[0001]The present invention relates to an olefin-based polymer composition and a molded product obtained from the composition. More specifically, the present invention has an olefin-based weight that is excellent in surface appearance, mechanical strength, and oil resistance even during injection molding. Concerning coalescing compositions.
Background technology
[0002]
　Thermoplastic elastomers are lightweight and easy to recycle, so they are widely used as energy-saving and resource-saving elastomers, especially as a substitute for vulcanized rubber, in automobile parts, industrial machine parts, electrical / electronic parts, building materials, etc. There is.
[0003]
　Among them, the olefin-based thermoplastic elastomer uses ethylene / propylene / non-conjugated diene copolymer (EPDM) and crystalline polyolefin such as polypropylene as raw materials, and therefore has a lighter specific gravity and heat resistance than other thermoplastic elastomers. Since it has excellent durability such as aging resistance and weather resistance, it is used in a wide range of applications by various molding methods.
[0004]
　Patent Document 1 describes that an elastoplastic composition composed of a polyolefin resin and EPDM rubber vulcanized with a phenol resin-based vulcanizing agent is a tough and strong elastomer composition that can be processed as a thermoplastic. It is also stated that it can be processed to the extent that an article can be formed from it by extrusion, injection molding, blow molding, thermal molding, or the like.
Prior art literature
Patent documents
[0005]
Patent Document 1: Japanese Unexamined Patent Publication No. 54-99156
Outline of the invention
Problems to be solved by the invention
[0006]
　The composition of the polyolefin resin and EPDM obtained by using the above-mentioned phenol resin-based cross-linking agent is excellent in oil resistance, mechanical strength, etc., and can be processed by various molding methods. On the other hand, when trying to obtain a molded body by injection molding, a pin gate may be adopted as the gate of the mold because the gate mark is small and there is an advantage that a large number of pieces can be taken.
[0007]
　However, when the composition obtained by using a phenol resin-based cross-linking agent is molded by injection molding using a mold having a pin gate, the surface of the molded product is inferior, and if it is a black molded product, it will be whitened. It has become clear that there are cases. It has also been found that this tendency is particularly remarkable in the case of low hardness to medium hardness in which the proportion of EPDM in the composition is relatively high.
[0008]
　An object of the present invention is to provide a thermoplastic crosslinked composition having excellent mechanical strength, oil resistance, and injection moldability.
Means to solve problems
[0009]
　The gist of the present invention is as follows.
(1) Containing a structural unit derived from ethylene, a structural unit derived from α-olefin having 3 to 20 carbon atoms, and a structural unit derived from a non-conjugated polymer, and (a-1) Mooney viscosity ML1 + 4 (125 ° C.). The following requirements (b-1) and (b-2):
(b-1) MFR (230 ° C., 2.16 kg load) are satisfied with respect to 100 parts by mass of the component derived from the copolymer (A) of 50 to 200. 0.1 to 4 g / 10 minutes,
(b-2)
One or more crystalline propylene-based polymers (B) having a melting point (Tm) of 100 to 200 ° C. measured by DSC , totaling 10 to 50 parts by mass. , The following
requirements (c-1) and (c-2):
(c-1) MFR (230 ° C., 2.16 kg load) is 5 to 15 g / 10 minutes,
(c-2) melting point (Tm) measured by DSC. ) Is
one or more of crystalline propylene-based polymers (C) satisfying 100 to 200 ° C. , totaling 5 to 30 parts by mass, and the following
requirements (d-1):
(d-1) Measured by gel permeation chromatography. It
contains 4 to 18 parts by mass of a low molecular weight polyolefin (D) having a number average molecular weight of 3000 to 10000 ,
and at least a part of the components derived from the copolymer (A) is made of a phenol resin-based cross-linking agent (E). A crosslinked olefin polymer composition.
(2) The low molecular weight polyolefin (D) further requires the following requirements (d-2):
(D-2)
The olefin-based polymer composition according to (1) above, wherein the heat of fusion measured by DSC satisfies 20 J / g or more .
(3) The olefin-based polymer composition according to (1) or (2) above, wherein the olefin-based polymer composition further contains 90 to 150 parts by mass of a component derived from the softening agent (F).
(4) The olefin-based polymer composition according to any one of (1) to (3) above, wherein the MFR (230 ° C., 10 kg load) of the olefin-based polymer composition is 5 to 150 g / 10 minutes.
(5) The total of the component (B), the component (C) and the low molecular weight polyolefin (D) is 20 to 80 parts by mass with respect to 100 parts by mass of the component derived from the copolymer (A) (1) to (4). ). The olefin-based polymer composition according to any one of.
(6) The olefin-based polymer composition according to any one of (1) to (5), wherein the shore A hardness (instantaneous value) measured in accordance with JIS K6253 of the olefin-based polymer composition is 50 to 80. thing.
(7) A molded product obtained from the olefin-based polymer composition according to any one of (1) to (6) above.
(8) The molded product according to (7) above, which is an injection molded product.
The invention's effect
[0010]
　According to the present invention, it is possible to provide a thermoplastic crosslinked composition having excellent mechanical strength, oil resistance, and injection moldability.
Mode for carrying out the invention
[0011]
　The polymer composition of the present invention is a polymer containing at least (i) a structural unit derived from ethylene, a structural unit derived from an α-olefin having 3 to 20 carbon atoms, and a structural unit derived from non-conjugated polyene. It is composed of a component derived from A), (ii) a crystalline propylene polymer (B), (iii) a crystalline propylene polymer (C), and (iv) a low molecular weight polyolefin (D).
[0012]
　In the present invention, "components derived" such as "copolymer (A) containing a constituent unit derived from ethylene, a constituent unit derived from an α-olefin having 3 to 20 carbon atoms, and a constituent unit derived from a non-conjugated polyene". Represents a component obtained by using the copolymer (A) or the like as a raw material.
[0013]
　 Ethylene / α-olefin / non-conjugated polyene copolymer (A) having 3 to 20 carbon atoms used in the present invention (present The copolymer (A) in the invention) is a structural unit derived from ethylene, a structural unit derived from at least one α-olefin having 3 to 20 carbon atoms, and a structural unit derived from at least one non-conjugated polyene. It is an ethylene / α-olefin / non-conjugated polyene copolymer containing, and has a Mooney viscosity of ML1 + 4 (125 ° C.) of 50 to 200.
[0014]
　Examples of the α-olefin having 3 to 20 carbon atoms include propylene (3 carbon atoms), 1-butene (4 carbon atoms), 1-nonene (9 carbon atoms), 1-decene (10 carbon atoms), and 1-nonadecene (10 carbon atoms). Linear α-olefin without side chain such as 19) carbon number, 1-eicosene (20 carbon number); 4-methyl-1-pentene, 9-methyl-1-decene, 11-methyl having side chain Examples thereof include α-olefins having side chains such as -1-dodecene and 12-ethyl-1-tetradecene. These α-olefins may be used alone or in combination of two or more. Among these, α-olefins having 3 to 10 carbon atoms are preferable, and propylene, 1-butene, 1-hexene, and 1-octene are more preferable. These α-olefins may be used alone or in combination of two or more.
