HIGH 1,2-CONTENT THERMOPLASTIC ELASTOMER OIL POLYOLEFIN COMPOSITION

Abstract: The present invention relates to a thermoplastic elastomeric composition comprising: a base composition comprising: (i) 15 to 60 weight percent of a block copolymer having at least two polymerized monovinyl aromatic endblocks, each having a molecular weight of at least 20,000, and a midblock of hydrogenated polymerized butadiene wherein at least 51 mole percent of said butadiene has polymerized at the 1,2-position, and wherein said block copolymer has a molecular weight of at least 130,000, (ii) 5 to 80 weight percent of a paraffinic oil, and (iii) 5 to 25 weight percent of a crystalline polyolefin having a crystallinity of at least 50 %. The present invention further relates to a process for preparing a thermoplastic elastomeric composition and to articles containing the thermoplastic elastomeric composition.

Description: HIGH 1,2-CONTENT THERMOPLASTIC ELASTOMER/OIL/POLYOLEFIN COMPOSITION This invention relates to thermoplastic elastomer compositions containing a block copolymer, oil and a polyolefin; to a process for preparing thermoplastic elastomer compositions; and to articles containing thermoplastic elastomer compositions. It is well known to incorporate olefin polymer ' s into thermoplastic elastomer compositions to improve processability and to otherwise enhance the mechanical and chemical properties. For instance, high melting olefin polymers such as polypropylene improve the upper service temperature and ozone resistance of the compositions. It is also known to use paraffinic oils, alone or in combination with olefin polymers, to soften thermoplastic elastomer compositions and also to improve processability. However, increasing the amount of oil is a limited option because, at high oil levels, oil migration occurs which results in surface tackiness. In many utilities, however, greater softness would be desirable. It is an object of this invention to provide thermoplastic elastomer compositions having greater softness; and It is yet a further object of this invention to provide thermoplastic elastomer compositions with lower hardness and improved melt flow without an increase in the amount of oil . Now, surprisingly, thermoplastic elastomer compositions have been found having a greater softness, lower hardness, improved melt flow and/or other advantages with respect to known thermoplastic elastomer compositions. Therefore, the present invention relates to a thermoplastic elastomer composition comprising: a base composition comprising: (i) 15 to 60 weight percent of a block copolymer having at least two polymerized monovinyl aromatic endblocks, each having a molecular weight of at least 20,000, and a midblock of hydrogenated polymerized butadiene wherein at least 51 mole percent of said butadiene has polymerized at the 1 , 2-position, and wherein said block copolymer has a molecular weight of at least 130,000, (ii) 5 to 80 weight percent of a paraffinic oil, and (iii) 5 to 25 weight percent of a crystalline polyolefin having a crystallinity of at least 50%. Surprisingly, it has been found that the use of high 1,2-addition (high vinyl) thermoplastic elastomer in a rubber/oil/polyolefin composition results in greater softness as compared with similar compositions using elastomers where the 1,2-addition is in the usual 18 to 50 mole percent range. Furthermore, these novel compositions also have improved processability and better elastic properties as measured by, for instance, by compression set. Thermoplastic Elastomer By thermoplastic elastomer is meant a block copolymer having at least two end-blocks A made of polymerized monovinyl aromatic compound, thus giving a glassy, (Resinous) aromatic segment, and a mid-block B made up at least predominantly of polymerized 1,3- butadiene monomer, thus giving an amorphous elastomeric segment. The copolymers can be linear, A-B-A, radial, (A-B) n X / or mixtures thereof. Some A-B diblock polymer can be present but preferably at least 70 weight percent of the block copolymer is A-B-A or radial (or otherwise branched so as to have 2 or more terminal (resinous) A blocks per molecule) so as to impart strength. Generally, 80 to 100 weight percent of the block copolymer has 2 or more terminal resinous blocks per molecule and it is preferred to have