WO2002094933A1 - Resin composition for automobile exterior parts - Google Patents
Resin composition for automobile exterior parts Download PDFInfo
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- WO2002094933A1 WO2002094933A1 PCT/JP2002/004936 JP0204936W WO02094933A1 WO 2002094933 A1 WO2002094933 A1 WO 2002094933A1 JP 0204936 W JP0204936 W JP 0204936W WO 02094933 A1 WO02094933 A1 WO 02094933A1
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- ethylene
- resin composition
- weight
- copolymer
- block copolymer
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/16—Ethylene-propylene or ethylene-propylene-diene copolymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
Definitions
- the present invention relates to an automotive exterior resin composition containing a propylene 'ethylene block copolymer, a specific elastomeric polymer and an inorganic filler, and in particular, a molded article with less occurrence of a flow mark or a weld mark.
- the present invention relates to a resin composition for automobile exteriors which can be produced.
- Polypropylene is used as a molding material in various fields such as daily necessities, kitchenware, packaging films, automobile parts, mechanical parts, and electrical parts. Therefore, it has been used in place of a composition in which various additives are blended with polypropylene. For example, in fields where mechanical strength is required, such as automotive parts, polypropylene compositions containing elastomer or talc are used.
- an object of the present invention is to provide an automotive exterior resin having excellent fluidity during molding, excellent balance of physical properties such as flexural elasticity, impact resistance, hardness and embrittlement temperature, and in which flow marks and weld marks are inconspicuous. It is to provide a fat composition. That is, the present invention relates to (A) a crystalline propylene 'ethylene block copolymer (A-1), or (A-1) and a crystalline propylene homopolymer (A_2) having an equivalent weight or less. 50 to 70% by weight of a polypropylene mixture consisting of
- the above-mentioned crystalline propylene / ethylene block copolymer (A-11) is composed of a propylene homopolymer part and a propylene'ethylene random copolymer part, and its melt mouth rate (ASTMD) -1 238, 230 ° C, load 2160 g) is 70 to 130 g / 10 minutes,
- the crystalline propylene 'ethylene block copolymer (A-11) has an isomeric pentad fraction (mmmm fraction) of 9 in the propylene homopolymer portion measured by 13 C-NMR. 7% or more, and the content of the propylene / ethylene random copolymer part is 5 to 20% by weight,
- the above crystalline propylene homopolymer (A-2) has an iso-annular pentad fraction (mmmm fraction) of 97% or more, And the melt flow rate (ASTM D—1238, 230 ° C, load 2160 g) is 100 to 300 g / 10 minutes,
- the hydrogenated block copolymer (B_3) is a hydrogenated product of the block copolymer represented by the formula (1) or the formula (2),
- X represents a polymer block of a monovinyl-substituted aromatic hydrocarbon compound
- Y represents a polymer block of a conjugated diene compound
- n is an integer of 1 to 5.
- the hydrogenation rate in the Y part is 90 mol% or more, the proportion in the X part is 10 to 25% by weight, and the melt flow rate (ASTM D-128, 190 ° C, load 2160 g) ) Is less than 15 g / 10 minutes
- the present invention relates to an automotive exterior resin composition.
- the crystalline propylene ethylene block copolymer (A-1) desirably has an ethylene unit content of 1 to 10% by weight. Further, the elastomeric polymer (B) is contained in 100% by weight of the resin composition.
- (B-1) a copolymer rubber of ethylene and a monoolefin having 6 or more carbon atoms is 10 to 20% by weight
- (B-2) 1 to 5% by weight of an ethylene / polyolefin / non-conjugated polyene random copolymer
- Ethylene and monoolefin having 6 or more carbon atoms are used as the copolymer rubber (B-1), which is produced by copolymerizing ethylene and high olefins having 6 or more carbon atoms using a single-site catalyst. Rubbery materials are preferred.
- the copolymerization ratio of —olefin units in the copolymer rubber (B-1) is preferably in the range of 10 to 50% by weight.
