Method for manufacturing an olefinic thermoplastic elastomer composition

Abstract: This invention relates to a method for manufacturing an olefinic thermoplastic elastomer composition, characterized by disposing specific kneading segment at least at one place of the screw on the occasion of manufacturing an olefinic thermoplastic elastomer composition comprising a polyolefin resin and a crosslinked rubber by dynamic crosslinking with a twin screw extruder.

Description: The present invention relates to a method for manufacturing an olefinic thermoplastic elastomer composition excellent in tensile properties and appearance of a molded product. An olefinic thermoplastic elastomer, being light and easy to be recycled, is widely used for automobile parts, industrial machine parts, electronic/electric instrument parts, construction materials and the like as an energy-saving and resources-saving thermoplastic elastomer particularly as an alternative to a soft polyvinyl chloride or a vulcanized rubber. The conventional olefinic thermoplastic elastomer, however, has the defect that it has poorer tensile strength compared to a soft polyvinyl chloride and a vulcanized rubber, and improving the defect has been desired strongly. Further, particularly in the case of forming into a sheet and extrusion forming into a profile, appearance of the molded product is very important, and inferior appearance due to roughness, minute projections and so forth on the surface of the molded product damages the value of the product remarkably. JP-A-58-25340 proposes a technique for manufacturing an olefinic thermoplastic elastomer by a dynamic crosslinking method with a twin screw extruder. Although this method produces sheets or extrusion moldings with sharply improved appearance compared to ones manufactured with a single screw extruder, it is not necessarily satisfactory. The reason for this is that kneading at high shearing velocity in a twin screw extruder generates much heat by shear, whereby the crosslinking reaction proceeds rapidly resulting in a tendency to lead to un-uniform crosslinking. JP-A-9-95540 describes a manufacturing method with a screw composed of specific kneading discs. But, this method is apt to cause the above-mentioned poor appearance when the screw revolution is raised and the extrusion throughput per hour is increased in order to increase productivity. The inventors studied earnestly to solve the above problem and have found that, in manufacturing an olefinic thermoplastic elastomer by dynamically crosslinking a polyolefin resin and a rubber component using a twin screw extruder, use of a screw having specific kneading segment allows to put down shear-derived heat generation, and that an olefinic thermoplastic elastomer composition excellent in tensile strength and appearance of a molding can be obtained by performing the dynamic crosslinking at an appropriate rate. Further, the inventors have found, on the occasion of manufacturing an olefinic thermoplastic elastomer by dynamically crosslinking a polyolefin resin and a rubber component using a twin screw extruder, by performing the dynamic crosslinking under the specific conditions, emergence of fish eyes (gel-like minute mass) decreases remarkably, and thus the inventors have completed the present invention. US 4,824,256 discloses a method of making a thermoplastic composition using a screw extruder. JP 08/267539 discloses a twin screw extruder in which a minimum gap between the tip parts of rotor blades and the inner surface of a barrel is set to permit passage of powder. US 4,824,256 discloses a twin screw extruder adapted to achieve maximum flow rate and melt homogeneity. A further example of a manufacturing method for making thermoplastic elastomers using a twin-screw extruder and an aqueous buffer solution in order to enhance the cross-linking reaction of said thermoplastic elastomers is shown in EP 1050548 A1. The present invention intends to alleviate the problem as mentioned above of the prior art, and the object is to provide a method that can produce with good productivity an olefinic thermoplastic elastomer composition superior in tensile strength and appearance of a molding and a method that can produce an olefinic thermoplastic elastomer composition wherein emergence of fish eyes (gel-like minute mass) is decreased markedly. The present invention comprises the following aspect: (i) A method for manufacturing an olefinfic thermoplastic elastomer composition characterized in that, in manufacturing an olefinic thermoplastic elastomer composition comprising a polyolefin resin and a crosslinked rubber by dynamic crosslinking with a twin screw extruder, a first kneading segment (A) is disposed at least at one place of the screw which first kneading segment (A) has the following features: A1) the kneading segment having three vertex portions in the cross-section the vertex portion being a point or portion at the farthest distance from the center of gravity in the cross-section, A2) the vertex portion ofthe kneading segment being composed ofa first portion (a1) continuously twisted to the contrary direction relative to the screw rotary direction and a second portion (a2) continuously twisted to the same direction relative to the screw rotary direction, respectively to the thickness direction, and A3) the sum of the thickness of said first portion