CN117120542A - Polyacetal resin composition, method for producing same, and resin gear - Google Patents

Polyacetal resin composition, method for producing same, and resin gear Download PDF

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Publication number
CN117120542A
CN117120542A CN202280024433.3A CN202280024433A CN117120542A CN 117120542 A CN117120542 A CN 117120542A CN 202280024433 A CN202280024433 A CN 202280024433A CN 117120542 A CN117120542 A CN 117120542A
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resin composition
mass
polyacetal resin
parts
polyacetal
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Inventor
森文哉
门间智宏
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Polyplastics Co Ltd
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Polyplastics Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2/00Addition polymers of aldehydes or cyclic oligomers thereof or of ketones; Addition copolymers thereof with less than 50 molar percent of other substances
    • C08G2/10Polymerisation of cyclic oligomers of formaldehyde
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/10Esters; Ether-esters
    • C08K5/101Esters; Ether-esters of monocarboxylic acids
    • C08K5/103Esters; Ether-esters of monocarboxylic acids with polyalcohols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/26Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers modified by chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L59/00Compositions of polyacetals; Compositions of derivatives of polyacetals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L71/00Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
    • C08L71/02Polyalkylene oxides
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16HGEARING
    • F16H55/00Elements with teeth or friction surfaces for conveying motion; Worms, pulleys or sheaves for gearing mechanisms
    • F16H55/02Toothed members; Worms
    • F16H55/06Use of materials; Use of treatments of toothed members or worms to affect their intrinsic material properties

Abstract

A process for producing a polyacetal resin composition, which comprises adding an alkaline inactivating agent (D) to a reaction product obtained by copolymerizing a predetermined heteropolyacid with a polymerization catalyst (C), wherein the reaction product comprises a trioxane as a main monomer (a), and a cyclic ether and/or cyclic methylal having a C-C bond of 1 or more as a comonomer (B), to a polymerization catalyst (C), and then performing a melt kneading treatment to inactivate the polymerization catalyst (C), wherein the polyacetal resin composition comprises a predetermined amount of a predetermined modified olefin polymer (B), a predetermined alkylene glycol polymer (C), a predetermined calcium carbonate (D), a partial ester of a polyhydric alcohol having 2 to 4 members and an (F) alpha-olefin oligomer (A) per 100 parts by mass of the polyacetal copolymer.

Description

Polyacetal resin composition, method for producing same, and resin gear
Technical Field
The present invention relates to a polyacetal resin composition, a method for producing the same, and a resin gear.
Background
Polyacetal resins (also referred to as polyoxymethylene resins, abbreviated as POM resins) have balanced mechanical properties and are excellent in friction/wear resistance, chemical resistance, heat resistance, electric characteristics, etc., and therefore are widely used in the fields of automobiles, electric/electronic products, etc. In the related art, as an example, the sliding property is desired to be further improved along with the general physical properties. The sliding characteristics are referred to as abrasion/wear resistance, and in order to achieve further improvement of such characteristics, POM resin compositions containing various additives have been proposed (see patent document 1).
Prior art literature
Patent literature
Patent document 1: japanese patent No. 5847261
Disclosure of Invention
Problems to be solved by the invention
However, gears generally have a function of transmitting rotational power through engagement of gears with each other. Further, since a high contact surface pressure is applied to the contact surfaces where gears mesh with each other when the gears rotate, fatigue is generated until damage after long-term use. Therefore, the performance required for the gear includes not only friction/wear resistance but also durability against fatigue.
Although the POM resin composition described in patent document 1 is excellent in sliding characteristics, there is still room for further improvement as a material for a resin gear.
The present invention has been made in view of the above-described conventional problems, and an object thereof is to provide a polyacetal resin composition having excellent sliding properties, particularly excellent wear resistance, and excellent fatigue durability when applied to gears, a method for producing the polyacetal resin composition, and a resin gear.
Means for solving the problems
One embodiment of the present invention for solving the above problems is as follows.
(1) A process for producing a polyacetal resin composition,
the polyacetal copolymer comprises (A) 100 parts by mass:
(B) The modified olefin polymer obtained by modifying an olefin polymer with at least 1 selected from unsaturated carboxylic acids, anhydrides of unsaturated fatty acids, and derivatives thereof is 0.5 to 10 parts by mass;
(C) An alkylene glycol polymer having a primary or secondary amino group and a number average molecular weight of 400 to 500,000 or less, in an amount of 0.01 to 5 parts by mass;
(D) BET specific surface area of 15m 2 0.1 to 20 parts by mass of cubic calcium carbonate, each of which has an average particle diameter of 50 to 200nm and an untreated surface;
(E) 0.1 to 10 parts by mass of a partial ester of a polyhydric alcohol having 2 to 4 members; and
(F) 0.1 to 10 parts by mass of an alpha-olefin oligomer,
the polyacetal copolymer (A) is obtained by adding an alkaline inactivating agent (d) to a reaction product obtained by copolymerizing a heteropoly acid represented by the following general formula (1) in a polymerization catalyst (c) using a cyclic ether and/or cyclic methylal having at least 1 carbon-carbon bond as a comonomer (b) and 80 to 99.9 mol% of a main monomer (a) having trioxane as a total monomer, then performing a melt kneading treatment, and inactivating the polymerization catalyst (c),
H m [M 1 x ·M 2 y O Z ]·nH 2 o.cndot.general formula (1)
[ in the general formula (1), M 1 Represents a central element composed of 1 or 2 elements selected from P and Si. M is M 2 Represents 1 or more coordinating elements selected from W, mo and V. x is an integer of 1 to 10, y is an integer of 6 to 40, z is an integer of 10 to 100, m is an integer of 1 to 1, and n is an integer of 0 to 50. A kind of electronic device
(2) A polyacetal resin composition produced by the method for producing a polyacetal resin composition according to (1) above.