- ethylene'1-octene copolymer rubber can be mentioned.
- ethylene / 1-olefin / non-conjugated polyene random copolymer (B-2) an ethylene / 1-propylene / terpolymer or an ethylene / 1-butene / terpolymer is preferred. .
- Examples of the hydrogenated block copolymer (B-3) include styrene “ethylene” ptene. Styrene block copolymer, styrene “ethylene / propylene / styrene block copolymer, or styrene / styrene block copolymer. Ethylene / propylene / ethylene block copolymer is preferred.
- Talc is preferred as the inorganic filler (C), and its average particle size measured by laser analysis is preferably 2 to 6 ⁇ m.
- Such a resin composition also has a melt flow rate (ASTM D—1238, 230 ° C., load 2160 g) of 3 0 g / 10 minutes or more, flexural modulus (ASTMD-790) is 19
- a crystalline propylene ethylene block copolymer (A-1) may be used alone, or the propylene copolymer (A-1) may have a crystallinity equal to or less than that of the block copolymer (A-1).
- the propylene ethylene block copolymer (A-1) is composed of a propylene homopolymer part and a propylene ethylene random copolymer part.
- the crystalline propylene / ethylene block copolymer (A-1) has a propylene / ethylene random copolymer content of 5 to 20% by weight, preferably 8 to 13% by weight.
- the total amount of the propylene ethylene random copolymer part and the propylene homopolymer part is 100% by weight.
- the content of the propylene / ethylene random copolymer in the crystalline propylene / ethylene block copolymer (A-1) was determined by separating the propylene copolymer sample at room temperature using a p-xylene solvent.
- the amount of the soluble portion can be measured from the amount of the soluble portion.
- the measurement method first, 5 g of a block copolymer sample is completely dissolved in boiling p-xylene, then the temperature is lowered to 20 ° C, the solution is left overnight, and then the insoluble portion is separated by filtration. . Next, 150 ml of methanol was added to the filtrate, and the mixture was stirred. The soluble portion was separated as a precipitate, and it was separated by filtration and dried to obtain the p-xylene soluble portion. Can be obtained by weighing the soluble part o
- the propylene homopolymer part in the crystalline propylene / ethylene block copolymer (A-1) has an isotactic pen pen fraction (mmmm fraction) measured by 13 C-NMR. More than 97%, preferably more than 97.5%.
- block copolymer (A-1) it is desirable to use one having an ethylene unit content of preferably 1 to 10% by weight, more preferably 3 to 8% by weight.
- the content of ethylene units was determined by subjecting a block copolymer (A-1) sample press film to infrared spectroscopy analysis. Can be asked. That is, the absorbance of 1155 cm- 1 based on the methyl group and the absorbance based on the methylene group are measured and measured using the calibration curve of Gardner (IJ Gardner et al, Rubber Chem. And Tech., 44, 1015, 1971).
- the crystalline propylene ethylene block copolymer (A-1) was measured under the conditions of 230 ° C and a load of 2160 g in accordance with ASTM D-1238.
- a liquid melt rate (MFR) of 70 to: L 30 g / 10 minutes, preferably 80 to L: 20 g / 10 minutes is used.
- MFR liquid melt rate
- a block copolymer having an MFR smaller than the above range is used, a flow mark or a weld mark is easily generated on the surface of a molded article from the obtained resin composition, and the heat shrinkage of the molded article is increased. It is not preferable.
- the crystalline propylene / ethylene block copolymer (A-1) can be used alone or in combination of two or more.
- a polymer is not a collection of identical molecules having the same molecular weight but a collection of molecules having different molecular weights, and a polymer having certain physical properties is constituted as a whole.
- the crystalline propylene.ethylene block copolymer (A-1) used in the present invention is also a collection of various molecules having different molecular weights, and the entire polymer is the specific propylene homopolymer described above. And a propylene / ethylene random copolymer part, and shows a specific range of MFI.