a1 and that of said second portion a2 being 1.0 times or more of the screw diameter. Hereunder, the preferred method for manufacturing the olefinic thermoplastic elastomer composition of the present invention is explained concretely. The present application is characterized by dynamically crosslinking a polyolefin resin and a rubber component with a twin screw extruder having specific kneading segments. Firstly, the components constituting the olefinic thermoplastic elastomer composition are explained. (Polyolefin resin) The polyolefin resin used in the present invention consists of a high molecular weight solid product obtained by polymerizing one or more of monoolefin by either high pressure method or low pressure method. As such a resin there are enumerated, for example, isotactic and syndiotactic monoolefin-based polymer resins. Resins representative of these are commercially available. As raw material olefins suitable for the polyolefin resin, there are enumerated, concretely, ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 2-methyl-1-propene, 3-methyl-1-pentene, 4-methyl-1-pentene and 5-methyl-1-hexene. These olefins are used alone or in a mixture of two or more. Any polymerization mode, regardless of random or block mode, can be adopted as long as it produces resinous substances. These polyolefin resins can be used singly or in a combination of two or more. Among these polyolefin resins, particularly preferred are propylene-based polymers, concretely such as propylene homopolymer, propylene-ethylene block copolymer, propylene-ethylene random copolymer and propylene-ethylene-butene random copolymer. The polyolefin resin used in the present invention preferably has a MFR (ASTM D-1238-65T, 230°C, load 2.16 kg) in the range of 0.01 to 100 g/10min. usually, 0.05 to 50 g/10min. particularly. The above polyolefin resin has a role of improving the flow and heat resistance of the composition. In the present invention, the polyolefin resin is used in a ratio of preferably 10 to 80 parts by weight, more preferably 15 to 60 parts by weight against the total 100 parts by weight of the polyolefin resin and crosslinked rubber. Using the polyolefin resin in the above-mentioned ratio affords a high heat resistant thermoplastic elastomer composition excellent in moldability as well as excellent in flexibility and rubbery elasticity. (Crosslinked rubber) As the crosslinked rubber used in the present invention, there is enumerated , for example, at least one rubber selected from the group consisting of ethylene-α-olefin-non-conjugated polyene copolymer rubber, ethylene-α-olefin copolymer rubber, isoprene rubber and hydrogenated product thereof, butadiene rubber and hydrogenated product thereof, styrene-butadiene rubber and hydrogenated product thereof, styrene-isoprene rubber and hydrogenated product thereof, chloroprene rubber, butyl rubber, halogenated butyl rubber, polyisobutylene rubber, acrylonitrile-butadiene rubber, chlorinated polyethylene rubber, fluorine rubber, silicone rubber, polysulfide rubber and urethane rubber. Among these, the ethylene-α-olefin-non-conjugated polyene copolymer rubber and ethylene-α-olefin copolymer rubber are favorable, and the ethylene-propylene-non-conjugated diene copolymer rubber having the following characteristics is particularly favorable: ethylene/propylene (molar ratio): 30/70 to 90/10 iodine value: 1 to 30 (g/100 g) Mooney viscosity ML 1+4 (100°C): 15 to 250 In the present invention, the crosslinked rubber is used in a ratio of preferably 20 to 90 parts by weight, more preferably 40 to 85 parts by weight against the total 100 parts by weight of the polyolefin resin and crosslinked rubber. (Other components) For the olefinic thermoplastic elastomer composition of the present invention, in addition to the polyolefin resin and crosslinked rubber, a softening agent and /or an inorganic filler can be incorporated. The softening agents may be any of those usually used for rubbers. Illustrative examples thereof may include petroleum softening agents, such as process oil, lubricating oil, paraffin oil, liquid paraffin, petroleum asphalt and vaseline; coal tars, such as coal tar and coal tar pitch; fatty oils, such as castor oil, linseed oil, rape oil, soybean oil and coconut oil; tall oil; waxes, such as beeswax, carnauba wax and lanolin; fatty acids and metal salts thereof, such as ricinolic acid, palmitic acid, stearic acid, barium stearate, calcium stearate and zinc laurate; synthetic polymeric substances, such as terpene resin, petroleum resin, coumarone-indene resin and atactic polypropylene; ester softening agents, such as dioctyl phthalate, dioctyl adipate and dioctyl sebacate; microcrystalline wax; rubber substitute(factice); liquid polybutadiene; modified liquid polybutadiene; liquid Thiokol™; and hydrocarbon based synthetic lubricating oils. In the present invention, the softening agent can be used, from the viewpoint of the heat resistance of the obtained thermoplastic elastomer composition, usually in a ratio of 150 or less parts by weight, preferably 2 to 100 parts by weight, more preferably 5 to 80 parts by weight to the total 100 parts by weight of the polyolefin resin and crosslinked rubber. When the softening agent is used in the ratio mentioned above, the obtained thermoplastic elastomer composition is excellent in flow property at molding without the