JP5937716B2 - Contact parts with reduced squeaking noise - Google Patents

Description

  The present invention relates to a contact part, and more particularly, to a contact part made of a thermoplastic resin composition in which the squeaking noise generated by contacting and rubbing with other members is greatly reduced.

  ABS resins are widely used in the manufacture of automotive interior parts due to their excellent mechanical properties, heat resistance, and moldability.

  However, due to vibrations during automobile travel, ABS interior parts made of ABS resin may be used together with other parts and other parts such as polyvinyl chloride, chloroprene rubber, polyurethane, natural rubber, polyester or polyethylene lining sheets, foam, etc. In the case where they come into contact with each other and rub against each other, a squeaking noise (friction) may be generated. For example, a ventilator made of ABS resin is equipped with a valve shutter that uses chloroprene rubber foam as a sealing material to adjust the air volume. When the valve shutter is rotated to adjust the air volume, the ABS resin The case of the ventilator made of metal and the case of the sealing material as another member may rub against each other, and a squeaking noise may occur.

In addition, since ABS resin and ASA resin are amorphous resins, they have a higher coefficient of friction compared to crystalline resins such as polyethylene, polypropylene, and polyacetal, and are used for air conditioner outlets and car stereo buttons in automobiles. As described above, when mating with a member made of another resin, it is well known that a stick-slip phenomenon as shown in FIG. ing. The stick-slip phenomenon occurs when two objects rub against each other, and an object M connected by a spring is placed on a driving table that moves at a driving speed V as shown in the model of FIG. In this case, first, the object M moves to the right as shown in FIG. When the force that the object M is about to return to the original by the spring becomes equal to the static friction force, the object M starts to slide in the direction opposite to the driving speed V. At this time, the object M receives a dynamic frictional force, but when the force of the spring and the dynamic frictional force become equal, the sliding stops and the object M becomes attached to the driving table again. It moves again in the same direction as the drive speed V (FIG. 2D). In this way, when an object is slid, it refers to a phenomenon of repeatedly catching or sliding on the way, which is called a stick-slip phenomenon, and the object M is subjected to a load with time as shown in FIG. It is said that if the difference Δμ between the static friction coefficient μs in FIG. 1 (at the time of FIG. 2B) and μl at the lower end of the sawtooth waveform (at the time of FIG. 2C) is large, itching is likely to occur. The dynamic friction coefficient is an intermediate value between μs and μl.
These squeaking noises are a major cause of impairing comfort and quietness when riding, and there is a strong demand for reduction of squeaking noises.

  On the other hand, it is known that the stick-slip phenomenon appears remarkably when the friction speed dependency of the friction coefficient obtained by Ammonton-Coulomb's law takes a negative value (see Non-Patent Document 1). By making the friction speed dependency close to zero or a positive value of zero or more, it is possible to suppress the occurrence of stick-slip phenomenon and reduce the occurrence of squeaking noise.

  Therefore, in order to prevent such squeaking noise, a method of applying a Teflon (registered trademark) coating to the surface of the member, a method of mounting a Teflon (registered trademark) tape, a method of applying silicone oil, etc. have been performed. The process such as coating is not only complicated and time-consuming, but also has a problem that the effect is not maintained when it is placed at a high temperature for a long time.

  Further, as a method for modifying the material itself used for automobile interior parts, a method of blending silicone oil with ABS resin, a method of blending an epoxy-containing olefin copolymer with ABS resin, and the like have been proposed. For example, a technique of blending an organosilicon compound into a resin made of polycarbonate resin and ABS resin (see Patent Document 1), and a technique of blending a flame retardant, a flame retardant aid and silicone oil into ABS resin (see Patent Document 2) ), A technique of blending silicone oil into ABS resin, MBS resin and HIPS (high impact polystyrene) resin (see Patent Document 3), and a technique of blending alkanesulfonate surfactant into ABS resin (Patent Document 4). In addition, a modified polyorganosiloxane containing at least one reactive group selected from an epoxy group, a carboxyl group and an acid anhydride group is added to the ABS resin to increase water repellency and increase the water in the bathroom and toilet. A technique (see Patent Document 5) used for a rotating part is disclosed.

  However, the stagnation noise reduction effect by these methods is not sufficient, and even if it shows a certain level of stagnation noise prevention effect immediately after molding, the effect persists poorly, especially when placed at high temperatures for a long time Has a problem that its effect is greatly reduced.

Japanese Patent Publication No. 63-56267 Japanese Patent No. 2798396 Japanese Patent No. 2688619 Japanese Patent No. 2659467 JP 10-316833 A

Surface Science Vol.24, No.6, PP 328-333, 2003

  In view of such circumstances, the present invention significantly reduces the occurrence of squeaking noise that occurs when the members rub against each other, and maintains the squeaking noise reduction effect even when placed under high temperature for a long time, and Is intended to provide a contact component comprising a thermoplastic resin composition having excellent impact resistance.

  As a result of diligent research to solve the above problems, the present inventors have significantly reduced the occurrence of squeaking noise by adding a specific amount of a specific silicone oil to a specific rubber-modified vinyl resin, and at a high temperature. It has been found that a contact component made of a thermoplastic resin composition excellent in impact resistance can be obtained, even when left under a long time, the squeaking noise reduction effect is maintained without deterioration. It came to be completed.

According to the present invention, the following contact parts are provided. That is,
1. The rubber-reinforced vinyl resin (A) 100 parts by weight of a silicone oil kinematic viscosity at 25 ° C. as measured by Ubbelohde viscometer according to ASTM D445-46T or JIS 8803 is 200 ～100,000CSt [B] 0.1 to 8 Combining parts by mass,
The rubber-reinforced vinyl resin [A] includes a rubber-reinforced vinyl resin [A1] obtained by polymerizing a vinyl monomer [b1] in the presence of a diene rubber polymer [a1], ethylene A rubber-reinforced vinyl resin [A2] obtained by polymerizing a vinyl monomer [b2] in the presence of an α-olefin rubber polymer [a2],
The total amount of the diene rubbery polymer [a1] and the ethylene / α-olefin rubbery polymer [a2] is 5 to 30% by mass based on 100% by mass of the entire rubber-reinforced vinyl resin [A]. And
The weight ratio of the diene-based rubbery polymer [a1] and the ethylene · alpha-olefin-based rubbery polymer [a2] [a1]: [a2] is 10 to 66: a 90 to 34,
The vinyl-based monomer [b1] and [b2] is Ri Do a thermoplastic resin composition comprising an aromatic vinyl compound and a vinyl cyanide compound, the thermoplastic resin composition or another made of other thermoplastic resin method for producing contact parts, characterized in Rukoto used in contact with rub parts and members.
2. 2. The rubber-reinforced vinyl resin [A] further comprises a (co) polymer [C] of a vinyl monomer [b3] containing an aromatic vinyl compound and a vinyl cyanide compound. Manufacturing method for contact parts.
3. 3. The method for producing a contact component according to 1 or 2 above, wherein the ethylene / α-olefin rubber polymer [a2] has an ethylene: α-olefin mass ratio of 5 to 95:95 to 5.
4). 4. The method for producing a contact part according to any one of 1 to 3, wherein the ethylene / α-olefin rubbery polymer [a2] is an ethylene / propylene copolymer.
5 . 5. The method for producing a contact component according to any one of 1 to 4 above, wherein the other thermoplastic resin is polycarbonate / ABS.

