WO2005040276A1 - Phenolic resin molding material and molded article thereof - Google Patents

Phenolic resin molding material and molded article thereof Download PDF

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Publication number
WO2005040276A1
WO2005040276A1 PCT/JP2003/013816 JP0313816W WO2005040276A1 WO 2005040276 A1 WO2005040276 A1 WO 2005040276A1 JP 0313816 W JP0313816 W JP 0313816W WO 2005040276 A1 WO2005040276 A1 WO 2005040276A1
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Prior art keywords
phenolic resin
molding material
mass
modified
polyvinyl acetate
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PCT/JP2003/013816
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French (fr)
Japanese (ja)
Inventor
Shigehiro Kitaya
Nobuyuki Kawamura
Hideki Kawakita
Masanori Miyoshi
Yuya Kitagawa
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Matsushita Electric Works, Ltd.
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Application filed by Matsushita Electric Works, Ltd. filed Critical Matsushita Electric Works, Ltd.
Priority to JP2005509865A priority Critical patent/JP4874649B2/en
Priority to PCT/JP2003/013816 priority patent/WO2005040276A1/en
Priority to AU2003280584A priority patent/AU2003280584A1/en
Publication of WO2005040276A1 publication Critical patent/WO2005040276A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/04Condensation polymers of aldehydes or ketones with phenols only
    • C08L61/06Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/04Condensation polymers of aldehydes or ketones with phenols only
    • C08L61/06Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
    • C08L61/14Modified phenol-aldehyde condensates