- the block copolymer (A-1) a polymer in which a propylene homopolymer part and a propylene'ethylene random copolymer part have the following molecular weights and compositions.
- propylene alone is used as the block copolymer (A-1).
- the MFR (230 ° C, load: 210 g) of the polymer part is preferably 100-300 gZ10O, particularly preferably 120-250 g / It is preferable to use a 10 minute one.
- the propylene-ethylene random copolymer part has an intrinsic viscosity [77] measured at 135 ° C. in decahydraphthalene of GS dlZg, and the ethylene content in the copolymer part is It is preferred to use 20 to 40% by weight, especially 24 to 32% by weight.
- a polypropylene mixture consisting of:
- the crystalline propylene homopolymer (A-2) has an isotopic pentad fraction (mmmm fraction) of 97% or more, preferably 97.5% or more, and an MF R (AS TM D—1 238, 2330, C, load 2160 g) is 100-300 g / 10 min, preferably 120-250 g / 10 minutes is desirable.
- the crystalline propylene / ethylene block copolymer (A_1) can be produced by various methods. For example, a known olefin such as a Ziegler-Natane-based catalyst or a meta-aqueous catalyst can be used. It can be produced using a stereoregular polymerization catalyst.
- Examples of the production of a block copolymer (A-1) using a Ziegler-Na-base catalyst include, for example, a solid titanium catalyst component, an organometallic compound catalyst component, and, if necessary, an electronic component.
- Examples of the method include a method in which propylene is polymerized in the presence of a catalyst formed from a donor and then propylene and ethylene are subsequently copolymerized.
- Polypropylene mixture The crystalline propylene homopolymer (A-2) as one of the constituent components can also be produced using the same olefin stereoregular polymerization catalyst as described above.
- the elastomeric polymer (B) used in the present invention is a copolymer rubber of ethylene and a monoolefin having 6 or more carbon atoms (B-1), an ethylene. It is composed of three types of copolymers: a polyene random copolymer (B-12) and a hydrogenated block copolymer (B-3).
- the copolymer rubber (B-1) of ethylene and a monoolefin having 6 or more carbon atoms is a rubber-like copolymer obtained by copolymerizing ethylene and a one-year-old fin having 6 or more carbon atoms, preferably 6 to 12 carbon atoms. Things.
- olefins examples include 1-hexene, 4-methyl-11-pentene, 1-octene, 1-decene, and 1-dodecene.
- MFR As a copolymer rubber (B-1) of ethylene and a monoolefin having 6 or more carbon atoms, MFR (ASTM D-1238, 230 ° C; load: 2160) g) is from 0.5 to: LO gZlO content, preferably 1 to 8 g / 10 minutes. It is not preferable to use a copolymer rubber having an MFR larger than the above range, since the rigidity and low-temperature impact resistance of a molded article produced from the obtained resin composition are reduced.
- the weight ratio of ethylene in the copolymer rubber (B-1) to the carbon fiber having a carbon number of 6 or more (—olefin having a carbon number of 6 or more) is 90/10 to 50/50. It is desirable to use those of 80/20 to 640.
- Suitable copolymer rubbers (B-1) include ethylene'1-octene copolymer rubber. Such ethylene-polyolefin copolymer rubber (B-1) is produced by copolymerizing ethylene and polyolefin having 6 or more carbon atoms using an olefin stereoregular polymerization catalyst. be able to.
- ethylene-ethyl-propylene copolymer produced using a single-site polymerization catalyst has a relatively narrow molecular weight distribution and composition distribution.
- the effect of improving the impact strength is excellent.
- a single-site catalyst a meta-containing compound in which a compound having a cyclopentene skeleton is coordinated to a transition metal such as zirconium metal and an organoaluminoxy compound are included. Mouth-based catalysts can be mentioned.
- Ethylene-olefin 'non-conjugated polyene random copolymer (B-2) is a random terpolymer rubber of ethylene, olefin and non-conjugated polyene compound.