(3) A resin gear which is produced by molding the polyacetal resin composition according to (2).
Effects of the invention
The present invention provides a polyacetal resin composition having excellent sliding properties, particularly excellent wear resistance, and excellent fatigue durability when applied to gears, a method for producing the polyacetal resin composition, and a resin gear.
Detailed Description
Process for producing polyacetal resin composition
The method for producing the polyacetal resin composition according to the present embodiment comprises the steps of: (B) The modified olefin polymer obtained by modifying an olefin polymer with at least 1 selected from unsaturated carboxylic acids, anhydrides of unsaturated fatty acids, and derivatives thereof is 0.5 to 10 parts by mass; (C) An alkylene glycol polymer having a primary or secondary amino group and a number average molecular weight of 400 to 500,000 or less, in an amount of 0.01 to 5 parts by mass; (D) BET specific surface area of 15m 2 0.1 to 20 parts by mass of a cubic calcium carbonate having an average particle diameter of 50 to 200nm inclusive and an untreated surface; (E) 0.1 to 10 parts by mass of a partial ester of a polyhydric alcohol having 2 to 4 members; and (F) 0.1 to 10 parts by mass of an alpha-olefin oligomer, wherein the polyacetal copolymer (A) is obtained by adding an alkaline inactivating agent (d) to a reaction product obtained by copolymerizing a polymerization catalyst (c) using a heteropoly acid represented by the following general formula (1) with a cyclic ether and/or cyclic methylal having at least 1 carbon-carbon bond as a comonomer (b) and using 80 to 99.9 mol% of trioxane as a total monomer, and then performing a melt kneading treatment to inactivate the polymerization catalyst (c),
H m [M 1 x ·M 2 y O Z ]·nH 2 o.cndot.general formula (1)
[ in the general formula (1) ],M 1 Represents a central element composed of 1 or 2 elements selected from P and Si. M is M 2 Represents 1 or more coordinating elements selected from W, mo and V. X represents an integer of 1 to 10, y represents an integer of 6 to 40, z represents an integer of 10 to 100, m represents an integer of 1 to 1, and n represents an integer of 0 to 50. A kind of electronic device
In the method for producing a polyacetal resin composition according to the present embodiment, a polyacetal resin composition having excellent sliding properties, particularly excellent abrasion resistance, and excellent fatigue durability when applied to gears can be obtained by containing a predetermined amount of the components (B) to (F) in 100 parts by mass of the polyacetal copolymer (a). It is known from patent document 1 that the excellent sliding properties are mainly attributable to the components (B) to (F). On the other hand, it is found that the fatigue durability is excellent when the polyacetal copolymer is applied to gears, and the polyacetal copolymer (A) obtained by a predetermined production method cannot be obtained by adding only the components (B) to (F). However, since the structure and properties of the polyacetal copolymer (A) are difficult to specify, it is not clear how the polyacetal copolymer (A) contributes. It is known that the sliding properties and fatigue durability in the case of application to gears are improved by interaction of the polyacetal copolymer (A) obtained by the predetermined production method with the components (B) to (F).
The following first describes each component used in the production method of the present embodiment.
[ (A) polyacetal copolymer ]
In this embodiment, (a) the polyacetal copolymer is obtained by adding an alkaline inactivating agent (d) to a reaction product obtained by copolymerizing a heteropoly acid represented by the following general formula (1) with a polymerization catalyst (c) using a cyclic ether and/or cyclic methylal having at least 1 carbon-carbon bond as a comonomer (b) and then performing melt kneading treatment to inactivate the polymerization catalyst (c), wherein the main monomer (a) is 80 to 99.9 mol% of the total monomer which is trioxane.
(Main monomer (a))
As the main monomer (a), trioxane may be used. Trioxane is a cyclic trimer of formaldehyde, and is generally obtained by reacting an aqueous formaldehyde solution in the presence of an acidic catalyst, and is purified by a method such as distillation. The trioxane used for polymerization is preferably one in which impurities such as water and methanol are reduced as much as possible.
(comonomer (b))
As comonomer (b) cyclic ethers and/or cyclic formals having at least 1 carbon-carbon bond can be used. Representative examples of the compound used as the comonomer (b) include 1, 3-dioxolane, diethylene glycol methylal, 1, 4-butanediol methylal, 1, 3-dioxane, ethylene oxide, propylene oxide, epichlorohydrin, and the like. Among them, 1, 3-dioxolane, diethylene glycol methylal, 1, 4-butanediol methylal, 1, 3-dioxane and ethylene oxide are preferable from the viewpoint of polymerization stability.
In addition, a known modifier comonomer such as a branching agent may be added as the third comonomer component in addition to the main monomer (a) and the comonomer (b) within a range that does not significantly deteriorate the performance of the polyacetal resin composition obtained.