[0015]
　Non-conjugated polyenes include chains of 1,4-hexadiene, 1,6-octadien, 2-methyl-1,5-hexadiene, 6-methyl-1,5-heptadiene, 7-methyl-1,6-octadene and the like. Non-conjugated diene; cyclohexadiene, dicyclopentadiene, methyltetrahydroinden, 5-vinyl-2-norbornene, 5-ethylidene-2-norbornene, 5-methylene-2-norbornene, 5-isopropylidene-2-norbornene, 6 Cyclic non-conjugated diene such as -chloromethyl-5-isopropenyl-2-norbornene; 2,3-diisopropylidene-5-norbornene, 2-ethylidene-3-isopropylidene-5-norbornene, 2-propenyl-2, 5-norbornene, 1,3,7-octatriene, 1,4,9-decatorien, 4,8-dimethyl-1,4,5-decatorien, 4-ethylidene-8-methyl-1,7-nonadien, etc. Examples include trien. These non-conjugated polyenes may be used alone or in combination of two or more. Among these, a mixture of cyclic non-conjugated diene such as 1,4-hexadiene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene, 5-ethylidene-2-norbornene and 5-vinyl-2-norbornene Preferably, 5-ethylidene-2-norbornene and 5-vinyl-2-norbornene are more preferable.
[0016]
　Examples of the copolymer (A) include ethylene / 1-butene / 1,4-hexadiene copolymer, ethylene / 1-pentene / 1,4-hexadene copolymer, ethylene / 1-hexene / 1,4-hexaziene. Copolymers, ethylene / 1-heptene / 1,4-hexadene copolymers, ethylene / 1-octene / 1,4-hexadene copolymers, ethylene / 1-nonene / 1,4-hexaziene copolymers, Ethylidene 1-decene 1,4-hexadiene copolymer, ethylene 1-butene 1-octene 1,4-hexadiene copolymer, ethylene 1-butene 5-ethylidene-2-norbornene copolymer , Ethylidene 1-pentene / 5-ethylidene-2-norbornene copolymer, ethylene / 1-hexene / 5-ethylidene-2-norbornene copolymer, ethylene / 1-hepten / 5-ethylidene-2-norbornene Polymers, ethylene / 1-octene / 5-ethylidene-2-norbornene copolymer, ethylene / 1-nonene / 5-ethylidene-2-norbornene copolymer, ethylene / 1-decene / 5-ethylidene-2-norbornene Copolymers, ethylene / 1-butene / 1-octene / 5-ethylidene-2-norbornene copolymers, ethylene / 1-butene / 5-ethylidene-2-norbornene / 5-vinyl-2-norbornene copolymers, Ethylidene, 1-pentene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene copolymer, ethylene, 1-hexene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene copolymer, Ethylidene 1-hepten 5-ethylidene-2-norbornene 5-vinyl-2-norbornene copolymer, ethylene 1-octene 5-ethylidene-2-norbornene 5-vinyl-2-norbornene copolymer , Ethylidene 1-nonene 5-ethylidene-2-norbornene 5-vinyl-2-norbornene copolymer, ethylene 1-decene-5-ethylidene-2-norbornene 5-vinyl-2-norbornene copolymer , Ethylidene, 1-butene, 1-octene, 5-ethylidene-2-Examples thereof include norbornene / 5-vinyl-2-norbornene copolymer.
[0017]
　The copolymer (A) may be used alone or in combination of two or more.
[0018]
　The ethylene / α-olefin / non-conjugated polyene copolymer (A) having 3 to 20 carbon atoms has an ethylene / α-olefin ratio, that is, an ethylene-derived structural unit [A] and an α-olefin-derived structural unit. The molar ratio [[A] / [B]] with [B] is in the range of 40/60 to 90/10. The lower limit of the molar ratio [A] / [B] is preferably 45/55, more preferably 50/50, and particularly preferably 55/45. The upper limit of the molar ratio [A] / [B] is preferably 80/20, more preferably 75/25.
[0019]
　The copolymer (A) has a Mooney viscosity ML1 + 4 (125 ° C.) at 125 ° C. obtained by measuring according to JIS K6300 (1994) of 50 to 200, preferably 60 to 200, and more preferably 100. It is in the range of ~ 200. If the Mooney viscosity is less than 50, the mechanical strength and heat resistance are inferior, and if it exceeds 200, the moldability of the thermoplastic elastomer deteriorates.
[0020]
　The iodine value of the copolymer (A) is usually 2 to 50 g / 100 g, preferably 5 to 40 g / 100 g, and more preferably 7 to 30 g / 100 g. If the iodine value falls below this range, the shape recovery property at high temperature deteriorates, and if it exceeds this range, the moldability deteriorates.
[0021]
　The content of the structural unit [C] derived from the non-conjugated polyene of the copolymer (A) is preferably 100 mol% based on the total of the structural units of [A], [B] and [C]. Range of 0.1-6.0 mol%, more preferably 0.5-4.0 mol%, even more preferably 0.5-3.5 mol%, particularly preferably 0.5-3.0 mol% It is in. When the content of the structural unit [C] derived from the non-conjugated polyene is within the above range, an ethylene-based copolymer having sufficient crosslinkability and flexibility tends to be obtained.
[0022]
　The copolymer can be used, for example, in "Polymer Manufacturing Process (Kogyo Chosakai Co., Ltd., published p.309-330)" or JP-A-9-71617 and JP-A-9-71618 according to the application of the applicant of the present application. , JP-A-9-208615, JP-A-10-67823, JP-A-10-67824, JP-A-10-110054, WO2009 / 081792 pamphlet, WO2009 / 081794 pamphlet, etc. It can be manufactured by such a method.
[0023]
　Examples of the olefin polymerization catalyst preferably used in the production of the ethylene / α-olefin / non-conjugated polyene copolymer (A) used in the present invention include vanadium (V), zirconium (Zr), and titanium (Ti). ) And other known transition metal compounds and organic aluminum compounds (organic aluminum oxy compounds); transition metal metallocene compounds selected from Group 4 of the periodic table of elements, and organic aluminum oxy compounds or ionized ions. A known metallocene catalyst composed of a sex compound, for example, a metallocene catalyst described in JP-A-9-40586; a known metallocene catalyst composed of a specific transition metal compound and a cocatalyst such as a boron compound, for example, WO2009 / The metallocene catalyst described in Pamphlet No. 072553; a transition metal compound catalyst comprising a specific transition metal compound and an organic metal compound, an organic aluminum oxy compound or a compound that reacts with the transition metal compound to form an ion pair, for example. Transition metal compound catalysts described in JP-A-2011-52231; Examples thereof include catalysts described in JP-A-2010-241897. It can also be produced using the catalyst described in WO 2016/152711 pamphlet. In particular, the use of a metallocene catalyst is particularly preferable because the distribution of diene becomes uniform and high cross-linking efficiency can be obtained even if the introduction of diene is small, and the chlorine content derived from the catalyst can be reduced due to the high catalytic activity.
[0024]
　 As the crystalline propylene polymer (B)
　used in the present invention, for example, propylene alone or propylene and one or more other monoolefins may be used by a high pressure method or a low pressure method. Examples thereof include crystalline high-molecular-weight solid products obtained by polymerization by the method. Examples of such a polymer include an isotactic monoolefin polymer and a syndiotactic monoolefin polymer.
[0025]
　The crystalline propylene-based polymer (B) may be obtained by synthesizing it by a conventionally known method, or a commercially available product may be used.
[0026]
　The crystalline propylene-based polymer (B) may be used alone or in combination of two or more.
[0027]
　Suitable raw material olefins other than propylene of the crystalline propylene-based polymer (B) are preferably α-olefins having 2 or 4 to 20 carbon atoms, specifically, ethylene, 1-butene, 1-pentene, 1 -Hexene, 1-octene, 1-decene, 2-methyl-1-propene, 3-methyl-1-pentene, 4-methyl-1-pentene, 5-methyl-1-hexene and the like can be mentioned. When these α-olefins having 2 or 4 to 20 carbon atoms are used, one type or two or more types may be used. The polymerization mode may be a random type or a block type as long as a resinous material is obtained. These propylene-based polymers may be used alone or in combination of two or more.