Definitions

  • the present invention relates to a phenolic resin molding material used for producing heat-resistant parts such as a commutator of a motor for an automobile electric motor, and a molded article obtained therefrom.
  • phenolic resin molding materials have been used for commutators of motors for automobile electrical components or structural components around them due to their excellent moldability and excellent heat resistance and strength obtained by molding and hardening.
  • the mechanical and thermal loads in the commutator failing process performed after the molding from the phenolic resin molding material or the hyging process performed in the commutator mounting process, or the heat generated by the motor itself when the motor is driven.
  • the heat generated by the engine of a car causes a dimensional change in the commutator.
  • the phenol tree lumber molding material used for manufacturing commutators in the prior art cannot meet the demand for noise reduction because of large dimensional changes with respect to mechanical or thermal loads. .
  • An object of the present invention is to provide a phenolic resin molding material having a small dimensional change with respect to a mechanical or thermal load, and a molded article obtained therefrom. .
  • a phenolic resin molding material comprising a novolak-type phenolic resin and a filler, wherein at least a part of the nopolak-type phenolic resin is a polyvinyl acetate-modified nopolak-type phenolic resin.
  • the polyvinyl acetate-modified novolak phenolic resin in the present invention is a modified nopolak-type phenolic resin produced using polyvinyl acetate in a synthesis step from phenol and formaldehyde, particularly phenol and formaldehyde in the presence of polyvinyl acetate.
  • the step between the commutator copper segments and the deterioration of the roundness of the commutator caused in the environment where a mechanical or thermal load is applied are reduced by manufacturing the commutator using the phenolic resin molding material of the present invention. And can be prevented. As a result, it is possible to satisfy the demand for noise reduction in the commutator.
  • the phenolic resin molding material of the present invention is characterized by containing a novolac type phenolic resin modified with polyvinyl acetate.
  • the polyacetate-modified novolak-type phenol resin can be produced as follows:
  • the nopolak type phenolic resin is usually produced by performing an addition reaction of phenol and formanolaldehyde in water in the presence of an acid catalyst, followed by dehydration condensation.
  • the polyacetate-vinyl-modified novolak phenolic resin of the present invention is produced by adding polyacetate to a reaction mixture formed from phenol and formaldehyde before the dehydration condensation in the production of the nopolak-type phenolic resin.
  • the addition of poly (vinyl acetate) is added before and after the addition reaction between phenol and formaldehyde. Can be done in between.
  • Such acid catalysts are p-toluenesulfonic acid, hydrochloric acid, formic acid, phthalic anhydride, boric acid and oxalic acid, preferably oxalic acid. .
  • Formaldehyde is usually used in the form of an aqueous formalin solution.
  • Formaldehyde concentration in formalin aqueous solution is usually 3 7-5 0% by weight, preferably instrument 4 0-5 0 weight 0/0.
  • the addition reaction between phenol and formaldehyde is carried out usually at 80 to 120 ° C, preferably 90 to 110 ° C, for usually 1 to 4 hours, preferably for 2 to 3 hours.
  • dehydration and condensation of phenol and formaldehyde (dehydration and condensation of phenol and formaldehyde adducts) are performed in the presence of polyvinyl acetate.
  • the dehydration condensation is carried out at a temperature of usually 130-180 ° C., preferably 150-170 ° C., and usually 50-: L 0 0 kPa, preferably 60-7. It is carried out under a pressure of 5 kP'a, usually for 1 to 5 hours, preferably for 2 to 3 hours.
  • Polyvinyl acetate Biel-modified novolac-type Fueno one Honoré resin of the present invention based on the weight of polyvinyl acetate Bulle modified Noporakku type phenolic resin, of 6 0-7 5 wt% Fueno le, 1 5 to 2 0 mass 0/0 formaldehyde, 0.2 0 to 0.2 5 weight 0/0 using a polyvinyl acetate Bulle of oxalic acid and 5-2 0 weight 0/0, preferably to produce.
  • the ratio of poly (vinyl acetate) in the poly (vinyl acetate) -modified novolak type phenol resin is 5% by mass or more. This is because the dimensional change of the phenolic resin molding material with respect to mechanical and thermal loads can be more effectively reduced by setting the polyacetic acid butyl compounding ratio to 5% by mass or more.
  • the blending ratio of polyacetate in the polyacetate-modified nopolak-type phenolic resin increases, the curing rate of the phenolic resin molding material containing the polyacetate-modified nopolak-type phenolic resin decreases. Therefore, in order to secure the desired curing rate, the polyacetic acid in the polyacetic acid-modified novolak type phenol resin
  • the vinyl compounding ratio is preferably 20% by mass or less.
  • polyacetate-modified vinyl acetate novolak phenol resin having good water resistance and chemical resistance
  • a polyacetate biale having a weight average molecular weight of 1000 or more.
  • the polyvinyl acetate-modified nopolak phenol resin in order to ensure good dispersibility of the polyvinyl acetate in the reaction mixture, the polyvinyl acetate modified with a molecular weight of 100 Q It is preferred to use.
  • the polyacetic acid-modified nopolak type phenol resin produced as described above preferably has a weight average molecular weight of 2000 to 600.
  • the polyvinyl sulphate-modified nopolak type phenolic resin having a weight average molecular weight in this range has a melt viscosity suitable for kneading and the like in the subsequent production of a phenolic resin molding material.
  • the nopolak phenol resin preferably has a weight-average molecular weight of 2000 to 400.
  • the polyphenol-modified nopolak-type phenol resin is usually taken out in a vat at a high temperature after its production, cooled and solidified, and then used for the production of a phenol resin molding material. In order to improve the subsequent handleability, it is preferable to pulverize the cooled and solidified polyvinyl acetate novolak type phenol resin.
  • Phenolic resin molding material of the present invention preferably, based on the weight of the phenolic resin molding material, 1 0-3 0% by weight of polyvinyl acetate Bulle modified Noporakku type phenolic resins, novolac type 5-2 0 weight 0/0 phenol ⁇ , 4 0 - including 6 0 mass 0/0 glass fibers and 5-2 0% by weight of an inorganic filler.
  • the phenolic resin molding material of the present invention can be produced.
  • the compounding ratio of the polyacetic acid-modified nopolak type phenol resin in the phenol resin molding material is preferably 10% by mass or more. This is because the dimensional change of the phenolic resin molding material can be reduced more effectively by setting the compounding ratio of the polyacetic acid butyl modified nopolak phenolic resin to 10% by mass or more. Because it can.
  • the blending ratio of the modified nopolak type phenol resin is preferably 30% by mass / 0 or less.
  • a commutator having good strength can be obtained from a phenol resin molding material containing 40% by mass or more of glass fibers.
  • the glass weight is preferably 60% by mass or less.
  • inorganic fillers included in the phenolic resin molding material include, but are not limited to, wollastonite, calcium carbonate, talc, mushylin and my mushy. These inorganic fillers can be used alone or in combination. .
  • the present invention also provides a commutator obtained by molding the phenolic resin molding material of the present invention.
  • Examples of the method for molding the phenolic resin molding material of the present invention include, but are not limited to, injection molding, transfer molding, and compression molding.
  • a curing agent is used to harden the phenolic resin molding material of the present invention containing a nopolak-type phenolic resin as a component.
  • Hexamethylenetetramine is preferred as the curing agent.
  • Hexamethylenetetramine is more preferably a granular hexamethylenetetramine, particularly a fine-particle hexamethylenetetramine containing at least 99% by mass of particles passing through an 80-mesh sieve, particularly a 150-mesh sieve.
  • Hexamethylenetetramine in the form of fine particles containing 98% by mass or more of particles passing through is used.
  • a granular or fine particle of hexamethylenetetramine uniform dispersion thereof is ensured, and the appearance of a molded article can be improved, and variations in moldability and physical properties can be suppressed.
  • the phenol resin composition of the present invention may be used.
  • Additives or auxiliaries such as coupling agents, mold release agents, lubricants, dyes and pigments can be used with the form material.
  • phenol and formalin (about 50% aqueous solution) are reacted at 100 ° C for 90 minutes in the presence of oxalic acid, and emulsified at 100 ° C for 120 minutes.
  • Acid beer (weight-average molecular weight: 1500) was added to the reaction mixture, dehydration-condensed at 160 ° C and 70 kPa for 180 minutes, and a polyvinyl acetate-modified novolak phenolic resin was added.
  • To manufacture It is taken out at a high temperature, 7 solidified, and pulverized and used for the production of the following molding materials. :. ————
  • the raw materials in the amounts shown in parts by mass in the following table were mixed for 1 minute, and the mixture was heated at a product temperature of 100 using a twin-screw kneader. Knead with C ⁇ 110 for 3 minutes. This kneaded material is pulverized after solidification by rejection, and the granulated molding material is used for forming test pieces for evaluating dimensional changes and the like.
  • the raw materials listed in the table are:
  • Modified phenol resin Polyvinyl acetate-modified novolak phenol resin produced as described above, with a weight average molecular weight of 300. Ratio described in Table (mass. / 0) were used for the production of polyvinyl acetate Bulle modified novolac-type phenolic resin, shows the ratio of polyvinyl acetate Biel.
  • Phenol resin Novolak type phenol resin, BRP590P manufactured by Showa Kogyo Co., Ltd.
  • Inorganic filler NY CO 400 wollastonite NYAD 400.
  • Hardener Hexamethylenetetramine Pulfine form, passing through an 80-mesh sieve, particle content of 99% by mass or more, passing through a 150-mesh sieve Particle content 98 mass. /. (7 parts by mass), Carnava lubricant (1 part by mass) (Carnava F-1 manufactured by Dainichi Kagaku 'Industries Co., Ltd.) and Dye Solvent Black (1 part by mass) (SAP-L manufactured by Orient Chemical Co., Ltd.) .
  • the molding material preferably has an outflow time of 60 to 80 seconds from the viewpoint of practical molding.
  • the above molding material is formed by extrusion molding using a test piece mold with a JIS bending test shape at a mold temperature of 170 ° C, a curing time of 90 seconds, and an injection pressure of 128 MPa, and shrinks.
  • the test piece is annealed at 180 ° C. for 3 hours and then at 210 ° C. for 7 hours, and the dimensional change of the test piece due to the annealing treatment is measured.
  • the specimen preferably has a small absolute dimensional change rate.
  • the annealed test piece is further subjected to a high-temperature treatment at 200 ° C. for 500 hours, and the dimensional change of the test piece due to the high-temperature treatment is measured.
  • the specimen preferably has a small absolute dimensional change rate.
  • the bending strength of the test piece [JIS K 6911] was measured.
  • the test piece preferably has a bending strength of 15 OMPa or more.
  • Example 1 Example 2
  • Example 3 Example 4
  • Example 5 Modified 3% by mass 1---1 phenol 5% by mass ° /. -11-11 mass% resin--15 10-
  • Example 11 Example 12 Comparative Example 1 Comparative Example 2 denatured single - A one Fueno, Les 5 wt% one 18 one first resin 10 mass 0/0 eleven eleven

Abstract

A phenolic resin molding material comprising one or more phenolic novolaks and a filler, characterized in that at least part of the phenolic novolaks is a phenolic novolak modified with polyvinyl acetate; and a molded article obtained from the molding material.