In this embodiment, the amount of the compound selected from the cyclic ether and/or cyclic methylal used as the comonomer (b) is preferably 0.1 to 20 mol%, more preferably 0.2 to 10 mol% based on the total monomer (total amount of the main monomer and the comonomer). When the amount of the comonomer (b) is less than 0.1 mol%, the unstable terminal part of the crude polyacetal copolymer produced by polymerization may be increased, and the stability may be deteriorated.
When the amount of the comonomer exceeds 20 mol%, the resulting copolymer may become soft, resulting in a decrease in melting point.
(polymerization catalyst (c))
In the present embodiment, in the production of the polyacetal copolymer as described above, a heteropoly acid represented by the following general formula (1) is used as the polymerization catalyst (c).
H m [M 1 x ·M 2 y O Z ]·nH 2 O.cndot.general formula (1)
In the formula (1), M 1 Represents a central element composed of 1 or 2 elements selected from P and Si. M is M 2 Represents 1 or more coordinating elements selected from W, mo and V. x is an integer of 1 to 10, y is an integer of 6 to 40, z is an integer of 10 to 100, m is an integer of 1 to 1, and n is an integer of 0 to 50.
Specific examples of the heteropoly acid include phosphomolybdic acid, phosphotungstic acid, phosphomolybdic vanadic acid, phosphotungstic vanadic acid, tungstic silicic acid, silicomolybdic tungstic acid, silicomolybdic vanadic acid, and the like. Among them, from the viewpoints of polymerization stability and stability of the heteropoly acid itself, the heteropoly acid is preferably 1 or more of silicomolybdic acid, tungstic silicic acid, phosphomolybdic acid and phosphotungstic acid.
In the present embodiment, the amount of the heteropoly-acid to be used varies depending on the kind thereof, and the polymerization reaction can be appropriately modified, but is generally in the range of 0.05 to 100ppm (hereinafter, mass/mass ppm) and preferably 0.1 to 50ppm based on the total amount of the monomers to be polymerized. In addition, as the phosphomolybdic acid, phosphotungstic acid and other very strong heteropoly acid, 0.1-10 ppm of the use amount is sufficient.
Even if the catalyst is used in a small amount, the catalyst can be used to inhibit unstable formate end groups (-O-CH=O) and hemiacetal end groups (-O-CH) by keeping the unfavorable reactions such as main chain decomposition and depolymerization of the polymer to a minimum 2 -OH), etc., and is economically advantageous.
In order to uniformly perform the reaction, the polymerization catalyst is preferably diluted with an inert solvent which does not adversely affect the polymerization, and added to the main monomer (a) and/or the comonomer (b) to be used. The inert solvent is preferably an ester obtained by condensing a low-molecular-weight carboxylic acid having 1 to 10 carbon atoms such as formic acid, acetic acid, propionic acid, butyric acid, etc., with a low-molecular-weight alcohol having 1 to 10 carbon atoms such as methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-methyl-1-propanol, 2-methyl-2-propanol, 1-pentanol, 3-methyl-1-butanol, 1-hexanol, etc.; ketones having a low molecular weight of 1 to 10 such as acetone, 2-butanone, 2-pentanone, 3-pentanone, 2-hexanone, 3-hexanone, methyl isobutyl ketone, methyl tert-butyl ketone, and the like, but are not limited thereto. Methyl formate, ethyl formate, methyl acetate, ethyl acetate, butyl acetate, acetone, 2-butanone, methyl isobutyl ketone, and the like are most suitable when industrial availability and the like are also considered. The polymerization catalyst is suitably dissolved in the above-mentioned inert solvent at a concentration of 1 to 30 mass/mass%, but is not limited thereto. In addition, a method of adding a predetermined amount of the polymerization catalyst to the polymerization system and polymerizing the mixture in advance in a part or the whole of any 1 or more of the main monomer (a), the comonomer (b), the molecular weight regulator, and the like is also preferable.
[ preparation of copolymer ]
In the present embodiment, the production of the crude polyacetal copolymer by the polymerization can be conventionally carried out by the same equipment and method as those for the copolymerization of trioxane. That is, the batch type, continuous type, and semi-continuous type are all possible, and a method of obtaining a solid powder bulk polymer with the progress of polymerization using a liquid monomer is generally used. As the polymerization apparatus used in the present embodiment, a reaction tank with a stirrer which is generally used in a batch type may be used. Further, as the continuous type, a kneading extruder, a biaxial screw type continuous extrusion mixer, a biaxial paddle type continuous mixer, and other continuous polymerization apparatuses of trioxane and the like proposed so far can be used. Furthermore, 2 or more types of polymerizers may be used in combination.
The polymerization method is not particularly limited, but as previously proposed, the comonomer (b) and the heteropoly acid as the polymerization catalyst (c) may be sufficiently mixed while maintaining a liquid phase state in advance, and the obtained mixed liquid may be supplied to a polymerization apparatus together with trioxane as the main monomer (a) to perform copolymerization. Thus, the amount of the catalyst necessary can be reduced, and as a result, a polyacetal copolymer having a smaller formaldehyde emission amount can be advantageously obtained, which is a more suitable polymerization method. The polymerization temperature is carried out in the temperature range of 60 to 120 ℃.