- those having usually 3 to 20 carbon atoms, preferably 3 to 10 carbon atoms can be used.
- propylene, 1-butene, 1-pentene, 1- Xen, 1-octene, 1-decene, 4-methyl-1-pentene and the like can be mentioned.
- non-conjugated polyvalent compounds include 5-ethylidene-1-norbornene, 5-propylidene-2-norbornene, dicyclohexane, 5-vinyl-12-norbornene, and 5-methylene-1-21 Norbornene, 5-Isopropylidene- 1 2 -Norbornene, Norbornadiene, and other cyclic non-conjugated diene compounds, 1,4-hexadiene, 4 -Methyl-1, 4 -Hexadiene, 5 -Methyl-1, 4 -I-Hexadiene , 5 — methyl-1,5 — hebutadiene, 6 — methyl 1, 5 — hebutadiene, 6 — methyl-1,7 — octane, 7 — methyl — 1, 6 — octane Chain non-conjugated gen And triene compounds such as 2,3-diisopropyliden
- MFR ethylene / chiseki refine ′ non-conjugated poly (ethylene random copolymer) ( ⁇ —2) is used. lg / 10 minutes or less, preferably 0.1 to 0.510 minutes is used. It is not preferable to use a copolymer having a MFR larger than the above range, since a flow mark or a yellow mark easily occurs on the surface of a molded product produced from the obtained resin composition.
- the copolymerization ratio of ethylene and ⁇ -olefin in the random copolymer (B-2) is preferably from 90/10 to 40/60, expressed by a molar ratio (ethylene- ⁇ olefin). And more preferably 85/15 to 50/50.
- the ratio of the non-conjugated polyene compound component in the random copolymer ( ⁇ -2) is preferably 1 to 40, more preferably 2 to 35, expressed by the iodine value of the random copolymer.
- ethylene-phorefine 'non-conjugated polyene random copolymers include ethylene' propylene 'gen terpolymer (EPDM) and ethylene' 1-butene 'gen ternary. Copolymers can be mentioned.
- the hydrogenated block copolymer (B-3) is a hydrogenated product of the block copolymer represented by the formula (1) or (2).
- X represents a polymer of a monovinyl-substituted aromatic hydrocarbon compound
- J, ⁇ , and Y represent a polymer block of a co-projection compound
- n is an integer of 1 to 5.
- Examples of the monovinyl-substituted aromatic hydrocarbon compound constituting the polymer block represented by X include styrene such as styrene, permethylstyrene, p-methylstyrene, chlorostyrene, lower alkyl-substituted styrene, and vinylnaphthylene, and derivatives thereof. And so on.
- styrene such as styrene, permethylstyrene, p-methylstyrene, chlorostyrene, lower alkyl-substituted styrene, and vinylnaphthylene, and derivatives thereof. And so on.
- These monovinyl-substituted aromatic hydrocarbon compounds can be used alone or in a combination of two or more. Especially preferred is styrene.
- Examples of the conjugated diene compound constituting the polymer block represented by Y include butadiene, isoprene, and chloroprene. These can be used alone or in combination of two or more. Particularly preferred is butadiene or isoprene.
- the proportion of 1,2-bonds in the polybutadiene block is preferably 20 to 80% by weight, more preferably 30 to 60% by weight. Is desirable.
- n is an integer of 1 to 5, preferably 1 or 2.
- the hydrogenation rate of the conjugated gen polymer block is 90 mol% or more, preferably 95 mol% or more, and the content of the X part is 10 to 25 wt%.
- the MFR (ASTME) —1238, 190 ° C., 2160 g load) is 15 g / l0 min or less, preferably 1-1 Og / 10 min.
- a specific example of the hydrogenated block copolymer (B-3) is a styrene / ethylene / butene / styrene block copolymer (SEBS) obtained by hydrogenating styrene / butadiene / styrene / tripropylene copolymer. ), Styrene-isoprene styrene-propylene copolymer obtained by hydrogenation of styrene-isoprene-styrene copolymer, and styrene-block copolymer (SEPS). Styrene obtained by hydrogenation of range block copolymer ⁇ Styrene block copolymer such as ethylene / propylene / ethylene block copolymer (SEP).