[0028]
　The crystalline propylene-based polymer (B) used in the present invention is preferably a propylene-based polymer having a propylene content of 51 mol% or more when the total constituent units are 100 mol%.
[0029]
　Among these propylene-based polymers, propylene homopolymers, propylene / ethylene block copolymers, propylene / ethylene random copolymers, propylene / ethylene / butene random copolymers, and the like are particularly preferable.
[0030]
　The crystalline propylene polymer (B) has an MFR (ASTM D1238-65T; 230 ° C., 2.16 kg load) of 0.1 to 4 g / 10 minutes, preferably 0.5 to 3 g / 10 minutes. .. When the MFR of the crystalline propylene-based polymer (B) is less than 0.1 g / 10 minutes, the fluidity of the polymer composition decreases, and when it exceeds 4 g / 10 minutes, the mechanical strength of the polymer composition increases. descend.
[0031]
　The crystalline propylene-based polymer (B) has a melting point (Tm) measured by differential scanning calorimetry (DSC) of 100 to 200 ° C., preferably 130 to 200 ° C., and more preferably 130 to 180 ° C. .. If the melting point (Tm) is less than 100 ° C., the oil resistance and heat resistance of the polymer composition are lowered, and if it exceeds 200 ° C., the components derived from the copolymer (A) are dispersed in the polymer composition. Sex gets worse.
[0032]
　The crystalline propylene-based polymer (B) plays a role of improving the mechanical properties of the polymer composition.
[0033]
　The blending amount of the crystalline propylene-based polymer (B) is 10 to 50 parts by mass with respect to 100 parts by mass of the component derived from the copolymer (A) from the viewpoint of rubber elasticity and mechanical strength of the polymer composition. , Preferably 15 to 45 parts by mass. If the blending amount of the crystalline propylene-based polymer (B) is less than 10 parts by mass, the mechanical strength of the polymer composition decreases, and if it exceeds 50 parts by mass, the rubber elasticity of the polymer composition decreases.
[0034]
　
　The crystalline propylene-based polymer (C) used in the present invention is propylene alone, or propylene and one or more other monoolefins by a high-pressure method or a low-pressure method. It consists of a crystalline high molecular weight solid product obtained by polymerization. Examples of such a polymer include an isotactic monoolefin polymer and a syndiotactic monoolefin polymer.
[0035]
　The crystalline propylene-based polymer (C) may be obtained by synthesizing it by a conventionally known method, or a commercially available product may be used.
[0036]
　The crystalline propylene-based polymer (C) may be used alone or in combination of two or more.
[0037]
　Suitable raw material olefins other than propylene of the crystalline propylene-based polymer (C) are preferably α-olefins having 2 or 4 to 20 carbon atoms, specifically, ethylene, 1-butene, 1-pentene, 1 -Hexene, 1-octene, 1-decene, 2-methyl-1-propene, 3-methyl-1-pentene, 4-methyl-1-pentene, 5-methyl-1-hexene and the like can be mentioned. When these α-olefins having 2 or 4 to 20 carbon atoms are used, one type or two or more types may be used. The polymerization mode may be a random type or a block type as long as a resinous material is obtained. These propylene-based polymers may be used alone or in combination of two or more.
[0038]
　The crystalline propylene-based polymer (C) used in the present invention is preferably a propylene-based polymer having a propylene content of 51 mol% or more when the total constituent units are 100 mol%.
[0039]
　Among these propylene-based polymers, propylene homopolymers, propylene / ethylene block copolymers, propylene / ethylene random copolymers, propylene / ethylene / butene random copolymers, and the like are particularly preferable.
[0040]
　The crystalline propylene polymer (C) has an MFR (ASTM D1238-65T; 230 ° C., 2.16 kg load) of 5 to 15 g / 10 minutes, preferably 7 to 13 g / 10 minutes. If the MFR of the crystalline propylene-based polymer (C) is less than 5 g / 10 minutes, the molded appearance of the polymer composition deteriorates, and if it exceeds 15 g / 10 minutes, the mechanical strength of the polymer composition decreases. ..
[0041]
　The total MFR of the crystalline propylene-based polymer (B) and the crystalline propylene-based polymer (C) is as follows:
(x / 100) × log (MFR (B)) + (y / 100) × log ( MFR (C)) = (100/100) × logMFR
(In the formula, x is the crystalline propylene-based polymer (C) with respect to the total of the crystalline propylene-based polymer (B) and the crystalline propylene-based polymer (C). The mass fraction of B), y is the mass fraction of the crystalline propylene-based polymer (C) with respect to the total of the crystalline propylene-based polymer (B) and the crystalline propylene-based polymer (C), MFR (B). Was obtained with the MFR of the crystalline propylene-based polymer (B), MFR (C) was obtained with the MFR of the crystalline propylene-based polymer (C), and MFR was obtained with ASTM D1238-65T (230 ° C., 2.16 kg load). In
the present invention, the total MFR is preferably 1 to 9, and is preferably 1 to 6, from the viewpoint of the molded appearance and mechanical properties of the polymer composition. Is even more preferable.
[0042]
　The crystalline propylene-based polymer (C) has a melting point (Tm) measured by differential scanning calorimetry (DSC) of 100 to 200 ° C., preferably 130 to 200 ° C., and more preferably 130 to 180 ° C. .. If the melting point (Tm) is less than 100 ° C., the oil resistance and heat resistance of the polymer composition are lowered, and if it exceeds 200 ° C., the components derived from the copolymer (A) are dispersed in the polymer composition. Sex gets worse.
[0043]
　The crystalline propylene-based polymer (C) plays a role of improving the molded appearance of the polymer composition.
[0044]
　The blending amount of the crystalline propylene-based polymer (C) is 5 to 30 parts by mass with respect to 100 parts by mass of the component derived from the copolymer (A) from the viewpoint of rubber elasticity and molded appearance of the polymer composition. , Preferably 5 to 20 parts by mass. If the blending amount of the crystalline propylene-based polymer (C) is less than 5 parts by mass, the molded appearance of the polymer composition deteriorates, and if it exceeds 30 parts by mass, the mechanical properties of the polymer composition deteriorate.
[0045]
　
　The low molecular weight polyolefin (D) used in the present invention is a polyolefin having a polypropylene equivalent number average molecular weight (Mn) of 3000 to 10000 measured by gel permeation chromatography (GPC method). Those containing no non-conjugated polyene are preferable, and polyethylene wax, polypropylene wax, and more preferably polypropylene wax are preferable. Especially in the case of polypropylene wax, the composition has excellent oil resistance.
[0046]
　The polyethylene wax used in the present invention may be obtained by directly polymerizing ethylene alone or by directly polymerizing ethylene and α-olefin, or is obtained by thermally decomposing high molecular weight polyethylene. You may. Preferred polyethylene waxes are directly polymerized. Further, the polyethylene wax may be purified by a method such as solvent separation in which the wax is separated by the difference in solubility in a solvent, or molecular distillation in which the wax is separated by the difference in boiling point. Examples of preferable polyethylene wax are described in, for example, Japanese Patent Application Laid-Open No. 2009-144146, but will be briefly described below.