essentially no diblock. In the above radial formula the n is an integer of at least 3, generally 3 to 50, more generally 6 to 13, and the X is the remnant of a coupling agent. The A-B-A compositions can be made by either sequential polymerization or coupling. In the sequential polymerization technique, the monovinyl aromatic monomer is first introduced to produce an aromatic block followed by the introduction of the butadiene monomer to produce the rubbery midblock followed by additional monovinyl aromatic compound to produce the other terminal aromatic block. This is broadly disclosed in U.S. 3,231,635. The production of such polymers and also radial polymers is broadly disclosed in U.S. 5,194,530. Another patent broadly disclosing the anionic polymerization of thermoplastic elastomers using an organo alkali metal initiator is U.S. 4,764,572. It is well known in the art to drive the polymerization toward the 1,2-addition of butadiene. Broadly, this can be done by utilizing an organic polar compound such as an ether, including cyclic ethers, polyethers and thioethers or an amine including secondary and tertiary amines. Preferred are chelating ethers and amines. By chelating- ether is meant an ether having more than one oxygen as exemplified by the formula R (OR' ) (OR") o 0R where each R is individually selected from 1 to 8, preferably 2 to 3, carbon atom alkyl radicals; R' and R" are individually selected from 1 to 6, preferably 2 to 3, carbon atom alkylene radicals; and m and o are independently selected integers of 1-3, preferably 1-2. One of m or o can be zero. Examples of preferred ethers include diethoxypropane, 1, 2-dioxyethane (dioxo) and 1,2- dimethyoxyethane (glyme) . Other suitable materials include CH3-OCH2-CH2-OCH2-CH2-OCH3 (diglyme) and CH3-CH2-OCH2-CH2-OCH2-CH2-OCH2-CH3. By chelating amine is meant an amine having more than 1 nitrogen such as N, N, N' , N' -tetramethylethylene diamine. Monoamines are operable but less preferred. Less preferred also (but still operable) are straight chain and cyclic monoethers such as dimethylether, diethylether , anisole, and tetrahydrofuran . This microstructure promoter is used in an amount of at least 0.1 moles per mole of organo alkalimetal initiator, such as an organo lithium initiator, preferably 1-50, more preferably 2-25, moles of promoter per mole of the initiator. Alternatively, the concentration can be expressed in parts per million by weight based on the total weight of solvent and monomer. Based on this criteria from 10 parts per million to about 1 weight percent, preferably 100 parts per million to 2000 parts per million are used. This can vary widely, however, since extremely small amounts of some of the preferred promoters are very effective. At the other extreme, particularly with less effective promoters, the promoter itself can be the solvent. Again, these techniques are well known in the art, disclosed for instance in U.S. 3,686,366, U.S. 3,700,748 and U.S. 5, 194,535. The resulting 1,2-vinyl content for the polymers useful in this invention is at least 51 mole percent, preferably at most 90, more preferably at least 56, even more preferably 65-90, most preferably 65-80 mole percent. The thermoplastic elastomer as it is actually used in this invention is hydrogenated and hence there is little or no vinyl unsaturation left. Nonetheless, it is still a high 1,2 addition polymer (from a high vinyl precursor) . Even the hydrogenated product is typically referred to as "high vinyl" because of its origin. The thermoplastic elastomers utilized in the compositions of this invention are selectively hydrogenated so as to remove most of the vinyl unsaturation and any ethylenic unsaturation in the polymer backbone from the monomer which did not polymerize in the 1,2 manner. By selective hydrogenation is meant that the aliphatic unsaturation is significantly removed while leaving unaffected most of the aromatic unsaturation. Suitable known catalysts for accomplishing this include nickel compounds in combination with a reducing agent such as an aluminum alkyl. Hydrogenation is taught in U.S. Patent 3,634,549, U.S. 3,670,054, U.S. 3,700,633 and Re 27,145. Each individual aromatic endblock must have a molecular weight of at least 20,000. Preferably the endblocks have a molecular weight within the range of 20,000 to 50,000, more