lowering of mechanical properties of molded products. In the present invention, the softening agent may be added at the time of manufacturing the olefinic thermoplastic elastomer or may be oil extended in the raw material rubber beforehand. The inorganic filler includes, concretely, calcium carbonate, calcium silicate, clay, kaolin, talc, silica, diatomaceous earth, mica powder, asbestos, alumina, barium sulfate, aluminum sulfate, calcium sulfate, basic magnesium carbonate, molybdenum disulfide, graphite, glass fiber, glass balloon, shirasu balloon, basic magnesium sulfate whisker, calcium titanate whisker and aluminum borate whisker. In the present invention, the inorganic filler can be used, from the viewpoint of rubbery elasticity and moldability of the obtained thermoplastic elastomer composition, usually in a ratio of 100 or less parts by weight, preferably 2 to 50 parts by weight to the total 100 parts by weight of the polyolefin resin and crosslinked rubber. Further, in the present invention, the olefinic thermoplastic elastomer composition can contain heretofore known heat stabilizers, age resistors, weathe rresisting agents, anti-static agents and lubricants such as metal soap and wax in such an extent not to damage the object of the present invention. In a preferred process, the olefinic thermoplastic elastomer composition is obtained by blending the above-mentioned polyolefin resin, crosslinked rubber as raw material rubber and optionally incorporated softening agent and/or inorganic filler, and thereafter by dynamically crosslinking in the presence of a crosslinking agent. Here, "dynamically crosslinking" means to effect crosslinking reaction by kneading in a molten state in the presence of a crosslinking agent. The crosslinking agent used with the present invention includes crosslinking agents generally used in thermosetting type rubbers, such as organic peroxide, phenol resin, sulfur, hydrosilicone compound, amino resin, quinone and its derivatives, amine compound, azo compound, epoxy compound and isocyanate. Of these crosslinking agents, organic peroxides are particularly preferable. As the organic peroxide used in the present invention, there are enumerated, concretely, dicumyl peroxide, di-tert-butyl peroxide, 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexane, 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexyne-3, 1,3-bis(tert-butylperoxyisopropyl)benzene, 1,1-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane, n-butyl 4,4-bis(tert-butylperoxy)valerate, benzoyl peroxide, p-chlorobenzoyl peroxide, 2,4-dichlorobenzoyl peroxide, tert-butyl peroxybenzoate, tert-butylperoxyisopropylcarbonate, diacetyl peroxide, lauroyl peroxide and tert-butyl cumyl peroxide. Of these, in the viewpoint of odor and scorch stability preferred are 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexane, 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexyne-3 and 1,3-bis(tert-butylperoxyisopropyl)benzene. Among these, 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexane is most preferable. The organic peroxide is used usually in an amount to make 0.02 to 3 parts by weight, preferably 0.05 to 1 part by weight to the total 100 parts by weight of the polyolefin resin and crosslinked rubber, from the standpoints of heat resistance, tensile properties, elastic recovery, impact resilience and moldability of the obtained olefinic thermoplastic elastomer composition. In the present invention, upon crosslinking treatment by the organic peroxides, there can be incorporated crosslinking aids such as sulfur, p-quinone dioxime, p,p'-dibenzoylquinone dioxime, N-methyl-N-4-dinitrosoaniline, nitrosobenzene, diphenylguanidine, trimethylolpropane, N,N'-m-phenylene bismaleimide, divinylbenzene and triallyl cyanurate, or polyfunctional methacrylate monomers such as ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, trimethylolpropane trimethacrylate and allyl methacrylate, or polyfunctional vinyl monomers such as vinyl butyrate and vinyl stearate. By using the above compounds, uniform and mild crosslinking reaction can be expected. Particularly, in the present invention, divinylbenzene is most preferable. Divinylbenzene, since being easy to handle, since being good in compatibility with the polyolefin resin and the rubber component such as ethylene-α-olefin-non-conjugated polyene copolymer rubber which constitute the main component of the mass to be crosslinked, and since having a function of solubilizing organic peroxides to work as dispersant thereof, produces the effect that the crosslinking by heat treatment is uniform to result in a thermoplastic elastomer composition balanced in flow and physical properties. The compound such as the above crosslinking aid or polyfunctional vinyl monomer is employed to make usually 2 parts by weight or less, preferably 0.2 to 1 parts by weight against the total 100 parts by weight of the polyolefin resin and crosslinked rubber. Further, in order to accelerate the decomposition of the organic peroxide, there can be used decomposition accelerators, for example, tertiary amines such as triethylamine, tributylamine and 2, 4, 6-tri(dimethylamino)phenol, and naphthenates of aluminum, cobalt, vanadium, copper, calcium, zirconium, manganese, magnesium, lead and mercury. The dynamic crosslinking (heat treatment) in the present invention is carried out in a twin