Description

明 細 書 フエノール樹脂成形材料およびその成形品 技術分野  Description Phenol resin molding materials and molded articles
本発明は、 自動車電装用モーターのコンミテータなどの耐熱部品を製造するた めに用いられるフエノール樹脂成形材料、 およびそれから得られる成形品に関す る。  The present invention relates to a phenolic resin molding material used for producing heat-resistant parts such as a commutator of a motor for an automobile electric motor, and a molded article obtained therefrom.
背景技術 Background art
従来からフエノール樹脂成形材料は、 その優れた成形性、 並びに成形および硬 化により得られる優れた耐熱性および強度により、 自動車電装用モーターのコン ミテータまたはその周辺の構造部品に使用されている。  Hitherto, phenolic resin molding materials have been used for commutators of motors for automobile electrical components or structural components around them due to their excellent moldability and excellent heat resistance and strength obtained by molding and hardening.
最近ではモーター部品、 特に自動車電装用モーター部品、 例えばモーターのコ ンミテータにおいて、 さらなる異音の低減、 即ち静音ィ匕が求められている。 この モーターのコンミテータによる異音の原因の 1つに、 力学的または熱的負荷によ つて発生する寸法変化が挙げられる。  Recently, there has been a demand for further reduction of abnormal noise, that is, silent noise, in motor parts, particularly motor electric parts for automobiles, for example, in commutators of motors. One of the causes of this motor commutation noise is dimensional changes caused by mechanical or thermal loads.
具体的には、 フエノール樹脂成形材料からの成形後に行われるコンミテータの ァエール処理またはコンミテータの実装工程に行われるヒユージング処理におけ る力学的および熱的負荷、 あるいはモータ駆動時におけるモーター自身の発熱ま たは自動車のエンジン部から発生する熱により、 コンミテータに寸法変化が生ず る。  Specifically, the mechanical and thermal loads in the commutator failing process performed after the molding from the phenolic resin molding material or the hyging process performed in the commutator mounting process, or the heat generated by the motor itself when the motor is driven. The heat generated by the engine of a car causes a dimensional change in the commutator.
このコンミテータの寸法変化が大きいと、 コンミテータの真円度が大きく悪ィ匕 し、 またコンミテータの銅製セグメント間に大きな段差が生じる。 その結果、 モ ータ駆動時に大きな異音が発生する。  If the dimensional change of the commutator is large, the roundness of the commutator is greatly degraded, and a large step occurs between the copper segments of the commutator. As a result, a loud noise is generated when the motor is driven.
これに関して、 従来技術においてコンミテータを製造するために用いられてい るフエノ一ル樹月旨成形材料は、 力学的または熱的負荷に対する寸法変ィ匕が大きい ため、 静音化の要求を満たすことができない。  In this regard, the phenol tree lumber molding material used for manufacturing commutators in the prior art cannot meet the demand for noise reduction because of large dimensional changes with respect to mechanical or thermal loads. .
従って、 力学的または熱的負荷に対する寸法変化が小さい、 フエノール樹脂成 形材料が求められている。 発明の開示 Therefore, there is a need for a phenolic resin molded material that has a small dimensional change due to mechanical or thermal load. Disclosure of the invention
本発明の目的は、 力学的または熱的負荷に対する寸法変化が小さいフエノール 樹脂成形材料およびそれから得られる成形品を提供することである。 .  An object of the present invention is to provide a phenolic resin molding material having a small dimensional change with respect to a mechanical or thermal load, and a molded article obtained therefrom. .
ノボラック型フエノール樹脂および充填材を含むフエノール樹脂成形材料であ つて、 該ノポラック型フエノール樹脂の少なくとも一部が、 ポリ酢酸ビュル変性 ノポラック型フエノール樹脂であることを特徴とするフエノ "ル樹脂成形材料は、 力学的または熱的負荷に対する寸法変化が小さいことを見出した。 .  A phenolic resin molding material comprising a novolak-type phenolic resin and a filler, wherein at least a part of the nopolak-type phenolic resin is a polyvinyl acetate-modified nopolak-type phenolic resin. , The dimensional change to mechanical or thermal loading was found to be small.
本発明におけるポリ酢酸ビュル変性ノボラック型フエノール樹脂とは、 フエノ ールおよびホルムアルデヒドからの合成段階でポリ酢酸ビニルを用いて製造され た変性ノポラック型フエノール樹脂、 特にポリ酢酸ビニルの存在下でフエノール およびホルムアルデヒドを脱水縮合することにより製造された変性ノボラヅク型 フエノール樹脂を意味する。 '  The polyvinyl acetate-modified novolak phenolic resin in the present invention is a modified nopolak-type phenolic resin produced using polyvinyl acetate in a synthesis step from phenol and formaldehyde, particularly phenol and formaldehyde in the presence of polyvinyl acetate. Means a modified novolak-type phenolic resin produced by dehydration-condensation. '
力学的または熱的負荷のかかる環境下において生ずるコンミテータ銅製セグメ ント間における段差、 およびコンミテータの真円度の悪化を、 本発明のフエノー ノレ樹脂成形材料を使用してコンミテータを製造することにより、 低減および防止 することができる。 その結果、 コンミテータにおける静音化の要求を満たすこと ができる。  The step between the commutator copper segments and the deterioration of the roundness of the commutator caused in the environment where a mechanical or thermal load is applied are reduced by manufacturing the commutator using the phenolic resin molding material of the present invention. And can be prevented. As a result, it is possible to satisfy the demand for noise reduction in the commutator.
発明を実施するための形態 BEST MODE FOR CARRYING OUT THE INVENTION
本発明のフエノール樹脂成形材料は、 ポリ酢酸ビニルにより変性したノボラッ ク型フエノール樹脂を含むことを特徴とする。  The phenolic resin molding material of the present invention is characterized by containing a novolac type phenolic resin modified with polyvinyl acetate.
該ポリ酢酸ビュル変性ノボラック型フエノール樹脂を、 以下のようにして製造 することができる :  The polyacetate-modified novolak-type phenol resin can be produced as follows:
ノポラック型フエノール樹脂は、 通常、 水中において、 酸触媒の存在下でフエ ノールとホルムァノレデヒドとの付加反応を行い、 次いで脱水縮合することにより 製造される。  The nopolak type phenolic resin is usually produced by performing an addition reaction of phenol and formanolaldehyde in water in the presence of an acid catalyst, followed by dehydration condensation.
本発明のポリ酢酸ビエル変性ノボラック型フエノール樹脂は、 このノポラック 型フエノール樹脂製造の脱水縮合前に、 フエノールおよびホルムアルデヒドから 形成された反応混合物にポリ酢酸ビュルを添加することにより製造する。 ポリ酢 酸ビュルの添加は、 フエノールとホルムアルデヒドとの付加反応の前およびその 間に行うことができる。 し力 し、 フエノールとホルムアルデヒドとの付加反応に 対するポリ酢酸ビュルによる阻害を回避するために、 付加反応後、 脱水縮合前に ポリ酢酸ビュルを添加することが好ましい。 The polyacetate-vinyl-modified novolak phenolic resin of the present invention is produced by adding polyacetate to a reaction mixture formed from phenol and formaldehyde before the dehydration condensation in the production of the nopolak-type phenolic resin. The addition of poly (vinyl acetate) is added before and after the addition reaction between phenol and formaldehyde. Can be done in between. However, in order to avoid the inhibition of the addition reaction between phenol and formaldehyde by the polyacetate, it is preferable to add the polyacetate after the addition reaction and before the dehydration condensation.
フエノールとホルムアルデヒドとの付加は、 通常、 水中において、 酸触媒の存 在下で行われる。  The addition of phenol and formaldehyde is usually carried out in water in the presence of an acid catalyst.
その酸触媒の例は、 パラトルエンスルホン酸、 塩酸、 ギ酸、 無水フタル酸、 ホ ゥ酸およびシユウ酸であり、 好ましくはシユウ酸を使用する。 .  Examples of such acid catalysts are p-toluenesulfonic acid, hydrochloric acid, formic acid, phthalic anhydride, boric acid and oxalic acid, preferably oxalic acid. .
ホルムアルデヒドは、 通常、 ホルマリン水溶液の形態で使用される。 ホルマリ ン水溶液中のホルムアルデヒド濃度は、 通常 3 7〜 5 0質量%、 好ましぐ 4 0〜 5 0質量0 /0である。 Formaldehyde is usually used in the form of an aqueous formalin solution. Formaldehyde concentration in formalin aqueous solution is usually 3 7-5 0% by weight, preferably instrument 4 0-5 0 weight 0/0.
フエノールとホルムアルデヒドとの付加反応は、 通常 8 0〜1 2 0 °C、 好まし くは 9 0〜 1 1 0 °Cで、 通常 1〜 4時間、 好ましくは 2〜 3時間行われる。 . 付加反応後に、 ポリ酢酸ビエルの存在下で、 フエノールぉょぴホルムアルデヒ ドの脱水縮合 (フエノールおよびホルムアルデヒド付加物の脱水縮合) を行う。 その脱水縮合は、'通常 1 3 0〜1 8 0 °C、 好ましくは 1 5 0〜1 7 0 °Cの温度、 および通常 5 0〜: L 0 0 k P a、 好ましくは 6 0〜7 5 k P' aの圧力下で、 通常 1〜 5時間、 好ましくは 2〜 3時間行われる。  The addition reaction between phenol and formaldehyde is carried out usually at 80 to 120 ° C, preferably 90 to 110 ° C, for usually 1 to 4 hours, preferably for 2 to 3 hours. After the addition reaction, dehydration and condensation of phenol and formaldehyde (dehydration and condensation of phenol and formaldehyde adducts) are performed in the presence of polyvinyl acetate. The dehydration condensation is carried out at a temperature of usually 130-180 ° C., preferably 150-170 ° C., and usually 50-: L 0 0 kPa, preferably 60-7. It is carried out under a pressure of 5 kP'a, usually for 1 to 5 hours, preferably for 2 to 3 hours.
本発明のポリ酢酸ビエル変性ノボラック型フエノ一ノレ樹脂を、 ポリ酢酸ビュル 変性ノポラック型フエノール樹脂の質量を基準に、 6 0〜 7 5質量%のフエノー ル、 1 5〜2 0質量0 /0のホルムアルデヒド、 0 . 2 0〜0 . 2 5質量0 /0のシユウ酸 および 5〜 2 0質量0 /0のポリ酢酸ビュルを用いて、 好ましくは製造する。 Polyvinyl acetate Biel-modified novolac-type Fueno one Honoré resin of the present invention, based on the weight of polyvinyl acetate Bulle modified Noporakku type phenolic resin, of 6 0-7 5 wt% Fueno le, 1 5 to 2 0 mass 0/0 formaldehyde, 0.2 0 to 0.2 5 weight 0/0 using a polyvinyl acetate Bulle of oxalic acid and 5-2 0 weight 0/0, preferably to produce.
特に、 ポリ酢酸ビュル変性ノボラック型フエノール樹脂中のポリ酢酸ビュル配 合比率は、 5質量%以上であることが好ましい。 なぜならポリ酢酸ビュル配合比 率を 5質量%以上にすることにより、 力学的および熱的負荷に対するフエノール 樹脂成形材料の寸法変化を、 より効果的に低減することができるからである。 一方、 ポリ酢酸ビエル変性ノポラック型フエノール樹脂中のポリ酢酸ビュルの 配合比率が多くなるにつれ、 ポリ酢酸ビュル変性ノポラック型フエノール樹脂を 含むフエノール樹脂成形材料の硬化速度が低下する。 従って、 望ましい硬化速度 を確保するため、 ポリ酢酸ビュル変性ノボラック型フエノール樹脂中のポリ酢酸 ビニル配合比率は 2 0質量%以下であることが好ましい。 In particular, it is preferable that the ratio of poly (vinyl acetate) in the poly (vinyl acetate) -modified novolak type phenol resin is 5% by mass or more. This is because the dimensional change of the phenolic resin molding material with respect to mechanical and thermal loads can be more effectively reduced by setting the polyacetic acid butyl compounding ratio to 5% by mass or more. On the other hand, as the blending ratio of polyacetate in the polyacetate-modified nopolak-type phenolic resin increases, the curing rate of the phenolic resin molding material containing the polyacetate-modified nopolak-type phenolic resin decreases. Therefore, in order to secure the desired curing rate, the polyacetic acid in the polyacetic acid-modified novolak type phenol resin The vinyl compounding ratio is preferably 20% by mass or less.
良好な耐水性および耐薬品性を有するポリ酢酸ビエル変性ノボラック型フエノ ール樹脂を得るために、 1 0 0 0 0以上の重量平均分子量を有するポリ酢酸ビエ ルを使用することが好ましい。  In order to obtain a polyacetate-modified vinyl acetate novolak phenol resin having good water resistance and chemical resistance, it is preferable to use a polyacetate biale having a weight average molecular weight of 1000 or more.