preferably 25,000 to 40,000, most preferably 25,000 to 37,000. The thermoplastic elastomers utilized in this invention have a total molecular weight which is relatively high compared with thermoplastic elastomers in general. The molecular weight is at least 130,000. For linear A-B-A polymers, the molecular weight will generally be within the range of 150,000 to 300,000. Actually, the upper limit is dictated by viscosity considerations and can be as high as can be tolerated and still be processable. The most preferred molecular weight for linear A-B-A polymers is 180,000 to 250,000. With radial polymers, the molecular weight can be much higher since these polymers have a lower viscosity for a given total molecular weight. Thus, for radial polymers the molecular weight generally will be in the range of 130,000 to 1 million, preferably 130,000 to 500,000. The total monovinyl aromatic content of the block copolymer will generally be within the range of 20 to 48 weight percent based on the total weight of the block copolymer, preferably 22 to 45, more preferably 25 to 35 weight percent. The upper limit is set by the maximum which can be tolerated such that the material is still elastomeric as opposed to resinous. At about 50 weight percent and higher the material is resinous. Below 20 weight percent, the oil retention in the thermoplastic elastomer composition is rather poor (initially or after ageing) at high oil content. Since the block copolymers utilized in this invention are hydrogenated to remove the aliphatic unsaturation as noted hereinabove, they can be viewed as S-EB-S polymers, the S referring to the monovinyl aromatic, generally styrene, endblocks. The EB represents ethylene/butylene which is the structure resulting from the hydrogenation of polymerized 1,3- butadiene . Oil The oil is one which is compatible with the elastomeric mid-block segment of the elastomeric block copolymer and which does not tend to go into the aromatic endblock portions to any significant degree. Thus, the oils can be viewed as paraffinic. Paraffinic oils which may be used in the elastomeric composition should be capable of being melt processed with other components of the elastomeric composition without degrading. Particularly important is the ability of the final composition to be melt extruded. An exemplary paraffinic 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 0.864-0.878 at 15.6°C (60°F), a flashpoint of 237.8°C (460°F), and a viscosity of 0.8-0.9 cm2 sec (370-420 SUS) at 37.8°C (100°F) . Polyolefin The polyolefins utilized in this invention are crystalline polyolefins. That is, polyolefins having a crystallinity of at least 50% (i.e. at least 50 weight percent is crystalline) . Crystallinity of polyolefins can be calculated using information on the heat loss (energy/mass x delta temperature) of melting obtained from differential scanning calorimetry and the referenced value of heat of fusion (energy/delta temperature) for a known single crystal (i.e. 100% crystallinity) of the polyolefin. Most preferred are high density polyethylene, which has a crystallinity of 80 to 90%, and crystalline polypropylene, the crystalline polypropylene being most preferred in many applications because of the improved high temperature properties it imparts. Other suitable polyolefins include polybutene, ethylene/higher α-olefin copolymers, propylene copolymers and butylene copolymers or mixtures of any of the above-described polyolefins. Most preferred is an injection molding grade crystalline polypropylene such as Polypropylene 5A15 homopolymer (melt flow rate 5g/10 min., from Shell Chemical Co.). Compounding The thermoplastic elastomer compositions of this invention may be viewed as comprising a hydrocarbon component made up of the elastomeric block copolymer, the paraffinic oil and the crystalline polyolefin. To this hydrocarbon component can be added other ingredients such as typically found in elastomeric compositions. Other ingredients which do not affect the essential elastomeric characteristics of the composition may be present including pigments, fragrances, stabilizers, flame retardants, surfactants, waxes, flow promoters, solvents, and materials added to enhance processability and pellet handling of the composition. The compositions can also contain 5 to 40 weight percent based