JPH04222853A - Phenolic resin molding material for injection molding - Google Patents

Phenolic resin molding material for injection molding

Info

Publication number
JPH04222853A
JPH04222853A JP40641790A JP40641790A JPH04222853A JP H04222853 A JPH04222853 A JP H04222853A JP 40641790 A JP40641790 A JP 40641790A JP 40641790 A JP40641790 A JP 40641790A JP H04222853 A JPH04222853 A JP H04222853A
Authority
JP
Japan
Prior art keywords
phenolic resin
molding material
glass fiber
molding
injection molding
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
JP40641790A
Other languages
Japanese (ja)
Inventor
Manabu Goto
学 後藤
Toshiyuki Enomoto
敏行 榎本
Hideto Ogasawara
英人 小笠原
Yoshiyuki Shindo
進藤 義之
Shuhei Imon
修平 井門
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP40641790A priority Critical patent/JPH04222853A/en
Publication of JPH04222853A publication Critical patent/JPH04222853A/en
Pending legal-status Critical Current

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  • Injection Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain a phenolic resin molding material for injection molding having excellent fluidity and heat stability in a cylinder and remarkably improved in impact resistance of molding. CONSTITUTION:The objective phenolic resin molding material obtained by adding alpha, alpha-dimethoxy-p-xylene to a mixture consisting essentially of phenolic resin, hexamethylene tetramine and glass fiber, having 30-70wt.% glass fiber content and having 0.3-3.0mm number-average fiber length of glass fiber. The molding material can remarkably improve heat stability in a cylinder and impact resistance of the molding.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は流動性、シリンダー内熱
安定性に優れ、成形品の耐衝撃性を大幅に向上させるこ
とができる射出成形用フェノール系樹脂成形材料に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a phenolic resin molding material for injection molding which has excellent fluidity and in-cylinder thermal stability, and which can significantly improve the impact resistance of molded products.

【0002】0002

【従来の技術】一般に、射出成形用フェノール系樹脂成
形材料においては、安定的に連続成形するために、充分
な流動性、シリンダー内熱安定性を有することが必須で
ある。この流動性、シリンダー内熱安定性を向上させる
為に、α,α’−ジメトキシ−p−キシレンをフェノー
ル系樹脂成形材料に添加することにより、金型内での賦
形後の硬化性を損なうことなく、流動性、シリンダー内
熱安定性を向上させることが開示されている(特開昭6
3−264310号公報)。
BACKGROUND OF THE INVENTION In general, phenolic resin molding materials for injection molding must have sufficient fluidity and in-cylinder thermal stability for stable continuous molding. In order to improve this fluidity and in-cylinder thermal stability, α,α'-dimethoxy-p-xylene is added to the phenolic resin molding material, which impairs the hardening properties after shaping in the mold. It has been disclosed that the fluidity and in-cylinder thermal stability can be improved without any
3-264310).

【0003】一方、フェノール系樹脂成形品の耐衝撃性
を向上させるためには、充填材にガラス繊維を用いるの
が一般的であり、ガラス繊維は長いほど、耐衝撃性も高
くなる。この為、耐衝撃性の高いフェノール系樹脂成形
品を得るためには、長いガラス繊維を用いたフェノール
系樹脂成形材料が良い。しかし成形材料中に存在するガ
ラス繊維が長いと、射出成形時する場合、可塑化計量時
に成形材料がスクリューの回転による剪断力を受け発熱
し、硬化反応により流動性、シリンダー内熱安定性が低
下し、安定的に連続成形するには大きな問題があった。
On the other hand, in order to improve the impact resistance of phenolic resin molded articles, it is common to use glass fiber as a filler, and the longer the glass fiber, the higher the impact resistance. Therefore, in order to obtain a phenolic resin molded product with high impact resistance, a phenolic resin molding material using long glass fibers is preferable. However, if the glass fibers present in the molding material are long, during injection molding, the molding material receives shearing force from the rotation of the screw during plasticization measurement and generates heat, resulting in a decrease in fluidity and in-cylinder thermal stability due to the curing reaction. However, there were major problems in achieving stable continuous molding.