screw extruder having specific kneading segments. The dynamic crosslinking is preferably conducted under the inert gas atmosphere of nitrogen and carbon dioxide. The temperature of the extruder is in the range from the melting point or softening point of the polyolefin resin to 300 °C, usually 100 to 250 °C, favorably 140 to 225 °C. In the method, in the point of optimizing the kneading conditions and the reaction rate of the dynamic crosslinking, the clearance between the vertex portion of the kneading segment (A) (here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section) and the cylinder inner wall of the extruder is 1/60 or more, preferably 2/100 or more of the screw diameter, and 1/6 or less, preferably 1/10 or less, more preferably 7/100 or less of the screw diameter. That is, it is requisite for the above clearance to be 1/60 or more to 1/6 or less of the screw diameter, and, for example, it is preferably 1/60 or more to 1/10 or less, more preferably 2/100 or more to 7/100 or less. Further, in the method, in the point of performing effective kneading, it is preferable to dispose a kneading segment (B) downstream the kneading segment (A) which segment (B) has a ratio of the clearance between the vertex portion of the kneading segment (here, the vertex portion means a point or portion at the farthest distance from the gravity center in the cross-section) and the cylinder inner wall of the extruder to the screw diameter which ratio is smaller than the ratio as set forth regarding the kneading segment (A). In the invention, in the point of optimizing the reaction rate of the dynamic crosslinking, it is preferable to set the temperature of at least one of upstream barrels to 170 °C or below and the temperature of at least one of downstream barrels to 190 °C or above. As used herein, upstream means the side nearest to the feeding hopper from the intermediate point and downstream means the side nearest to the die from the intermediate point. The kneading time is usually 1 to 20 minutes, preferably 1 to 10 minutes. The shearing force applied is in the range of 10 to 10,000 sec -1 , preferably 100 to 2,000 sec -1 , more preferably 200 to 1,000 sec -1 in terms of shearing velocity applied to the specific kneading segment (A), and in the range of 100 to 50,000 sec -1 , preferably 200 to 10,000 sec -1 , more preferably 500 to 5,000 sec -1 in terms of shearing velocity applied to the specific kneading segment (B). The dynamic crosslinking is preferably conducted under the conditions satisfying the following expression: 4.5 < 2.2 logX + logY - logZ + (T-180) ÷ 100 < 6.0 wherein T is a resin temperature (°C) at the die outlet of the twin screw extruder, X is a screw diameter (mm) of the extruder, Y is a maximum shearing velocity (sec -1 ) generated at the part of the kneading segment (A) in the extruder and Z is an extrusion throughput (kg/h) of the extruder, and the maximum shearing velocity Y (sec -1 ) is determined from the equation Y= (X× π×S)/U wherein X is a screw diameter (mm) of the twin screw extruder, S is a screw revolution number per second (rps) and U is a distance (mm) at the narrowest portion of the clearance between the barrel inner wall and kneading segment of the screw. By conducting the dynamic crosslinking under the conditions satisfying the above expression, an elastomer composition can be produced which is superior in compatibility as to each component constituting the olefinic thermoplastic elastomer composition and superior in tensile strength and appearance of molded product. The twin screw extruder usable for the present invention can be any one wherein the rotary directions of the two screws are the same or different, or wherein the two screws are completely engaged each other, partially engaged or not engaged. Among these, particularly preferred is one wherein the screw rotary directions are the same and the two screws are completely or partially engaged. In the twin screw extruder used in the present invention, the ratio of the screw length (L) to the screw diameter (D), ratio L/D, is usually 25 to 70, preferably 30 to 65, more preferably 35 to 60. In the following the kneading segment used in the present invention is explained. Kneading segment (A) The kneading segment (A) used in the invention is one that has: A1) the kneading segment having three vertex portions (a) in the cross-section (here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section). A2) the vertex portion of the kneading segment being composed of a portion (a1) continuously twisted to the contrary direction relative to the screw rotary direction and a portion (a2) continuously twisted to the same direction relative to the screw rotary direction, respectively to the thickness direction, and A3) the thickness of the kneading segment (the total of the thickness of a1 and that of a2) being 1.0 times or more of the screw diameter. Kneading segment (B) The kneading segment (B) preferably used in the invention has, in the viewpoint of achieving the effective kneading by interrupting the mass to be kneaded that is tending downstream and retaining at the portion of the kneading segment (A), a value of less than 1/60 which value is a ratio of the clearance between the vertex portion (here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section) and the cylinder inner wall of the extruder to the screw