JPS62148567A - Polyphenylene sulfide resin composition - Google Patents

Polyphenylene sulfide resin composition

Info

Publication number
JPS62148567A
JPS62148567A JP60287959A JP28795985A JPS62148567A JP S62148567 A JPS62148567 A JP S62148567A JP 60287959 A JP60287959 A JP 60287959A JP 28795985 A JP28795985 A JP 28795985A JP S62148567 A JPS62148567 A JP S62148567A
Authority
JP
Japan
Prior art keywords
polyphenylene sulfide
sulfide resin
pps
pigment
glass fiber
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.)
Granted
Application number
JP60287959A
Other languages
Japanese (ja)
Other versions
JPH0548784B2 (en
Inventor
Katsumi Nishizaki
西崎 克巳
Shigeyoshi Adachi
安達 茂好
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.)
Hodogaya Chemical Co Ltd
Tosoh Corp
Original Assignee
Hodogaya Chemical Co Ltd
Toyo Soda Manufacturing 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 Hodogaya Chemical Co Ltd, Toyo Soda Manufacturing Co Ltd filed Critical Hodogaya Chemical Co Ltd
Priority to JP60287959A priority Critical patent/JPS62148567A/en
Publication of JPS62148567A publication Critical patent/JPS62148567A/en
Publication of JPH0548784B2 publication Critical patent/JPH0548784B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Abstract

PURPOSE:To obtain the titled composition outstanding in both color tone and mechanical strength, suitable for electric and electronic parts especially connectors, etc., by blending specific polyphenylene sulfide resin, glass fiber, inorganic filler and pigment in each specified amount. CONSTITUTION:The objective composition can be obtained by blending (A) 80-30wt% of a polyphenylene sulfide resin (a copolymer from p-dichlorobenzene and trichlorobenzene) prepared by rinsing and extraction of an uncrosslinked polyphenylene sulfide resin having a melt viscosity (at 300 deg.C) 30-100Pa.s at a shear rate 500sec<-1> with an organic solvent (e.g. acetone) to such a point as to be <=1wt% in the oligomer content, (B) 10-50wt% of glass fiber (e.g. chopped strand with a diameter 20-5mu), (C) 0-40wt% of inorganic filler with an average particle size 30-1mum (e.g. calcium carbonate) and (D) 0.1-5wt% of pigment (e.g. titanium dioxide).

Description

【発明の詳細な説明】 [産業上の利用分野〕 本発明は電気・電子部品として1効に用いられる着色性
に優れたポリフェニレンサルファイド樹脂組成物に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a polyphenylene sulfide resin composition with excellent coloring properties that is used for one purpose as electrical and electronic parts.

[従来の技術] ポリフェニレンサルファイド樹脂(以下PPSと略記す
る)は優れた耐熱性、耐薬品性、難燃性を有しており、
ガラス繊維などの補強材と複合化され、電気・電子部品
、自動車部品として巾広く使用されている。
[Prior Art] Polyphenylene sulfide resin (hereinafter abbreviated as PPS) has excellent heat resistance, chemical resistance, and flame retardancy.
It is compounded with reinforcing materials such as glass fiber and is widely used in electrical/electronic parts and automobile parts.

電子部品においては、コネクター、スイッチなどとして
使用されているがこれら用途においては通常石仏によっ
て各部品の分類・仕分けを行っており、PPSに対して
も着色の要求は強く存在している。しかるにPPSは重
合によって得られた粉末状ポリマーを酸素の存在下20
0〜260℃という高温で酸化架橋した後に用いられる
ため褐色に青色することは避けられない。由に成形体は
チョコレート色を呈し、着色は黒色とすることのみが可
能で、これ以外の色、例えば青、緑といったものは、多
量のガj料、白色化する為のT io 2等を添加して
もなおかつくすんだ色しか得られず、強度的にも大巾な
低下を余儀なくさせられていた。
In electronic parts, they are used as connectors, switches, etc. In these applications, each part is usually classified and sorted using stone Buddha statues, and there is a strong demand for coloring PPS as well. However, PPS is a powdery polymer obtained by polymerization in the presence of oxygen.
Since it is used after being oxidized and crosslinked at a high temperature of 0 to 260°C, it is inevitable that it will turn brown to blue. Therefore, the molded product has a chocolate color and can only be colored black. Other colors such as blue and green can be produced by using a large amount of galvanic material, Tio 2, etc. for whitening. Even when it was added, only a dull color could be obtained, and the strength was also forced to deteriorate significantly.