【0004】以上のことから、流動性、シリンダー内熱
安定性に優れ、かつ成形品の耐衝撃性の高いガラス繊維
を充填材とした射出成形用フェノール系樹脂成形材料は
未だ見出されていないのが実情であった。
[0004] From the above, a phenolic resin molding material for injection molding using glass fiber as a filler, which has excellent fluidity and in-cylinder thermal stability and has high impact resistance for molded products, has not yet been found. That was the reality.

【0005】[0005]

【発明が解決しようとする問題点】本発明の目的は、ガ
ラス繊維を充填材とし、流動性、シリンダー内熱安定性
に優れ、かつ耐衝撃性に優れた射出成形用フェノール系
樹脂成形材料を提供することにある。
[Problems to be Solved by the Invention] The object of the present invention is to provide a phenolic resin molding material for injection molding, which uses glass fiber as a filler, has excellent fluidity, thermal stability inside the cylinder, and has excellent impact resistance. It is about providing.

【0006】[0006]

【問題点を解決するための手段】本発明者らは、鋭意検
討した結果、フェノール系樹脂、ヘキサメチレンテトラ
ミン、ガラス繊維を主成分とする混合物にα,α’−ジ
メトキシ−p−キシレンを添加してなる射出成形用フェ
ノール系樹脂成形材料において、特定量のガラス繊維と
数平均繊維長を調整したガラス繊維を含有するフェノー
ル系樹脂成形材料が上記問題点を解決しうることを見出
し、本発明に到った。
[Means for solving the problem] As a result of intensive studies, the present inventors added α,α'-dimethoxy-p-xylene to a mixture whose main components are phenolic resin, hexamethylenetetramine, and glass fiber. It has been discovered that a phenolic resin molding material for injection molding, which contains a specific amount of glass fibers and glass fibers with an adjusted number average fiber length, can solve the above problems, and the present invention reached.

【0007】すなわち、本発明は、フェノール系樹脂、
ヘキサメチレンテトラミン、ガラス繊維を主成分とする
混合物にα,α’−ジメトキシ−p−キシレンを添加し
てなる射出成形用フェノール系樹脂成形材料において、
成形材料中のガラス繊維の含有量が30〜70重量%で
あり、ガラス繊維の数平均繊維長が0.3〜3.0mm
であることを特徴とする射出成形用フェノール系樹脂成
形材料であり、さらに射出成形用フェノール系樹脂成形
材料の製造において、フェノール系樹脂、ヘキサメチレ
ンテトラミン、ガラス繊維を主成分とする混合物及びα
,α’−ジメトキシ−p−キシレンを混合、分散処理す
る際に、各成分の合計量100重量部に対し、有機溶剤
および/または水を4〜15重量部添加して混練するこ
とを特徴とする射出成形用フェノール系樹脂成形材料の
製造方法でもある。
[0007] That is, the present invention provides phenolic resins,
In a phenolic resin molding material for injection molding, which is obtained by adding α,α'-dimethoxy-p-xylene to a mixture containing hexamethylenetetramine and glass fiber as main components,
The content of glass fiber in the molding material is 30 to 70% by weight, and the number average fiber length of the glass fiber is 0.3 to 3.0 mm.
A phenolic resin molding material for injection molding characterized by
When mixing and dispersing α'-dimethoxy-p-xylene, 4 to 15 parts by weight of an organic solvent and/or water are added to 100 parts by weight of each component in total and kneaded. It is also a method for producing a phenolic resin molding material for injection molding.

【0008】以下、本発明の内容を詳細に説明する。[0008] The contents of the present invention will be explained in detail below.