  According to the present invention, by adding a specific amount of a specific silicone oil to a specific rubber-modified vinyl resin, the squeaking noise generated when the members rub against each other is significantly reduced, and the resin is placed at a high temperature for a long time. Even in such a case, it is possible to obtain a contact component made of a thermoplastic resin composition, in which the effect of reducing squeaking noise does not decrease.

FIG. 1 is an explanatory diagram of the stick-slip phenomenon. FIGS. 2A, 2B, 2C, and 2D are stick-slip model diagrams.

Hereinafter, the present invention will be described in detail.
The thermoplastic resin composition forming the contact component in the present invention is composed of 100 parts by mass of rubber-reinforced vinyl resin [A], silicone oil [B] 0.1 having a kinematic viscosity at 25 ° C. of 10 to 100,000 cSt. ~ 8 parts by mass,
The rubber-reinforced vinyl resin [A] contains a diene rubber polymer [a1] and an ethylene / α-olefin rubber polymer [a2],
The total amount of the diene rubbery polymer [a1] and the ethylene / α-olefin rubbery polymer [a2] is 5 to 30% by mass based on 100% by mass of the entire rubber-reinforced vinyl resin [A]. And
The mass ratio [a1]: [a2] of the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] is 10 to 85: 90-15.
It is characterized by being.

  In the present specification, “(co) polymerization” means homopolymerization and copolymerization, “(meth) acryl” means acryl and / or methacryl, and “(meth) acrylate” Means acrylate and / or methacrylate.

1. Rubber-reinforced vinyl resin [A] (hereinafter also referred to as “component [A]”):
The component [A] used in the present invention is a rubber-reinforced vinyl resin [A1] obtained by polymerizing a vinyl monomer [b1] in the presence of a diene rubber polymer [a1], ethylene · α A rubber-reinforced vinyl resin [A2] obtained by polymerizing the vinyl monomer [b2] in the presence of the olefin rubber polymer [a2], and, if necessary, a vinyl monomer [ b3] is a rubber-reinforced vinyl resin made of a mixture with the (co) polymer [C]. The (co) polymer [C] is obtained by polymerizing the vinyl monomer [b3] in the absence of the rubbery polymer.

1-1. Diene rubbery polymer [a1] (hereinafter also referred to as “component [a1]”):
The rubbery polymers contained in the rubber-reinforced vinyl resin [A] are a diene rubbery polymer [a1] and an ethylene / α-olefin rubbery polymer [a2].
Diene rubber polymer [a1] includes homopolymers such as polybutadiene and polyisoprene; styrene / butadiene copolymer, styrene / butadiene / styrene copolymer, acrylonitrile / styrene / butadiene copolymer, and acrylonitrile / butadiene. Butadiene copolymers such as copolymers; styrene / isoprene copolymers, styrene / isoprene / styrene copolymers, isoprene copolymers such as acrylonitrile / styrene / isoprene copolymers, and the like. These may be random copolymers or block copolymers, and may be used alone or in combination of two or more. The diene rubbery polymer [a1] may be a crosslinked polymer or an uncrosslinked polymer.

1-2. Ethylene / α-olefin rubbery polymer [a2] (hereinafter also referred to as “component [a2]”):
Examples of the ethylene / α-olefin rubbery polymer [a2] include an ethylene / α-olefin copolymer and an ethylene / α-olefin / non-conjugated diene copolymer. Examples of the α-olefin constituting the component [a2] include α-olefins having 3 to 20 carbon atoms, specifically, propylene, 1-butene, 1-pentene, 1-hexene, 4- Examples include methyl-1-pentene, 1-heptene, 1-octene, 1-decene, 1-dodecene, 1-hexadecene, 1-eicosene and the like. These α-olefins can be used alone or in admixture of two or more. The carbon number of the α-olefin is preferably 3 to 20, more preferably 3 to 12, and still more preferably 3 to 8. When the number of carbon atoms exceeds 20, the copolymerizability is lowered and the surface appearance of the molded product may not be sufficient. The mass ratio of ethylene: α-olefin is usually 5 to 95:95 to 5, preferably 50 to 90:50 to 10, more preferably 60 to 88:40 to 12. When the α-olefin mass ratio exceeds 95, the weather resistance is not sufficient. On the other hand, when it is less than 5, the rubber elasticity of the rubbery polymer is not sufficient, so that sufficient impact resistance may not be exhibited. .
Among these, from the viewpoint of reducing squeaking noise, an ethylene / α-olefin copolymer is preferable, and an ethylene / propylene copolymer is particularly preferable.

Non-conjugated dienes include alkenyl norbornenes, cyclic dienes and aliphatic dienes, with 5-ethylidene-2-norbornene and dicyclopentadiene being preferred. These non-conjugated dienes can be used alone or in admixture of two or more. The ratio of the nonconjugated diene to the total amount of the rubbery polymer is usually 0 to 30% by mass, preferably 0 to 20% by mass, and more preferably 0 to 10% by mass. If the proportion of the non-conjugated diene exceeds 30% by mass, the molded appearance and weather resistance may not be sufficient. In addition, the amount of unsaturated groups in component [a1] is preferably in the range of 4 to 40 in terms of iodine value. If the iodine value exceeds 40, the molding appearance and weather resistance of the molded product may not be sufficient, and if the iodine value is less than 4, the impact resistance of the molded product may not be sufficient.
Moreover, the Mooney viscosity (ML1 _{+ 4} , 100 degreeC; based on JISK6300) of component [a2] is 5-80 normally, Preferably it is 10-65, More preferably, it is 15-45. When the Mooney viscosity exceeds 80, the fluidity of the resulting rubber-reinforced vinyl resin is insufficient, and when the Mooney viscosity is less than 5, the resulting molded article may have insufficient impact resistance.

  In addition, this ethylene / α-olefin rubbery polymer [a2] is a polymer obtained by hydrogenating a block (co) polymer obtained by using a conjugated diene compound such as butadiene or isoprene (of a conjugated diene moiety). The hydrogenation rate of the double bond is preferably 90% or more from the viewpoint of weather resistance. The polymer may be a crosslinked polymer or an uncrosslinked polymer.

1-3. Vinyl monomers [b1] to [b3]:
The vinyl monomers [b1], [b2] and [b3] are not particularly limited as long as they are all polymerizable compounds having an unsaturated bond.
The vinyl monomers [b1], [b2] and [b3] usually contain an aromatic vinyl compound and a vinyl cyanide compound. In addition, if necessary, other copolymerizable vinyl monomers such as (meth) acrylic acid ester and maleimide compound, carboxyl group, acid anhydride group, hydroxyl group, amino group, amide group, epoxy group A functional group-containing vinyl monomer having at least one functional group such as an oxazoline group may be used in combination. The vinyl monomers [b1] and [b2] used for forming the rubber-reinforced vinyl resins [A1] and [A2] may be the same as or different from each other.
The vinyl monomer [b3] used for forming the (co) polymer [C] may be the same as or different from the vinyl monomer [b1] and / or [b2]. May be.