diameter. In the method, in the point of performing effective kneading, the kneading segments (A) and (B) are preferably disposed adjacently. The kneading segment (B) is preferably one that has the same features (hereunder described) as those of the kneading segment (B) used in the second invention of the application: B1) the kneading segment having two vertex portions (a) in the cross-section (here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section), and B2) the vertex portion of the kneading segment having a structure twisted discontinuously to the thickness direction. Kneading segment (A) <Figure 1> The kneading segment (A) used in the present invention has three vertex portions (a) in the cross-sectional shape. Here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section. Further, the kneading segment (A) is composed of a portion (a1) in which the vertex portion is continuously twisted to the thickness direction to the contrary direction relative to the screw rotary direction and a portion (a2) in which continuously twisted to the same direction to relative to the rotary direction. Moreover, the thickness of kneading segment (the total of thickness of a1 and that of a2) is 1.0 times or more of the screw diameter, preferably 2.0 times or more. In the viewpoint of optimizing the kneading conditions and the reaction rate of the dynamic crosslinking, the clearance between the vertex portion and the cylinder inner wall is preferably 1/100 or more, more preferably 1/60 or more, particularly preferably 2/100 or more of the screw diameter, and preferably 1/6 or less, more preferably 1/10 or less, particularly preferably 7/100 or less of the screw diameter. For example, the above clearance is preferably 1/100 or more to 1/6 or less of the screw diameter, more preferably 1/100 or more to 1/10 or less, or 1/60 or more to 1/6 or less, particularly preferably 2/100 or more to 7/100 or less. Kneading segment (B) <Figure 2> The kneading segment (B) favorably used in the second invention of the application is a so-called double-thread type kneading disc and has two vertex portions (b) in the cross-sectional shape. Here, the vertex portion means a point or portion at the farthest distance from the center of gravity in the cross-section. Further, the segment is usually composed of plural discs and has a structure wherein the vertex portions adjacent each other are discontinuously twisted to the thickness direction. The direction of the twist can be the same or different relative to the rotary direction. When the discs that are adjacent together are twisted less than 90° to the contrary direction relative to the rotary direction in the direction of from the upstream side to the downstream side, they are sometimes called a feeding (forward feeding) kneading segment (BF), when twisted less than 90° to the samedirection, a returning (backward feeding) kneading segment (BR), and when twisted 90°, a neutral (orthogonal) kneading segment (BN). In the invention, in the viewpoint of carrying out effective kneading, the kneading segment (A) and kneading segment (B) are each preferably disposed at one or more places of the screw, more preferably disposed at two or more places. At that time, in the point of performing more effective kneading, it is preferable to dispose the kneading segment (B) at the downstream side of the kneading segment (A) without other mediate segment between them. In such a case, it is preferable to improve the kneading efficiency by disposing the returning kneading segment (BR) or neutral kneading segment (BN) to the downstream of the kneading segment (A) and thereby increasing the material to be kneaded that stays at the portion of the kneading segment (A). By the dynamic crosslinking using a twin screw extruder which has screws disposed with the kneading segments, an olefinic thermoplastic elastomer composition comprising the polyolefin resin and crosslinked rubber is obtained. The method can provide an olefinic thermoplastic elastomer composition which has an average number of fish eyes of 10 or less, by conducting the dynamic crosslinking, at the time of producing an olefinic thermoplastic elastomer composition comprising the polyolefin resin and crosslinked rubber through dynamic crosslinking with a twin screw extruder, under the conditions satisfying the following expression: Z/X 2.3 ≧ 0.01 wherein Z is a throughput (kg/h) of the twin screw extruder at a steady-state and X is a diameter (mm) of the screw of the extruder. Here, "steady-state" means a state in which the various conditions of the extruder have substantially become stable and a substantially homogeneous thermoplastic elastomer composition is being obtained. Concretely, in the method, it is preferable to use a twin screw extruder having the kneading segment (α) or kneading segment (A) as mentioned above in the first or the second aspect of the invention. Particularly, the maximum shearing velocity Y (sec -1 ) generated at the part of the kneading segment (α) or kneading segment (A) is preferably 10 to 10,000 sec -1 , morepreferably 100 to 2,000 sec -1 , furthermore preferably 200 to 1,000 sec -1 . In the present invention, that the rubber in an olefinic thermoplastic elastomer composition has been crosslinked means the case where the gel content measured by the following method is preferably in the range of 20 wt.