JPH08302159A - Production of phenol resin molding material - Google Patents

Production of phenol resin molding material

Info

Publication number
JPH08302159A
JPH08302159A JP10435295A JP10435295A JPH08302159A JP H08302159 A JPH08302159 A JP H08302159A JP 10435295 A JP10435295 A JP 10435295A JP 10435295 A JP10435295 A JP 10435295A JP H08302159 A JPH08302159 A JP H08302159A
Authority
JP
Japan
Prior art keywords
molding material
resin
phenol resin
resin molding
phenolic resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10435295A
Other languages
Japanese (ja)
Inventor
Satoyuki Saito
智行 斉藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP10435295A priority Critical patent/JPH08302159A/en
Publication of JPH08302159A publication Critical patent/JPH08302159A/en
Pending legal-status Critical Current

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  • Reinforced Plastic Materials (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE: To obtain a phenol resin molding material which gives an injection molded item having impact strength and static strengths well balanced at high level, greatly improves impact strength esp. in high-productivity injection molding, and greatly promotes the substitution for metals in the fields of automobiles and electric appliances. CONSTITUTION: A process for producing this phenol resin molding material is provided which comprises compounding a binder comprising 20-40wt.% dimethylene ether type resole resin and 5-15wt.% random novolak resin with 3-10wt.% carboxylated NBR. 40-60wt.% glass fibers, and a small amt. of a solvent and mixing the resulting compsn. under high-speed stirring to thereby remove the solvent and simultaneously granulate the compsn.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、レゾール型フェノール
樹脂にノボラック型フェノール樹脂、カルボキシル変性
NBR及びガラス繊維を配合することにより、特に射出
成形においても高い衝撃強度を与え、自動車、電機分野
の金属部品からの代替に適した衝撃強度に優れるフェノ
ール樹脂成形材料の製造方法に関するものである。
BACKGROUND OF THE INVENTION The present invention provides a high resilience type phenolic resin, a novolac type phenolic resin, a carboxyl-modified NBR and a glass fiber to give a high impact strength even in injection molding, and to provide a metal for automobiles and electric appliances. The present invention relates to a method for producing a phenolic resin molding material having excellent impact strength, which is suitable for substitution from parts.

【0002】[0002]

【従来の技術】フェノール樹脂成形材料は耐熱性、寸法
安定性、成形性等に優れ、自動車、電気、電子等の基幹
産業分野で長期にわたり使用されてきた実績がある。特
に最近では、金属部品をガラス繊維で強化した高強度の
フェノール樹脂成形品に置換することで、大幅な低コス
ト化が可能となることから、積極的な代替の検討が行な
われている。しかしながら、本来フェノール樹脂を初め
とする熱硬化性樹脂成形材料は、極端に言えば、落とせ
ば割れるというように衝撃強度が弱い欠点があり、これ
が金属部品への適用化拡大を阻害してきた一因と言え
る。この欠点を改善する試みは以前から数多くなされて
おり、例えば特開平3−137151号公報にあるよう
にレゾール樹脂、ノボラック樹脂、変性NBR及びガラ
ス繊維の配合により、この問題を解決している例もあ
る。但しこの公開特許公報に開示されたフェノール樹脂
成形材料でも、射出成形ではシリンダー部での混練時の
剪断力によりガラス繊維の破断が大きく十分満足できる
耐衝撃性を得ることが出来ない場合が多い。他方、製品
コストを下げるべく生産性の高い射出成形が成形方式と
して主流になりつつあることも事実である。
2. Description of the Related Art Phenolic resin molding materials are excellent in heat resistance, dimensional stability, moldability and the like, and have a long history of use in core industrial fields such as automobiles, electricity and electronics. Particularly in recent years, since replacement of metal parts with high-strength phenol resin molded products reinforced with glass fibers enables a significant cost reduction, active alternative studies are being conducted. However, in the extreme, thermosetting resin molding materials such as phenolic resins have the drawback of weak impact strength, such as cracking when dropped, which is a factor that has hindered the expansion of application to metal parts. Can be said. Many attempts have been made to ameliorate this drawback. For example, as disclosed in Japanese Patent Laid-Open No. 3-137151, a resol resin, a novolac resin, a modified NBR and a glass fiber are mixed to solve this problem. is there. However, even in the case of the phenol resin molding material disclosed in this publication, the glass fiber is often ruptured by the shearing force at the time of kneading in the cylinder portion in injection molding, and it is often impossible to obtain sufficiently satisfactory impact resistance. On the other hand, it is also a fact that injection molding with high productivity is becoming the main molding method in order to reduce the product cost.