on the weight of hydrocarbon component of a filler such as a hard inorganic mineral filler. The stabilizer can be any conventional stabilizer or stabilizer system and is frequently simply an antioxidant such as a hindered phenol, alone or in combination with a thiosynergist . Particularly preferred is IRGANOX 1010® alone or in combination with a thiosynergist such as DLTDP . IRGANOX 1010® is tetrakis [methylene (3, 5-di-t-butyl-4- hydroxyhydrocinnamate) ] methane. DLTDP is dilaurylthiodipropionate . Suitable stabilizers are shown in U.S. 5,149,741 and U.S. 4,835,200. More volatile materials such as 2, 6-di-tert-butylphenol are less preferred because of the volatility. The stabilizer is generally present in an amount within the range of 0.01 to 4, preferably 0.5 to 1 weight percent based on the weight of the base composition. The compositions of this invention may be thought of in terms of (A) a base composition comprising (i) the elastomeric block copolymer, (ii) the oil, (iii) the crystalline polyolefin, and (B) any other ingredients. The base composition comprises 15 to 60 weight percent of the hydrogenated high 1,2 elastomeric block copolymer; 5 to 80, preferably 25 to 60, more preferably 35 to 60 weight percent of said paraffinic oils; and 5 to 25, preferably 5 to 20, more preferably 5 to 15, most probably 10 to 15 weight percent of the crystalline polyolefin. The base composition preferably comprises up to 55, more preferably up to 50, even more preferably up to 45 weight percent of the block copolymer. Preferably, the base composition comprises at least 25 weight percent of the block copolymer. All of the percentages are based on the total weight of the base composition, i.e. the block copolymer, oil and polyolefin . The ingredients preferably are compounded by contacting the block copolymer with the oil and allowing time for the oil to be absorbed into the copolymer. Generally, the copolymer will absorb the oil to the appearance of dryness. Thereafter the oil/block copolymer composition is generally dry blended in a tumble blender with the polyolefin and antioxidant after which the blend is rendered molten and extruded. According to a further aspect, the present invention relates to a process for preparing a thermoplastic elastomer composition, comprising: combining a block copolymer with a paraffinic oil, said block copolymer having at least two polymerized monovinyl aromatic compound endblocks, each having a molecular weight of at least 20,000, and a midblock of hydrogenated polymerized butadiene wherein at least 51 mole percent of said butadiene has polymerized at the 1 , 2-position, and wherein said block copolymer has a molecular weight of at least 130,000; allowing time for said block copolymer to absorb said paraffinic oil to give an oil-containing block copolymer composition; tumble blending said oil-containing block copolymer composition with a crystalline polyolefin to give a block copolymer/oil/polyolefin mixture; melt extruding said mixture, wherein said block copolymer is present in an amount within the range of 15 to 60 weight percent, said oil is present in an amount within the range of 5 to 80 weight percent, and said crystalline polyolefin is present in an amount within the range of 5 to 25 weight percent based on the total weight of said block copolymer, oil and polyolefin. The thermoplastic elastomeric compositions may be used for utilities such as overmoulding onto hard substrates, grips, medical articles like medical tubing and other rubber articles. Therefore, according to yet another aspect, the present invention relates to articles containing the thermoplastic elastomer composition as described above. Definitions As used herein, the terms "tensile strength" or "TS" refer to the resistance of an elastic material to being elongated as determined in accordance with ASTM D- 412 using 0.318 cm (0.125 inch) wide and 0.203 cm (0.080 inch) thick dumbbell samples that are cut from inspection molded plaques. Tensile testing is performed on an INSTRON (trade mark) Model 1123 Universal Test Machine utilizing a crosshead speed of 25.4 cm/min (10 inch/min) . As used herein, the terms "elongation" or "Eb" refer to the percent extension of an elastic material until breakage as determined in accordance with ASTM-D- 412 as described above. A mechanical