  The aromatic vinyl compound is not particularly limited as long as it is a compound having at least one vinyl bond and at least one aromatic ring. Examples include styrene, α-methyl styrene, o-methyl styrene, p-methyl styrene, vinyl toluene, β-methyl styrene, ethyl styrene, pt-butyl styrene, vinyl xylene, vinyl naphthalene, monochlorostyrene, dichloromethane. Examples thereof include styrene, monobromostyrene, dibromostyrene, and fluorostyrene. These can be used alone or in combination of two or more. Of these, styrene and α-methylstyrene are preferred.

  Examples of the vinyl cyanide compound include acrylonitrile and methacrylonitrile. These can be used alone or in combination of two or more. Of these, acrylonitrile is preferred.

  Examples of the (meth) acrylic acid ester include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, amyl acrylate, hexyl acrylate, octyl acrylate, 2-ethylhexyl acrylate, cyclohexyl acrylate, acrylic acid Acrylic esters such as phenyl and benzyl acrylate; methyl methacrylate, ethyl methacrylate, propyl methacrylate, butyl methacrylate, amyl methacrylate, hexyl methacrylate, octyl methacrylate, 2-ethylhexyl methacrylate, dodecyl methacrylate, methacrylic acid And methacrylic acid esters such as octadecyl acid, cyclohexyl methacrylate, phenyl methacrylate, and benzyl methacrylate. These can be used alone or in combination of two or more. Of these, methyl methacrylate is preferred.

Examples of the maleimide compound include maleimide, N-methylmaleimide, N-butylmaleimide, N-cyclohexylmaleimide, and N-phenylmaleimide. These can be used alone or in combination of two or more. Of these, N-cyclohexylmaleimide and N-phenylmaleimide are preferable.
As a method for introducing a monomer unit comprising this maleimide compound into a polymer, there is a method in which maleic anhydride is copolymerized in advance and then imidized.

  Among the functional group-containing vinyl monomers, examples of the unsaturated compound having a carboxyl group include acrylic acid, methacrylic acid, ethacrylic acid, maleic acid, fumaric acid, itaconic acid, crotonic acid, and cinnamic acid. . These can be used alone or in combination of two or more.

Examples of the unsaturated compound having an acid anhydride group include maleic anhydride, itaconic anhydride, and citraconic anhydride. These can be used alone or in combination of two or more.
Examples of unsaturated compounds having a hydroxyl group include hydroxystyrene, 3-hydroxy-1-propene, 4-hydroxy-1-butene, cis-4-hydroxy-2-butene, trans-4-hydroxy-2-butene, 3 -Hydroxy-2-methyl-1-propene, 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, N- (4-hydroxyphenyl) maleimide and the like. These can be used alone or in combination of two or more.

As unsaturated compounds having an amino group, aminoethyl acrylate, propylaminoethyl acrylate, dimethylaminomethyl acrylate, diethylaminomethyl acrylate, 2-dimethylaminoethyl acrylate, aminoethyl methacrylate, propylaminoethyl methacrylate , Dimethylaminomethyl methacrylate, diethylaminomethyl methacrylate, 2-dimethylaminoethyl methacrylate, phenylaminoethyl methacrylate, p-aminostyrene, N-vinyldiethylamine, N-acetylvinylamine, acrylicamine, methacrylamine, N- Examples include methylacrylamine. These can be used alone or in combination of two or more.
Examples of the unsaturated compound having an amide group include acrylamide, N-methylacrylamide, methacrylamide, N-methylmethacrylamide and the like. These can be used alone or in combination of two or more.

  Examples of the unsaturated compound having an epoxy group include glycidyl acrylate, glycidyl methacrylate, and allyl glycidyl ether. These can be used alone or in combination of two or more.

  Examples of the unsaturated compound having an oxazoline group include vinyl oxazoline. These can be used alone or in combination of two or more.

  The vinyl monomers [b1], [b2] and [b3] are selected according to their purpose, usage, etc., and their types and amounts used. The total amount of the aromatic vinyl compound and the vinyl cyanide compound is as follows. The total amount of vinyl monomers is 100 to 100% by mass, usually 30 to 100% by mass, preferably 50 to 100% by mass, and more preferably 70 to 100% by mass. The content of the other copolymerizable vinyl monomer is usually 0 to 70% by mass, preferably 0 to 50% by mass, more preferably 0 to 30% with respect to 100% by mass of the whole vinyl monomer. % By mass. The content of the functional group-containing vinyl monomer is usually 0 to 40% by mass, preferably 0 to 30% by mass, more preferably 0 to 20% by mass with respect to 100% by mass of the total amount of the vinyl monomer. %. The use ratio of the aromatic vinyl compound and the vinyl cyanide compound (aromatic vinyl compound / vinyl cyanide compound) is usually 40 to 85% by mass / 15 to 60% by mass when the total of these is 100% by mass. Preferably, it is 45-85 mass% / 15-55 mass%.

1-4. Method for producing the rubber-reinforced vinyl resin [A]:
The rubber-reinforced vinyl resin [A] is a polymer component containing a diene rubber polymer [a1] and an ethylene / α-olefin rubber polymer [a2]. It is not limited.
In the rubber-reinforced vinyl resin [A], a graft copolymer in which a (co) polymer of a vinyl monomer is grafted to a rubber polymer, and a rubber polymer are not grafted. (Co) polymers of vinyl monomers are included. However, this graft copolymer may contain a rubbery polymer to which a (co) polymer of a vinyl monomer is not grafted.
Accordingly, the content of the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] is exemplified below.
(1) The case where both the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] are contained as a graft copolymer.
(2) The case where either one of the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] is contained as a graft copolymer.
(3) The case where both the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] are contained as an ungrafted rubber polymer.
Of these, (1) is particularly preferred.

Examples of the rubber-reinforced vinyl resin [A] of the above aspect (1) are as follows.
[I] A rubber-reinforced vinyl resin [A1] obtained by polymerizing a vinyl monomer [b1] in the presence of the diene rubber polymer [a1], and the ethylene / α-olefin system. A mixture comprising a rubber-reinforced vinyl resin [A2] obtained by polymerizing a vinyl monomer [b2] in the presence of a rubbery polymer [a2].
[Ii] A mixture comprising the above mixture [i] and a (co) polymer of the vinyl monomer [b3] (hereinafter also referred to as “(co) polymer [C]”).
[Iii] Rubber reinforcement obtained by polymerizing vinyl monomer [b1] in the presence of the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] Vinyl resin [A3].
[Iv] A mixture comprising the rubber-reinforced vinyl resin [A3] and the (co) polymer [C].
Among these, [i] and [ii] are preferable from the viewpoint of productivity, and [ii] is particularly preferable.
The rubber-reinforced vinyl resin [A] may be a combination of two or more of the above [i], [ii], [iii] and [iv].