【0003】[0003]

【発明が解決しようとする課題】本発明の衝撃強度に優
れるフェノール樹脂成形材料の製造方法は、得られた成
形材料中にガラス繊維を長く残すように製造すること
で、射出成形においても高い衝撃性を維持することがで
き、また一般に混練の程度を低くしてガラス繊維を長く
残した成形材料では、曲げ強度等の静的強度が低くなる
という欠点があるが、射出成形におけるシリンダー部で
の混練作用の調整により、その欠点もある程度補うこと
のできることが分かった。特に射出成形において高位に
衝撃強度、静的強度がバランスがとれるという知見が得
られ、本発明を完成するに至った。
DISCLOSURE OF THE INVENTION The method for producing a phenolic resin molding material having excellent impact strength according to the present invention is such that glass fiber is left in the obtained molding material for a long time, so that high impact is achieved even in injection molding. In addition, the molding material in which the kneading degree is kept low and the glass fiber is left for a long time has the drawback that the static strength such as bending strength becomes low, but in the cylinder part in injection molding, It was found that the drawback can be compensated to some extent by adjusting the kneading action. In particular, it was found that impact strength and static strength were well balanced in injection molding, and the present invention was completed.

【0004】[0004]

【課題を解決するための手段】本発明は、レゾール型フ
ェノール樹脂(レゾール樹脂)及びノボラック型フェノ
ール樹脂(ノボラック樹脂)よりなる結合剤に、カルボ
キシル変性NBR、ガラス繊維及び溶剤を必須成分とし
て配合したのち、高速撹拌混合しながら溶剤を除去し粒
状化することを特徴とする衝撃強度に優れるフェノール
樹脂成形材料の製造方法に関するものである。
According to the present invention, a carboxyl-modified NBR, glass fiber and a solvent are added as essential components to a binder consisting of a resol type phenol resin (resole resin) and a novolac type phenol resin (novolac resin). Then, the present invention relates to a method for producing a phenol resin molding material having excellent impact strength, which comprises granulating by removing a solvent while mixing with high speed stirring.

【0005】本発明で使用されるレゾール樹脂はジメチ
レンエーテル型のものが好ましく、数平均分子量500
〜900であることが好ましい。次にノボラック樹脂
は、特に限定はされないが、ランダム型ノボラック樹脂
が好ましく、数平均分子量800〜1200のものが好
ましい。従って、これらの樹脂を併用して用いるのが好
ましい。この理由としては、1つは高速撹拌混合して生
産する際の安定生産性であり、もう一つは硬化物の靭性
の向上効果である。例えばフェノール樹脂をレゾール樹
脂のみにすると、衝撃強度の大幅な向上は望めないし、
成形材料化の時のフローコントロールが難しく、安定し
た生産が困難となる。これに対して、ノボラック樹脂と
レゾール樹脂の併用では衝撃強度の大幅な向上が実現す
る。これはノボラック樹脂とレゾール樹脂とを併用する
と、硬化物がミクロ硬化物の集合体でなく、両者の反応
により一つの均一な硬化物になると考えられるためであ
る。
The resole resin used in the present invention is preferably a dimethylene ether type resin having a number average molecular weight of 500.
It is preferably from 900 to 900. Next, the novolac resin is not particularly limited, but a random novolac resin is preferable, and one having a number average molecular weight of 800 to 1200 is preferable. Therefore, it is preferable to use these resins in combination. The reason for this is that one is stable productivity when producing by high-speed stirring and mixing, and the other is the effect of improving the toughness of the cured product. For example, if you use only resol resin as the phenol resin, you cannot expect a significant improvement in impact strength,
It is difficult to control the flow when forming a molding material, which makes stable production difficult. On the other hand, the combined use of the novolac resin and the resol resin can significantly improve the impact strength. This is because when the novolac resin and the resole resin are used in combination, the cured product is not an aggregate of the micro-cured products, but is considered to be one uniform cured product by the reaction of both.