[0047]
　The polyethylene wax used in the present invention is, for example, a homopolymer of ethylene or a copolymer of ethylene and an α-olefin. Examples of this α-olefin include α-olefins having 3 to 20 carbon atoms, preferably 3 to 10 carbon atoms. Specific examples of α-olefins include propylene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-octene and the like; preferably propylene, 1-butene, 1-. Includes hexene, 4-methyl-1-pentene.
[0048]
　The proportion of ethylene-derived constituent units in the total constituent units of polyethylene wax is usually 60 to 100% by mass, preferably 70 to 100% by mass.
[0049]
　The density of the polyethylene wax measured according to the density gradient tube method of JIS K7112 (1999) is preferably 890 to 980 kg / m 3 , and more preferably 900 to 980 kg / m 3 .
[0050]
　The density of the polyethylene wax is controlled, for example, by adjusting the ratio of α-olefin to ethylene and selecting the type of α-olefin when the polyethylene wax is a copolymer of ethylene and α-olefin. Can be done. For example, the density of polyethylene wax can be reduced by increasing the amount of α-olefin used with respect to ethylene. The density of the polyethylene wax can also be adjusted by the polymerization temperature in production.
[0051]
　The polyethylene equivalent number average molecular weight (Mn) of the polyethylene wax measured by gel permeation chromatography is 3000 to 10000, preferably 4000 to 9000, and more preferably 5000 to 9000.
[0052]
　If the number average molecular weight (Mn) of the polyethylene wax is less than 3000, the mechanical properties are deteriorated, and if it exceeds 10,000, the molded appearance is deteriorated.
[0053]
　The number average molecular weight (Mn) of the polyethylene wax can be adjusted, for example, by the polymerization temperature in production.
[0054]
　The polyethylene-equivalent weight average molecular weight (Mw) of the polyethylene wax measured by gel permeation chromatography is preferably 10,000 to 30,000, more preferably 15,000 to 30,000.
[0055]
　The melt viscosity of the polyethylene wax at 140 ° C. is preferably 3000 to 9000 mPa · s, more preferably 5000 to 9000 mPa · s. The melt viscosity of the polyethylene wax can be measured by, for example, a Brookfield viscometer, a strain-controlled or stress-controlled rheometer.
[0056]
　The melting point (Tm) of the polyethylene wax measured by DSC is preferably 60 to 150 ° C., more preferably 100 to 180 ° C. from the viewpoint of heat resistance.
[0057]
　The calorific value of melting measured by DSC of polyethylene wax is preferably 20 J / g or more, more preferably 40 J / g or more, still more preferably 40 to 150 J / g, and particularly preferably 50 to 120 J / g from the viewpoint of oil resistance. Is.
[0058]
　The polypropylene wax used in the present invention is a propylene homopolymer obtained by copolymerizing propylene with another monomer, if necessary, in the presence of a steric specific catalyst, or a propylene-based polypropylene wax. It may be a polymer, or it may be obtained by thermally decomposing high molecular weight polypropylene. The polypropylene wax may be purified by a method such as solvent separation in which the wax is separated by the difference in solubility in a solvent, or molecular distillation in which the wax is separated by the difference in boiling point. Examples of other monomers include ethylene, 1-butene, 1,3-butadiene, 1-hexene, 3-hexene, 1-octene, 4-octene and the like.
[0059]
　As the polypropylene wax used in the present invention, polypropylene having a propylene content of 90% by mass or more is preferable from the viewpoint of heat resistance.
[0060]
　The density of polypropylene wax measured according to the density gradient tube method of JIS K7112 is preferably 900 to 910 kg / m 3 .
[0061]
　The polypropylene equivalent number average molecular weight (Mn) of polypropylene wax measured by gel permeation chromatography is 3000 to 10000, preferably 4000 to 9000, and more preferably 5000 to 9000.
[0062]
　If the number average molecular weight (Mn) of the polypropylene wax is less than 3000, the mechanical properties are deteriorated, and if it exceeds 10,000, the molded appearance is deteriorated.
[0063]
　The number average molecular weight (Mn) of polypropylene wax can be adjusted, for example, by the polymerization temperature in production.
[0064]
　The polypropylene-equivalent mass average molecular weight (Mw) of the polypropylene wax measured by gel permeation chromatography is preferably 10,000 to 30,000, more preferably 15,000 to 30,000.
[0065]
　The melt viscosity of the polypropylene wax at 180 ° C. is preferably 300 to 1500 mPa · s, more preferably 500 to 1000 mPa · s. The melt viscosity of polypropylene wax can be measured by, for example, a Brookfield viscometer, a strain-controlled or stress-controlled rheometer.
[0066]
　The melting point (Tm) of the polypropylene wax measured by DSC is preferably 60 to 180 ° C., more preferably 100 to 180 ° C. from the viewpoint of heat resistance.
[0067]
　The calorific value of melting measured by DSC of polypropylene wax is preferably 20 J / g or more, more preferably 30 to 140 J / g, and further preferably 50 to 120 J / g from the viewpoint of oil resistance.
[0068]
　In the olefin-based polymer composition of the present invention, the total of the component (B), the component (C) and the low molecular weight polyolefin (D) is the sum of 100 parts by mass of the component derived from the copolymer (A) from the viewpoint of molded appearance. It is preferably 20 to 80 parts by mass, and more preferably 20 to 70 parts by mass.
[0069]
　 In the
　present invention, the phenol resin-based cross-linking agent (E) is used as the cross-linking agent.
　The phenol resin-based cross-linking agent (E) (also referred to as the cross-linking agent (E) in the present invention) is a resol resin, which is a condensation of an alkyl-substituted phenol or an unsubstituted phenol with an aldehyde in an alkaline medium, preferably with formaldehyde. , Or it is also preferable to be produced by condensation of bifunctional phenol dialcohols. The alkyl-substituted phenol is preferably an alkyl group substituted product having 1 to 10 carbon atoms. Further, dimethylolphenols or phenol resins substituted with an alkyl group having 1 to 10 carbon atoms at the p-position are preferable. The phenol resin-based cured resin is typically a heat-crosslinkable resin, and is also called a phenol resin-based cross-linking agent or a phenol resin.
[0070]
　Examples of the phenol resin-based cured resin (phenol resin-based cross-linking agent) include the following general formula (I).
[0071]
[Chemical formula 1]

(In the formula, Q is, -CH 2 - and -CH 2 -O-CH 2 - is a bivalent group selected from the group consisting of, m is 0 or 1 to 20 positive integers Yes, R'is an organic group).
[0072]
　Preferably, Q is a divalent radical -CH 2 -O-CH 2 - and is, m is 0 or a positive integer of 1 ~ 10, R 'is an organic radical having less than 20 carbon atoms. More preferably, m is 0 or a positive integer of 1-5 and R'is an organic group having 4-12 carbon atoms. Specific examples thereof include an alkylphenol formaldehyde resin, a methylolated alkylphenol resin, a halogenated alkylphenol resin, and the like, preferably a halogenated alkylphenol resin, and more preferably a terminal hydroxyl group brominated. An example of a phenol resin-based cured resin having a brominated terminal is shown in the following general formula (II).
[0073]
[Chemical

formula 2] (In the formula, n is an integer of 0 to 10 and R is a saturated hydrocarbon group having 1 to 15 carbon atoms.)