In this embodiment, when the main monomer (a) and the comonomer (b) are polymerized to prepare the polyacetal copolymer, a known chain transfer agent, for example, a linear acetal having a low molecular weight such as formaldehyde dimethyl acetal (methyl) may be added to adjust the degree of polymerization.
Further, the polymerization reaction is desirably carried out in a state where impurities having active hydrogen, such as water, methanol, formic acid, and the like, are substantially absent, for example, in a state where they are each 10ppm or less. For this reason, it is desirable to use trioxane, cyclic ether and/or cyclic methylal prepared so as to be as free of these impurity components as possible as a main monomer and a comonomer.
Next, deactivation of the polymerization catalyst by adding an alkaline deactivator will be described.
(alkaline deactivator (d))
The type and method of adding the alkaline deactivator are not particularly limited, but it is preferable that the alkaline deactivator is added to the crude polyacetal copolymer in its original state without washing the crude polyacetal copolymer, and the mixture is melt-kneaded, so that the alkaline deactivator can be used for deactivation of the polymerization catalyst and stabilization of the unstable terminal of the crude polyacetal copolymer. Specifically, the alkali inactivating agent preferably contains at least 1 selected from carbonates, bicarbonates, or carboxylates of alkali metal elements or alkaline earth metal elements or hydrates thereof, and triazine ring-containing compounds having an amino group or a substituted amino group.
In the case of using a carbonate, bicarbonate, or carboxylate of an alkali metal element or an alkaline earth metal element or a hydrate thereof, the formaldehyde generation amount of the composition to be finally obtained is particularly low, and more preferably. Specifically, it is more preferable to contain at least 1 selected from sodium formate, sodium acetate, sodium carbonate, sodium bicarbonate, disodium succinate, sodium laurate, sodium palmitate, sodium stearate, and calcium stearate.
In this embodiment, the above-mentioned alkali deactivator may be used in 1 kind, or in combination of plural kinds, or in the form of a hydrate, a mixture, a double salt, or the like.
After the polymerization and deactivation treatment, the unreacted monomers may be separated, recovered, dried, and the like by a conventionally known method, if necessary.
Next, the components (B) to (F) used in the present embodiment will be described below.
[ (B) modified olefin Polymer obtained by modifying olefin Polymer with at least 1 selected from unsaturated carboxylic acids, anhydrides of unsaturated fatty acids and derivatives thereof ]
In the present specification, the modified olefin polymer is also referred to as a "(component B"). The polyacetal resin composition according to the present embodiment is excellent in sliding characteristics by containing the component (B). In contrast, when an olefin polymer other than the component (B) is contained in the polyacetal resin composition, the sliding properties are poor.
The olefin-based polymer (before modification) used in the component (B) includes a single polymer of an α -olefin such as ethylene, propylene, butene, hexene, octene, nonene, decene, dodecene, etc., a random, block or graft copolymer composed of 2 or more of them, a non-conjugated diene component such as 1, 4-hexadiene, dicyclopentadiene, 5-ethylidene-2-norbornene, 2, 5-norbornadiene, etc., a conjugated diene component such as butadiene, isoprene, piperylene, etc., an α, β -unsaturated acid such as acrylic acid, methacrylic acid, etc., a derivative of an α, β -unsaturated acid such as an ester thereof, etc., acrylonitrile, styrene, an aromatic vinyl compound such as α -methylstyrene, etc., a vinyl ester such as vinyl acetate, a vinyl ether such as an ethylene methyl ether, etc., and a random, block or graft copolymer composed of at least 1 of a comonomer component such as a derivative of an ethylene compound, etc., regardless of the degree of polymerization, side chain, branching, degree, copolymerization, and the like.
Examples of the olefin-based polymer include high-pressure polyethylene, medium-low-pressure polyethylene, gas-phase ethylene- α -olefin copolymer, LLDPE, polypropylene, polybutene, ethylene-vinyl acetate copolymer, ethylene-methyl acrylate copolymer, ethylene-ethyl acrylate copolymer, ethylene-butyl acrylate copolymer, ethylene-propylene copolymer, and ethylene-propylene-diene terpolymer. Preferably, polyethylene, ethylene-methyl acrylate copolymer, ethylene-ethyl acrylate copolymer.
The component (B) used in the present embodiment is a modified olefin polymer obtained by modifying at least 1 selected from unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, citraconic acid, itaconic acid, tetrahydrophthalic acid, norbornene diacid, methylnorbornene diacid, allylsuccinic acid, and unsaturated carboxylic acid anhydrides such as maleic anhydride, citraconic anhydride, itaconic anhydride, tetrahydrophthalic anhydride, norbornene dianhydride, methylnorbornene dianhydride, allylanhydrous succinic acid, derivatives thereof, and the like.
As the preferable component (B), the Melt Flow Rate (MFR) is 0.01 to 100g/10 min, more preferably 0.1 to 50g/10 min, and particularly preferably 0.2 to 30g/10 min. Furthermore, the Melt Flow Rate (MFR) is determined according to ISO 1133.
Specific examples of the preferable component (B) include polyethylene modified with maleic anhydride, polypropylene, ethylene-propylene copolymer, ethylene-ethyl acrylate copolymer, and the like. Among them, when the component (B) contains a polyethylene modified with maleic anhydride, it is preferable in that the sliding properties of a molded article obtained by molding the polyacetal resin composition are improved.