- SEBS styrene / ethylene / butene / styrene block copolymer
- SEPS styrene-block copolymer
- the block copolymer before hydrogenation can be produced, for example, by a method of performing block copolymerization of each monomer component in an inert solvent in the presence of a lithium catalyst or a Ziegler catalyst.
- the detailed manufacturing method is described in, for example, Japanese Patent Publication No. 40-23798.
- the hydrogenation treatment can be carried out by subjecting the block copolymer to an inert solvent in the presence of a known hydrogenation catalyst.
- a detailed method is described in, for example, Japanese Patent Publication No. 42-87. No. 04, No. 43-6666, and No. 46-210814.
- the hydrogenated block copolymer (B-3) is available from Clayton G1657 (product of Shell Chemical Co., Ltd., trademark), septon 204 (product of Kurare Co., Ltd., trademark), Tuftec They are marketed under the trade names such as H1052 and Tuftec1062 (products and trademarks of Asahi Kasei Corporation), and commercially available products can also be used.
- the copolymer (B-2) and the hydrogenated block copolymer (B-3) can be used alone or in combination of two or more.
- Examples of the inorganic filler (C) used in the present invention include talc, clay, calcium carbonate, myriki, silicates, carbonates, glass fibers and the like. Of these, talc is particularly preferred. As the talc, the average particle size measured by laser analysis is preferably used.
- Resin composition 1 to: L 0 m, more preferably 2 to 6 / m.
- Such inorganic fillers can be used alone or in combination of two or more.
- A a crystalline propylene 'ethylene block copolymer (A-1) or a polypropylene mixture comprising (A-1) and a crystalline propylene homopolymer (A-2) having an equivalent weight or less. But 50 to 70% by weight, preferably 55 to 65% by weight,
- the inorganic filler is composed of 15 to 25% by weight, preferably 18 to 23%.
- the total amount of the three components (A), (B) and (C) is 100% by weight.
- the elastomeric polymer (B) is within the above range, (B-1) a copolymer rubber of ethylene and a monoolefin having 6 or more carbon atoms is 10 to 20% by weight, preferably 13 to 19% by weight,
- (B-2) Ethylene monoolefin 'unconjugated polyene random copolymer is 1 to 5% by weight, preferably 2 to 5% by weight, and (B-3) hydrogenated block copolymer is 1 to 10% by weight, preferably 3 to 8% by weight
- the resin composition may further contain, if necessary, a heat stabilizer, an antistatic agent, a weather stabilizer, a light stabilizer, an antioxidant, an antioxidant, and an ultraviolet ray.
- a heat stabilizer such as absorbents, softeners, dispersants, coloring agents such as pigments, and lubricants can be contained within a range that does not impair the object of the present invention.
- the composition of the present invention comprises the components (A) to (C) and additives to be blended as required, such as a Banbury mixer, a single-screw extruder, a twin-screw extruder, and a high-speed twin-screw extruder. It is obtained by mixing or melt-kneading using a mixing device. At this time, each component of (A-1), (A-2), (B-1), (B-2), (B-3), and (C) and, if necessary, blending
- the order of mixing the additives and the like is arbitrary, and they may be mixed at the same time, or a multi-stage mixing method such as a method of mixing some components and then mixing the other components may be employed.
- the resin composition of the present invention obtained in this way has excellent fluidity during molding, and the obtained molded product has a balance of physical properties such as flexural modulus, impact resistance, hardness and brittleness temperature. Is excellent.
- load 2 16 MFR measured under 0 g condition is preferably 30 g / 10 minutes or more, more preferably 35 to 60 minutes,
- the flexural modulus measured in accordance with ASTM D-790 is preferably at least 190 MPa
- the embrittlement temperature measured in accordance with ASTM D-746 is preferably 120 ° C or less, more preferably 125 ° C or less.