【0006】レゾール樹脂とノボラック樹脂の併用比率
は、60/40〜90/10程度であれば使用可能であ
り、70/30〜80/20が衝撃強度の点で効果的で
あり、好ましいものである。レゾール比率を高くすると
衝撃強度が低下し、またノボラック比率をこの範囲以上
にすると硬化性が悪くなる。
The resol resin and the novolac resin can be used in a combined ratio of about 60/40 to 90/10, and 70/30 to 80/20 is effective in terms of impact strength and is preferable. is there. When the resol ratio is increased, the impact strength is lowered, and when the novolac ratio is more than this range, the curability is deteriorated.

【0007】次に、カルボキシル変性NBRは、特に限
定されるものではないが、SP値が9〜10で、常温で
固形のものであれば好ましく使用することができる。ポ
リブタジエン、ニトリルゴムそれぞれのSP値は文献に
よれば8.5、9.5であるので、SP値が9〜10に
なるようにブタジエン、アクリロニトリル結合比率が調
整されているものであれば良い。また、カルボキシル基
はレゾール樹脂のメチロール基と反応することが知られ
ており、レゾール樹脂及びノボラック樹脂と混合され反
応したカルボキシル変性NBRの分散状態を良好にする
効果があり(ミクロ相分離構造)、カルボキシル基の存
在が意味あるのである。カルボキシル変性NBRにおけ
るカルボキシル基の割合は2〜10モル%が好ましい。
2モル%未満ではカルボキシル基の効果が小さく、10
モル%を越えると成形材料の流動特性が低下するように
なる。カルボキシル変性NBRの分子量については、特
に規制はしないが常温で固形であるのが好ましい。成形
材料全体に対する配合量は3重量%未満であれば、衝撃
強度の向上効果が少なく、10重量%以上であると耐熱
性が低下するようになるので、3〜10重量%が好まし
い。
Next, the carboxyl-modified NBR is not particularly limited, but can be preferably used as long as it has a SP value of 9 to 10 and is solid at room temperature. According to the literature, the SP values of polybutadiene and nitrile rubber are 8.5 and 9.5, respectively, so that the butadiene and acrylonitrile bond ratios may be adjusted so that the SP values are 9 to 10. Further, it is known that the carboxyl group reacts with the methylol group of the resole resin, and has an effect of improving the dispersion state of the carboxyl-modified NBR mixed with the resole resin and the novolac resin and reacting (micro phase separation structure), The presence of carboxyl groups is significant. The proportion of carboxyl groups in the carboxyl-modified NBR is preferably 2 to 10 mol%.
If it is less than 2 mol%, the effect of the carboxyl group is small and 10
If it exceeds mol%, the flow characteristics of the molding material will deteriorate. The molecular weight of the carboxyl-modified NBR is not particularly limited, but it is preferably solid at room temperature. If the compounding amount is less than 3% by weight with respect to the entire molding material, the effect of improving the impact strength is small, and if it is 10% by weight or more, the heat resistance tends to decrease, so 3-10% by weight is preferable.