As a modification method thereof, a method of heating and reacting an olefin polymer and at least 1 compound selected from the group consisting of an unsaturated carboxylic acid, an anhydrous compound thereof, and a derivative thereof in a solution state or a molten state in the presence of a radical initiator such as an appropriate organic peroxide or the like is suitable, but not particularly limited thereto. The mixing amount of the two components is preferably 0.1 to 20 parts by mass, more preferably 0.1 to 10 parts by mass, based on 100 parts by mass of the olefin polymer. When the amount of the effective compound in the olefin polymer modified with such a compound is too small, the affinity between the component (a) and the component (B) may be insufficient, and when the amount is too large, physical properties such as sliding properties may be lowered to be improved.
In the present embodiment, the component (B) is preferably contained in an amount of 0.5 to 10 parts by mass, more preferably 2 to 7 parts by mass, based on 100 parts by mass of the component (a). In the polyacetal resin composition obtained, the blending amount of the component (B) is less than 0.5 part by mass, and the frictional wear may be increased, which is not preferable. (B) If the mixing amount of the components exceeds 10 parts by mass, there is a possibility that the mechanical properties may be lowered, and thus it is not preferable.
[ (C) alkylene glycol-based Polymer having Primary or Secondary amino groups and having a number average molecular weight of 400 to 500,000 ]
In the present specification, the alkylene glycol polymer is also referred to as a "(C) component". The polyacetal resin composition according to the embodiment is excellent in sliding characteristics by containing the component (C).
The alkylene glycol polymer having a primary or secondary amino group as the component (C) is a homopolymer or copolymer of ethylene glycol, propylene glycol or tetramethylene glycol, and has a primary or secondary amino group at the terminal or in the molecular chain thereof. Further, a polymer slightly modified with an ester with a fatty acid, an ether with an aliphatic alcohol, or the like may be formed. Examples thereof include polyethylene glycol, polypropylene glycol, polytetramethylene glycol, and copolymers of these constituent units, and those having at least 1 aminopropyl group and aminooctyl group.
The kind of the polymer is not particularly limited, but it is preferable in that the sliding property of a molded article obtained by molding the polyacetal resin composition is improved if the alkylene glycol-based polymer is a polymer slightly modified with an ester of a fatty acid, an ether of an aliphatic alcohol or the like.
(C) The number average molecular weight of the component (A) is 400 to 500,000, preferably 400 to 100,000, more preferably 1,000 to 6,000. This is because, by mixing the component (C), dispersibility of the component (B) in the polyacetal resin is improved, but the component (C) has a number average molecular weight of less than 400, and mechanical physical properties and sliding properties of the polymer material as the component (a) or the component (B) are impaired, and the number average molecular weight exceeds 50 ten thousand, and the melt viscosity is increased, so that the dispersion in the polyacetal resin becomes difficult.
(C) The mixing amount of the component (a) is 0.01 to 5 parts by mass, more preferably 0.1 to 4 parts by mass, still more preferably 0.3 to 3 parts by mass, and particularly preferably 1 to 2 parts by mass, based on the component (a).
Of these, the blending amount of the component (C) is preferably 1 part by mass or more, in that the sliding properties of a molded article obtained by molding the polyacetal resin composition can be significantly improved. (C) When the content is less than 0.01 parts by mass, the effect of modifying the sliding properties of the molded article cannot be sufficiently obtained, and when it exceeds 5 parts by mass, the mechanical properties are deteriorated, which is not preferable.
[ (D) BET specific surface area of 15m 2 Per gram or less, an average particle diameter of 50nm to 200nm, and surface-untreated, cubic calcium carbonate]
In this specification, this calcium carbonate is also referred to as the "(D) component. The polyacetal resin composition according to the embodiment is excellent in sliding characteristics by containing the component (D).
Conventionally, in order to improve the sliding properties of resin molded articles, it has been known to use an inorganic filler as a component of a polyacetal resin composition. As the inorganic filler, calcium carbonate, potassium titanate, barium carbonate, talc, wollastonite, mica, zinc oxide, and the like are known. However, in the present embodiment, calcium carbonate is an essential component. The inorganic filler is not preferable because the surface properties of the molded article are not so excellent as compared with the case of containing the component (D), even if the inorganic filler other than calcium carbonate is contained as the component (D).
(D) The BET specific surface area of the component is 15m 2 And/g or less. In the present specification, BET specific surface area means a specific surface area (surface area per unit mass) obtained from the adsorption amount at the completion of a monolayer obtained by the BET formula using nitrogen as a reference gas, and the BET specific surface area measurement method is as defined in ASTM D-3037And (5) setting. When the BET specific surface area exceeds 15m 2 In the case of/g, the molded article obtained by molding the polyacetal resin composition is not preferable because of poor surface properties and sliding properties.
(D) The average particle diameter of the component (A) is 50nm to 200nm, more preferably 80nm to 170 nm. In the present specification, the particle diameter means an arithmetic average value of the long diameter and the short diameter when the long diameter and the short diameter of the target particle are measured by observation at 30,000 times magnification using a scanning electron microscope S3000H manufactured by hitachi High-Tech company. In the present specification, the average particle diameter means an arithmetic average of particle diameters of 100 samples. When the average particle diameter is less than 50nm, there is a possibility that the condensation is carried out 2 times in the product, and when the average particle diameter exceeds 200nm, it is not preferable in that the surface properties and sliding properties of a molded article obtained by molding the polyacetal resin composition are poor.