extensiometer is used during the testing to obtain a more accurate elongation. The gap distance for the extensiometer is 2.54 cm (1 inch) . As used herein, the terms "compression set" or "CS" refer to a value determined according to ASTM-D-395, Method A, Type I. Disks of 2.54 cm (1 inch) diameter are cut out of injection molded plaques. These disks are stacked to approximately 1.27 cm (0.5 inches) in height and compressed between two flat chrome plates. The degree of compression is controlled by the use of standard metal spacers. The disk stacks are placed under compression for 22 hours at room temperature or 70°C , and then allowed to recover for 30 minutes before their final thickness is measured. As used herein, the term "hardness" refers to a value determined according to ASTM D2240 after 10 seconds of resistance on the Shore A hardness scale. The hardness value is the average of five measurements taken at different locations around a 10.16 cm (4 inch) by 12.7 cm (5 inch) injection molded plaque. As used herein the melt flow index ("MFI") is an indication of melt viscosity determined according to ASTM D1238 Procedure A at a temperature of 230°C and 2.16 kg piston loading (Old Condition L) . The procedure utilizes a dead-weight piston plastometer. By "molecular weight" as used herein is meant the following. Molecular weights of linear block copolymer are conveniently measured by Gel Permeation Chromatography (GPC) , where the GPC system has been appropriately calibrated. Polymers of known molecular weight are used to calibrate and these must be of the same molecular structure and chemical composition as the unknown linear polymers or segments that are to be measured. For anionically polymerized linear polymers, the polymer is essentially monodispersed and it is both convenient and adequately descriptive to report the "peak" molecular weight of the narrow molecular weight distribution observed. Hence, this is what is meant with regard to references herein to molecular weight of linear polymers. This is also what is meant by the references herein to the molecular weight of the aromatic resinous A block. Polystyrene is used to calibrate, thus directly giving the absolute molecular weight of polystyrene endblocks. From this and the known percent styrene, the absolute molecular weight of the midblock is calculated. That is, an aliquot is removed after the first step of the polymerization, terminated to deactivate the initiator and the molecular weight measured. Measurement of the true molecular weight of final coupled star polymer is not as straightforward or as easy to make using GPC. This is because the star shaped molecules do not separate and elute through the packed GPC columns in the same manner as do the linear polymers used for the calibration, and, hence, the time of arrival at a UV or refractive index detector may not be a good indicator of the molecular weight. A good analytical method to use for a star polymer is to measure the weight average molecular weight by light scattering techniques. The sample is dissolved in a suitable solvent at a concentration less than 1.0 gram of sample per 100 millimeters of solvent and filtered using a syringe and porous membrane filters of less than 0.5 microns pore size directly onto the light scattering cell. The light scattering measurements are performed as a function of scattering angle and of polymer concentration using standard procedures. The differential refractive index (DRI) of the sample is measured at the same wavelength and in the same solvent used for the light scattering. Thus, the reference to molecular weight in reference to final star or radial polymers means molecular weight determined in this fashion. However, even with the star polymers, the endblocks are still measured by taking an aliquot and using GPC as described for the linear polymers. Example I In the following example two polymers were utilized. The first, designated "A," was a high vinyl thermoplastic elastomer produced as follows. Utilizing the conventional secondary butyllithium initiator, styrene, then 1, 3-butadiene, then styrene were sequentially introduced to give an A-B-A polymer wherein the molecular weight of the segments was as follows 25,000-145,000-37,000. The polystyrene content was 30 weight percent. Polymerization of the butadiene segment