【0008】無機充填材はガラス繊維のみを使用するの
が好ましい。ガラス繊維のようなアスペクト比が高い繊
維状の無機充填材を用いる方が衝撃強度向上に効果的で
あるからである。その配合量は成形材料全体に対し40
〜60重量%の範囲が好ましい。40重量%未満では衝
撃強度が低下し、60重量%を越えると成形材料化が困
難になる。ガラス繊維長は1〜3mmであることが衝撃
強度向上効果、材料化の容易さの点で有利である。更
に、充填材と樹脂の密着性を上げるのに、アミノシラ
ン、エポキシシラン等のシランカップリング剤を使用す
れば、強度、耐熱性向上に効果的である。
It is preferable to use only glass fibers as the inorganic filler. This is because using a fibrous inorganic filler having a high aspect ratio such as glass fiber is more effective in improving impact strength. The compounding amount is 40 with respect to the entire molding material.
The range of ˜60% by weight is preferred. If it is less than 40% by weight, the impact strength will decrease, and if it exceeds 60% by weight, it will be difficult to make it into a molding material. The glass fiber length of 1 to 3 mm is advantageous in terms of the impact strength improving effect and the ease of materialization. Furthermore, if a silane coupling agent such as aminosilane or epoxysilane is used to improve the adhesion between the filler and the resin, it is effective in improving strength and heat resistance.

【0009】次に本発明に係るフェノール樹脂成形材料
の製造方法を一例によって説明する。高速撹拌混合する
ための装置として代表的なものに流動型高速撹拌機があ
る。この装置は、例えば4枚の撹拌羽を混合槽内に有
し、側部には、水、蒸気が通ずるジャケット式温調装置
を備え、内部に樹脂温度測定用センサー、上部には排気
管を設けてなるものである。まず、このような混合機に
これまで説明したフェノール樹脂組成物と必要量の硬化
助剤、離型剤、着色剤を投入し、数十秒間撹拌混合しメ
タノール等の低沸点溶剤の適量と少量のカップリング剤
を投入する。溶剤等の投入量は合計量で2〜5%である
のが好ましい。溶剤の役割は粒子化を容易にするためで
あり、2%以下では材料化の際、結合剤であるフェノー
ル樹脂とガラス繊維が十分に密着せず、ガラス繊維が解
繊し毛玉が発生しやすい。逆に5%以上では粒子同士が
密着し粒子が巨大化することがある。いずれにおいても
射出成形可能な粒子形状にできないということになる。
続いて粒子化については、槽内温度を60〜100℃に
保ちつつ10〜30分間高速(500〜3000rp
m)で撹拌混合しながら、溶剤、水分を排気管より除去
し、乾燥と粒子化を同時に行わしめるものである。撹拌
初期においてはフェノール樹脂の縮重合反応を生起させ
るため加熱し、加熱撹拌によるフェノール樹脂とガラス
繊維の相互の摩擦熱、反応熱により樹脂温度が上昇して
くると冷却する。即ち低温では反応が進まず、高温では
反応が進みすぎてフェノール樹脂がゲル化することによ
る。撹拌速度については遅すぎるとフェノール樹脂成形
材料の粒子化が遅れ、しかも均一な粒状品が得られず、
速すぎるとガラス繊維の切断等が生じて好ましくない。
Next, the method for producing the phenolic resin molding material according to the present invention will be described by way of example. A fluid type high speed agitator is a typical device for high speed agitation and mixing. This device has, for example, four stirring blades in a mixing tank, a side temperature is equipped with a jacket type temperature control device through which water and steam pass, a resin temperature measuring sensor is provided inside, and an exhaust pipe is provided above. It is provided. First, such a mixer is charged with the phenol resin composition and the necessary amount of the curing aid, the release agent, and the colorant described above, and the mixture is stirred and mixed for several tens of seconds, and an appropriate amount and a small amount of a low boiling solvent such as methanol. Add the coupling agent. The total amount of the solvent and the like added is preferably 2 to 5%. The role of the solvent is to facilitate particle formation. When it is less than 2%, the phenol resin as a binder and the glass fiber do not sufficiently adhere to each other when the material is made, and the glass fiber is defibrated and pills are generated. Cheap. On the other hand, if it is 5% or more, the particles may adhere to each other and the particles may become huge. In either case, the particle shape cannot be injection-molded.
Subsequently, regarding particle formation, while maintaining the temperature in the tank at 60 to 100 ° C., high speed (500 to 3000 rp) for 10 to 30 minutes.
While stirring and mixing in m), the solvent and water are removed from the exhaust pipe, and drying and particle formation can be performed at the same time. In the initial stage of stirring, heating is carried out to cause a polycondensation reaction of the phenol resin, and cooling is carried out when the resin temperature rises due to mutual friction heat and reaction heat between the phenol resin and glass fiber due to heating and stirring. That is, the reaction does not proceed at low temperature, and the reaction proceeds too much at high temperature and the phenol resin gels. If the stirring speed is too slow, the granulation of the phenolic resin molding material is delayed, and a uniform granular product cannot be obtained.
If it is too fast, the glass fiber may be cut, which is not preferable.