(D) The components are surface untreated. When the surface of component (D) is treated, the molded article obtained by molding the polyacetal resin composition is not preferable because of poor abrasion property.
In the present specification, "surface-untreated" means that the surface of the calcium carbonate particles is not treated with a surface treatment agent such as an epoxy compound, an isocyanate compound, a titanate compound, or a silane compound.
(D) The components are cubic. Here, the cube shape includes not only a cube that is a regular hexahedron, but also a hexahedron that cannot be said to be a complete cube but also a nearly cubic shape.
(D) When the shape of the component is not a cube but is an irregular shape, it is not preferable in that the surface properties and sliding properties of a molded article obtained by molding the polyacetal resin composition are poor. In the present specification, whether or not the component (D) is cubic in shape is confirmed by, for example, burning the product at 500 ℃ for 3 hours and observing the residue with an electron microscope.
(D) The mixing amount of the component (a) is 0.1 to 20 parts by mass, more preferably 0.1 to 1 part by mass. (D) If the content is less than 0.1 parts by mass, the frictional wear amount may be increased, and if it exceeds 20 parts by mass, the surface properties may be deteriorated, which is not preferable.
[ (E) partial esters of polyhydric alcohols having 2 to 4 members ]
In this specification, the partial esters of the polyols are also referred to as the "(E) component. The polyacetal resin composition according to the present embodiment contains the component (E), and thus is excellent in surface properties and sliding properties.
Conventionally, as a component of a polyacetal resin composition, use of a lubricant has been known. Further, as lubricants, mineral oils, hydrocarbons, fatty acids, aliphatic alcohols, aliphatic esters formed from fatty acids and aliphatic alcohols, partial and/or full esters of polyhydric alcohols, esters of carboxylic acids and inorganic acids, amides of fatty acids and amine compounds, metal soaps, natural waxes, silicones and derivatives thereof, substituted diphenyl ethers, and the like are known.
However, in the present embodiment, both the partial ester as the component (E) and the α -olefin oligomer as the component (F) described later are essential components.
Even if the lubricant contains other lubricants than the component (E) and the component (F), it cannot be said that the surface properties are excellent as in the present embodiment, and therefore, it is not preferable.
Specific examples of the component (E) include glycerol monostearate, glycerol distearate, glycerol monobehenate, pentaerythritol monostearate, and the like.
The partial ester as the component (E) is not preferable in that the surface properties and sliding properties of a molded article obtained by molding the polyacetal resin composition are poor if the ester is not a partial ester.
(E) The mixing amount of the component (a) is 0.1 to 10 parts by mass, more preferably 0.5 to 2 parts by mass. (E) If the content is less than 0.1 parts by mass, the frictional wear may increase, and if it exceeds 10 parts by mass, leakage may occur, which is not preferable.
[ (F) alpha-olefin oligomer ]
In this specification, the oligomer is also referred to as the "(F) component". The polyacetal resin composition according to the present embodiment is excellent in sliding characteristics by containing the component (F).
(F) The mixing amount of the component (a) is 0.1 to 10 parts by mass, more preferably 1 to 5 parts by mass. (F) If the content is less than 0.1 parts by mass, the sliding properties of a molded article obtained by molding the polyacetal resin composition may be poor, and if it exceeds 10 parts by mass, leakage or peeling may occur, which is not preferable.
[ other stabilizers and additives ]
The polyacetal resin composition according to the present embodiment may further comprise various known stabilizers to enhance stability. Further, various known additives may be further mixed in accordance with the intended use to improve physical properties thereof.
Examples of the additives include various colorants, mold release agents, nucleating agents, antistatic agents, other surfactants, and heterogeneous polymers (other than the aforementioned graft copolymers). Further, 1 or 2 kinds of fibrous, granular or plate-like fillers such as inorganic, organic, or metal may be mixed and used as long as the properties of the target composition of the present embodiment are not significantly reduced.
[ preparation of polyacetal resin composition ]
The polyacetal resin composition according to the present embodiment can be easily produced by a known method generally used as a conventional resin composition production method. For example, a method of (1) mixing all the components constituting the composition and feeding the mixture to an extruder to melt-knead the mixture to obtain a granular composition, (2) feeding a part of the components constituting the composition from a main feed port of the extruder and feeding the rest of the components from a side feed port to melt-knead the mixture to obtain a granular composition, and (3) temporarily preparing pellets having different compositions by extrusion or the like, and mixing the pellets to adjust the composition to a predetermined composition may be employed.
Polyacetal resin composition
The polyacetal resin composition of the present embodiment is produced by the method for producing a polyacetal resin composition described above. Therefore, the sliding property is excellent, and the fatigue durability is excellent when applied to a gear. The polyacetal resin composition of the present embodiment is excellent in fatigue durability when applied to a gear, but is not limited to a gear, and can be applied to a member having a requirement for fatigue durability similar to a gear.
< resin Gear >
The resin gear of the present embodiment is formed by molding the polyacetal resin composition. As with the polyacetal resin composition of the present embodiment described above, the resin gear of the present embodiment is excellent in sliding characteristics and fatigue durability.