[発明が解決しようとする問題点コ 本発明は上記欠点を排除しようとするもので、特定のベ
ースレジンとガラス繊維、無機フィラーさらに顔料を組
合せることにより色調、機械的強度共に優れた組成物を
得ようとするものである。
[Problems to be Solved by the Invention] The present invention aims to eliminate the above-mentioned drawbacks, and provides a composition that has excellent color tone and mechanical strength by combining a specific base resin, glass fiber, inorganic filler, and pigment. It is an attempt to obtain.

[問題を解決するための手段] すなわち本発明は、 1)特定のPPS樹脂 80〜30重量%2)ガラス繊
維    10〜50重−%3)無機フィラー    
0〜40重量%4)顔料      0.1〜5重量%
からなる組成物に関するものである。
[Means for Solving the Problems] That is, the present invention provides: 1) Specific PPS resin 80-30% by weight2) Glass fiber 10-50% by weight3) Inorganic filler
0-40% by weight 4) Pigment 0.1-5% by weight
The present invention relates to a composition comprising:

本発明において使用されるPPS樹脂は、300℃にお
ける溶融粘度がせん断速度500sec−1において3
0〜100Pa*sの未架橋樹脂である。
The PPS resin used in the present invention has a melt viscosity of 3 at a shear rate of 500 sec-1 at 300°C.
It is an uncrosslinked resin of 0 to 100 Pa*s.

このようなPPS樹脂を得る方法としては特公昭45−
3368に示されるごとくp−ジクロルベンゼンと硫化
ナトリウム等のアルカリ金属硫化物をN−メチル−2−
ピロリドン中で200〜250°Cの高温下重合させる
方法を挙げることが採用できる。
As a method for obtaining such PPS resin,
3368, p-dichlorobenzene and an alkali metal sulfide such as sodium sulfide are combined with N-methyl-2-
A method of polymerizing in pyrrolidone at a high temperature of 200 to 250°C can be adopted.

重合に際し、少量の共重合成分を添加することも可能で
ある。共重合成分としては、m−ジクロルベンゼン、0
−ジクロルベンゼン、4,4′−ジクロルジフェニルエ
ーテル、ジクロルジフェニルスルフォン、2,5−ジク
ロルトルエン、トリクロルベンゼンなど特公昭45−3
368に例示されるごとき成分はいづれも使用可能であ
る。
It is also possible to add a small amount of copolymerization component during polymerization. As a copolymerization component, m-dichlorobenzene, 0
-Dichlorobenzene, 4,4'-dichlorodiphenyl ether, dichlordiphenyl sulfone, 2,5-dichlorotoluene, trichlorobenzene, etc.
Any of the components exemplified in No. 368 can be used.

特にトリクロルベンゼンの様な多ハロゲン誘導体は粘度
の上昇の点から望ましいものである。
In particular, multihalogen derivatives such as trichlorobenzene are desirable from the viewpoint of increasing viscosity.

これら共重合成分はPPS樹脂の結晶化度を大きく低下
させる程添加することは望ましくなく通常5モル%以下
が選択される。又反応に際し、酢酸リチウム、酢酸ナト
リウムなどに代表されるアルカリ金属カルボン酸塩を添
加することも粘度の上昇の点で望ましい。
It is undesirable to add these copolymerization components to the extent that they greatly reduce the crystallinity of the PPS resin, and the amount of these copolymerization components is usually selected to be 5 mol % or less. Further, during the reaction, it is desirable to add an alkali metal carboxylate such as lithium acetate or sodium acetate from the viewpoint of increasing the viscosity.

得られたPPS樹脂はさらに熱架橋を行うことなく有機
溶剤によってオリゴマー含有量が1wt%以下になるま
で洗浄抽出される。ここでいうオリゴマーの含有量とは
ソックスレー抽出器によってTHFで12時間抽出を行
い抽出された値である。
The obtained PPS resin is washed and extracted with an organic solvent until the oligomer content becomes 1 wt % or less without further thermal crosslinking. The oligomer content referred to herein is the value extracted by performing extraction with THF using a Soxhlet extractor for 12 hours.

PPS樹脂の洗浄抽出方法としては、特に制限はないが
槽中にPPS粉末と有機溶剤を存在させ加熱撹拌を行い
、その後遠心分離等によってPPS樹脂を分離回収する
方法が簡便で望ましい。
Although there are no particular restrictions on the method for washing and extracting PPS resin, it is preferable to use a method in which PPS powder and an organic solvent are present in a tank, heated and stirred, and then the PPS resin is separated and recovered by centrifugation or the like.