【0010】上記の製造方法を用いた結果、フェノール
樹脂成形材料は直径2〜10mmの粒子状になり、射出成
形において高位に衝撃強度、静的強度がバランスのとれ
た成形材料が得られるのである。
As a result of using the above-mentioned manufacturing method, the phenol resin molding material is in the form of particles having a diameter of 2 to 10 mm, and a molding material in which impact strength and static strength are well balanced in injection molding can be obtained. .

【0011】[0011]

【実施例】以下、実施例により本発明を説明する。実施
例及び比較例の配合と特性を表1に示す。
The present invention will be described below with reference to examples. Table 1 shows the formulations and characteristics of the examples and comparative examples.

【0012】表1において組成の数値は重量%を示す。
特性の測定についてはJIS K 6911に準じて行っ
た。
In Table 1, the numerical values of the composition show% by weight.
The properties were measured according to JIS K 6911.

【表1】 [Table 1]

【0013】(注1)レゾール型フェノール樹脂:ジメ
チレンエーテル型フェノール樹脂(数平均分子量70
0) ノボラック型フェノール樹脂:ランダムノボラック型フ
ェノール樹脂(数平均分子量1000) (注2)ガラス繊維:繊維長1.5mm、繊維径10μ
m (注3)カルボキシル変性NBR:カルボキシル変性率
4モル% (注4)試験片は100tの射出成形機を用い、金型温
度180℃、シリンダー先端温度80℃に設定し、硬化
時間は60秒で成形した。更にその試験片を180℃、
8時間加熱エージングした。 (注5)射出成形性は100tの射出成形機を用い行っ
た。○:計量ばらつきがなく、連続成形性良好、△:連
続成形可能であるが、計量ばらつきがある。 (注6)材料中のガラス繊維長は成形材料を灰化して測
定した。
(Note 1) Resol type phenol resin: dimethylene ether type phenol resin (number average molecular weight 70
0) Novolac type phenol resin: Random novolac type phenol resin (number average molecular weight 1000) (Note 2) Glass fiber: Fiber length 1.5 mm, fiber diameter 10 μ
m (Note 3) Carboxyl-modified NBR: Carboxyl modification rate 4 mol% (Note 4) The test piece was set to a mold temperature of 180 ° C and a cylinder tip temperature of 80 ° C using an injection molding machine of 100 tons, and the curing time was 60 seconds. It was molded in. Furthermore, the test piece is heated to 180 ° C.
Heat aged for 8 hours. (Note 5) The injection moldability was 100 t using an injection molding machine. ◯: There is no variation in measurement and good continuous moldability. Δ: Continuous molding is possible, but there is variation in measurement. (Note 6) The glass fiber length in the material was measured by ashing the molding material.