【0009】本発明に用いるフェノール系樹脂としては
、ヘキサメチレンテトラミンにより硬化させることので
きるフェノール系樹脂の全てを対象とすることができ、
例えば、フェノール、クレゾール、キシレノール、レゾ
ルシノール、ビスフェノールA、p−ブチルフェノール
、p−オクチルフェノール、スチレン化フェノールなど
のフェノール類とホルマリン、パラホルムアルデヒド、
トリオキサン、フルフラールなどのアルデヒド類とを酸
性触媒あるいは塩基性触媒を用いて反応させて得られる
フェノール系樹脂、フェノール類とα,α’−ジクロロ
−p−キシレンなどのp−キシリレンジハライド、α,
α’−ジメトキシ−p−キシレンなどのp−キシリレン
ジアルキルエーテルなどから誘導されるフェノールアラ
ルキル樹脂などがあり、これらの1種または2種以上を
混合して用いることができる。
The phenolic resin used in the present invention may include all phenolic resins that can be cured with hexamethylenetetramine.
For example, phenols such as phenol, cresol, xylenol, resorcinol, bisphenol A, p-butylphenol, p-octylphenol, and styrenated phenol, formalin, paraformaldehyde,
Phenolic resins obtained by reacting aldehydes such as trioxane and furfural using an acidic or basic catalyst, phenols and p-xylylene dihalides such as α,α'-dichloro-p-xylene, α,
There are phenol aralkyl resins derived from p-xylylene dialkyl ethers such as α'-dimethoxy-p-xylene, etc., and these resins can be used alone or in combination of two or more.

【0010】本発明において、ヘキサメチレンテトラミ
ンの使用量は、フェノール系樹脂100重量部に対して
3〜20重量部、好ましくは6〜15重量部である。3
重量部未満では、成形品の熱時剛性が悪く、20重量部
を越えると、成形品の表面にフクレが発生し、好ましく
ない。
In the present invention, the amount of hexamethylenetetramine used is 3 to 20 parts by weight, preferably 6 to 15 parts by weight, based on 100 parts by weight of the phenolic resin. 3
If it is less than 20 parts by weight, the molded product will have poor rigidity when heated, and if it exceeds 20 parts by weight, blistering will occur on the surface of the molded product, which is not preferable.

【0011】本発明におけるガラス繊維は、成形材料中
の含有量が30〜70重量%であり、数平均繊維長が0
.3〜3.0mm、好ましくは0.4〜2.5mmであ
る。ガラス繊維の含有量が30重量%未満ではガラス繊
維の充填材としての補強効果が出ず、成形品の耐衝撃性
が低く、70重量%を越えると、流動性が乏しく安定的
に連続成形できない。また、ガラス繊維の数平均繊維長
が0.3mm未満では成形品の耐衝撃性が低く、3.0
mmを越えると、流動性、シリンダー内熱安定性が低下
し、成形上支障を来す。
The content of glass fiber in the present invention in the molding material is 30 to 70% by weight, and the number average fiber length is 0.
.. It is 3 to 3.0 mm, preferably 0.4 to 2.5 mm. If the content of glass fiber is less than 30% by weight, the reinforcing effect of glass fiber as a filler will not be achieved, and the impact resistance of the molded product will be low; if it exceeds 70% by weight, fluidity will be poor and stable continuous molding will not be possible. . Furthermore, if the number average fiber length of the glass fiber is less than 0.3 mm, the impact resistance of the molded product will be low;
If it exceeds mm, fluidity and in-cylinder thermal stability will decrease, causing problems in molding.

【0012】本発明において、α,α’−ジメトキシ−
p−キシレンの使用量は、フェノール系樹脂100重量
部に対して1〜15重量部、好ましくは2〜10重量部
である。1重量部未満では流動性、シリンダー内熱安定
性の改善の効果が乏しく、15重量部を越えると、射出
成形する場合逆流が激しい上、成形品の外観を損ない好
ましくない。
In the present invention, α,α'-dimethoxy-
The amount of p-xylene used is 1 to 15 parts by weight, preferably 2 to 10 parts by weight, per 100 parts by weight of the phenolic resin. If it is less than 1 part by weight, the effect of improving fluidity and in-cylinder thermal stability is poor, and if it exceeds 15 parts by weight, backflow will be severe during injection molding and the appearance of the molded product will be impaired, which is not preferable.