[0074]
　Examples of the phenol resin-based cured resin products include Tackylol (registered trademark) 201 (alkylphenol formaldehyde resin, manufactured by Taoka Chemical Industry Co., Ltd.) and Tuckylol (registered trademark) 250-I (bromination rate of 4%). Alkylphenol formaldehyde resin, manufactured by Taoka Chemical Industry Co., Ltd.), Tackiroll (registered trademark) 250-III (brominated alkylphenol formaldehyde resin, manufactured by Taoka Chemical Industry Co., Ltd.), PR-4507 (Gunei Chemical Industry Co., Ltd.) Vulkarest 510E (Hoechst), Vulkarest 532E (Hoechst), Vulkalesen E (Hoechst), Vulkalesen105E (Hoechst), Vulkaresen130E (Hoechst), Vulkaresen130E (Hoechst) (Manufactured by Rohm & Haas), Sumilite Resin (registered trademark) PR-22193 (manufactured by Sumitomo Durez Co., Ltd.), Symphon-C-100 (manufactured by Anchor Chem.), Symphon-C-1001 (manufactured by Archor Chem.) ), Tamanol (registered trademark) 531 (manufactured by Arakawa Chemical Co., Ltd.), Spectady SP1059 (manufactured by Spectady Chem.), Spectady SP1045 (manufactured by Spectady Chem.), CRR-0803 (manufactured by UCC). , Chemical SP1055F (Chemistry Chem., Brominated alkylphenol formaldehyde resin), Chemical SP1056 (Chemical Chem.), CRM-0803 (Showa Union Synthetic Co., Ltd.), Vulkadur A (Bayer). Be done. Among them, halogenated phenol resin-based cross-linking agents are preferable, and Tuckyrol (registered trademark) 250-I, Tuckyroll (registered trademark) 250-III, Schenectady.
[0075]
　Specific examples of cross-linking of thermoplastic cross-linked rubber with phenol resin include US Pat. No. 4,311,628, US Pat. No. 2,972,600, and US Pat. No. 3,287,440. Described in the document, these techniques can also be used in the present invention.
[0076]
　US Pat. No. 4,311,628 discloses a phenolic curative system comprising a phenolic curing resin and a cure activator. Basic components of the system are substituted phenol in an alkaline medium (e.g., halogen substituted phenol, C 1 -C 2 alkyl substituted phenol) or unsubstituted phenol with an aldehyde, preferably either by condensation with formaldehyde, or bifunctional phenol Dialcohols (preferably Phenol C 5- C 10It is a phenol resin-based cross-linking agent produced by condensation of (dimethylolphenols) substituted with an alkyl group. Halogenated alkyl-substituted phenol-resin-based cross-linking agents produced by halogenation of alkyl-substituted phenol-resin-based cross-linking agents are particularly suitable. Phenol resin-based cross-linking agents composed of methylolphenol curable resins, halogen donors and metal compounds are particularly recommended, the details of which are described in US Pat. Nos. 3,287,440 and 3,709,840. Has been done. The non-halogenated phenolic resin-based cross-linking agent is used together with the halogen donor, preferably with a hydrogen halide scavenger. Generally, a halogenated phenolic resin-based cross-linking agent, preferably a brominated phenol-resin-based cross-linking agent containing 2 to 10% by mass of bromine, does not require a halogen donor, but for example, iron oxide, titanium oxide, or oxidation. Used concurrently with hydrogen halide scavengers such as magnesium, magnesium silicate, silicon dioxide and zinc oxide, preferably metal oxides such as zinc oxide. These hydrogen halide scavengers such as zinc oxide are usually used in an amount of 1 to 20 parts by mass with respect to 100 parts by mass of the phenol resin-based cross-linking agent. The presence of such a scavenger promotes the cross-linking action of the phenol-resin-based cross-linking agent, but in the case of rubber that is not easily cross-linked by the phenol-resin-based cross-linking agent, it is desirable to share the halogen donor and zinc oxide. Methods for producing halogenated phenolic curable resins and their use in cross-linking agents that use zinc oxide are described in US Pat. Nos. 2,972,600 and 3,093,613. The disclosure is the above-mentioned US Pat. Nos. 3,287,440 and 3,709, No. 840 It shall be incorporated into this specification for reference together with the disclosure of each specification. Examples of suitable halogen donors include stannous chloride, ferric chloride, or halogen-donating weights such as chlorinated paraffins, chlorinated polyethylene, chlorosulfonated polyethylene and polychlorobutadiene (neoprene rubber). Coalescence is mentioned. As used herein, the term "crosslinking accelerator" means any substance that virtually increases the crosslinking efficiency of phenolic resin-based crosslinkers, and includes metal oxides and halogen donors, which alone. Or in combination. For more details on phenolic cross-linking agents, see Vulcanization and Vulcanizing Agents (W. Hoffman, Palmerton Publishing Company). Suitable phenolic resin-based cross-linking agents and brominated phenol-resin-based cross-linking agents are commercially available, for example, such cross-linking agents are traded from Schenectady Chemicals, Inc. under trade names "SP-1045", "CRJ-352", It can be purchased as "SP-1055F" and "SP-1056". Similar operatively equivalent phenolic resin-based crosslinkers can also be obtained from other suppliers. Can be purchased from under the trade names "SP-1045", "CRJ-352", "SP-1055F" and "SP-1056". Similar operatively equivalent phenolic resin-based crosslinkers can also be obtained from other suppliers. Can be purchased from under the trade names "SP-1045", "CRJ-352", "SP-1055F" and "SP-1056". Similar operatively equivalent phenolic resin-based crosslinkers can also be obtained from other suppliers.
[0077]
　The cross-linking agent (E) is a suitable cross-linking agent from the viewpoint of preventing fogging because it generates less decomposition products. The cross-linking agent (E) is used in an amount sufficient to achieve essentially complete cross-linking of the rubber.
[0078]
　From the viewpoint of rubber elasticity of the polymer composition, the cross-linking agent (E) is usually used in an amount of 0.1 to 20 parts by mass, preferably 0.5 to 15 parts by mass with respect to 100 parts by mass of the copolymer (A). It is desirable to do.
[0079]
　In the present invention, sulfur, p-quinone dioxime, p, p'-dibenzoylquinone dioxime, N-methyl-N, 4-dinitrosoaniline, nitrosobenzene, etc. are used for dynamic cross-linking with the cross-linking agent (E). Peroxy cross-linking aids such as diphenylguanidine, trimethylolpropane-N, N'-m-phenylenedimaleimide, divinylbenzene, triallyl cyanurate, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, trimethylolpropane Auxiliary agents such as polyfunctional methacrylate monomers such as trimethacrylate and allyl methacrylate and polyfunctional vinyl monomers such as vinyl butyrate and vinyl stearate can be blended.
[0080]
　Further, a dispersion accelerator may be used to promote the decomposition of the cross-linking agent (E). Degradation accelerators include tertiary amines such as triethylamine, tributylamine, 2,4,6-tri (dimethylamino) phenol;
　aluminum, cobalt, vanadium, copper, calcium, zirconium, manganese, magnesium, lead, mercury, etc. Examples thereof include naphthenate of naphthenic acid and various metals (for example, Pb, Co, Mn, Ca, Cu, Ni, Fe, Zn, rare earths).
[0081]
　 In addition to the
　copolymer (A), the crystalline propylene-based polymer (B), the crystalline propylene-based polymer (C), and the low molecular weight polyolefin (D), the composition of the present invention includes Additives may be added as long as the effects of the present invention are not impaired. The additive is not particularly limited, and examples thereof include a softener (F) and a filler. Examples of the additive include rubbers other than the copolymer (A) (for example, polyisobutylene, butyl rubber, propylene / ethylene copolymer rubber, propylene / butene copolymer rubber, propylene / butene / ethylene copolymer rubber, etc.). Propylene-based elastomer, ethylene-based elastomer such as ethylene / propylene copolymer rubber, styrene-based thermoplastic elastomer); crystalline propylene-based polymer (C) such as thermosetting resin, thermoplastic resin such as polyolefin, and low molecular weight Resins other than polyolefin (D); Acid receiving agents, UV absorbers; Antioxidants; Heat-resistant stabilizers; Anti-aging agents; Light-resistant stabilizers, Weather-resistant stabilizers; Antistatic agents; Metallic sheets; Other than polyethylene wax and polypropylene wax Examples thereof include known additives used in the field of polymers such as waxes and lubricants such as aliphatic amides.