【0014】[0014]

【発明の効果】以上の実施例および比較例から明らかな
ように、本発明のフェノール樹脂成形材料は、射出成形
において高位に衝撃強度、静的強度のバランスがとれて
いる。特に生産性の高い射出成形における衝撃強度が大
きく向上しているので、自動車、電機分野における金属
からの代替を大幅に促進するものである。
As is clear from the above Examples and Comparative Examples, the phenolic resin molding material of the present invention has a high balance of impact strength and static strength in injection molding. In particular, the impact strength in injection molding, which has high productivity, has been greatly improved, and therefore, it will greatly promote the substitution of metal in the fields of automobiles and electric machines.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08K 7/14 C08K 7/14 C08L 13/00 LBN C08L 13/00 LBN ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C08K 7/14 C08K 7/14 C08L 13/00 LBN C08L 13/00 LBN

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 レゾール型フェノール樹脂及びノボラッ
ク型フェノール樹脂よりなる結合剤に、カルボキシル変
性NBR(アクリロニトリルブタジエンゴム)、ガラス
繊維及び溶剤を必須成分として配合したのち、高速撹拌
混合しながら溶剤を除去し粒状化することを特徴とする
衝撃強度に優れるフェノール樹脂成形材料の製造方法。
1. A binder consisting of a resol type phenolic resin and a novolac type phenolic resin is mixed with carboxyl-modified NBR (acrylonitrile butadiene rubber), glass fiber and a solvent as essential components, and then the solvent is removed by high speed stirring and mixing. A method for producing a phenolic resin molding material having excellent impact strength, which is characterized by granulating.
【請求項2】 成形材料全体に対し、レゾール型フェノ
ール樹脂としてジメチレンエーテル型レゾール樹脂20
〜40重量%、ノボラック型フェノール樹脂としてラン
ダム型ノボラック樹脂5〜15重量%、カルボキシル変
性NBR3〜10重量%、及びガラス繊維40〜60重
量%からなる請求項1記載のフェノール樹脂成形材料の
製造方法。
2. A dimethylene ether type resole resin 20 as a resole type phenol resin for the whole molding material.
The method for producing a phenolic resin molding material according to claim 1, wherein the phenolic resin molding material comprises 40 to 40% by weight, a random novolac resin as a novolac phenolic resin 5 to 15% by weight, a carboxyl-modified NBR 3 to 10% by weight, and a glass fiber 40 to 60% by weight. .
【請求項3】 ガラス繊維が繊維長1〜3mmである請
求項1又は2記載のフェノール樹脂成形材料の製造方
法。
3. The method for producing a phenol resin molding material according to claim 1, wherein the glass fiber has a fiber length of 1 to 3 mm.
【請求項4】 撹拌混合は加熱撹拌である請求項1、2
又は3記載のフェノール樹脂成形材料の製造方法。
4. The stirring and mixing is heating stirring.
Or the method for producing the phenolic resin molding material according to 3 above.
JP10435295A 1995-04-27 1995-04-27 Production of phenol resin molding material Pending JPH08302159A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10435295A JPH08302159A (en) 1995-04-27 1995-04-27 Production of phenol resin molding material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10435295A JPH08302159A (en) 1995-04-27 1995-04-27 Production of phenol resin molding material

Publications (1)

Publication Number Publication Date
JPH08302159A true JPH08302159A (en) 1996-11-19

Family

ID=14378494

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10435295A Pending JPH08302159A (en) 1995-04-27 1995-04-27 Production of phenol resin molding material

Country Status (1)

Country Link
JP (1) JPH08302159A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009155747A1 (en) * 2008-06-26 2009-12-30 Sino Legend (Zhangjiagang) Chemical Co., Ltd. Modified phenolic tackifying resins for rubber compounding applications
WO2019093192A1 (en) * 2017-11-07 2019-05-16 住友ベークライト株式会社 Fiber-containing resin composition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009155747A1 (en) * 2008-06-26 2009-12-30 Sino Legend (Zhangjiagang) Chemical Co., Ltd. Modified phenolic tackifying resins for rubber compounding applications
WO2019093192A1 (en) * 2017-11-07 2019-05-16 住友ベークライト株式会社 Fiber-containing resin composition
JPWO2019093192A1 (en) * 2017-11-07 2019-11-14 住友ベークライト株式会社 Fiber-containing resin composition

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