was carried out at 50°C and cyclohexane solvent utilizing 300 parts per million based on the weight of solvent and monomer of glyme so as to induce high 1,2- addition. The resulting polymer had a 1,2-addition of 75.2 mole percent. The polymer was then hydrogenated utilizing a conventional nickel/aluminum hydrogenation catalyst to give the S-EB-S structure. Polymer B was a sequentially polymerized polymer prepared in a similar manner except glyme was not utilized, instead 6 weight percent diethylether , based on the weight of solvent and monomer, was used. Thus, the 1,2-addition was a conventional 38.0 mole percent. The resulting A-B-A polymer had a molecular weight as follows: 29,000-123,000-29,000. The polystyrene content was 32 weight percent. The polymer was hydrogenated in the same manner as Polymer A. Three aliquots of conventional Polymer B and four aliquots of the high vinyl Polymer A were separately compounded with various amounts of oil and polyolefin as set out hereinbelow in the Table. Compounding was carried out by contacting the oil and the block copolymer and allowing 8 hours for absorption of the oil into the block copolymer. Thereafter the composition was tumbled with the polyolefin for 15 minutes and then extruded at a temperature of 225°C. From this extrudate tensile specimens and compression set specimens were molded and the melt flow determined. The results are set out hereinbelow. TABLE I Blend SBC 3 Oil 4 pp5 Hardness TS (RT) Eb TS (70) Eb CS MFI # SBC Grade (w%) (w%) (w%) (Shore A) MPa (psi) (RT) MPa (psi) (70) (70) (230/2.16) (%) (%) (%) (g/lOmin) 1 A 1 40 50 10 28.6/23.1 3.5 (506) 800 0.83 (121) 507 49.6 3.15 2 B 2 40 50 10 35.9/31.3 5.5 (802) 831 1.3 (190) 720 56.5 1.23 3 A 45 45 10 30.0/22.5 4.0 (583) 978 0.79 (115) 583 46 2.56 4 A 45 45 10 31.6/25.4 3.9 (559) 991 0.83 (121) 535 1.76 5 B 45 45 10 41.5/36.5 5.1 (742) 706 1.3 (183) 613 58.7 0.095 6 A 55 35 10 39.3/33.1 4.1 (592) 751 1.1 (160) 573 50.9 <0.06 7 B 55 35 10 49.3/45.8 5.4 (782) 628 2.0 (292) 677 60 <0.01 1 High vinyl S-EB-S polymer as described above. 2 Normal vinyl S-EB-S polymer as described above. 3 Styrenic Block Copolymer (SBC) . 4 DRAKEOL® 34. Polypropylene sold under the trade designation 5A15 from Shell Oil Co. As can be seen comparing Runs 1 and 2, significantly lower hardness (greater softness) was obtained with Invention Run 1 as compared with the comparable Control Run 2. As can be seen further, this was achieved with better set compression (49.6 versus 56.5) the lower number indicating better elasticity, i.e. less permanent deformation. Finally, a comparison of the melt flow index shows that all of these beneficial results were obtained with an improvement rather than a sacrifice in melt flow. Similarly, a comparison of Invention Runs 3 and 4 at a slightly lower oil ratio with a comparable Control Run 5 shows the same lower hardness (better softness), and the same improvement in compression set and melt flow. A comparison of Invention Run 6 with comparable Control Run 7 shows once again improved softness (lower hardness), improved (lower) compression set and marginally improved melt flow, although the melt flow test at the conditions used does not meaningfully distinguish such viscous compositions. Example II Example I was repeated but using different high vinyl block copolymers as depicted in Table II. Table II Block PSC (%) 1 , 2-vinyl Mw (A-B-A) (kg/mol) copolymer COntent (%) C 35.3 77 (25-93-39) D 28.1 71 (26-131-26) E 32.8 72.3 (29.5-120.1-34.5) F 32.5 72.5 (28.8-117.6-31.5) G 32.9 72.1 (28.9-116.0-31.0) H 32.9 69.4 (29.0-116.9-31.5) PSC = polystyrene content Compounds were prepared from the polymers as set out in Example I. The composition of the compounds (blends) and test results are depicted in Table III. It can be seen that lower hardness (greater softeness) was obtained with invention Runs 8, 11, 14, 15, 16, 17 as compared with control Run 5; with better compression set and an improvement rather than a sacrifice in melt flow. Invention Runs 9 and 12 in Table III depict results with compounds containing filler and invention Runs 10 and 13 in Table III depict results with compounds containing a high amount of polypropylene . While this invention has been described in detail for the purpose of illustration, it is not to be construed as limited thereby but is