 0.878 at 15°C; and flash point by ASTM D-92 of about 238°C. Additives are included in the following examples and comparative examples include a heat stabilizer, an antiblocking agent and a slip agent to improve stability of the composition and limit the blocking tendency of the blown films. The melt index of the blend compositions was determined according to ASTM Method D-1238, condition E. Tests were conducted using a 2.4 kilogram plunger weight and measurements were carried out at 190°C. The ultimate tensile strength and elongation were determined according to ASTM D-882-81 method using an Instron Model 1122 tester. The properties of the film were measured in the direction of extrusion of the film (machine direction, MD); and in the direction perpendicular to the direction of extrusion (cross-machine direction, CD). To determine permanent set, a specimen was prepared according to ASTM D-882-81. Test specimens were cut along the direction of extrusion of the film (MD). An Instron Model 1122 tester was used to subject the specimens to maximum extension of 150% strain and then relaxation at the same rate as the extension until the specimen was in the relaxed state (near zero force). Subsequently another loading cycle was imposed. The length at which the specimen reaches its relaxed state in the unloading cycle was measured and the permanent set was then calculated according to the following equation: Perm. set=100% x (length at relaxed state - original length) (length at max extension - original length) The recoverable energy is the ratio of the energy released during the unloading cycle to the energy stored during the loading cycle. Examples 12 and 13 and Comparative Example F were prepared by mixing the hydrogenated block copolymers with other ingredients as shown in Table 10 with a twin-screw extruder (diameter=2.03 cm, screw length to diameter ratio, L/d, of 20:1). The elastic films were obtained by a cast film process using a 1.9 cm diameter single screw Brabender extruder equipped with a 30.5 cm width slit die and 0.05 cm die gap. Thin gage (0.005-0.0127 cm) films were obtained at 200C melt temperatures. Examples 12 and 13 were prepared by adding 25 and 33 parts per hundred parts of hydrogenated block copolymers, respectively, of metallocene polyolefin in the composition, whereas no metallocene polyolefin was added in the composition of Comparative Example F. The films produced by addition of metallocene polyolefin show good elastic recovery and mechanical properties, as is indicated by the properties included in Table 10. Examples Comparative Ex. 12 13 F Composition, Part Weight High Mw Block Copolymer 60 60 60 Low Mw Block Copolymer 40 40 40 Metallocene Polyolefin 25 33 Piccolastic D125 20 20 20 Process oil, Penreco 4434 45 45 45 Additive package 1.5 1.5 1.5 Film Casting Melt temperature, °C 200 200 200 Film Thickness, mils 5 5 5 Physical Properties Melt index, gm/10min 1.8 2.2 1.8 Tensile Strength, atm (10 5 Pa) Machine direction 122.6 110.3 177.1 Transverse direction 115.8 95.3 173.0 Ultimate elongation, % Machine direction 920 850 930 Transverse direction 840 790 910 100% modules, atm (10 5 Pa) Machine direction 10.2 12.3 15.7 Transverse direction 8.9 8.9 7.5 300% modules, atm (10 5 Pa) Machine direction 18.4 21.1 26.6 Transverse direction 15.7 15.0 12.9 After 150 % extension cyclic test, MD, Permanent set, % 11 12 10 Recoverable energy, % 72 70 68

Claims: Claims for the following Contracting States : BE, DE, ES, FR, GB, IT An elastomeric composition comprising a first hydrogenated block copolymer, a second hydrogenated block copolymer and a metallocene polyolefin of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, having a density from 0.86 to 0.91 and a molecular weight distribution (Mw/Mn) of less than 3, wherein both the first and second hydrogenated block copolymers comprise at least two blocks A which are predominantly polymerised monoalkenyl arene and at least one block B which is predominantly polymerised conjugated diene, and comprise less than 20% residual ethylenic unsaturation in the conjugated diene block, wherein the ratio of the number average molecular weight of the first hydrogenated block copolymer to the number average molecular weight of the second hydrogenated block copolymer is greater than 1.1:1. The composition according to claim 1, comprising one block copolymer which has the structure S-EB-S. The composition according to claim 1 or 2, wherein the comonomer in the metallocene polyolefin is octene. A composition according to any one of claims 1 to 3 comprising i) 90 parts by weight of the block copolymers having at least two monoalkenyl arene blocks separated by a saturated conjugated diene block and ii) from 10 to 70 parts by weight of the polymer components of the metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3. An elastomeric composition comprising i) from 25% to 70% by weight of a block copolymer having at least two monoalkenyl arene blocks separated by a hydrogenated conjugated diene block comprising less than 20% residual ethylenic unsaturation; ii) from 15% to 60% by weight of a metallocene polyolefin of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, having a density from 0.86 to 0.91 and a molecular weight distribution (Mw/Mn) less than 3; iii) from 0% to 25% by weight of a crystalline polyolefin; and iv) from 15% to 28% by weight of a tackifying resin. The composition according to any one of claims 1 to 3 comprising i) from 20% to 35% by weight of a first hydrogenated block copolymer comprising at least two blocks A which are predominantly polymerised alkenyl arene and at least one block B which is predominantly polymerized conjugated diene, the first hydrogenated block copolymer comprising from 1 to 60 percent by weight of polymerised monoalkenyl arene, having a number average molecular weight within the range of 55,000 to 200,000, and comprising less than 20% residual ethylenic unsaturation in the conjugated diene block; ii) from 8% to 33% by weight of a second hydrogenated block copolymer comprising at least two blocks A which are predominantly polymerised monoalkenyl arene and at least one block B which is predominantly polymerized conjugated diene, the second hydrogenated block copolymer comprising from 1 to 60 percent by weight of polymerised monoalkenyl arene, having a number average molecular weight within the range of 15,000 to 85,000, and comprising less than 20% residual ethylenic unsaturation of the conjugated diene block, wherein