[0082]
　Each of these additives may be used alone or in combination of two or more.
[0083]
　As the softener (F), a softener usually used for rubber can be used. As the softening agent (F), petroleum-based softeners such as process oil, lubricating oil, paraffin oil, liquid paraffin, petroleum asphalt, and vaseline; , Fatty oil softeners such as rapeseed oil, soybean oil, palm oil; tall oil; sub (factis); waxes such as beeswax, carnauba wax, lanolin; ricinolic acid, palmitic acid, stearic acid, barium stearate, steer Fatty or fatty acid salts such as calcium phosphate, zinc laurate; naphthenic acid; pine oil, rosin or derivatives thereof; synthetic polymer substances such as terpene resin, petroleum resin, atactic polypropylene, kumaron inden resin; dioctylphthalate, dioctyl adipate, Ester-based softeners such as dioctyl sebacate; examples thereof include microcrystallin wax, liquid polybutadiene, modified liquid polybutadiene, liquid thiocol, and hydrocarbon-based synthetic lubricating oil.
[0084]
　These softeners (F) are not particularly limited as long as they exert the effects of the present invention, but are preferably 90 to 150 parts by mass, more preferably 100 to 140 parts by mass with respect to 100 parts by mass of the component derived from the copolymer (A). It is used in the amount of parts by mass. When the softening agent (F) is used in such an amount, the polymer composition is excellent in fluidity and oil resistance.
[0085]
　As the filler, an inorganic filler and an organic filler can be arbitrarily used, but the inorganic filler is particularly preferably used. Examples of the inorganic filler used in this application include glass fiber, carbon fiber, silica fiber, asbestos, metal (stainless steel, aluminum, titanium, copper, etc.) fiber, carbon black, graphite, silica, silas balloon, glass bead, and the like. Silates (calcium silicate, talc, clay, kaolin, etc.), silica soil, metal oxides (iron oxide, titanium oxide, alumina, etc.), metal carbonates (calcium carbonate, barium carbonate, basic magnesium carbonate, etc.), metals Sulfates (barium sulfate, aluminum sulfate, calcium sulfate, basic magnesium sulfate whisker, etc.), metal sulfides (molybdenum disulfide, etc.), and various metal (magnesium, silicon, aluminum, titanium, copper, etc.) powders, mica , Mica powder, glass flakes, glass bulbs, calcium titanate whisker, aluminum borate whisker and the like. These fillers may be used alone or in combination of two or more.
[0086]
　Among these, the effect of the present invention is remarkable when carbon black is contained in an amount of 0.1 to 20 parts by mass, preferably 1 to 5 parts by mass, based on 100 parts by mass of the copolymer (A). Is.
[0087]
　Antacids include oxides or hydroxides of divalent metals such as ZnO, MgO, CaO, Mg (OH) 2 , Ca (OH) 2 , or hydrotalcite Mg 6 Al 2 (OH) 16 CO 3 -NH 2 O is used. These acid receiving agents are usually used in a proportion of 20 parts by mass or less, preferably 0.1 to 10 parts by mass, based on 100 parts by mass of the component derived from the copolymer (A).
[0088]
　Examples of the anti-aging agent include aromatic secondary amine-based anti-aging agents such as phenylbutylamine, N, N-di-2-naphthyl-p-phenylenediamine; dibutylhydroxytoluene, tetrakis [methylene (3,5-di). -T-Butyl-4-hydroxy) hydrocinnamate] Phenolic anti-aging agents such as methane; Bis [2-methyl-4- (3-n-alkylthiopropionyloxy) -5-t-butylphenyl] sulfides, etc. Thioether-based anti-aging agents; dithiocarbamate-based anti-aging agents such as nickel dibutyldithiocarbamate; zinc salts of 2-mercaptobenzoylimidazole, 2-mercaptobenzoimidazole, dilaurylthiodipropionate, distearylthiodipropionate, etc. There are sulfur-based anti-aging agents.
[0089]
　Further, the blending amount of the additive other than the additive whose blending amount is described in the present specification is not particularly limited as long as the effect of the present invention is obtained, but the component derived from the copolymer (A), the crystalline propylene type. With respect to a total of 100 parts by mass of the polymer (B) and the crystalline propylene-based polymer (C), each is usually 5 parts by mass or less, preferably 0.01 to 5 parts by mass, and the total is usually 10 parts by mass or less. It is preferably 0.1 to 5 parts by mass.
[0090]
　[Method for producing
　composition ] The method for producing the composition is not particularly limited, and for example, an uncrosslinked copolymer (A), a crystalline propylene-based polymer (B), a crystalline propylene-based polymer (C), and the like. The low molecular weight polyolefin (D) may be produced by a method including dynamically heat-treating in the presence of the phenol resin-based cross-linking agent (E).
[0091]
　In the present invention, "dynamically heat-treating" means kneading the mixture in a molten state in the presence of the cross-linking agent (E). Further, "dynamic cross-linking" means cross-linking the mixture while applying a shearing force.
[0092]
　More specifically, for example, an uncrosslinked copolymer (A) and at least a part of a crystalline propylene-based polymer (B), a crystalline propylene-based polymer (C), and a low molecular weight polyolefin (D). A composition precursor produced by dynamically heat-treating a cross-linking agent (E), a softening agent (F) if necessary, and a cross-linking aid, and the remaining crystalline propylene-based polymer (B), if necessary. ), The crystalline propylene polymer (C), the low molecular weight polyolefin (D), and other components are melt-kneaded under normal conditions, and then granulated or pulverized.
[0093]
　The dynamic heat treatment in the present invention is preferably performed in a non-open type apparatus, and is preferably performed in an atmosphere of an inert gas such as nitrogen or carbon dioxide. The temperature of the heat treatment is in the range of 300 ° C. from the melting point of the crystalline propylene-based polymer (B) and the crystalline propylene-based polymer (C), and is usually 150 to 270 ° C., preferably 170 to 250 ° C. The kneading time is usually 1 to 20 minutes, preferably 1 to 10 minutes. Further, the shear force applied is shear rate at 10 ~ 50,000Sec -1 , preferably 100 ~ 10,000Sec -1 in the range of.
[0094]
　As the kneading device, a mixing roll, an intensive mixer (for example, a Banbury mixer, a kneader), a single-screw or twin-screw extruder, or the like can be used, but a non-open type device is preferable.
[0095]
　By the dynamic heat treatment described above, a thermoplastic elastomer in which at least a part of the copolymer (A) is crosslinked is obtained. The polymer crosslinked with the obtained thermoplastic elastomer is mainly the copolymer (A).
[0096]
　[Physical Properties of Composition] In
　the olefin-based polymer composition of the present invention, at least a part of the components derived from the copolymer (A) is crosslinked by the phenol resin-based cross-linking agent (E).
[0097]
　The MFR (230 ° C., 10 kg load) of the olefin polymer composition of the present invention is preferably 5 to 150 g / 10 minutes, more preferably 5 to 140 g / 10 minutes, from the viewpoint of moldability. It is more preferably 5 to 100 g / 10 minutes.