- the resin composition of the present invention having such resin properties can be suitably used as a resin raw material for injection molding. In this case, it is possible to easily mold an injection-molded product that exhibits very good fluidity during injection molding and has excellent dimensional stability.
- composition of the present invention can be used for molding automobile parts, especially automobile exterior parts, for example, parts such as bumpers, over fenders, side moldings, and rocker moldings.
- parts such as bumpers, over fenders, side moldings, and rocker moldings.
- Isocratic pendant fraction (mmmm fraction); 98% • Propylene-ethylene random copolymer: 10% by weight
- ISO pentagon fraction 98% • propylene / ethylene random copolymer: 10% by weight
- Ethylene '1-octene random copolymer rubber (EOR-2) • MFR (190 ° C; load 2160 g): 25 g / 10 minutes • 1-octene content : 24% by weight
- EPT-2 Ethylene 'propylene' 5-ethylidene-12-norbornane terpolymer
- MFR Melt edge rate
- Heat shrinkage obtained by injection molding a flat plate with a length of 150 mm, a width of 150 mm, and a thickness of 2 mm at a resin temperature of 230 ° C and a mold temperature of 40 ° C. . After the plate was allowed to stand at room temperature for 72 hours, the dimensions in the length and width directions were measured, and the average value was used as the initial dimension value. Then The plate was heated in a heating bath at 120 ° C. for 30 minutes, and then left at room temperature for 24 hours. The dimensions were measured in the same manner to obtain the dimensions after heating. Heat shrinkage (%) was calculated from the following equation.
- Flow mark generation rate The molded article for measuring the spiral flow length obtained by the above method was observed, and the flow length at a position where the flow mark began to be generated was measured. The ratio of the flow length at the point where the flow mark began to occur to the total flow length was expressed as the occurrence rate (%).
- Weld mark generation length When molding a flat plate with a length of 350 mm, a width of 135 mm, and a thickness of 3 mm, a gate is placed 70 mm from the width on the side surface in the length direction. The mold provided was used, and the resin flowed 20 mm in length, 20 mm in width, and 3 mm in thickness immediately below the gate in the flow direction (at a position 50 mm below the gate). Weirs are provided to block the water. The length of occurrence of the weld mark was determined by measuring the length of the weld mark generated after the weir until it could not be discriminated visually after injection molding using the mold.
- the MFR (230 ° C, load 2160 g) of the obtained resin composition was It was 40 g / 10 minutes.
- the test piece used for the measurement was an injection molding machine (manufactured by Nippon Steel Works Co., Ltd., product type J100S AII).
- the cylinder set temperature was 230 ° C and the mold temperature was 40 ° C. It was manufactured by injection molding under the conditions of C.
- Table 1 shows the measurement results of physical properties. As is clear from the results in Table 1, this resin composition had high melt fluidity, was excellent in moldability, and had a small tendency to generate flow marks and eld marks. It also had a small heat shrinkage, high rigidity, and a sufficiently low embrittlement temperature.
- Example 1 the amount of PEBC-1 was changed from 59 parts by weight to 40 parts by weight, and the amount of EOR-1 was changed from 13 parts by weight to 15 parts by weight. 17 parts by weight of a homopolymer (PP) was blended. Other conditions were the same as in Example 1 to obtain a resin composition.
- PP homopolymer
- Example 1 was repeated in the same manner as in Example 1 except that SEBS-1 was not added and E ⁇ R-1 was increased to 18 parts by weight. Physical properties of the resin composition were evaluated, and the results are shown in Table 1. The embrittlement temperature of the obtained resin composition was high, and the low-temperature impact resistance was poor.
- Example 1 was repeated in the same manner as in Example 1 except that EBS1 was increased to 18 parts by weight instead of adding EOR-1.