Next, a method for producing the rubber-reinforced vinyl resins [A1], [A2] and [A3] will be described.
Examples of the polymerization method include known polymerization methods such as emulsion polymerization, solution polymerization, suspension polymerization, and bulk polymerization. In any case, in the presence of the rubbery polymer, the vinyl monomer may be charged all at once, and may be reacted, or may be divided or continuously added for reaction. Further, the rubbery polymer may be added or reacted in the whole or in part during the polymerization with the vinyl monomer.
In addition, the usage-amount of a rubber-like polymer is 5-80 mass% normally when the sum total of a rubber-like polymer and a vinyl-type monomer is 100 mass%, Preferably it is 10-70 mass%.

As the method for producing the rubber-reinforced vinyl resin [A1], emulsion polymerization, solution polymerization and suspension polymerization are preferable, and emulsion polymerization is more preferable. As the method for producing the rubber-reinforced vinyl resin [A2], emulsion polymerization, solution polymerization and bulk polymerization are preferable, and solution polymerization is more preferable. As the method for producing the rubber-reinforced vinyl resin [A3], emulsion polymerization and solution polymerization are preferable.
When the above rubber-reinforced vinyl resins [A1], [A2] and [A3] are produced by emulsion polymerization, a polymerization initiator, a chain transfer agent, an emulsifier, water and the like are usually used. In addition, when the said rubbery polymer is not a latex form but a solid form, it can be used as a latex form by re-emulsification.

As the polymerization initiator, a combination of an organic peroxide such as cumene hydroperoxide, diisopropylbenzene hydroperoxide, paramentane hydroperoxide and a reducing agent represented by a sugar-containing pyrophosphate formulation, a sulfoxylate formulation, etc. Redox polymerization initiators by: persulfates such as potassium persulfate; peroxides such as benzoyl peroxide (BPO), lauroyl peroxide, t-butyl peroxylaurate, t-butyl peroxymonocarbonate; Examples thereof include azo polymerization initiators such as 2′-azobis (isobutyronitrile). These can be used alone or in combination of two or more. The amount of the polymerization initiator used is usually 0.05 to 5% by mass, preferably 0.1 to 1% by mass, based on the total amount of the vinyl monomer [b1] or [b2].
The polymerization initiator is usually added all at once or continuously to the reaction system.

  Examples of chain transfer agents include mercaptans such as octyl mercaptan, n-dodecyl mercaptan, t-dodecyl mercaptan, n-hexyl mercaptan, n-hexadecyl mercaptan, n-tetradecyl mercaptan, t-tetradecyl mercaptan; terpinolenes, α -Methylstyrene dimer, tetraethylthiuram sulfide, acrolein, methacrolein, allyl alcohol, 2-ethylhexylthioglycol and the like. These can be used alone or in combination of two or more. The amount of the chain transfer agent used is usually 0.05 to 2% by mass with respect to the total amount of the vinyl monomer [b1] or [b2].

  Examples of the emulsifier include anionic surfactants and nonionic surfactants. Examples of the anionic surfactant include sulfates of higher alcohols; alkylbenzene sulfonates such as sodium dodecylbenzene sulfonate; aliphatic sulfonates such as sodium lauryl sulfate; rosinates and phosphates. Examples of nonionic surfactants include polyethylene glycol alkyl ester compounds and alkyl ether compounds. These can be used alone or in combination of two or more. The usage-amount of the said emulsifier is 0.3-5 mass% normally with respect to the whole quantity of the said vinylic monomer [b1] or [b2].

  Emulsion polymerization can be performed under known conditions according to the type and amount of the vinyl monomer [b1] or [b2] used, the polymerization initiator, and the like. The latex obtained by the above emulsion polymerization is usually purified by coagulating with a coagulant to form a polymer component in powder form, and then washing with water and drying. Examples of the coagulant include inorganic salts such as calcium chloride, magnesium sulfate, magnesium chloride, and sodium chloride; inorganic acids such as sulfuric acid and hydrochloric acid; organic acids such as acetic acid, lactic acid, and citric acid. These can be used alone or in combination of two or more. Further, depending on the required performance, washing may be carried out after adding an alkali component or an acid component after solidification to neutralize it.

When the above rubber-reinforced vinyl resins [A1], [A2] and [A3] are produced by solution polymerization, usually a solvent, a polymerization initiator, a chain transfer agent and the like are used.
Examples of the solvent include inert polymerization solvents used in known radical polymerization, for example, aromatic hydrocarbons such as ethylbenzene and toluene; ketones such as methyl ethyl ketone and acetone; halogenated hydrocarbons such as dichloromethylene and carbon tetrachloride. Acetonitrile, dimethylformamide, N-methylpyrrolidone and the like can be used. These can be used alone or in combination of two or more.

Examples of the polymerization initiator include organic peroxides such as ketone peroxide, dialkyl peroxide, diacyl peroxide, peroxy ester, and hydroperoxide. These can be used alone or in combination of two or more.
Examples of chain transfer agents include mercaptans, terpinolenes, α-methylstyrene dimers, and the like. These can be used alone or in combination of two or more.

  Solution polymerization can be carried out under known conditions depending on the type of vinyl monomer [b1] or [b2] used, the polymerization initiator, and the like. The polymerization temperature is usually in the range of 80 to 140 ° C. In addition, in the case of solution polymerization, it can also manufacture without using a polymerization initiator.

  Also in the case of bulk polymerization and suspension polymerization, known methods can be applied. As the polymerization initiator, chain transfer agent and the like used in these methods, for example, compounds exemplified in solution polymerization can be used.

1-5. Physical properties of rubber-reinforced vinyl resin [A]:
The graft ratios of the rubber-reinforced vinyl resins [A1], [A2] and [A3] obtained as described above are usually 10 to 150% by mass, preferably 20 to 120% by mass. When the graft ratio is less than 10% by mass, the interfacial strength between the graft copolymer and the (co) polymer of the vinyl monomer [b1] or [b2] is inferior, and the impact resistance may not be sufficient. . On the other hand, if it exceeds 150% by mass, the layer made of the (co) polymer of the vinyl monomer [b1] or [b2] on the surface of the rubber polymer becomes thick, and the rubber polymer is grafted inside. Since the layer made of the (co) polymer is developed, the rubber elasticity is lowered, and as a result, the impact resistance may be lowered.

  The graft ratio can be determined by the following formula.