またポリ酢酸ビニル変性ノポラック型フエノール樹脂の製造段階において、 反 応混合物中へのポリ酢酸ビュルの良好な分散性を確保するために、 1 0 Q 0 0 0 以下の分子量を有するポリ酢酸ビュル変性を使用することが好ましい。  In addition, at the stage of producing the polyvinyl acetate-modified nopolak phenol resin, in order to ensure good dispersibility of the polyvinyl acetate in the reaction mixture, the polyvinyl acetate modified with a molecular weight of 100 Q It is preferred to use.
上記のように製造したポリ酢酸ビュル変性ノポラック型フエノール樹脂は、 2 0 0 0〜 6 0 0 0の重量平均分子量を有することが好ましい。 この範囲の重量平 均分子量を有するポリ醉酸ビュル変性ノポラック型フエノール樹脂は、 その後の フエノール樹脂成形材料を製造する際の混練等に適した溶融粘度を有するからで める。 ' ' ' .' · · ' ' ' . :  The polyacetic acid-modified nopolak type phenol resin produced as described above preferably has a weight average molecular weight of 2000 to 600. The polyvinyl sulphate-modified nopolak type phenolic resin having a weight average molecular weight in this range has a melt viscosity suitable for kneading and the like in the subsequent production of a phenolic resin molding material. '' '.' · '' ':
また本発明のフエノール樹脂成形材料が、 未変性のノポラック型フエノール樹 脂を含む場合、 そのノポラック型フエノール樹脂は、 好ましくは 2 0 0 0〜4 0 0 0の重量平均分子量を有する。  When the phenol resin molding material of the present invention contains an unmodified nopolak phenol resin, the nopolak phenol resin preferably has a weight-average molecular weight of 2000 to 400.
ポリ酢酸ビュル変性ノポラック型フエノール樹脂は、 その製造後に通常、 高温 のままバットに取り出され、 冷却固化した後、 その後のフエノール樹脂成形材料 の製造に使用される。 その後の取扱い性を向上させるため、 冷却固化したポリ酢 酸ビニルノボラック型フエノール樹脂を、 粉砕することが好ましい。  The polyphenol-modified nopolak-type phenol resin is usually taken out in a vat at a high temperature after its production, cooled and solidified, and then used for the production of a phenol resin molding material. In order to improve the subsequent handleability, it is preferable to pulverize the cooled and solidified polyvinyl acetate novolak type phenol resin.
本発明のフエノール樹脂成形材料は、 好ましくは、 フエノール樹脂成形材料の 質量を基準に、 1 0〜 3 0質量%のポリ酢酸ビュル変性ノポラック型フエノール 樹脂、 5〜 2 0質量0 /0のノボラック型フエノール榭脂、 4 0 - 6 0質量0 /0のガラ ス繊維および 5〜 2 0質量%の無機充填材を含む。 Phenolic resin molding material of the present invention, preferably, based on the weight of the phenolic resin molding material, 1 0-3 0% by weight of polyvinyl acetate Bulle modified Noporakku type phenolic resins, novolac type 5-2 0 weight 0/0 phenol榭脂, 4 0 - including 6 0 mass 0/0 glass fibers and 5-2 0% by weight of an inorganic filler.
これらの混合物を、 例えば二軸口一ルを用いて混練および粉砕することにより、 本発明のフエノ一ノレ樹脂成形材料を製造することができる。  By kneading and pulverizing these mixtures using, for example, a twin-screw opening, the phenolic resin molding material of the present invention can be produced.
特に、 フエノール樹脂成形材料中のポリ酢酸ビュル変性ノポラック型フエノー ル樹脂の配合比率は、 1 0質量%以上であることが好まし 、。 なぜならポリ酢酸 ビュル変性ノポラック型フエノール樹脂の配合比率を 1 0質量%以上にすること により、 フエノール樹脂成形材料の寸法変化を、 より効果的に低減することがで きるからである。 In particular, the compounding ratio of the polyacetic acid-modified nopolak type phenol resin in the phenol resin molding material is preferably 10% by mass or more. This is because the dimensional change of the phenolic resin molding material can be reduced more effectively by setting the compounding ratio of the polyacetic acid butyl modified nopolak phenolic resin to 10% by mass or more. Because it can.
一方、 ポリ酢酸ビュル変性ノボラック型フエノール樹脂の配合比率が多くなる につれ、 フエノール樹脂成形材料の硬化速度が低下する。 従って、 望ましい硬化 速度を確保するため、 変性ノポラック型フエノール樹脂の配合比率は 3 0質量 °/0 以下であることが好ましい。 On the other hand, as the compounding ratio of the polyacetate-modified novolak type phenol resin increases, the curing rate of the phenol resin molding material decreases. Therefore, in order to secure a desired curing rate, the blending ratio of the modified nopolak type phenol resin is preferably 30% by mass / 0 or less.
4 0質量%以上のガラス繊維を含むフヱノール樹脂成形材料から、 良好な強度 を有するコンミテータを得ることができる。 一方、 フエノール樹脂成形材料自体 を製造する際、 またはフェノール樹脂成形材料から成形品を成形する際に適した 溶融粘度を確保するため、 ガラス |¾锥量は 6 0質量%以下であることが好ましい。 フエノール樹脂成形材料中に含まれる無機充填材の例として、 ウォラストナイ ト、 炭酸カルシウム、 タルク、 力オリンおよびマイ力などが挙げられるが、 これ らに限定されない。 これらの無機充填材を、 単独または組合せて、 '使用すること · ができる。 .  A commutator having good strength can be obtained from a phenol resin molding material containing 40% by mass or more of glass fibers. On the other hand, in order to ensure a suitable melt viscosity when manufacturing the phenolic resin molding material itself or when molding a molded article from the phenolic resin molding material, the glass weight is preferably 60% by mass or less. . Examples of inorganic fillers included in the phenolic resin molding material include, but are not limited to, wollastonite, calcium carbonate, talc, mushylin and my mushy. These inorganic fillers can be used alone or in combination. .
本発明のフエノール樹脂成形材料を成形することにより; 力学的および熱的負 荷に対して寸法変化の小さいコンミテータを得ることができる。 ·  By molding the phenolic resin molding material of the present invention; a commutator having a small dimensional change with respect to mechanical and thermal loads can be obtained. ·
従つて本発明は、 本発明のフエノール樹脂成形材料を成形することにより得ら れるコンミテータも提供する。  Therefore, the present invention also provides a commutator obtained by molding the phenolic resin molding material of the present invention.