本洗浄操作に使用される有機溶剤としては、メタノール
、エタノール、プロパツール等のアルコール類、アセト
ン、メチルエチルケトンの様なケトン類、ジエチルエー
テル、THFなどのエーテル類、ヘキサン、ヘプタンな
どの脂肪族炭化水素、ベンゼン、トルエン、キシレン等
の芳香族炭化水素、酢酸エチル、酢酸ブチルの様なエス
テル類、クロロホルム、トリクロロエチレン、四塩化炭
素等のハロゲン系有機溶剤、DMF、DMSO,N−メ
チル−2−ピロリドンの様な非プロトン性極性溶剤等が
挙げられる。特にアセトン、THF。
Organic solvents used in this cleaning operation include alcohols such as methanol, ethanol, and propatool, ketones such as acetone and methyl ethyl ketone, ethers such as diethyl ether and THF, and aliphatic hydrocarbons such as hexane and heptane. , aromatic hydrocarbons such as benzene, toluene, and xylene, esters such as ethyl acetate and butyl acetate, halogenated organic solvents such as chloroform, trichloroethylene, and carbon tetrachloride, DMF, DMSO, and N-methyl-2-pyrrolidone. Examples include various aprotic polar solvents. Especially acetone and THF.

トルエンなどは人手が容易である上に抽出効率も良好で
あり望ましいものである。この洗浄抽出操作によって得
られる組成物の色相が改良され、更に機械的強度も大1
11に改良される。この時のオリゴマー含有量は1wt
%以下であることが必要である。これより多いと得られ
る組成物の色相、機械的強度共に劣ったものとなってし
まう。
Toluene and the like are desirable because they are easy to use and have good extraction efficiency. The hue of the composition obtained by this washing and extraction operation is improved, and the mechanical strength is also greatly improved.
Improved to 11. The oligomer content at this time is 1wt
% or less. If the amount is more than this, the resulting composition will be inferior in both hue and mechanical strength.

本発明に使用されるガラス繊維としては直径20〜5μ
程度のチョツプドストランド、ローピン、ミルドファイ
バー等が使用される。その添加量としては10〜50重
量%の範囲で選択される。
The glass fiber used in the present invention has a diameter of 20 to 5μ.
Chopped strands, low pins, milled fibers, etc. are used. The amount added is selected within the range of 10 to 50% by weight.

10%未満であると成形体の機械的強度が不十分となり
又50%を越えると流動性が極度に低下するため成形か
困難となる。ガラス繊維は通常シランカップリング剤に
よって表面処理されており、シランとしてはアミノシラ
ン、メルカプトシラン、エポキシシラン等が選定される
。無機フィラーとしては特に制限はないが白変が高く純
度の高いものが望ましく具体的には炭酸カルシウム、タ
ルク、ケイ酸カルシウム、シリカ、硫酸カルシウムなど
があげられる。これら無機フィラーの平均粒径は30〜
1μmの範囲か望ましい。又その添加量は0〜40重量
%の範囲で選択される。40重量%を越えると流動性の
低下、機械的強度の低下など問題が多くなる。
If it is less than 10%, the mechanical strength of the molded product will be insufficient, and if it exceeds 50%, the fluidity will be extremely reduced, making molding difficult. Glass fibers are usually surface-treated with a silane coupling agent, and aminosilane, mercaptosilane, epoxysilane, etc. are selected as the silane. There are no particular restrictions on the inorganic filler, but it is desirable to use one with high white discoloration and high purity, and specific examples include calcium carbonate, talc, calcium silicate, silica, and calcium sulfate. The average particle size of these inorganic fillers is 30~
A range of 1 μm is desirable. Further, the amount added is selected within the range of 0 to 40% by weight. If it exceeds 40% by weight, problems such as a decrease in fluidity and a decrease in mechanical strength will occur.