【0013】本発明においては、必要に応じて顔料、滑
剤等の配合剤を添加することができる。配合剤としては
、顔料、滑剤、導電性付与剤、酸化防止剤、硬化促進剤
、エポキシ樹脂などの合成樹脂、シランカップリング剤
など通常のフェノール系樹脂成形材料に用いられるもの
を挙げることができる。
In the present invention, additives such as pigments and lubricants may be added as necessary. Compounding agents include pigments, lubricants, conductivity imparting agents, antioxidants, curing accelerators, synthetic resins such as epoxy resins, silane coupling agents, and other materials used in normal phenolic resin molding materials. .

【0014】本発明の射出成形用フェノール系樹脂成形
材料は、フェノール系樹脂、ヘキサメチレンテトラミン
、ガラス繊維を主成分とする混合物にα,α’−ジメト
キシ−p−キシレンを添加し、公知の方法、すなわちロ
ール、ニーダー、2軸混練押出機等により混練すること
により製造される。
The phenolic resin molding material for injection molding of the present invention is produced by adding α,α'-dimethoxy-p-xylene to a mixture containing a phenol resin, hexamethylenetetramine, and glass fiber as main components, and then using a known method. That is, it is produced by kneading with a roll, kneader, twin-screw kneading extruder, or the like.

【0015】成形材料中のガラス繊維の数平均繊維長を
0.3〜3.0mmに調整する方法としては、有機溶剤
または水を用いた湿式混練法が混練時のガラス繊維の折
損を防止しかつ均一に混練できるので望ましい。湿式混
練時に使用するガラス繊維は、通常のフェノール系樹脂
成形材料に用いられる直径が6〜13mm、カット長が
1.5〜12mmのチョップドストランドを挙げること
ができる。
[0015] As a method for adjusting the number average fiber length of the glass fibers in the molding material to 0.3 to 3.0 mm, a wet kneading method using an organic solvent or water is used to prevent breakage of the glass fibers during kneading. It is also desirable because it can be kneaded uniformly. The glass fibers used during wet kneading include chopped strands with a diameter of 6 to 13 mm and a cut length of 1.5 to 12 mm, which are used in ordinary phenolic resin molding materials.

【0016】また、湿式混練に用いる有機溶剤としては
、メタノール、エタノール等のアルコール類、アセトン
、メチルエチルケトン等のケトン類、フルフラール、ス
チレン等が挙げられ、これらの1種または2種以上併用
して使用できる。湿式混練における有機溶剤または水の
使用量は、フェノール系樹脂、ヘキサメチレンテトラミ
ン、ガラス繊維を主成分とする混合物及びα,α’−ジ
メトキシ−p−キシレンの各成分の合計量100重量部
に対し、4〜15重量部である。4重量部未満では混練
時にガラス繊維が折損し、15重量部を越えるとフェノ
ール系樹脂とガラス繊維の分散が不均一となる。
[0016] Examples of organic solvents used in wet kneading include alcohols such as methanol and ethanol, ketones such as acetone and methyl ethyl ketone, furfural, and styrene, and these may be used alone or in combination of two or more. can. The amount of organic solvent or water used in wet kneading is based on 100 parts by weight of the mixture containing phenolic resin, hexamethylenetetramine, glass fiber as the main components, and α,α'-dimethoxy-p-xylene. , 4 to 15 parts by weight. If it is less than 4 parts by weight, the glass fibers will break during kneading, and if it exceeds 15 parts by weight, the phenolic resin and glass fibers will not be uniformly dispersed.