- Example 1 was repeated, except that E 0 R-1 was increased to 16 parts by weight instead of adding EPT-1. Physical properties of the resin composition were evaluated, and the results are shown in Table 1. The obtained resin composition was liable to generate flow marks and weld marks, and was not satisfactory for use as a large thin resin for molding.
- Example 1 was repeated in the same manner as in Example 1 except that ethylene-propylene-5-ethylidene-12-norbornene terpolymer (EPT-2) was used instead of EPT_1.
- EPT-2 ethylene-propylene-5-ethylidene-12-norbornene terpolymer
- the obtained resin composition was similar to the resin composition obtained in Comparative Example 3 and caused a flow mark to occur.
- Example 1 was carried out in the same manner as in Example 1 except that a propylene ethylene block copolymer (PEBC-2) was used instead of PEBC-1.
- PEBC-2 propylene ethylene block copolymer
- Example 1 was carried out in the same manner as in Example 1 except that styrene 'ethylene / butene' styrene tripolymer copolymer (SEBS-2) was used instead of SEBS-1.
- SEBS-2 styrene 'ethylene / butene' styrene tripolymer copolymer
- the obtained resin composition had a large heat shrinkage and did not have a sufficiently low embrittlement temperature.
- Example 1 was carried out in the same manner as in Example 1 except that ethylene / 1-octene random copolymer rubber (EOR-2) was used instead of EOR-1.
- EOR-2 ethylene / 1-octene random copolymer rubber
- Example 1 the amount of talc was reduced from 20 parts by weight to 10 parts by weight, while the amount of PEBC-1 was reduced from 59 parts by weight to 69 parts by weight.
- the procedure was performed in the same manner as in Example 1 except that the amount was increased to parts by weight.
- the resin composition for automotive exterior of the present invention contains a specific amount of a specific crystalline propylene. Ethylene block copolymer, a specific elastomeric polymer, and an inorganic filler, the resin composition during molding has a fluidity. Excellent in physical properties such as flexural modulus, hardness and embrittlement temperature. In addition, the flow mark and the eld mark which usually appear on the surface of the molded product are almost inconspicuous when this resin composition is used. Therefore, the resin composition according to the present invention has sufficient mechanical strength characteristics when molding automotive exterior parts and has a good appearance of the molded product, so that the resin composition can be used as it is, that is, without coating. Can be used.
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Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP02728101A EP1400565B1 (en) | 2001-05-24 | 2002-05-22 | Resin composition for automobile exterior parts |
| US10/332,368 US6838510B2 (en) | 2001-05-24 | 2002-05-22 | Resin composition for automotive exterior parts |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001-155554 | 2001-05-24 | ||
| JP2001155554 | 2001-05-24 |
Publications (1)
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| WO2002094933A1 true WO2002094933A1 (en) | 2002-11-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/JP2002/004936 Ceased WO2002094933A1 (en) | 2001-05-24 | 2002-05-22 | Resin composition for automobile exterior parts |
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| Country | Link |
|---|---|
| US (1) | US6838510B2 (ja) |