本発明のフエノール樹脂成形材料の成形方法の例として、 射出成形、 トランス ファ一成形およぴ圧縮成形などを挙げることができるが、 これらに限定されない。 コンミテータを成形する際には、 ノポラック型フエノール樹脂を成分とする本 発明のフエノール樹脂成形材料を硬ィ匕するために、 硬化剤が使用される。 硬化剤 として、 へキサメチレンテトラミンが好ましい。 へキサメチレンテトラミンとし て、 より好ましくは粒状へキサメチレンテトラミン、 特に 8 0メッシュのふるい を通過する粒子 9 9質量%以上を含む微粒子状のへキサメチレンテトラミン、 と りわけ 1 5 0メッシュのふるいを通過する粒子 9 8質量%以上を含む微粒子状の へキサメチレンテトラミンを使用する。 このような粒状ないし微粒子状のへキサ メチレンテトラミンを使用することにより、 その均一分散が確保され、 成形品外 観の向上並びに成形性および物性のバラツキの抑制を達成することができる。  Examples of the method for molding the phenolic resin molding material of the present invention include, but are not limited to, injection molding, transfer molding, and compression molding. When molding the commutator, a curing agent is used to harden the phenolic resin molding material of the present invention containing a nopolak-type phenolic resin as a component. Hexamethylenetetramine is preferred as the curing agent. Hexamethylenetetramine is more preferably a granular hexamethylenetetramine, particularly a fine-particle hexamethylenetetramine containing at least 99% by mass of particles passing through an 80-mesh sieve, particularly a 150-mesh sieve. Hexamethylenetetramine in the form of fine particles containing 98% by mass or more of particles passing through is used. By using such a granular or fine particle of hexamethylenetetramine, uniform dispersion thereof is ensured, and the appearance of a molded article can be improved, and variations in moldability and physical properties can be suppressed.
またコンミテータを成形する際に、 必要に応じて、 本発明のフエノール樹脂成 形材料と共に、 カップリング剤、 離型剤、 滑剤、 染料および顔料などの添加剤ま たは助剤を使用することができる。 Also, when forming the commutator, if necessary, the phenol resin composition of the present invention may be used. Additives or auxiliaries such as coupling agents, mold release agents, lubricants, dyes and pigments can be used with the form material.
実施例 Example
1 . ポリ酢酸ビュル変性ノポラック型フエノール樹脂の製造  1. Manufacture of poly (vinyl acetate) -modified nopolak phenolic resin
ポリ酢酸ビュル変性ノポラック型フエノール樹脂を、 その全質量を基準に、 3 Based on the total mass of the nopolak type phenolic resin modified with polybutyl acetate, 3
〜 2 5質量%のポリ酢酸ビュルを用いて以下のように製造した: Prepared using 225% by weight of polyacetate butyl as follows:
まずフエノールおょぴホルマリン (約 5 0 %水溶液) を、 シユウ酸の存在下で、 1 0 0 °Cで 9 0分間反応させ、 1 0 0 °Cで 1 2 0分間乳化させた後、 ポリ 酸ビ エル (重量平均分子量 1 5 0 0 0 ) を反応混合物に添加し、 1 6 0 °Cおよび 7 0 k P aで 1 8 0分間脱水縮合を行い、 ポリ酢酸ビニル変性ノボラック型フエノー ル樹脂を製造する。 それを高温のまま取出し、 7合却固化し、 粉砕したものをミ 以 下の成形材料の製造に使用する。 : . ——— First, phenol and formalin (about 50% aqueous solution) are reacted at 100 ° C for 90 minutes in the presence of oxalic acid, and emulsified at 100 ° C for 120 minutes. Acid beer (weight-average molecular weight: 1500) was added to the reaction mixture, dehydration-condensed at 160 ° C and 70 kPa for 180 minutes, and a polyvinyl acetate-modified novolak phenolic resin was added. To manufacture. It is taken out at a high temperature, 7 solidified, and pulverized and used for the production of the following molding materials. :. ———
2. 成形材料の製造 2. Production of molding materials
以下の表に質量部で示された量の原料を、 1分間混合し、 この混合物を二軸混 練機により、 品温 1 0 0。C〜 1 1 0 で 3分間混練する。 この混練物を、 令却固 化後に粉砕し、 造粒した成形材料を、 寸法変化等を評価するための試験片の成形 に使用する。  The raw materials in the amounts shown in parts by mass in the following table were mixed for 1 minute, and the mixture was heated at a product temperature of 100 using a twin-screw kneader. Knead with C ~ 110 for 3 minutes. This kneaded material is pulverized after solidification by rejection, and the granulated molding material is used for forming test pieces for evaluating dimensional changes and the like.
表に記載されている原料は、 以下のものである:  The raw materials listed in the table are:
•変性フェノ一ノレ樹脂:上記のように製造したポリ酢酸ビュル変性ノボラック 型フエノーノレ樹脂、 重量平均分子量 3 0 0 0。 表中に記載されている比率 (質 量。 /0) は、 ポリ酢酸ビュル変性ノボラック型フエノール樹脂の製造に使用した、 ポリ酢酸ビエルの比率を示す。 • Modified phenol resin: Polyvinyl acetate-modified novolak phenol resin produced as described above, with a weight average molecular weight of 300. Ratio described in Table (mass. / 0) were used for the production of polyvinyl acetate Bulle modified novolac-type phenolic resin, shows the ratio of polyvinyl acetate Biel.
■フエノール樹脂:ノボラック型フエノール樹脂、 昭和高分子株式会社製 B R P 5 9 0 P。  ■ Phenol resin: Novolak type phenol resin, BRP590P manufactured by Showa Kogyo Co., Ltd.
'ガラス ¾锥: 日東紡績株式会社製 C S 3 E— 4 7 9 S、 平均繊維径 ψ 1 2 、 鎩锥長 3 mm0 'Glass ¾ 锥: Nitto Boseki Co., Ltd. CS 3 E—4 79 S, average fiber diameter ψ12, length 3 mm 0
•無機充填材: NY C O社製ウォラストナイト NYAD 4 0 0。  • Inorganic filler: NY CO 400 wollastonite NYAD 400.
•添加剤:硬化剤へキサメチレンテトラミン (微粒子形態、 8 0メッシュのふ るいを通過する粒子含有量 9 9質量%以上、 1 5 0メッシュのふるいを通過する 粒子含有量 9 8質量。/。以上) (7質量部) 、 滑剤カルナバ (1質量部)(大日化学' 工業株式会社製カルナバ F— 1 ) および染料ソルベントブラック (1質量部)(ォ リエント化学工業株式会社製 S A P— L) 。 • Additive: Hardener Hexamethylenetetramine (Particulate form, passing through an 80-mesh sieve, particle content of 99% by mass or more, passing through a 150-mesh sieve Particle content 98 mass. /. (7 parts by mass), Carnava lubricant (1 part by mass) (Carnava F-1 manufactured by Dainichi Kagaku 'Industries Co., Ltd.) and Dye Solvent Black (1 part by mass) (SAP-L manufactured by Orient Chemical Co., Ltd.) .