intended to cover all changes and modifications within the spirit and scope thereof. Table III Blend SBC SBC Oil PP Filler TS(RT) Eb CS MFT Hardness # grade (w%) (w%) ( %) ( %) Mpa(Psi) (RT)% (70)% 230/2.16) (Shore A) g/10 min) 8 C 45 45 10 - 4.7 (685) 814 50.6 5 30.1/25.2 9 C 21.3 31.9 8.5 38.3 3.1 (443) 647 61 9.7 47.4/41.3 10 c 30 50 20 - 4.7 (688) 736 57.8 45.7 56.5/51.4 11 D 45 45 10 - 4.2 (607) 693 35.1 0.57 31.3/25.3 12 D 21.3 31.9 8.5 38.3 2.9 (419) 609 42.1 3.8 46.2/39.0 13 D 30 50 20 - 4.5 (650) 769 46.1 26.5 53.1/46.7 14 E 45 45 10 - 3.9 (566) 596 34.1 0.12 34.3/29.0 15 F 45 45 10 - 3.8 (553) 593 32.2 0.23 33.7/28.9 16 G 45 45 10 - 3.8 (545) 616 32.4 0.4 32.9/27.5 17 H 45 45 10 - 4.2 (616) 721 34.2 0.16 34.8/29.4 5 B 45 45 10 _ 5.1 (742) 706 58.7 0.095 41.5/36.5 The filler was a calcium carbonate marketed under the tradename VICRON 25-11

Claims: C L A I S 1. A thermoplastic elastomer composition comprising: a base composition comprising: (i) 15 to 60 weight percent of a block copolymer having at least two polymerized monovinyl aromatic endblocks, each having a molecular weight of at least 20,000, and a midblock of hydrogenated polymerized butadiene wherein at least 51 mole- percent of said butadiene has polymerized at the 1 , 2-position, and wherein said block copolymer has a molecular weight of at least 130,000, (ii) 5 to 80 weight percent of a paraffinic oil, and (iii) 5 to 25 weight percent of a crystalline polyolefin having a crystallinity of at least 50%. 2. A thermoplastic elastomer composition as claimed in claim 1, wherein the base composition comprises 15 to 55 weight percent of the block copolymer. 3. A thermoplastic elastomer composition as claimed in claim 2, wherein the base composition comprises 15 to 50 weight percent of the block copolymer. 4. A thermoplastic elastomer composition as claimed in any one of claims 1 to 3, wherein the block copolymer comprises 20-48 weight percent of said monovinyl aromatic compound. 5. A thermoplastic elastomer composition as claimed in any one of claims 1 to 4, wherein at most 90 mole percent of the butadiene has polymerised at the Imposition . 6. A thermoplastic elastomer composition as claimed in claim 5, wherein at least 56 mole percent of the butadiene has polymerised at the 1, 2-position . 7. A thermoplastic elastomer composition as claimed in any one of the preceding claims, wherein the crystalline polyolefin is present in the base composition in an amount from 5 to 20 weight percent. 8. A thermoplastic elastomer composition as claimed in any one of the preceding claims, further comprising a stabilizer, such stabilizer being present in an amount within the range of .01 to 4 weight percent based on the weight of the base composition. 9. A thermoplastic elastomer composition as claimed in any one of the preceding claims, further comprising a filler and/or a flame retardant. 10. A process for preparing a thermoplastic elastomer composition, comprising: combining a block copolymer with a paraffinic oil, said block copolymer having at least two polymerized monovinyl aromatic compound endblocks, each having a molecular weight of at least 20,000, and a midblock of hydrogenated polymerized butadiene wherein at least 51 mole percent of said butadiene has polymerized at the 1, 2-position, and wherein said block copolymer has a molecular weight of at least 130,000; allowing time for said block copolymer to absorb said paraffinic oil to give an oil-containing block copolymer composition; tumble blending said oil-containing block copolymer composition with a crystalline polyolefin to give a block copolymer/oil/polyolefin mixture; melt extruding said mixture, wherein said block copolymer is present in an amount within the range of 15 to 60 weight percent, said oil is present in an amount within the range of 5 to 80 weight percent, and said crystalline polyolefin is present in an amount within the range of 5 to 25 weight percent based on the total weight of said block copolymer, oil and polyolefin. 11. Articles containing the thermoplastic elastomer composition as claimed in any one of the preceding claims 1 to 9.

Inventors: DJIAUW LIE KHONG, MODIC MICHAEL JOHN, DJIAUW, LIE, KHONG, MODIC, MICHAEL, JOHN
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1997
Main classification: C08L53
IPC codes: C08L23, C08L53, C08L91