[0098]
　From the viewpoint of rubber elasticity, the olefin-based polymer composition of the present invention preferably has a shore A hardness (instantaneous value) of 50 to 80, and more preferably 50 to 70, as measured in accordance with JIS K6253. preferable.
[0099]
　There are no particular restrictions on the compression set (measured value after compression under the conditions of CS, 25% compression, 70 ° C., 22 hours) of the olefin polymer composition of the present invention measured by the method of Examples described later. No, but preferably in the range of 10% to 40%.
[0100]
　[Molded product]
　The molded product of the present invention uses the above-mentioned polymer composition as an injection molding method, an extrusion molding method, a solution casting method, an inflation molding method, a compression molding method, a transfer molding method, a casting molding method, or the like. It is obtained by molding by a known molding method.
[0101]
　Examples of the molded body of the present invention include an air cleaner seal, an air intake hose, a cable connector, and a cushion rubber.
[0102]
　This specification includes the contents described in the specification of Japanese Patent Application No. 2019-030631 which is the basis of the priority of the present application.
Example
[0103]
　Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited thereto.
[0104]
　[Measurement method and evaluation method]
[Mole amount and mass of each structural unit of ethylene / α-olefin / non-conjugated polyene copolymer]
　Constituent unit derived from ethylene, structural unit derived from α-olefin and non-conjugated polyene The molar amount and mass of the derived building blocks were determined by intensity measurement using a 1 H-NMR spectrum meter.
[0105]
[Mooney Viscosity]
　The Mooney viscosity ML1 + 4 (125 ° C.) of an ethylene / α-olefin / non-conjugated polyene copolymer is measured according to JIS K6300 (1994) using a Mooney viscometer (SMV202 type manufactured by Shimadzu Corporation). bottom.
[0106]
[Melting points (Tm) of components (B), (C) and (D)]
　Measured by the following method using a differential scanning calorimetry (DSC ) in accordance with JIS K7121.
[0107]
　About 5 mg of the polymer was sealed in a measuring aluminum pan of a differential scanning calorimeter (DSC220C type) manufactured by Seiko Instruments Inc., and heated from room temperature to 200 ° C. at 10 ° C./min. The polymer was held at 200 ° C. for 5 minutes and then cooled to −50 ° C. at 10 ° C./min to completely melt the polymer. After standing at −50 ° C. for 5 minutes, the polymer was heated to 200 ° C. at 10 ° C./min for the second time, and the peak temperature (° C.) at the second heating was defined as the melting point (Tm) of the polymer. When a plurality of peaks were detected, the peak detected on the highest temperature side was adopted.
[0108]
[Mn of component (D) in terms of polypropylene] The
　number average molecular weight Mn was determined by GPC measurement. The measurement was performed under the following conditions. The number average molecular weight Mn and the weight average molecular weight Mw were determined by preparing a calibration curve using commercially available monodisperse standard polystyrene and converting it into polypropylene (general-purpose calibration method).
[0109]
　　Equipment: Gel permeation chromatograph HLC-8321 HT type (manufactured by Tosoh)
　　Solvent: o-dichlorobenzene
　　column: TSKgel GMH6-HT x 2, TSKgel GMH6-HTL column x 2 (both manufactured by Tosoh)
　　Flow velocity: 1.0 ml / Minute
　　sample: 0.15 mg / mL o-dichlorobenzene solution
　　Temperature: 140 ° C
[0110]
[Mn of component (D) in terms of polyethylene] The
　number average molecular weight Mn was determined by GPC measurement. The measurement was performed under the following conditions. The number average molecular weight Mn and the weight average molecular weight Mw were determined by preparing a calibration curve using commercially available monodisperse standard polystyrene and converting it into polyethylene (general-purpose calibration method).
[0111]
　　Equipment: Gel permeation chromatograph HLC-8321 HT type (manufactured by Tosoh)
　　Solvent: o-dichlorobenzene
　　column: TSKgel GMH6-HT x 2, TSKgel GMH6-HTL column x 2 (both manufactured by Tosoh)
　　Flow velocity: 1.0 ml / Minute
　　sample: 0.15 mg / mL o-dichlorobenzene solution
　　Temperature: 140 ° C
[0112]
[Physical Properties of Thermoplastic Elastomer Composition (Olefin Polymer Composition) and Mold] The
　method for evaluating the physical characteristics of the thermoplastic elastomer composition in the following Examples and Comparative Examples is as follows.
[0113]
[Shore A hardness] Using a
　100-ton electric heating automatic press (manufactured by Shoji Co., Ltd.), the obtained pellets of the thermoplastic elastomer composition were press-molded at 230 ° C. for 6 minutes, and then cooled and pressed at room temperature for 5 minutes to achieve the thickness. A 2 mm press sheet was prepared. Using the sheet, the scale was read immediately after contact with the needle pusher using a type A measuring instrument in accordance with JIS K6253.
[0114]
[Tensile characteristics]
　Measured according to the method of JIS K6301.
　The test piece used was a No. 3 dumbbell piece punched out from a press sheet having a thickness of 2 mm.
　Measurement temperature: 23 ° C.
　M100: Stress at 100% elongation (MPa)
　TB: Tensile breaking strength (MPa)
　EB: Tensile breaking point elongation (%)
[0115]
[Compression Permanent Strain (CS)] Using a
　100-ton electric heating automatic press (manufactured by Shoji Co., Ltd.), the obtained pellets of the thermoplastic elastomer composition were press-molded at 230 ° C. for 6 minutes, and then cooled and pressed at room temperature for 5 minutes. A press sheet having a thickness of 2 mm was prepared.
[0116]
　A press sheet having a thickness of 2 mm produced as described above was laminated according to JIS K6250, and a compression set test was performed according to JIS K6262.
[0117]
　The test conditions were a laminated sheet with a thickness of 12 mm (4 layers of 3 mm thick pieces), compressed at 25%, 70 ° C., and 22 hours, and measured 30 minutes after strain removal (compression). bottom.
[0118]
[Oil resistance test: Weight change rate]
　Liquid paraffin (soft) (Nacalai Tesque Co., Ltd. code number: 26132-35) was used as the test oil, and a 2 mm press sheet was immersed at 80 ° C. for 24 hours. After that, the surface of the sample was wiped off, and the rate of change in weight was measured at n number = 2.
[0119]
[Molding appearance] Using a
　vertical injection molding machine SV-50 manufactured by Sumitomo Heavy Industries, Ltd., using a columnar mold with a pin gate diameter of 1 mm, inner diameter of 16 mm, outer diameter of 22 mm, and width of 100 mm, molding temperature: 220 ° C. Molding was performed at an injection speed of 70 mm / s.
　Judgment criteria:
◯: A white pattern was visually observed on the surface of the molded product.
X: No white pattern is visually observed on the surface of the molded product.
[0120]
[Materials used]
(1) Copolymer (A) As the
　copolymer (A), commercially available ethylene / propylene / 5-ethylidene-2-norbornene copolymer rubber (EPDM) (ethylene / propylene ratio = 73/27) Mol%, iodine value 13, Mooney viscosity ML1 + 4 (125 ° C.) = 116) were used.
[0121]
(2) Crystalline propylene-based polymer The
　following crystalline propylene-based polymer was used as the crystalline propylene-based polymer.
(B-1) Commercially available propylene homopolymer (MFR (condition: 230 ° C., 2.16 kgf) = 0.5 g / 10 minutes, melting point measured by DSC = 165 ° C.)