この成形材料の成形性を調べるため、 成形材料 4 0 gを使用し、 1 6 0。Cおよ び 2 9. 4 MP aで押出し式流れ試験 [JIS K 6911] を行い、 その流出時間を測 定した。 その結果を、 以下の表に示す。 成形材料は、 実施上の成形の観点から、 6 0〜8 0秒の流出時間を有することが好ましい。  In order to examine the moldability of this molding material, 40 g of molding material was used. Extrusion flow tests [JIS K 6911] were performed at C and 29.4 MPa, and the outflow times were measured. The results are shown in the table below. The molding material preferably has an outflow time of 60 to 80 seconds from the viewpoint of practical molding.
3.評価用試験片の成形  3.Formation of test specimen for evaluation
上記の成形材料を、 出成形により、 J I S曲げ試験形状の試験片金型を用い て、 金型温度 1 7 0 °C、 硬化時間 9 0秒および射出圧力 1 2 8 M P aで成形し、 収縮試験おょぴ曲げ試験のための J I S規格形状を有する試験片を製造する。 こ れらの試験片について、 以下のような評価を行う。  The above molding material is formed by extrusion molding using a test piece mold with a JIS bending test shape at a mold temperature of 170 ° C, a curing time of 90 seconds, and an injection pressure of 128 MPa, and shrinks. Manufacture test specimens having JIS standard shape for test bending test. The following evaluation is performed on these test pieces.
4.試験片の評価  4.Evaluation of test piece
試験片について以下の評価を行った。 その結果を、 以下の表に示す。 . •ァニール処理による寸法変化  The following evaluation was performed about the test piece. The results are shown in the table below. • Dimensional change due to annealing treatment
試験片に、 1 8 0 °Cで 3時間、 次いで 2 1 0 °Cで 7時間ァニール処理を行い、 ァニール処理による試験片の寸法変化率を測定する。 試験片は、 小さい絶対値の 寸法変化率を有することが好ましい。  The test piece is annealed at 180 ° C. for 3 hours and then at 210 ° C. for 7 hours, and the dimensional change of the test piece due to the annealing treatment is measured. The specimen preferably has a small absolute dimensional change rate.
•高温処理による寸法変化  • Dimensional change due to high temperature treatment
上記のァニール処理した試験片に、 さらに 2 0 0 °Cで 5 0 0時間高温処理を行 い、 高温処理による試験片の寸法変化率を測定する。 試験片は、 小さい絶対値の 寸法変化率を有することが好ましい。 試験片の曲げ強さ [JIS K 6911] を測定した。 試験片は、 1 5 O MP a以上の 曲げ強さを有することが好ましい。 (表 1 ) The annealed test piece is further subjected to a high-temperature treatment at 200 ° C. for 500 hours, and the dimensional change of the test piece due to the high-temperature treatment is measured. The specimen preferably has a small absolute dimensional change rate. The bending strength of the test piece [JIS K 6911] was measured. The test piece preferably has a bending strength of 15 OMPa or more. (table 1 )
実施例 1 実施例 2 実施例 3 実施例 4 実施例 5 · 変性 3質量% 一 ― ― ― 一 フエノール 5質量 °/。 一 一 ― 一 一 樹脂 10質量% . ― 一 15 10 —  Example 1 Example 2 Example 3 Example 4 Example 5 Modified 3% by mass 1---1 phenol 5% by mass ° /. -11-11 mass% resin--15 10-
15質量% 12 18 一 一 15 15% by mass 12 18
20質量0 /0 一 ― ― 一 ―20 mass 0/0 one - - A -
25質量% 25% by mass
フエノール樹 Bヒ Phenol tree B
曰 19 13 16 20 16 ホ°リ酢酸ビニル  Says 19 13 16 20 16 Polyvinyl acetate
力、、ラス繊維 48 48 45 45 50 無機充填材 . 12 12 ' 15 15 10 添加剤 9 9 9 9 9 流動時間 (秒) 75 68 65 69 78 ァ二 ;レ処理による 0. 04 0. 09 0. 02 -0. 04 0. 10 寸法変化率 (%) Force, lath fiber 48 48 45 45 50 Inorganic filler. 12 12 '15 15 10 Additive 9 9 9 9 9 Flow time (sec) 75 68 65 69 78 . 02 -0. 04 0.10 Dimensional change rate (%)
高温処理による - 0. 18 - 0. 14 - 0. 22 - 0. 24 -0. 15 寸法変化率 (%) High temperature treatment-0.18-0.14-0.22-0.24 -0.15 Dimensional change (%)
曲げ強さ (MPa) 178 185 164 172 188Flexural strength (MPa) 178 185 164 172 188
(表 2 ) (Table 2)
実施例 6 実施例 7 実施例 8 実施例 9 実施例 10 変性. 18  Example 6 Example 7 Example 8 Example 9 Example 10 Modification.18
フエノール 10 Phenol 10
樹脂 10質量% Resin 10% by mass
15質量0 /0 515 mass 0/0 5
20質量0 /0 18 20 mass 0/0 18
25質量0 /0 18 25 mass 0/0 18
フエノ-ル樹脂 20 13 13 13 25 ホ。リ醉酸ヒ、 'ニル Phenolic resin 20 13 13 13 25 e. Rishang acid arsenic, 'nil
力、、ラス繊維 45 48 45 50 45 無機充填材 15 12 15 10 15 添加剤 9 9 9 9 9 流動時間 (秒) 77 56 54 44 70 ァニ ル処理による - 0. 06 0. 10 -0. 12 0. 10 -0. 11 寸法変化率 (%) Force, lath fiber 45 48 45 50 45 Inorganic filler 15 12 15 10 15 Additive 9 9 9 9 9 Flow time (sec) 77 56 54 44 70 By aniline treatment-0.06 0.10 -0. 12 0. 10 -0. 11 Dimensional change rate (%)
高温処理による - 0. 25 -0. 12 - 0. 28 - 0. 15 - 0. 29 寸法変化率 (%) High temperature treatment-0.25 -0.12-0.28-0.25-0.29 Dimensional change rate (%)
曲げ強さ (MPa) 191 171 157 191 167 (表 3 ) Flexural strength (MPa) 191 171 157 191 167 (Table 3)
実施例 11 実施例 12 比較例 1 比較例 2 変性 一 ― 一 一 フエノ ,レ 5質量% 一 18 一 一 樹脂 10質量0 /0 一 一 一 一 Example 11 Example 12 Comparative Example 1 Comparative Example 2 denatured single - A one Fueno, Les 5 wt% one 18 one first resin 10 mass 0/0 eleven eleven
15質量% 31 ― 一 ― 15% by mass 31 ― one ―
20質量0 /0 一 一 一 ―20 mass 0/0 one hundred eleven -
25質量% 一 25% by mass
フエノール樹 B gヒ Phenol tree B g
曰 13 30 28 ホ。リ醉酸ビ ル 3 力、、ラス賺 48 37 48 48 無機充填材 12 23 12 12 添加剤 9 9 9 9 流動時間 (秒) 42 71 68 66 ァ;: レ処理による 0. 09 0. 05 - 0. 17 -0. 15 寸法変化率 (%)  Says 13 30 28 e. Liquorate acid 3 power, lath Note 48 37 48 48 Inorganic filler 12 23 12 12 Additive 9 9 9 9 Flow time (sec) 42 71 68 66 0.17 -0.15 Dimensional change rate (%)
高温処理による - 0. 16 - 0. 15 -0. 35 -0, 33 寸法変化率 ( By high temperature treatment-0.16-0.15 -0.35 -0, 33 Dimensional change rate (
曲げ強さ (MPa) 166 127 169 172 Flexural strength (MPa) 166 127 169 172