The method for molding a resin gear using the polyacetal resin composition according to the present embodiment is not particularly limited, and various methods known in the art can be employed. For example, the polyacetal resin composition according to the present embodiment may be produced by charging the polyacetal resin composition into an extruder, melt-kneading the composition to obtain pellets, and charging the pellets into an injection molding machine equipped with a predetermined metal mold to perform injection molding.
In addition, the resin gear according to the present embodiment is obtained by molding the polyacetal resin composition according to the present embodiment into a plate-like or rod-like shape, and then molding the polyacetal resin composition by a general molding process such as a cutting process.
The types of gears to which the resin gear according to the present embodiment can be applied are not particularly limited, but examples thereof include flat gears, racks, internal gears, helical gears, bevel gears, helical racks, herringbone gears, straight bevel gears, spiral bevel gears, zero bevel gears, spiral gears, and cylindrical worm gears.
Examples
Hereinafter, the present embodiment will be described more specifically with reference to examples, but the present embodiment is not limited to the following examples.
Preparation of polyacetal copolymer (A)
[ polyacetal copolymers A-1 to A-4 ]
As the polymerization apparatus, a continuous biaxial polymerization machine was used. The polymerizer has a housing for passing a medium for heating or cooling on the outside, and 2 rotary shafts each having a plurality of impellers for stirring and propulsion are provided in the longitudinal direction inside the housing. In the housing of the biaxial polymerization machine, a mixed solution of trioxane as the main monomer (a), 1, 3-dioxolane (3.3 mass% to total monomer) as the comonomer (b), and 1500 mass ppm (to total monomer) of formaldehyde dimethyl acetal as the chain transfer agent was continuously supplied to one end of the housing while rotating 2 rotating shafts at a constant speed by a heating medium of 80 ℃. Then, as a polymerization catalyst (methyl formate solution) shown in table 1, the above mixed solution was continuously added in an amount shown in table 1 with respect to the total monomers to carry out copolymerization. In Table 1, the amount of the polymerization catalyst added was the mass ratio (unit: ppm) to the total of the total monomers. Then, the crude polyacetal copolymer was discharged from a discharge port provided at the other end of the polymerizer, and an alkaline deactivator as shown in Table 1 was added for deactivating the polymerization catalyst. In Table 1, the amount of the alkaline deactivator was defined as the mass ratio (unit: ppm) to the crude polyacetal copolymer. Next, 0.3 parts by mass of triethylene glycol-bis [ 3- (3-t-butyl-5-methyl-4-hydroxyphenyl) propionate ] was added as an antioxidant, and the mixture was melt kneaded and extruded at a temperature of 220℃and a vacuum degree of a vent portion of 5mmHg using a twin-screw extruder having a vent. The polyacetal copolymers (A-1 to A-4) were obtained by the above-mentioned steps. Further, the Melt Flow Rate (MFR) of each polyacetal copolymer was measured using a measuring device: melt index L202 (manufactured by TAKARA thermistor) under a load of 2.16kg at 190℃in accordance with ISO 1133.
[ polyacetal copolymer A' -1 ]
As the catalyst, boron trifluoride in a gaseous state was used, and the process was carried out in the same manner as in the polyacetal copolymers A-1 to A-4 until the crude polyacetal copolymer was discharged from the discharge port provided at the other end of the polymerizer. The discharged reaction product was rapidly passed through a crusher and added to a 60℃aqueous solution containing 0.05 mass% of triethylamine to deactivate the catalyst. Then, the crude polyacetal copolymer was obtained by separation, washing and drying. Subsequently, 3 mass% of a 5 mass% aqueous solution of triethylamine and 0.3 mass% of pentaerythritol-tetrakis [ 3- (3, 5-di-t-butyl-4-hydroxyphenyl) propionate ] were added to 100 parts by mass of the crude polyacetal copolymer, and the mixture was melt-kneaded at 210℃by a biaxial extruder to remove an unstable part, thereby obtaining a polyacetal copolymer of the polyacetal copolymer A' -1.
TABLE 1
Preparation of polyacetal resin composition
The components (a) and the following components (B) to (F) obtained in the preparation of the polyacetal copolymer < (a) were premixed in the proportions (unit parts by mass) shown in table 2, and then fed into the main feed port of a 30mm diameter twin-screw extruder having a vent at 1 position, and melt-mixed (extrusion conditions: L/d=35, extrusion temperature=200 ℃, number of screw rotations=120 rpm, degree of vacuum for evacuation= -700mmHg, discharge amount=12 kg/hr), to prepare a granular composition.