  Graft ratio (mass%) = {(S−T) / T} × 100

  In the above formula, S represents 1 gram of rubber-reinforced vinyl resin in 20 ml of acetone (acetonitrile when the rubbery polymer is an acrylic rubber) and shakes with a shaker for 2 hours at 25 ° C. After that, the mass (g) of insoluble matter obtained by centrifuging for 60 minutes with a centrifuge (rotation speed: 23,000 rpm) under a temperature condition of 5 ° C. to separate the insoluble matter and the soluble matter. Yes, T is the mass (g) of the rubbery polymer contained in 1 gram of rubber-reinforced vinyl resin. The mass of the rubbery polymer can be obtained by a method of calculating from a polymerization prescription and a polymerization conversion rate, a method of obtaining from an infrared absorption spectrum (IR), and the like.

  In addition, the intrinsic viscosity [η] (measured in methyl ethyl ketone at 30 ° C.) of the acetone-soluble components of the rubber-reinforced vinyl resins [A1], [A2] and [A3] is usually 0.1 to 1. 0.5 dl / g, preferably 0.2 to 1.0 dl / g. When the intrinsic viscosity [η] is within the above range, the physical property balance between molding processability and impact resistance is excellent.

The intrinsic viscosity [η] was measured by the following method. First, acetone-soluble components of the rubber-reinforced vinyl resins [A1], [A2], and [A3] were dissolved in methyl ethyl ketone, and five different concentrations were prepared. The intrinsic viscosity [η] was determined from the results of measuring the reduced viscosity of each concentration at 30 ° C. using an Ubbelohde viscosity tube. The unit is dl / g.
The intrinsic viscosity can be adjusted by appropriately selecting the type and amount of chain transfer agent used during production, the type and amount of polymerization initiator, the polymerization temperature, and the like.

  As described above, the rubber-reinforced vinyl resin [A] according to the present invention may be a mixture of separately prepared rubber-reinforced vinyl resins [A1] and [A2]. Rubber reinforced vinyl resin [A3] obtained by polymerizing vinyl monomer [b1] in the presence of rubber polymer [a1] and ethylene / α-olefin rubber polymer [a2] It may be used. Therefore, when using a plurality of rubber-reinforced vinyl resins such as the former, a mixture of resins obtained in each manufacturing process may be used, but as another method, for example, each resin is obtained by emulsion polymerization. Can be obtained by mixing latexes and then coagulating them.

1-6. Production method of (co) polymer [C]:
In addition, the (co) polymer [C] is obtained by polymerizing the vinyl monomer [b3] by a known method such as solution polymerization, bulk polymerization, emulsion polymerization or suspension polymerization in the presence of a polymerization initiator or the like. Can be manufactured. These polymerizations may be catalytic polymerization using a polymerization initiator, or may be thermal polymerization without using a polymerization initiator.

1-7. Physical properties of (co) polymer [C]:
The intrinsic viscosity [η] (measured in methyl ethyl ketone at 30 ° C.) of the polymer [C] is usually 0.1 to 1.5 dl / g, preferably 0.2 to 1.0 dl / g. When the intrinsic viscosity [η] is within the above range, the physical property balance between molding processability and impact resistance is excellent.

The intrinsic viscosity [η] was measured by the following method. First, the above (co) polymer [C] was dissolved in methyl ethyl ketone to prepare 5 samples having different concentrations. The intrinsic viscosity [η] was determined from the results of measuring the reduced viscosity of each concentration at 30 ° C. using an Ubbelohde viscosity tube. The unit is dl / g.
The intrinsic viscosity can be adjusted by appropriately selecting the type and amount of chain transfer agent used during production, the type and amount of polymerization initiator, the polymerization temperature, and the like.

2. Silicone oil [B] (hereinafter also referred to as “component [B]”):
The silicone oil as the component [B] used in the present invention is not particularly limited except the kinematic viscosity at 25 ° C. Any known oil can be used as long as it has a polyorganosiloxane structure. The silicone oil [B] may be an unmodified silicone oil such as dimethyl silicone oil, methylphenyl silicone oil, methyl hydrogen silicone oil, or a part of side chains in the polyorganosiloxane structure and / or polyorgano It may be a modified silicone oil in which various organic groups are introduced into one terminal part of the siloxane structure or both terminal parts of the polyorganosiloxane structure. Examples of the modified silicone oil include alkyl modified silicone oil, polyether modified silicone oil, fluorine modified silicone oil, higher alkoxy modified silicone oil, higher fatty acid modified silicone oil, methyl styryl modified silicone oil, methyl chlorinated phenyl silicone oil, methyl hydro Diene silicone oil, amino modified silicone oil, epoxy modified silicone oil, carboxyl modified silicone oil, acrylic modified silicone oil, methacryl modified silicone oil, mercapto modified silicone oil, phenol modified silicone oil, carbinol modified silicone oil, etc. may be used. it can.
These silicone oils may be used alone or in combination of two or more.

  The kinematic viscosity at 25 ° C. of the silicone oil [B] used in the present invention is 10 to 100,000 cSt, preferably 10 to 50,000 cSt, more preferably 25 to 50,000 cSt, and still more preferably 50 to 30,000 cSt, particularly preferably 200 to 15,000 cSt. When the kinematic viscosity at 25 ° C. of the silicone oil [B] is less than 10 cSt, the effect of reducing the squeaking noise is inferior. On the other hand, when the kinematic viscosity exceeds 100,000 cSt, the silicone oil [B] in the rubber-reinforced vinyl resin [A] [ The dispersibility of B] is deteriorated, the impact resistance and the stagnation noise reduction effect are not stably exhibited, and the extrusion processability at the time of melt-kneading is also lowered.

  The kinematic viscosity of the silicone oil was measured by an Ubbelohde viscometer according to ASTM D445-46T (JIS 8803 is acceptable).

3. Thermoplastic resin composition:
The thermoplastic resin composition in the present invention can be obtained by mixing the above-mentioned component [A], the above-mentioned component [B] and, if desired, the above-mentioned component [C] at a predetermined blending ratio, and melt-kneading.

  The compounding amount of the silicone oil [B] with respect to 100 parts by mass of the rubber-reinforced vinyl resin [A] is 0.1 to 8 parts by mass, preferably 0.2 to 6 parts by mass, more preferably 0.5 to 5 parts. Part by mass, particularly preferably 2.5 to 3.5 parts by mass. If the amount of the component [B] is less than 0.1 parts by mass, the effect of reducing the squeaking noise cannot be obtained. On the other hand, when the compounding amount of the component [B] exceeds 8 parts by mass, the appearance and impact resistance of the molded product are deteriorated, and melt-mixing becomes difficult.

  The total amount of the diene rubbery polymer [a1] and the ethylene / α-olefin rubbery polymer [a2] in the component [A] is 100 masses of the whole rubber-reinforced vinyl resin [A]. % Is 5 to 30% by mass, preferably 5 to 25% by mass, more preferably 8 to 20% by mass, and particularly preferably 10 to 18% by mass. When the total amount is less than 5% by mass, the impact resistance is inferior, whereas when it exceeds 30% by mass, the heat resistance is lowered.

  The mass ratio [a1]: [a2] of the diene rubber polymer [a1] and the ethylene / α-olefin rubber polymer [a2] in the component [A] is 10 to 85:90. -15, preferably 20-80: 80-20, more preferably 25-75: 75-25. By setting the mass ratio of each rubbery polymer within this range, the squeaking noise reduction effect, impact resistance and heat resistance are excellent.