| EP (1) | EP1400565B1 (ja) |
| CZ (1) | CZ2003226A3 (ja) |
| WO (1) | WO2002094933A1 (ja) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7553887B2 (en) * | 2002-08-22 | 2009-06-30 | Prime Polymer Co., Ltd. | Resin composition for automotive parts |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2005194297A (ja) * | 2003-12-26 | 2005-07-21 | Toyoda Gosei Co Ltd | プロピレン系樹脂組成物 |
| CN101855293B (zh) * | 2007-11-09 | 2012-12-05 | 普瑞曼聚合物株式会社 | 汽车材料用聚丙烯类树脂组合物 |
| JP5636320B2 (ja) * | 2011-03-29 | 2014-12-03 | 日本ポリプロ株式会社 | 自動車部材用ポリプロピレン系樹脂組成物及び自動車用外装部材 |
| KR101440384B1 (ko) | 2012-11-26 | 2014-11-04 | 한일이화 주식회사 | 자동차 내외장재용 조성물 |
| ES2542435T3 (es) | 2012-11-29 | 2015-08-05 | Borealis Ag | Modificador del defecto de rayas de tigre |
| WO2015005239A1 (ja) * | 2013-07-08 | 2015-01-15 | 株式会社プライムポリマー | プロピレン系樹脂組成物 |
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| JP2000256531A (ja) * | 1999-03-05 | 2000-09-19 | Grand Polymer:Kk | ポリオレフィン系組成物 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2802023B2 (ja) * | 1993-08-10 | 1998-09-21 | 宇部興産株式会社 | 強化ポリプロピレン樹脂組成物 |
| JP3213481B2 (ja) * | 1994-07-07 | 2001-10-02 | トヨタ自動車株式会社 | 自動車内装用ポリプロピレン樹脂組成物 |
| AU696168B2 (en) * | 1995-04-28 | 1998-09-03 | Sumitomo Chemical Company, Limited | Thermoplastic resin composition |
| AU699597B2 (en) * | 1995-07-17 | 1998-12-10 | Toyota Jidosha Kabushiki Kaisha | Polypropylene resin composition |
| KR100222350B1 (ko) * | 1995-10-09 | 1999-10-01 | 나카히로 마오미 | 자동차 외장재용 폴리프로필렌 수지 조성물 |
| JP3290076B2 (ja) * | 1995-12-01 | 2002-06-10 | 宇部興産株式会社 | ポリプロピレン樹脂組成物 |
| US5880198A (en) * | 1996-03-04 | 1999-03-09 | Tonen Chemical Corporation | Thermoplastic resin composition comprising propylene elastomer, and talc components |
| JP3347958B2 (ja) * | 1996-11-26 | 2002-11-20 | 日本ポリケム株式会社 | プロピレン系樹脂組成物 |
| US6759475B2 (en) * | 1997-04-24 | 2004-07-06 | Mitsui Chemicals, Inc. | Resin composition based on crystalline polypropylene |
| DE19821718A1 (de) * | 1997-05-15 | 1998-11-19 | Sumitomo Chemical Co | Harzmasse auf Polypropylenbasis und spritzgeformter Gegenstand daraus |
| US6180709B1 (en) * | 1997-05-16 | 2001-01-30 | Japan Polychem Corporation | Thermoplastic polypropylene composition |
| DE19821937B4 (de) * | 1997-05-16 | 2013-03-14 | Sumitomo Chemical Co., Ltd. | Harzmasse auf Polypropylenbasis, spritzgeformter Gegenstand daraus und Verwendung einer Harzmasse auf Polypropylenbasis zur Herstellung von Formkörpern |
| EP0926195A1 (en) * | 1997-12-26 | 1999-06-30 | Japan Polychem Corporation | Polypropylene resin composition |
-
2002
- 2002-05-22 EP EP02728101A patent/EP1400565B1/en not_active Expired - Lifetime
- 2002-05-22 US US10/332,368 patent/US6838510B2/en not_active Expired - Fee Related
- 2002-05-22 CZ CZ2003226A patent/CZ2003226A3/cs unknown
- 2002-05-22 WO PCT/JP2002/004936 patent/WO2002094933A1/ja not_active Ceased
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000256531A (ja) * | 1999-03-05 | 2000-09-19 | Grand Polymer:Kk | ポリオレフィン系組成物 |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7553887B2 (en) * | 2002-08-22 | 2009-06-30 | Prime Polymer Co., Ltd. | Resin composition for automotive parts |
Also Published As
| Publication number | Publication date |
|---|---|
| US20030176554A1 (en) | 2003-09-18 |
| EP1400565A4 (en) | 2006-12-06 |
| US6838510B2 (en) | 2005-01-04 |
| EP1400565A1 (en) | 2004-03-24 |
| EP1400565B1 (en) | 2008-09-10 |
| CZ2003226A3 (cs) | 2003-05-14 |
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