% or more, more preferably 45 wt.% or more. [Measurement of gel content] A thermoplastic elastomer composition sample 100 mg is taken, cut into small pieces of 0.5mm × 0.5mm × 0.5mm, immersed in 30 ml cyclohexane in a closed container at 23 °C for 48 hours, then taken out on a filter paper and dried at room temperature for 72 hours or more until a constant weight is obtained. From the weight of the residue after drying there are subtracted the weights of all the cyclohexane insoluble components (fibrous filler, filler, pigment, etc.) other than the polymer component and the weight of the polyolefin resin in the sample before cyclohexane immersion. The value obtained thus is named "corrected final weight (Y)". On the other hand, the weight of the rubber in the sample is named "corrected initial weight (X)". The gel content is obtained by the following equation. Gel content [wt.%] = [corrected final weight (Y) / corrected initial weight (X)] × 100 According to the present invention, an olefinic thermoplastic elastomer composition excellent in tensile properties and appearance of moldings can be manufactured with good productivity. Since the olefinic thermoplastic elastomer composition produced in accordance with the invention has the above excellent characteristics, it can be used suitably for the interior skin materials of automobile such as instrumental panel, door, ceiling and seat; the exterior parts of automobile such as bumper, mud guard, side molding, window molding and roof molding; various sealing parts of automobile such as glass-run channel and weather strip; various gaskets and sealing parts in the field of earthwork and construction; and other daily needs. The present invention will be more particularly described, by way of example only, with reference to the accompanying drawings, in which:- In Fig.1, (1-A) is a transverse sectional view of the kneading segment (A) of the twin screw extruder, and (1-B) is a vertical sectional view of the kneading segment (A) of the same. In Fig.2, (BF) is a schematic illustration of the feeding (forward feeding) kneading segment, (BR) is that of the returning (backward feeding) kneading segment, and (BN) is that of the neutral (orthogonal) kneading segment. The direction of the resin flow is from this side of the paper to the opposite side. Fig. 3 illustrstes the screw arrangements used in Examples and Comparative examples. The drawing (a) shows a screw arrangement used in Example 1; (b), Comparative example 1; (c), Example 2 and Comparative example 5; (d), Comparative example 2; (e), Example 3 and Comparative example 4; and (f), Comparative example 3. Fig.4 is a drawing for explaining the measuring method of fish eyes. The meaning of each mark used in Figs. 1 to 4 is as follows. r: rotary direction of screw s: direction of resin flow c: clearance a1: portion twisted continuously to contrary direction relative to rotary direction of screw a2: portion twisted continuously to same direction relative to rotary direction of screw 1: first feeding port 2: second feeding port 3: vent port F: feeding (forward feeding) kneading segment R: returning (backward feeding) kneading segment N: neutral (orthogonal) kneading segment 4: press sheet 5: glass 6: fluorescent light The present invention is explained hereunder by way of examples, by which, however, the present invention is not limited. The measuring methods of physical properties which were carried out on olefinic thermoplastic elastomer compositions of Examples and Comparative examples were as follows. [Measuring method of physical properties] (1) Tensile strength: Tensile strength at break was measured according to JIS K6301 using a tensile speed of 200 mm/min. (2) Tensile elongation: Tensile elongation at break was measured according to JIS K6301 using a tensile speed of 200 mm/min. (3) Number of gel particle: A sheet press-formed at 190 °C (100×100×0.5 mm size) wasplacedonaglass and checked carefully with light shed from under with a scaled loupe about how many gel particles are present which are 0.3×0.1 mm or larger. (4) Measurement of fish eye: A press sheet sized in 100× 100×0.5 mm was prepared, placed on a glass of the box shown in Fig.4, and searched for fish eyes in the press sheet which were 0.3×0.1 mm or larger with a scaled loupe with light of fluorescent light being shed from under. The number of fish eyes was counted. The average number of fish eyes was determined on five samples taken every hour after one hour's lapse from the time when the steady-state had been reached, and they are shown in Table 1. (The average numbers were rounded to the nearest whole numbers.) (Example 1) 75 parts by weight of pellets of ethylene-propylene-5-ethylidene-2-norbornene copolymer rubber (R-1; Mooney viscosity ML 1+4 (100 °C) 94, ethylene/propylene molar ratio 78/22, iodine value 13), 25 parts by weight of pellets of propylene homopolymer 1 (MFR (ASTM D1238-65T, 230°C, load 2.16 kg) 11g/10min., density 0.91 g/cm 3 ), 0.2 part by weight of 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexane and 0.3 part by weight of divinylbenzene were thoroughly stirred and blended in a Henschel mixer, charged into a hopper of a twin screw extruder fitted with the screw shown in Fig. 3 (a) , and subjected to dynamic crosslinkig under the following conditions to manufacture pellets of a thermoplastic elastomer. Extruder: complete engaged