【0017】混練温度及び混練時間につていは、用いる
混練機、有機溶剤の種類及び使用量等によって異なり、
特に限定するものではないが、それぞれ室温〜120℃
(沸点が120℃以下の有機溶剤については室温〜沸点
)、1〜30分が好ましい。混練温度が120℃を越え
ると、フェノール系樹脂とヘキサメチレンテトラミンの
硬化反応が起こり好ましくない。また、混練時間が1分
未満ではフェノール系樹脂とガラス繊維の分散が悪く、
30分を越えるとガラス繊維の折損が著しく好ましくな
い。
The kneading temperature and kneading time vary depending on the kneading machine used, the type and amount of organic solvent used, etc.
Although not particularly limited, each room temperature to 120℃
(room temperature to boiling point for organic solvents with a boiling point of 120°C or lower), preferably 1 to 30 minutes. If the kneading temperature exceeds 120°C, a curing reaction between the phenol resin and hexamethylenetetramine will occur, which is undesirable. In addition, if the kneading time is less than 1 minute, the dispersion of the phenolic resin and glass fibers will be poor.
If the time exceeds 30 minutes, it is undesirable that the glass fibers will be significantly broken.

【0018】以上により混練された混合物をロール、ま
たは押出機によりシート状に整形し、粉砕機にて粉砕す
るか、シートペレタイザー等のカッター式造粒機にて切
断して、成形材料とすることができる。
The mixture kneaded above is shaped into a sheet using a roll or an extruder, and then pulverized using a pulverizer or cut using a cutter type granulator such as a sheet pelletizer to obtain a molding material. I can do it.

【0019】[0019]

【実施例】以下、実施例、試験例により本発明を具体的
に説明する。
[Examples] The present invention will be specifically explained below with reference to Examples and Test Examples.

【0020】(実施例1〜5)表−1に示す通り、フェ
ノールノボラック樹脂(三井東圧化学株製、ノボラック
#1000HS及び#2000)、フェノールアラルキ
ル樹脂(三井東圧化学株製、ミレックスXL−225)
、ヘキサメチレンテトラミン、ステアリン酸マグネシウ
ム、カーボンブラックを粉砕、混合し、ニーダーに装入
、さらにα,α’−ジメトキシ−p−キシレン、アセト
ン、直径11μm、カット長6mmのガラスチョップス
トランド及びγ−アミノプロピルトリエトキシシランを
加え、混練した。混練物をシート状の整形後、ヘンシェ
ルミキサーにて粉砕、造粒し、乾燥して成形材料を得た
。得られた成形材料中の数平均ガラス繊維長についても
表−1に併記する。
(Examples 1 to 5) As shown in Table 1, phenol novolac resin (manufactured by Mitsui Toatsu Chemical Co., Ltd., Novolac #1000HS and #2000), phenol aralkyl resin (manufactured by Mitsui Toatsu Chemical Co., Ltd., Mirex XL- 225)
, hexamethylenetetramine, magnesium stearate, and carbon black were crushed and mixed, and charged into a kneader, and then α,α'-dimethoxy-p-xylene, acetone, glass chopped strands with a diameter of 11 μm and a cut length of 6 mm, and γ-amino Propyltriethoxysilane was added and kneaded. The kneaded material was shaped into a sheet, then pulverized and granulated using a Henschel mixer, and dried to obtain a molding material. The number average glass fiber length in the obtained molding material is also listed in Table-1.

【0021】(比較例1〜4)実施例1〜5と同様にし
て成形材料を得た。 (試験例)実施例1〜5、比較例1〜4で得た成形材料
について以下の試験を行なった。 ■流動性、シリンダー内熱安定性 東芝機械株製、射出成形機IR45Pを用いて、シリン
ダー前部温度95℃、シリンダー後部温度60℃、スク
リュー回転数50rpmで成形材料を計量し、計量直後
一定時間成形材料をシリンダー内に滞留させておき、射
出圧力800kg/cm2 で180℃に設定されたキ
ャビティ容量42cm3のJISファミリーモールド(
曲げ強度、シャルピー衝撃強度、吸水率試験片用)金型
に射出した。このとき、充填不良が起こらない最高の滞
留時間を熱安定性時間とした。 ■耐衝撃性 上記の条件にて成形して得られたシャルピー衝撃強度試
験片を用いて、JISK6911に準じシャルピー衝撃
強度を測定した。
(Comparative Examples 1 to 4) Molding materials were obtained in the same manner as in Examples 1 to 5. (Test Example) The following tests were conducted on the molding materials obtained in Examples 1 to 5 and Comparative Examples 1 to 4. ■Fluidity, thermal stability inside the cylinder Using an injection molding machine IR45P manufactured by Toshiba Machinery Co., Ltd., the molding material was weighed at a cylinder front temperature of 95°C, a cylinder rear temperature of 60°C, and a screw rotation speed of 50 rpm, and for a certain period of time immediately after the measurement. The molding material was retained in the cylinder, and a JIS family mold (with a cavity capacity of 42 cm3) set at 180°C and an injection pressure of 800 kg/cm2 was used.
(for bending strength, Charpy impact strength, and water absorption test pieces) was injected into a mold. At this time, the maximum residence time without causing filling defects was defined as the thermal stability time. (2) Impact resistance Charpy impact strength was measured according to JIS K6911 using the Charpy impact strength test piece obtained by molding under the above conditions.