Claims

請 求 の 範 囲 The scope of the claims
1 . ノポラック型フエノール樹脂および充填材を含むフェノ一ノレ樹脂成形材料で あって、 該ノボラック型フエノール樹脂の少なくとも一部が、 ポリ酢酸ビ-ノレ変 性ノポラック型フエノール樹脂であることを特徴とする、 フエノ一ル樹月旨成形材 料。 . . 1. A phenolic resin molding material containing a nopolak-type phenolic resin and a filler, wherein at least a part of the novolak-type phenolic resin is a polyvinyl acetate-modified nopolak-type phenolic resin. , Fenoll Jujube molding material. .
2 . ポリ酢酸ビュル変性ノポラック型フエノール樹月旨を、 ポリ酢酸ビニル変性ノ ポラック型フエノール樹脂の質量を基準に 5〜 2 0質量0 /0のポリ酢酸ビュルを用 いて製造したことを特徴とする、 請求項 1に記載のフエノール樹脂成形材料。2. Polyvinyl acetate Bulle modified Noporakku type phenolic trees month effect, characterized in that the mass of polyvinyl acetate modified Bruno Pollack type phenolic resin produced had use of polyvinyl acetate Bulle of 5-2 0 weight 0/0 to the reference The phenolic resin molding material according to claim 1.
3 . ポリ酢酸ビニノレ変性ノポラック型フエノール樹脂を、 ポリ酢酸ビニル変性ノ ボラック型フエノ ル樹脂の質量を基準に、 6 0〜 7 5質量0 /0のフエノール、 1 5〜·2 0質量%のホルムアルデヒド、 0 . 2 0〜0 . 2 5質量%のシユウ酸および 5〜 2 0質量%のポリ酢酸ビュルを用いて製造したことを特 ί数とする、 請求項 1 または 2に記載のフエノール榭脂成形材料。 . 3. The polyvinyl acetate Bininore modified Noporakku type phenolic resin, based on the weight of polyvinyl acetate modified novolac type Fueno Le resin, 6 0-7 5 mass 0/0 of phenol, 1 5, 2 0% by weight of formaldehyde The phenolic resin according to claim 1 or 2, characterized in that the phenolic resin is manufactured using 0.20 to 0.25% by mass of oxalic acid and 5 to 20% by mass of polyacetic acid butyl. Molding material. .
4 . ポリ酢酸ビュル変性ノポラック型フエノール樹脂を、 重量平均分子量 1 0 0 0 0〜1 0 0 0 0 0を有するポリ酢酸ビュルを用いて製造したことを特徴とする、 請求項 1 ~ 3のいずれかに記載のフエノール樹脂成形材料。  4. The poly (vinyl acetate) -modified nopolak phenolic resin is produced using poly (vinyl acetate) having a weight-average molecular weight of 100,000 to 1,000,000. A phenolic resin molding material according to any one of the above.
5 . 重量平均分子量 2 0 0 0〜 6 0 0 0を有するポリ酢酸ビニル変性ノポラック 型フエノール樹脂を含むことを特徴とする、 請求項 1〜4のいずれかに記載のフ ェノール樹脂成形材料。  5. The phenolic resin molding material according to any one of claims 1 to 4, comprising a polyvinyl acetate-modified nopolak phenolic resin having a weight-average molecular weight of 2000 to 600.
6 . フエノール樹脂成形材料の質量を基準に、 1 0〜 3 0質量%のポリ酢酸ビニ ル変性ノボラック型フエノール樹脂を含むことを特徴とする、 請求項 1〜 5のい ずれかに記載のフエノール樹脂成形材料。  6. The phenol according to any one of claims 1 to 5, comprising 10 to 30% by mass of a phenolic resin-modified novolak type phenolic resin based on the mass of the phenolic resin molding material. Resin molding material.
7 . フエノール樹脂成形材料の質量を基準に、 1 0〜 3 0質量0/。のポリ酢酸ビエ ル変性ノボラック型フエノール樹脂、 5〜 2 0質量0 /0のノボラック型フエノール 樹脂、 4 0 - 6 0質量0 /0のガラス繊維および 5〜 2 0質量0 /0の無機充填材を含む ことを特徴とする、 請求項 1〜 6のいずれかに記載のフエノール樹脂成形材料。7. 10 to 30 masses 0 / based on the mass of the phenolic resin molding material. Polyvinyl acetate Bie Le-modified novolac-type phenolic resin, 5-2 0 weight 0/0 novolak phenolic resins, 4 0 - 6 0 mass 0/0 Glass fiber and 5-2 0 weight 0/0 of inorganic filler The phenolic resin molding material according to any one of claims 1 to 6, further comprising:
8 . 請求項 1〜 7のいずれかに記載のフエノール樹脂成形材料を成形することに より得られたコンミテータ。 8. A commutator obtained by molding the phenolic resin molding material according to any one of claims 1 to 7.
PCT/JP2003/013816 2003-10-29 2003-10-29 Phenolic resin molding material and molded article thereof WO2005040276A1 (en)

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JP2008184488A (en) * 2007-01-26 2008-08-14 Matsushita Electric Works Ltd Phenolic resin molding material and molded article
JP2008184490A (en) * 2007-01-26 2008-08-14 Matsushita Electric Works Ltd Phenolic resin molding material and molded article
WO2010061793A1 (en) * 2008-11-25 2010-06-03 パナソニック電工株式会社 Phenol resin molding material and phenol resin molded article
WO2011052127A1 (en) * 2009-10-26 2011-05-05 パナソニック電工株式会社 Phenol resin molding material and phenol resin molded article
WO2015093260A1 (en) * 2013-12-20 2015-06-25 住友ベークライト株式会社 Thermosetting resin composition and metal-resin composite

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JPH0269510A (en) * 1988-09-02 1990-03-08 Matsushita Electric Works Ltd Molding material of phenolic resin
JPH0463858A (en) * 1990-07-02 1992-02-28 Toshiba Chem Corp Phenolic resin molding material
JP2000044771A (en) * 1998-07-30 2000-02-15 Sumitomo Bakelite Co Ltd Phenol resin molding material excellent in dimensional stability under heat

Cited By (7)

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Publication number Priority date Publication date Assignee Title
JP2008184488A (en) * 2007-01-26 2008-08-14 Matsushita Electric Works Ltd Phenolic resin molding material and molded article
JP2008184490A (en) * 2007-01-26 2008-08-14 Matsushita Electric Works Ltd Phenolic resin molding material and molded article
WO2010061793A1 (en) * 2008-11-25 2010-06-03 パナソニック電工株式会社 Phenol resin molding material and phenol resin molded article
WO2011052127A1 (en) * 2009-10-26 2011-05-05 パナソニック電工株式会社 Phenol resin molding material and phenol resin molded article
WO2015093260A1 (en) * 2013-12-20 2015-06-25 住友ベークライト株式会社 Thermosetting resin composition and metal-resin composite
CN105829452A (en) * 2013-12-20 2016-08-03 住友电木株式会社 Thermosetting resin composition and metal-resin composite
JPWO2015093260A1 (en) * 2013-12-20 2017-03-16 住友ベークライト株式会社 Thermosetting resin composition and metal resin composite

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