type twin screw extruder (same rotary direction) Screw diameter: 46 mm Thickness of kneading segment (total of thickness of a1 and that of a2) : 108 mm L/D: 44 Temperature setting:C1/C2/C3/C4/C5/C6/C7/C8/C9/C10/C11/D =120/120/140/140/160/180/200/220/220/220/220/200 (°C) Number of revolution: 400 rpm Extrusion throughput: 100 kg/h The obtained pellets were press formed into a sheet at 190 °C, which was punched into specimens having a predetermined shape, and the physical properties were measured. The results are shown in Table 1. (Comparative Example 1) From the same raw materials and composition as in Example 1, pellets of a thermoplastic elastomer were produced using the same extruder as in Example 1 except for using the screw shown in Fig.3 (b) . The physical properties were measured in the same manner as Example 1. The results are shown in Table 1. (Example 2) Pellets 60 parts by weight of oil-extended ethylene-propylene-dicyclopentadiene copolymer rubber [R-2; Mooney viscosity ML 1+4 (100 °C) 70, ethylene/propylene molar ratio 79/21, iodine value 13, oil amount 40 parts by weight (paraffinic process oil made by Idemitsu Kosan Co., trade name: Diana Process PW-380)], pellets 25 parts by weight of propylene-ethylene block copolymer (MFR (ASTMD1238-65T, 230 °C, load 2.16 kg) 15 g/10 min., density 0.91 g/cm 3 , n-decane extraction amount 8.2% by weight), pellets 15 parts by weight of ethylene-1-hexene random copolymer (MFR (ASTM D1238-65T, 190 °C) 18 g/10 min., density 0.92 g/cm 3 , ethylene content 97 mol%), 0.2 part by weight of 2,5-dimethyl-2,5-di-(tert-butylperoxy)hexane and 0.3 part by weight of divinylbenzene were fully stirred and blended in a Henschel mixer, charged into a hopper of a twin screw extruder equipped with the screw shown in Fig.3 (c), and subjected to dynamic crosslinking under the following conditions to manufacture pellets of a thermoplastic elastomer. Extruder: complete engaged type twin screw extruder (same rotary direction) Screw diameter: 46 mm Thickness of kneading segment (total of thickness of a1 and that of a2): 108 mm L/D: 44 Temperature setting:C1/C2/C3/C4/C5/C6/C7/C8/C9/C10/C11/D =120/120/140/140/160/160/180/220/220/220/220/200 (°C) Number of revolution: 450 rpm Extrusion throughput: 90 kg/h Using the obtained pellets, measurement of physical properties was conducted in the same way as Example 1. The results are shown in Table 1. (Comparative Example 2) From the same raw materials and composition as in Example 2, pellets of a thermoplastic elastomer were produced using the same extruder as in Example 2 except for using the screw shown in Fig.3 (d). The physical properties were measured in the same manner as Example 1. The results are shown in Table 1. (Example 3) Pellets 70 parts by weight of an oil-extended product of ethylene-propylene-5-ethylidene-2-norbornene copolymer rubber [R-3; Mooney viscosity ML 1+4 (100 °C) 70, ethylene/propylene molar ratio 80/20, iodinevalue 11, oil amount 40 parts by weight (paraffinic process oil made by Idemitsu Kosan Co., trade name: Diana Process PW-380)], pellets 30 parts by weight of propylene homopolymer 2 (MFR (ASTM D1238-65T, 230 °C, load 2.16 kg) 2 g/10 min., density 0.91 g/cm 3 ) and 0.2 part by weight of N,N'-m-phenylenebismaleimide were fully stirred and blended in a Henschel mixer, charged into a hopper of a twin screw extruder equipped with the screw shown in Fig.3 (e) and fed at 120 kg/h to the first feeding port of the extruder. 2,5-Dimethyl-2,5-di-(tert-butylperoxy)hexane diluted to 30% by weight with a softening agent (paraffinic process oil made by Idemitsu Kosan Co., trade name: Diana Process PW-380) was fed to the second feeding port at 240 g/h, and the mixture was subjected to dynamic crosslinking under the following conditions to prepare pellets of a thermoplastic elastomer. Extruder: complete engaged type twin screw extruder (same rotary direction) Screw diameter: 46 mm Thickness of kneading segment (total of thickness of a1 and that of a2): 108 mm L/D: 44 Temperature setting:C1/C2/C3/C4/C5/C6/C7/C8/C9/C10/C11/D =120/120/140/140/160/160/180/220/220/220/220/200 (°C) Number of revolution: 350 rpm Extrusion throughput: 120 kg/h Using the obtained pellets, measurement of physical properties was conducted in the same way as Example 1. The results are shown in Table 1. (Comparative Example 3) Method described in JP-A-9-095540 From the same raw materials and composition as in Example 3, pellets of a thermoplastic elastomer were produced using the same extruder as in Example 3 except for using the screw shown in Fig.3 (f). The physical properties were measured in the same manner as Example 1. The results are shown in Table 1. (Comparative Example 4) From the same raw materials and composition as in Example 3, pellets of a thermoplastic elastomer were produced using the same extruder as in Example 3 provided that the operation conditions of the extruder were as shown in Table 1. The physical properties were measured in the same manner as Example 1. The results are shown in Table 1. (Screw revolution: 150 rpm) (Comparative Example 5) From the same raw materials and composition as in Example 2, pellets of a thermoplastic elastomer were produced using the same extruder as in Example 2 provided that the operation conditions of the extruder were as shown in Table 1. The physical properties were measured in the same manner as Example 1. The results are shown in Table 1. (Screw revolution: 540 rpm)