【0022】■、■の試験結果についても表−1に併記
する。
The test results of ■ and ■ are also listed in Table 1.

【0023】[0023]

【表1】[Table 1]

【0024】[0024]

【発明の効果】本発明は上記した構成を取るので、従来
の射出成形用フェノール系成形材料にはない相反する2
つの特性、すなわち流動性、シリンダー内熱安定性と成
形品の耐衝撃性を両立させることが可能である。
[Effects of the Invention] Since the present invention has the above-described structure, it has two contradictory properties that are not present in conventional phenolic molding materials for injection molding.
It is possible to achieve both of the following properties: fluidity, in-cylinder thermal stability, and impact resistance of molded products.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】  フェノール系樹脂、ヘキサメチレンテ
トラミン、ガラス繊維を主成分とする混合物にα,α’
−ジメトキシ−p−キシレンを添加してなる射出成形用
フェノール系樹脂成形材料において、成形材料中のガラ
ス繊維の含有量が30〜70重量%であり、ガラス繊維
の数平均繊維長が0.3〜3.0mmであることを特徴
とする射出成形用フェノール系樹脂成形材料。
Claim 1: A mixture containing phenolic resin, hexamethylenetetramine, and glass fiber as main components contains α, α'
- In a phenolic resin molding material for injection molding containing dimethoxy-p-xylene, the content of glass fiber in the molding material is 30 to 70% by weight, and the number average fiber length of the glass fiber is 0.3. A phenolic resin molding material for injection molding, characterized in that the thickness is 3.0 mm.
【請求項2】  射出成形用フェノール系樹脂成形材料
の製造において、フェノール系樹脂、ヘキサメチレンテ
トラミン、ガラス繊維を主成分とする混合物及びα,α
’−ジメトキシ−p−キシレンを混合、分散処理する際
に、各成分の合計量100重量部に対し、有機溶剤およ
び/または水を4〜15重量部添加して混練することを
特徴とする請求項1記載の射出成形用フェノール系樹脂
成形材料の製造方法。
Claim 2: In the production of a phenolic resin molding material for injection molding, a mixture containing a phenolic resin, hexamethylenetetramine, glass fiber as the main components, and α, α
A claim characterized in that when mixing and dispersing '-dimethoxy-p-xylene, 4 to 15 parts by weight of an organic solvent and/or water are added to 100 parts by weight of each component in total and kneaded. Item 1. A method for producing a phenolic resin molding material for injection molding according to item 1.
JP40641790A 1990-12-26 1990-12-26 Phenolic resin molding material for injection molding Pending JPH04222853A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP40641790A JPH04222853A (en) 1990-12-26 1990-12-26 Phenolic resin molding material for injection molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP40641790A JPH04222853A (en) 1990-12-26 1990-12-26 Phenolic resin molding material for injection molding

Publications (1)

Publication Number Publication Date
JPH04222853A true JPH04222853A (en) 1992-08-12

Family

ID=18516035

Family Applications (1)

Application Number Title Priority Date Filing Date
JP40641790A Pending JPH04222853A (en) 1990-12-26 1990-12-26 Phenolic resin molding material for injection molding

Country Status (1)

Country Link
JP (1) JPH04222853A (en)

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