  As described above, the thermoplastic resin composition of the present invention comprising the component [A] and the component [B], and further, if necessary, the component [C], can be filled with a filler, a nucleating agent, a lubricant, a heat Various additives such as a stabilizer, an antioxidant, an ultraviolet absorber, a flame retardant, an anti-aging agent, a plasticizer, an antibacterial agent, and a colorant can be contained within a range that does not impair the object of the present invention.

  Furthermore, the thermoplastic resin composition of the present invention can be added to other resins such as polyethylene, polypropylene, polybutylene terephthalate, polyethylene terephthalate, polycarbonate, polyphenylene sulfide, polyamide, and the like, as necessary. Can be contained.

  The thermoplastic resin composition of the present invention is prepared by mixing each component at a predetermined mixing ratio using a tumbler mixer, a Henschel mixer, etc. It can be produced by melt-kneading under suitable conditions using a mixer. A preferred kneader is a twin screw extruder. Furthermore, when each component is kneaded, each component may be kneaded in a lump or may be kneaded in multiple stages. In addition, after knead | mixing with a Banbury mixer, a kneader, etc., it can also pelletize with an extruder. Moreover, it is more preferable to supply the fibrous thing among fillers from the middle of an extruder with a side feeder in order to prevent the cutting | disconnection in kneading | mixing. The melt kneading temperature is usually 200 to 300 ° C, preferably 220 to 280 ° C.

4). Contact parts:
The contact component of the present invention is obtained by molding the thermoplastic resin composition. There is no limitation on the method for producing the contact component of the present invention from the thermoplastic resin composition, and injection molding, injection compression molding, gas assist molding, press molding, calendar molding, blow molding, T-die extrusion molding, and irregular shape. It can be produced by a known method such as extrusion molding or film molding.

There is no particular limitation on the other members that come into contact with the contact component of the present invention. For example, thermoplastic resins, thermosetting resins, rubbers, organic materials, inorganic materials including the rubber-reinforced vinyl resin [A] of the present invention, A metal material etc. are mentioned.
Examples of the thermoplastic resin include polyvinyl chloride, polyethylene, polypropylene, AS resin, ABS resin, AES resin, ASA resin, polymethyl methacrylate, polystyrene, high impact polystyrene, EVA, polyamide (PA), polyethylene terephthalate, poly Examples include butylene terephthalate, polycarbonate (PC), polylactic acid, PC / ABS, PC / AES, PA / ABS, and PA / AES. These can be used alone or in combination of two or more.
Examples of the thermosetting resin include phenol resin, epoxy resin, urea resin, melamine resin, and unsaturated polyester resin. These can be used alone or in combination of two or more.
Examples of the rubber include chloroprene rubber, polybutadiene rubber, ethylene / propylene rubber, various synthetic rubbers such as SEBS, SBS, and SIS, and natural rubber. These can be used alone or in combination of two or more.
Examples of the organic material include insulation board, MDF (medium fiber board), hard board, particle board, lumbar core, LVL (single board laminate), OSB (orientation board), PSL (pararam), WB (wafer). Board), hard fiberboard, soft fiberboard, lumbar core plywood, board core plywood, special core-plywood, veneer core-plywood, laminated sheet / board of paper impregnated with tap resin, small pieces of crushed (old) paper, etc. -Boards obtained by mixing a linear body with an adhesive and heat-compressing, various kinds of wood, etc. These can be used alone or in combination of two or more.
Examples of the inorganic material include calcium silicate board, flexible board, homocement board, gypsum board, sizing gypsum board, reinforced gypsum board, gypsum lath board, decorative gypsum board, composite gypsum board, various ceramics, and glass. These can be used alone or in combination of two or more.
Furthermore, iron, aluminum, copper, various alloys, etc. are mentioned as a metal material. These can be used alone or in combination of two or more.
Among these, a thermoplastic resin, a thermosetting resin, and rubber are preferable, and ABS, AES, PC / ABS, and PC / AES are particularly preferable.

  The contact component of the present invention can greatly reduce the squeaking noise generated by contacting and rubbing with other members, such as a door trim, door lining, pillar garnish, console, Door pocket, ventilator, duct, air conditioner, meter visor, instrument panel upper garnish, instrument panel upper garnish, A / T indicator, on / off switch (slide part, slide plate), grill front defroster, grill side defroster, lid cluster, cover intro , Masks (mask switches, mask radios, etc.), glove boxes, pockets (pocket decks, pocket cards, etc.), cup holders, switch boxes, steering wheel horn pads, etc. be able to. Among them, it can be suitably used as an automobile ventilator, and can be particularly suitably used as a plate-shaped blade, a valve shutter, a louver and the like of an automobile ventilator and an automobile air conditioner. Thus, it is suitable for a component having a fitting portion with another member.

  EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated more concretely, this invention is not restrict | limited at all to the following Example, unless the summary is exceeded. In the examples, parts and% are based on mass unless otherwise specified.

(1) Evaluation method:
The measuring methods of various evaluation items in the following examples and comparative examples are shown below.

(1-1) Evaluation of stagnation noise (friction speed dependence of friction coefficient):
Using an electric injection molding machine “Erject NEX30” (model name) manufactured by Nissei Plastic Industry Co., Ltd., the thermoplastic resin composition shown in Table 1 and PC / ABS “CK43” (trade name) manufactured by Technopolymer Co., Ltd. A cylindrical test piece having an inner diameter of 20 mm, an outer diameter of 24.8 mm, and a height of 15 mm was injection molded, and then both test pieces were left in a gear oven at 80 ° C. for 400 hours. Next, using a wear friction tester “EFM-III-EN” (trade name) manufactured by Orientec Co., Ltd., set a test piece consisting of “CK43” as a contact partner on the rotating side, and in Table 1 on the fixed side The test piece which consists of the thermoplastic resin composition of description was set, and the inclination of the friction coefficient with respect to a friction speed was measured on the conditions of load 3kg and rotation speed (friction speed) 50mm / s, 100mm / s, 150mm / s.

(1-2) Itching sound evaluation (practical evaluation):
Using an injection molding machine “J-100E” (model name) manufactured by Nippon Steel Co., Ltd., from the thermoplastic resin composition described in Table 1 and PC / ABS “CK43” (trade name) manufactured by Techno Polymer Co., Ltd. The ISO dumbbell specimens were injection molded, and then both specimens were left in a gear oven at 80 ° C. for 200 hours and 400 hours. Next, 5 ISO dumbbell test pieces made of the thermoplastic resin composition shown in Table 1 and 5 ISO dumbbell test pieces made of “CK43” were left in a gear oven at 80 ° C. for 200 hours and 400 hours. The situation of the generation of itchiness was evaluated by alternately overlapping and twisting both ends by hand. Evaluation was performed 5 times, and determination was performed based on the following evaluation criteria.
(Double-circle): There was no generation | occurrence | production of a squeaking sound in all five evaluations.
○: In all five evaluations, the occurrence of itching was slight.
(Triangle | delta): The case where generation | occurrence | production of a squeaking sound was remarkable was contained in five evaluations.
X: In all five evaluations, the generation of itching sound was significant.