the ratio of the number average molecular weight of the first hydrogenated block copolymer to the number average molecular weight of the second hydrogenated block copolymer is greater than 1.1:1; iii)from 10% to 30% by weight of the metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, iv) from 10% to 30% by weight of a non-aromatic processing oil, and v) from 5% to 15% by weight of a polymer which is compatible with the hydrogenated block copolymers. The composition according to claim 6 wherein the number average molecular weight of the first hydrogenated block copolymer is between 60,000 and 110,000. The composition according to claim 6 or 7 wherein the number average molecular weight of the second hydrogenated block copolymer is between 30,000 and 60,000. The composition according to any one of claims 1 to 6, which further comprises an extending oil. A composition according to any one of claims 1 to 9 wherein the metallocene polyolefin has a good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. A process for producing an elastomeric film comprising the steps of providing a composition as described in any one of the preceding claims or an elastomeric composition comprising i) one block copolymer having at least two monoalkenyl arene blocks separated by a saturated conjugated diene block comprising less than 20% residual ethylenic unsaturation and ii) a metallocene polyolefin of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, having a density from 0.86 to 0.91 and a molecular weight distribution (Mw/Mn) less than 3; extruding the composition through a die, the die having a gap greater than 0.0125 cm and less than 0.305 cm; expanding the extruded film to a thickness of between 0.00125 cm and 0.0254 cm by application of differential pressure by a gas; and rapidly cooling the expanded extruded film. A film comprising the composition according to any one of claims 1 to 10. Claims for the following Contracting State : NL An elastomeric composition comprising i) one or more block copolymers having at least two monoalkenyl arene blocks separated by a saturated conjugated diene block comprising less than 20% residual ethylenic unsaturation and ii) a metallocene polyolefin of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms, having a density from 0.86 to 0.91 and a molecular weight distribution (Mw/Mn) less than 3. The composition according to claim 1, comprising one block copolymer which has the structure S-EB-S. The composition according to claim 1 or 2, wherein the comonomer in the metallocene polyolefin is octene. A composition according to any one of claims 1 to 3 comprising i) 90 parts by weight of the block copolymer having at least two monoalkenyl arene blocks separated by a saturated conjugated diene block and ii) from 10 to 70 parts by weight of the polymer components of the metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3. The composition according to any one of claims 1 to 3 comprising i) from 25% to 70% by weight of the block copolymer having at least two monoalkenyl arene blocks separated by a hydrogenated conjugated diene block; ii) from 15% to 60% by weight of the polymer components of the elastomeric metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3; iii)from 0% to 25% by weight of a crystalline polyolefin; and iv) from 15% to 28% by weight of a tackifying resin. The composition according to any one of claims 1 to 3 comprising more than one block copolymer. The composition according to claim 6 comprising i) from 20% to 35% by weight of a first hydrogenated block copolymer comprising at least two blocks A which are predominantly polymerised monoalkenyl arene and at least one block B which is predominantly polymerized conjugated diene the first hydrogenated block copolymer comprising from 1 to 60 percent by weight of polymerised monoalkenyl arene, having a number average molecular weight within the range of 55,000 to 200,000, and comprising less than 20% residual ethylenic unsaturation in the conjugated diene block; ii) from 8% to 33% by weight of a second hydrogenated block copolymer comprising at least two blocks A which are predominantly polymerised monoalkenyl arene and at least one block B which is predominantly polymerized conjugated diene, the second hydrogenated block copolymer comprising from 1 to 60 percent by weight of polymerised monoalkenyl arene, having a number average molecular weight within the range of 15,000 to 85,000, and comprising less than 20% residual ethylenic unsaturation in the conjugated diene block, wherein the ratio of the molecular weight of the first hydrogenated block copolymer to the molecular weight of the second hydrogenated block copolymer is greater than 1.1:1; iii) from 10% to 30% by weight of the metallocene polyolefin having a density from 0.86 to 0.91, a molecular weight distribution less than 3, iv) from 10% to 30% by weight of a non-aromatic processing oil, and v) from 5% to 15% by weight of a polymer which is compatible with the hydrogenated block copolymers. The composition according to claim 6 or 7 wherein the number average molecular weight of the first hydrogenated block copolymer is between 60,000 and 110,000. The composition according to any one of claims 6-8 wherein the number average molecular weight of the second hydrogenated block copolymer is between 30,000 and 60,000. The composition according to any one of claims 1 to 7, which further comprises an extending oil. A composition according to any one of claims 1 to 10 wherein the metallocene polyolefin has a good distribution of ethylene and from 8% to 30% by weight of an α-olefin comonomer having from 4 to 12 carbon atoms. A process for producing an elastomeric film comprising the steps of providing a composition as described in any one of the preceding claims; extruding the composition throught a die, the die having a gap greater than 0.0125 cm and less than 0.305 cm; expanding the extruded film to a thickness of between 0.00125 cm and 0.0254 cm by application of differential pressure by a gas; and rapidly cooling the expanded extruded film. A film comprising the composition according to any one of claims 1 to 11.

Inventors: DJIAUW LIE KHONG, HOXMEIER RONALD JAMES, PEASE RODNEY RAY, DJIAUW, LIE KHONG, HOXMEIER, RONALD JAMES, PEASE, RODNEY RAY, Djiauw, Lie Khong, c/o Shell Oil Company
Applicants: KRATON POLYMERS RES BV, KRATON POLYMERS RESEARCH B.V.
Application year: 1995
Main classification: C08L23
IPC codes: B29C55, C08L53, C08L23, B29K9, B29K23, C08J5