Claims: A method for manufacturing an olefinic thermoplastic elastomer composition comprising a polyolefin resin and a crosslinked rubber by dynamic crosslinking with a twin screw extruder characterized in that , a first kneading segment (A) is disposed at least at one place of the screw which first kneading segment (A) has the following features: A1) the first kneading segment having three vertex portions in the cross-section, the vertex portion being a point or portion at the farthest distance from the center of gravity in the cross-section, A2) the vertex portion of the first kneading segment being composed of a first portion (a1) continuously twisted to the contrary direction relative to the screw rotary direction and a second portion (a2) continuously twisted to the same direction relative to the screw rotary direction, respectively to the thickness direction, and A3) the sum of the thickness of said first portion (a1) and that of said second portion (a2) being 1.0 times or more of the screw diameter. A manufacturing method according to claim 1, wherein there is used a screw disposed with said first kneading segment (A) at least at one place and disposed with a second kneading segment (B) at least at one place having the following features: B1) the second kneading segment having two vertex portions in the cross-section, the vertex portion being a point or portion at the farthest distance from the center of gravity in the cross-section, and B2) the vertex portion of the second kneading segment having a structure twisted discontinuously to the thickness direction. A manufacturing method according to claim 2, wherein there is used a screw that has a structure disposed with the second kneading segment (B) on the downstream side of the first kneading segment (A) and with said first and second kneading segments being adjacent. A manufacturing method according to claim 3, wherein there is used a screw that is disposed with a combination of the first and second kneading segments (A) and (B) at least at two places, in which combination the second kneading segment (B) is disposed on the downstream side of the first kneading segment (A) with said first and second kneading segments being adjacent. A manufacturing method according to any one of claims 1 to 4, wherein the clearance between the vertex portion of the first kneading segment (A) and the inner wall of the extruder cylinder is 1/100 or more to 1/6 or less of the screw diameter. A manufacturing method according to any one of claims 2 to 4, wherein a ratio of the clearance between the vertex portion of the second kneading segment (B) and the inner wall of the extruder cylinder to the screw diameter is less than 1/60. A manufacturing method according to claim 5, wherein a second kneading segment (B) is disposed downstream of the first kneading segment (A) which second segment (B) has a ratio of the clearance between the vertex portion of the kneading segment, the vertex portion being a point or portion at the farthest distance from the center of gravity in the cross-section, and the cylinder inner wall of the extruder to the screw diameter which ratio is smaller than said ratio concerning said kneading segment (A). A manufacturing method according to any one of claims 5 to 7, wherein the clearance between the vertex portion of the kneading segment (A) and the cylinder inner wall of the extruder is 1/60 or more to 1/10 or less of the screw diameter. A manufacturing method according to claim 7, wherein a ratio of the clearance between the vertex portion of the second kneading segment (B) and the cylinder inner wall of the extruder to the screw diameter is less than 1/60. A manufacturing method according to any one of claims 1 to 9, wherein at least one of the upstream barrel of the twin screw extruder is set to a temperature of 170°C or lower and at least one of the downstream barrel is set to a temperature of 190°C or higher. A manufacturing method according to any one of claims 1 to 10, wherein the dynamic crosslinking is conducted under the conditions satisfying the following expression: 4.5 < 2.2 logX + logY - logZ + (T-180) ÷ 100 < 6.0 wherein T is a resin temperature ( °C) at the die outlet of the twin screw extruder, X is a screw diameter (mm) of the extruder, Y is a maximum shearing velocity (sec -1 ) generated at the part of the first kneading segment (A) in the extruder and Z is an extrusion throughput (kg/h) of the extruder, and said maximum shearing velocity Y (sec -1 ) is determined from the equation Y=(X x π xS )/U wherein X is a screw diameter (mm) of the twin screw extruder, S is a number of screw revolution per second (rps) and U is a distance (mm) of the narrowest portion of the clearance between the barrel inner wall and the kneading segment of the screw. A manufacturing method according to any one of claims 1 to 11, wherein the dynamic crosslinking is conducted under the conditions satisfying the following expression: Z/X 2.3 ≥ 0.01 wherein Z is a throughput (kg/h) of the twin screw extruder at a steady state and X is a screw diameter (mm) of the twin screw extruder.

Inventors: ITOH YUICHI, UCHIYAMA AKIRA, ITOH, YUICHI, UCHIYAMA, AKIRA
Applicants: MITSUI CHEMICALS INC, MITSUI CHEMICALS, INC.
Application year: 2001
Main classification: B29C47
IPC codes: B29C47, C08J3