(B) Modified olefin polymer
( B-1) maleic anhydride-modified Low Density Polyethylene (LDPE) (product name: TAFMER MM6850, manufactured by Mitsui Chemie Co., ltd )
( B-2) maleic anhydride-modified ethylene-ethyl acrylate copolymer (EEA) (product name: HPR AR2011 manufactured by Mitsui Dupont Polychemical Co., ltd )
(C) Alkylene glycol polymer having primary or secondary amino groups and having number average molecular weight of 400 to 500,000
( C-1) both terminal amine-modified polyethylene glycol (PEG) (product name: CHEMISTAT Y-400, number average molecular weight: 4,000, sanyo chemical industry Co., ltd )
(D) BET specific surface area of 15m 2 Calcium carbonate having average particle diameter of 50nm to 200nm, surface-untreated, and cubic
(D-1) BET specific surface area of 11.5m 2 Surface-untreated, cubic calcium carbonate (product name: brilliant1500, colloidal calcium carbonate, manufactured by Baishi industries Co., ltd.)/g having an average particle diameter of 150nm
(E) Partial esters of polyols
( E-1) glyceryl monostearate (product name: RIKEMAL S100 manufactured by Litamin )
(F) Alpha olefin oligomer
( F-1) alpha olefin oligomer (product name: LUCANT HC600, sanjingjingchu chemical Co., ltd )
TABLE 2
[ evaluation of Gear fatigue Properties ]
Shaping conditions: gear shaping
The pellet-shaped resin composition obtained under the previous production conditions was injection-molded using an injection molding machine (NEX 500) manufactured by Nikkin resin industries, ltd.) under injection conditions of a cylinder temperature of 200℃and a mold temperature of 80℃and an injection speed of 20mm/s, a holding pressure of 120MPa, and a cooling time of 8 seconds, whereby a flat gear having a die block 1, a tooth number of 54, and a tooth width of 10mm was obtained.
Gear durability test
The previous "forming conditions: the flat gear obtained in gear forming was set by meshing gears of the same material in a small gear fatigue tester of a small wild tester (strain). One gear is used as the driving side and the other gear is used as the driven side. Then, the gear on the driving side was rotated under a torque of 10N/m and a rotation number of 300rpm, and the total rotation number until the gear was broken was measured. The measurement results are shown in Table 3.
[ evaluation of Friction coefficient ]
Shaping conditions: cylindrical test piece shaping
The pellet-shaped resin composition obtained under the previous production conditions was injection-molded using an injection molding machine (. Alpha.S50i-A) manufactured by FANUC, the cylinder temperature was set to 200℃and the injection conditions of a mold temperature of 80℃and an injection speed of 10mm/S, a holding pressure of 70MPa, and a cooling time of 10 seconds, to obtain a cylindrical test piece having an inner diameter of 20.0mm, an outer diameter of 25.6mm, and a height of 15.0 mm.
Abrasion test
Previous "forming conditions: the cylindrical test piece obtained in the cylindrical test piece molding was set in the EFM-3-EN manufactured by ORIENTEC, inc., in a combination of the same materials. One cylindrical test piece was set as the driving side and the other as the fixing side. Then, the plate was rotated under a surface pressure of 0.06MPa and a linear velocity of 15cm/s, and the friction force was detected by a load cell, and after 23 hours from the start of the test, the coefficient of dynamic friction was calculated from the average value of 1 hour. The calculation results are shown in table 3.
TABLE 3
As is clear from table 3, each of examples 1 to 5 had a larger total number of rotations until the gear was broken than that of comparative example 1, and the fatigue durability of the gear was excellent. In examples 1 to 5 and comparative example 1, the friction coefficients were all the same.
From the above, it is clear that the polyacetal resin compositions of examples 1 to 5 are excellent in sliding properties and excellent in fatigue durability when applied to gears.

Claims (3)

1. A process for producing a polyacetal resin composition, characterized by,
the polyacetal copolymer comprises (A) 100 parts by mass:
(B) The modified olefin polymer obtained by modifying an olefin polymer with at least 1 selected from unsaturated carboxylic acids, anhydrides of unsaturated fatty acids, and derivatives thereof is 0.5 to 10 parts by mass;
(C) An alkylene glycol polymer having a primary or secondary amino group and a number average molecular weight of 400 to 500,000 or less, in an amount of 0.01 to 5 parts by mass;
(D) BET specific surface area of 15m 2 0.1 to 20 parts by mass of cubic calcium carbonate, each of which has an average particle diameter of 50 to 200nm and an untreated surface;
(E) 0.1 to 10 parts by mass of a partial ester of a polyhydric alcohol having 2 to 4 members; and
(F) 0.1 to 10 parts by mass of an alpha-olefin oligomer,
the polyacetal copolymer (A) is obtained by adding an alkaline inactivating agent (d) to a reaction product obtained by copolymerizing a heteropoly acid represented by the following general formula (1) in a polymerization catalyst (c) using a cyclic ether and/or cyclic methylal having at least 1 carbon-carbon bond as a comonomer (b) and using trioxane as a main monomer (a) in an amount of 80 to 99.9 mol% based on the total monomer, then performing a melt kneading treatment, and inactivating the polymerization catalyst (c),
H m [M 1 x ·M 2 y O Zn H 2 o.cndot.general formula (1)
In the general formula (1), M 1 Represents a central element composed of 1 or 2 elements selected from P and Si, M 2 And (b) represents 1 or more coordinating elements selected from W, mo and V, x represents an integer of 1 to 10, y represents an integer of 6 to 40, z represents an integer of 10 to 100, m represents an integer of 1 to 1, and n represents an integer of 0 to 50.
2. A polyacetal resin composition according to claim 1, wherein the polyacetal resin composition is produced by a method for producing the polyacetal resin composition.
3. A resin gear comprising the polyacetal resin composition according to claim 2.
CN202280024433.3A 2021-03-26 2022-02-25 Polyacetal resin composition, method for producing same, and resin gear Pending CN117120542A (en)

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