(B-2) Commercially available propylene homopolymer Combined (MFR (condition: 230 ° C, 2.16 kgf) = 2 g / 10 minutes, melting point measured by DSC = 170 ° C)
(B-3) Commercially available propylene block polymer (ethylene content 7% by mass, MFR (condition: condition:) 230 ° C., 2.16 kgf) = 3 g / 10 min, melting point measured by DSC = 160 ° C.)
(C-1) Commercially available propylene homopolymer (MFR (condition: 230 ° C., 2.16 kgf) = 9 g / 10 min. , DSC measured melting point = 165 ° C.
(X-1) Commercially available propylene block polymer (ethylene content 4% by mass, MFR (conditions: 230 ° C., 2.16 kgf) = 50 g / 10 minutes, melting point measured by DSC = 160 ° C)
[0122]
(3) Low Molecular Weight Polyolefin (D) The
　following polypropylene wax or polyethylene wax was used as the low molecular weight polyolefin (D).
(D-1) Commercially available polypropylene wax (propylene content 100% by mass, Mn = 5000, Mw = 20000, melting point measured by DSC = 160 ° C., calorific value of melting measured by DSC = 102 J / g)
(D-2) Commercially available Polypropylene wax (propylene content 95% by mass, Mn = 6000, Mw = 20000, melting point measured by DSC = 130 ° C., calorific value of melting measured by DSC = 53J / g)
(D-3) Commercially available polyethylene wax (ethylene content) 100% by mass, Mn = 5000, Mw = 20000, melting point measured by DSC = 130 ° C., calorific value of melting measured by DSC = 110 J / g, density = 920 kg / m 3 )
[0123]
(4)
　Lubricating lubricant As the lubricant, erucic acid amide (Alflow P-10 manufactured by NOF CORPORATION) was used.
[0124]
(5) Softener As the
　softener, a paraffin-based process oil (Diana Process Oil TM PW-100: manufactured by Idemitsu Kosan Co., Ltd.) was used.
[0125]
(6) Phenol resin-based cross-linking agent (E) As the
　phenol resin-based cross-linking agent, a brominated alkylphenol formaldehyde resin (trade name: SP-1055F, manufactured by Scienceday) was used.
[0126]
(7) Antacid As the
　antacid, zinc oxide (2 types of zinc oxide, manufactured by HakusuiTech Co., Ltd.) was used.
[0127]
(8) Filler A
　carbon black masterbatch (trade name: PEONY BLACK F32387MM, manufactured by DIC Corporation) was used as the filler.
[0128]
　[Example 1]
　100 parts by mass of ethylene / α-olefin / non-conjugated polyene copolymer (A), 27 parts by mass of crystalline propylene polymer (B-1) as crystalline propylene polymer (B), crystals 8 parts by mass of the propylene homopolymer (C-1) as the sex propylene-based polymer (C), 8 parts by mass of the polypropylene wax (D-1) as the low molecular weight polyolefin (D), and bromine as the phenol resin-based cross-linking agent (E). Alkylphenol Formaldehyde resin (trade name: SP-1055F, manufactured by Schenectday) 8 parts by mass, zinc oxide (2 types of zinc oxide, manufactured by Huxitec) 0.5 parts by mass as an acid receiving agent, carbon black master batch (manufactured by Huxitec) as a filler Product name: PEONY BLACK F32387MM, manufactured by DIC Co., Ltd. 3 parts by mass, and softener (Diana Process Oil TM PW-100, paraffin oil) 120 parts by mass, extruder (product number KTX-30, Kobe Steel Co., Ltd.) Manufactured, Cylinder temperature: C1: 50 ° C, C2: 90 ° C, C3: 100 ° C, C4: 120 ° C, C5: 180 ° C, C6: 200 ° C, C7 to C14: 200 ° C, Die temperature: 200 ° C, Screw rotation After kneading using a number: 500 rpm and an extrusion rate: 40 kg / h), the mixture was dynamically crosslinked to obtain pellets of a thermoplastic elastomer composition.
[0129]
　The pellets of the obtained thermoplastic elastomer composition were press-molded at 230 ° C. for 6 minutes using a 100-ton electric heating automatic press (manufactured by Shoji Co., Ltd.), and then cooled and pressed at room temperature for 5 minutes to obtain a test piece having a thickness of 2 mm. Obtained.
[0130]
　Each physical property was evaluated using these test pieces. The results are shown in Table 1.
[0131]
　[Examples 2 to 9 and Comparative Examples 1 to 8] In
　Example 1, the same procedure as in Example 1 was carried out except that the composition of each composition was changed as shown in Table 1 or Table 2. The results are shown in Table 1 or Table 2.
[0132]
[table 1]

[0133]
[Table 2]

[0134]
　From Tables 1 and 2, it can be seen that when the polymer composition satisfies the requirements of the present invention, the balance between mechanical properties, molded appearance, and oil resistance is good.
[0135]
　All publications, patents and patent applications cited herein are incorporated herein by reference in their entirety.

WE CLAIMS

[Claim 1]It contains a structural unit derived from ethylene, a structural unit derived from α-olefin having 3 to 20 carbon atoms, and a structural unit derived from a non-conjugated polymer, and (a-1) Mooney viscosity ML1 + 4 (125 ° C.) is 50 to 200. The following
requirements (b-1) and (b-2):
(b-1) MFR (230 ° C., 2.16 kg load) are 0.1 with respect to 100 parts by mass of the component derived from the copolymer (A). ~ 4g / 10 minutes,
(b-2)
One or more crystalline propylene-based polymer (B) having a melting point (Tm) of 100 to 200 ° C. measured by DSC , totaling 10 to 50 parts by mass, and the following
requirements (C-1) and (c-2):
(c-1) MFR (230 ° C., 2.16 kg load) is 5 to 15 g / 10 minutes, and
(c-2) melting point (Tm) measured by DSC is 100.
One or more crystalline propylene-based polymers (C) satisfying ~ 200 ° C. , totaling 5 to 30 parts by mass, and the following
requirements (d-1):
(d-1) Number average measured by gel permeation chromatography It
contains 4 to 18 parts by mass of a low molecular weight polyolefin (D) having a molecular weight of 3000 to 10000 ,
and at least a part of the components derived from the copolymer (A) is crosslinked by a phenol resin-based cross-linking agent (E). Olefin-based polymer composition.
[Claim 2]
The olefin-based polymer composition according to claim 1, wherein the 　low molecular weight polyolefin (D) further satisfies the following requirements (d-2):
(d-2) the heat of fusion measured by DSC is 20 J / g or more
.
[Claim 3]
　The olefin-based polymer composition according to claim 1 or 2, wherein the olefin-based polymer composition further contains 90 to 150 parts by mass of a component derived from the softening agent (F).
[Claim 4]
　The olefin-based polymer composition according to any one of claims 1 to 3, wherein the MFR (230 ° C., 10 kg load) of the olefin-based polymer composition is 5 to 150 g / 10 minutes.
[Claim 5]
　Any one of claims 1 to 4, wherein the total of the component (B), the component (C) and the low molecular weight polyolefin (D) is 20 to 80 parts by mass with respect to 100 parts by mass of the component derived from the copolymer (A). The olefin-based polymer composition according to the item.
[Claim 6]
　The olefin-based polymer composition according to any one of claims 1 to 5, wherein the shore A hardness (instantaneous value) measured according to JIS K6253 of the olefin-based polymer composition is 50 to 80.
[Claim 7]
　A molded product obtained from the olefin polymer composition according to any one of claims 1 to 6.
[Claim 8]
　The molded product according to claim 7, which is an injection molded product.