(1-3) Drop weight impact strength:
Using an electric injection molding machine “Erject NEX30” (model name) manufactured by Nissei Plastic Industrial Co., Ltd., an 80 mm × 55 mm × 2.4 mm flat plate type test piece made of the thermoplastic resin composition shown in Table 1 Injection molded. The test piece was provided with a side gate of 4 mm × 1 mm at the center of one side of 55 mm, the resin temperature during molding was 240 ° C., and the mold temperature was 50 ° C. Next, using the Shimadzu hydro-shot / high-speed puncture impact tester “HITS-P10” (model name) manufactured by Shimadzu Corporation, the test piece was punched under the following conditions to measure the fracture energy (J).
Measurement temperature: 23 ° C
Punching speed: 6.7mm / s
Punching test jig striker tip: φ12.7mm
Die diameter of specimen holder: 43 mm

(2-1) Component [A]
A-1: ABS-1
In a polymerization vessel equipped with a stirrer, 280 parts of water, 60 parts of a polybutadiene latex having a weight average particle size of 0.26 μm and a gel fraction of 90% (in terms of solid content), 0.3 part of sodium formaldehyde sulfoxylate, 0.1 part of ferrous sulfate. 0025 parts, 0.01 parts of disodium ethylenediaminetetraacetate, after deoxygenation, heated to 60 ° C. with stirring in a nitrogen stream, 10 parts of acrylonitrile, 30 parts of styrene, 0.2 parts of t-dodecyl mercaptan, A monomer mixture consisting of 0.3 part of cumene hydroperoxide was continuously added dropwise at 60 ° C. over 5 hours. After completion of the dropwise addition, the polymerization temperature was set to 65 ° C. and stirring was continued for 1 hour, and then the polymerization was terminated to obtain a latex of a graft copolymer. The polymerization conversion rate was 98%. Thereafter, 0.2 part of 2,2′-methylene-bis (4-ethylene-6-tert-butylphenol) is added to the obtained latex, and calcium chloride is added to coagulate, washing, filtering and drying steps. After that, a powdery resin composition was obtained. The graft ratio of the obtained resin composition was 40%, and the intrinsic viscosity [η] of the acetone-soluble component was 0.38 dl / g.

A-2: AES-1
A 20 liter stainless steel autoclave equipped with a ribbon-type stirrer blade, an auxiliary agent continuous addition device, a thermometer, etc., was charged with ethylene / α-olefin rubber (ethylene / propylene = 78/22 (%), Mooney viscosity (ML ₁ ). ₊₄ , 100 ° C.) 20 parts ethylene / propylene copolymer) 22 parts, 55 parts of styrene, 23 parts of acrylonitrile, 0.5 part of t-dodecyl mercaptan, 110 parts of toluene, and the internal temperature was raised to 75 ° C. Warm and stir the autoclave contents for 1 hour to make a homogeneous solution. Thereafter, 0.45 part of t-butylperoxyisopropyl monocarbonate was added, the internal temperature was further raised, and after reaching 100 ° C., the polymerization reaction was carried out at a stirring speed of 100 rpm while maintaining this temperature. went. From 4 hours after the start of the polymerization reaction, the internal temperature was raised to 120 ° C., and the reaction was further continued for 2 hours while maintaining this temperature to complete the polymerization reaction. Thereafter, the internal temperature was cooled to 100 ° C., and 0.2 part of octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenol) -propionate was added, and then the reaction mixture was extracted from the autoclave, Unreacted substances and the solvent were distilled off by distillation, and the volatile matter was substantially degassed using a 40 mmφ vented extruder (cylinder temperature 220 ° C., vacuum degree 760 mmHg), and pelletized. The resulting ethylene / α-olefin rubber-reinforced vinyl resin had a graft rate of 70% and an intrinsic viscosity [η] of acetone-soluble content of 0.47 dl / g.

A-3: AES-2
In a 20 liter stainless steel autoclave equipped with a ribbon stirrer blade, auxiliary agent addition device, thermometer, etc., ethylene / α-olefin rubber (ethylene / propylene / dicyclopentadiene = 63/32/5 (%)) 30 parts of an ethylene / propylene / dicyclopentadiene copolymer having a Mooney viscosity (ML _{1 + 4} , 100 ° C.) of 33, 45 parts of styrene, 25 parts of acrylonitrile, 0.5 part of t-dodecyl mercaptan, 140 parts of toluene The internal temperature was raised to 75 ° C., and the autoclave contents were stirred for 1 hour to obtain a uniform solution. Thereafter, 0.45 part of t-butylperoxyisopropyl monocarbonate was added, the internal temperature was further raised, and after reaching 100 ° C., the polymerization reaction was carried out at a stirring speed of 100 rpm while maintaining this temperature. went. From 4 hours after the start of the polymerization reaction, the internal temperature was raised to 120 ° C., and the reaction was further continued for 2 hours while maintaining this temperature to complete the polymerization reaction. Thereafter, the internal temperature was cooled to 100 ° C., and 0.2 part of octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenol) -propionate was added, and then the reaction mixture was extracted from the autoclave, Unreacted substances and the solvent were distilled off by distillation, and the volatile matter was substantially degassed using a 40 mmφ vented extruder (cylinder temperature 220 ° C., vacuum degree 760 mmHg), and pelletized. The resulting ethylene / α-olefin rubber-reinforced vinyl resin had a graft rate of 60% and an intrinsic viscosity [η] of acetone-soluble content of 0.45 dl / g.

A-4: ABS-2
In a glass reaction vessel equipped with a stirrer, 75 parts of ion exchange water, 0.8 part of potassium rosinate, 0.15 part of t-dodecyl mercaptan, polybutadiene latex (weight average particle size: 0.26 μm, gel content 90) %) 20 parts (in terms of solid content), 15 parts of styrene and 5 parts of acrylonitrile were added, and the temperature was increased while stirring in a nitrogen stream. When the internal temperature reached 45 ° C., a solution in which 0.2 parts of sodium pyrophosphate, 0.01 parts of ferrous sulfate heptahydrate and 0.2 parts of glucose were dissolved in 20 parts of ion-exchanged water was added. Thereafter, 0.1 part of cumene hydroperoxide was added to initiate polymerization, and polymerization was carried out for 1 hour. Subsequently, 50 parts of ion-exchanged water, 0.7 part of potassium rosinate, 45 parts of styrene, 15 parts of acrylonitrile, 0.08 part of t-dodecyl mercaptan and 0.015 part of cumene hydroperoxide are continuously added over 4 hours. did. After polymerization for 1 hour, 0.2 part of 2,2'-methylene-bis (4-ethylene-6-t-butylphenol) was added to complete the polymerization. Magnesium sulfate was added to this latex to coagulate the resin component. Then, the polybutadiene type graft copolymer was obtained by washing with water and further drying. The graft ratio was 62%, and the intrinsic viscosity [η] of the acetone-soluble component was 0.38 dl / g.

C-1: AS-1
In a polymerization vessel equipped with a stirrer, 250 parts of water and 1.0 part of sodium palmitate were charged, and after deoxygenation, the mixture was heated to 70 ° C. with stirring in a nitrogen stream. Further, 0.4 parts of sodium formaldehyde sulfoxylate, 0.0025 part of ferrous sulfate and 0.01 part of disodium ethylenediaminetetraacetate were added, and then 70 parts of α-methylstyrene, 25 parts of acrylonitrile, 5 parts of styrene, t- A monomer mixture composed of 0.5 parts of dodecyl mercaptan and 0.2 parts of cumene hydroperoxide was continuously added dropwise at a polymerization temperature of 70 ° C. over 7 hours. After completion of the dropping, the polymerization temperature was set to 75 ° C., and stirring was continued for 1 hour to complete the polymerization, thereby obtaining a copolymer latex. The polymerization conversion rate was 99%. Thereafter, the obtained latex was coagulated by adding calcium chloride, and a powdery copolymer was obtained through washing, filtration and drying steps. The intrinsic viscosity [η] of the acetone-soluble component of the obtained copolymer was 0.40 dl / g.

(2-2) Component [B] (silicone oil):
B-1: Dimethyl silicone oil; KF-96H-10,000 cSt (trade name: manufactured by Shin-Etsu Silicone Co., Ltd.), the kinematic viscosity at 25 ° C. was 10,000 cSt.

B-2: Dimethyl silicone oil; KF-96-100 cSt (trade name: manufactured by Shin-Etsu Silicone), kinematic viscosity at 25 ° C. was 100 cSt.

B-3: Dimethyl silicone oil; KF-96H-50,000 cSt (trade name: manufactured by Shin-Etsu Silicone Co., Ltd.); The kinematic viscosity at 25 ° C. was 50,000 cSt.

B-4: Dimethyl silicone oil; KF-96L-5cSt (trade name: manufactured by Shin-Etsu Silicone Co., Ltd.), kinematic viscosity at 25 ° C. was 5 cSt.

B-5: Dimethyl silicone oil; KF-96H-300,000 cSt (trade name: manufactured by Shin-Etsu Silicone), kinematic viscosity at 25 ° C. was 300,000 cSt.

(2-3) Additive:
D-1: Ethylene bis-stearic acid amide; Kao wax EB-P (trade name: manufactured by Kao Corporation)
D-2: 1,3,5-tris (3,5-di-t-butyl-4-hydroxybenzyl) -s-triazine-2,4,6- (1H, 3H, 5H) trione; Adekastab AO- 20 (Product name: Made by ADEKA Corporation)
D-3: Bis (2,4-di-t-butylphenyl) pentaerythritol diphosphite; ADK STAB PEP-24G (trade name: manufactured by ADEKA Corporation)

Examples 1-9 and Comparative Examples 1-5
After mixing the above components [A] to [D] with a Henschel mixer at the blending ratio shown in Table 1, they are kneaded with a twin-screw extruder (manufactured by Nippon Steel, TEX44, barrel set temperature 250 ° C.) and pelletized. did. Each test piece for evaluation was shape | molded with the obtained pellet. And it evaluated by the said method using the obtained test piece. The above evaluation results are shown in Table 1.

As can be seen from Table 1, the thermoplastic resin compositions of the present invention represented by Examples 1 to 9 are molded articles with reduced squeak noise that is the object of the present invention, and further having a good balance of impact resistance. Can be provided.
On the other hand, Comparative Example 1 is an example that does not contain the ethylene / α-olefin rubbery polymer [a2], and is inferior in the effect of reducing the squeaking noise. Comparative Example 2 is an example not containing the diene rubbery polymer [a1], and is inferior in falling weight impact strength. Comparative Example 3 is an example in which the blending amount of the silicone oil [B] of the present invention is too large, and melt kneading is difficult, and the silicone oil bleeds out on the surface of the molded product and cannot be used practically. Did not do. Comparative Example 4 is an example using a silicone oil that does not satisfy the kinematic viscosity in the present invention. Since the kinematic viscosity is too small, the effect of reducing the squeaking noise is inferior. Comparative Example 5 is an example using a silicone oil that does not satisfy the kinematic viscosity in the present invention. Since the kinematic viscosity was too large, melt kneading was difficult and evaluation was not performed.

  The contact component according to the present invention significantly reduces the squeaking noise that occurs when the members rub against each other, and maintains the squeaking noise reduction effect even when left at high temperatures for a long time. It is possible to provide a contact component comprising a thermoplastic resin composition having excellent properties, and it can be suitably used for an automobile ventilator or the like. In particular, it can be suitably used for a component having a fitting portion with another member.

M Object V Drive speed μs Static friction coefficient μl Sawtooth waveform lower end Δμ μs-μl

Claims (5)

The rubber-reinforced vinyl resin (A) 100 parts by weight of a silicone oil kinematic viscosity at 25 ° C. as measured by Ubbelohde viscometer according to ASTM D445-46T or JIS 8803 is 200 ～100,000CSt [B] 0.1 to 8 Combining parts by mass,
The rubber-reinforced vinyl resin [A] includes a rubber-reinforced vinyl resin [A1] obtained by polymerizing a vinyl monomer [b1] in the presence of a diene rubber polymer [a1], ethylene A rubber-reinforced vinyl resin [A2] obtained by polymerizing a vinyl monomer [b2] in the presence of an α-olefin rubber polymer [a2],
The total amount of the diene rubbery polymer [a1] and the ethylene / α-olefin rubbery polymer [a2] is 5 to 30% by mass based on 100% by mass of the entire rubber-reinforced vinyl resin [A]. And
The weight ratio of the diene-based rubbery polymer [a1] and the ethylene · alpha-olefin-based rubbery polymer [a2] [a1]: [a2] is 10 to 66: a 90 to 34,
The vinyl-based monomer [b1] and [b2] is Ri Do a thermoplastic resin composition comprising an aromatic vinyl compound and a vinyl cyanide compound, the thermoplastic resin composition or another made of other thermoplastic resin method for producing contact parts, characterized in Rukoto used in contact with rub parts and members. The rubber-reinforced vinyl resin [A] further comprises a (co) polymer [C] of a vinyl monomer [b3] containing an aromatic vinyl compound and a vinyl cyanide compound. Manufacturing method for contact parts. The method for producing a contact component according to claim 1 or 2, wherein the ethylene / α-olefin rubber polymer [a2] has an ethylene: α-olefin mass ratio of 5 to 95:95 to 5. The method for producing a contact component according to any one of claims 1 to 3, wherein the ethylene / α-olefin rubbery polymer [a2] is an ethylene / propylene copolymer . The method for producing a contact component according to any one of claims 1 to 4, wherein the other thermoplastic resin is polycarbonate / ABS.

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