本発明に使用される顔料は、無機系、有機系を特に問わ
ないが、PPSの成形温度である300℃以上の温度下
においても充分安定なものが望ましく、この点からは無
機系顔料が適している。具体的には酸化チタン、赤色酸
化鉄、群青、コバルトブルー、クロムグリーンライト、
カドミウムレッド、黄鉛などがあげられる。有機系の顔
料でもキナクリドンの様な耐熱性の優れたものは使用可
能である。その添加量は、0.1〜10重量%の範囲で
選択される。10重量%を大きく越えると色調は良いも
のの強度の低下が大きく実用上問題が多い。
The pigment used in the present invention does not particularly matter whether it is inorganic or organic, but it is desirable that it is sufficiently stable even at temperatures of 300°C or higher, which is the molding temperature of PPS, and from this point of view, inorganic pigments are suitable. ing. Specifically, titanium oxide, red iron oxide, ultramarine blue, cobalt blue, chrome green light,
Examples include cadmium red and yellow lead. Even organic pigments with excellent heat resistance such as quinacridone can be used. The amount added is selected within the range of 0.1 to 10% by weight. If it greatly exceeds 10% by weight, the color tone will be good, but the strength will drop significantly and there will be many practical problems.

本発明組成物にはさらに必要に応じて熱安定剤、酸化防
止剤、紫外線安定剤、帯電防止剤、滑剤、金型腐蝕防止
剤などを添加することも可能である。
It is also possible to further add heat stabilizers, antioxidants, ultraviolet stabilizers, antistatic agents, lubricants, mold corrosion inhibitors, etc. to the composition of the present invention, if necessary.

本発明組成物は主に射出成形によって成形されるが、こ
の他にも圧縮成形、押出し成形などの方法によっても成
形することが可能である。
The composition of the present invention is mainly molded by injection molding, but it can also be molded by other methods such as compression molding and extrusion molding.

[発明の効果コ 以上の説明から明らかなように本発明は(1)特定のP
PS樹脂(2)ガラス繊維(3)無機フィラー(4)顔
料よりなる組成物で、次に示すごとき優れた効果を得る
ことができる。
[Effects of the Invention] As is clear from the above explanation, the present invention provides (1) specific P
With a composition consisting of PS resin (2) glass fiber (3) inorganic filler (4) pigment, the following excellent effects can be obtained.

■)従来のPPS樹脂ではおよそ不可能であった色調の
着色組成物が得られる。
(2) A colored composition with a color tone that is almost impossible with conventional PPS resins can be obtained.

2)高い機械的強度を有する着色性組成物が得られる。2) A coloring composition having high mechanical strength can be obtained.

本組成物はPPS樹脂の優れた特性に加え優れた色調を
有していることから電気・電子部品特にコネクター、ス
イッチ等に極めてを効に使用される。
Since this composition has excellent color tone in addition to the excellent properties of PPS resin, it is extremely effectively used for electrical and electronic parts, especially connectors, switches, etc.

[実施例] 以下実施例に基づき本発明の一実施態様を例示するが本
発明はこれによってなんら限定されるものではない。
[Example] An embodiment of the present invention will be illustrated below based on an example, but the present invention is not limited thereto.

(PPS樹脂の製造−1) 15j2容量のオートクレーブにN a 2 S・2.
8H2014,8モル、N−メチル−2−ピロリドン4
.9Aを入れN2気流下撹拌して210℃まで昇温し、
437gの主に水からなる留出液を留去した。系を17
0℃まで冷却した後、p−ジクロルベンゼン14.8モ
ルを添加し、N2気流下に系を封入し、昇温しで250
℃にて3時間重合した。冷却後内容物を水中にあけ温水
で3回洗浄、ろ過を繰り返した後、120℃の熱風乾燥
機にて5時間乾燥を行った。得られたPPSは収量が1
485g、収率が95%であり、300℃における溶融
粘度がせん断速度500s ec−’において45Pa
−3であった。又オリゴマー含釘量はソックスレー抽出
器によるTHF12時間抽出の結果4.2%であった。
(Manufacture of PPS resin-1) In a 15j2 capacity autoclave, add Na2S.2.
8H2014, 8 mol, N-methyl-2-pyrrolidone 4
.. 9A was added, stirred under a N2 stream, and heated to 210°C.
437 g of a predominantly water distillate were distilled off. system 17
After cooling to 0°C, 14.8 mol of p-dichlorobenzene was added, the system was sealed under a N2 stream, and the temperature was raised to 250°C.
Polymerization was carried out at ℃ for 3 hours. After cooling, the contents were poured into water, washed three times with warm water, filtered repeatedly, and then dried in a hot air dryer at 120° C. for 5 hours. The yield of the obtained PPS is 1
485 g, yield is 95%, melt viscosity at 300°C is 45 Pa at shear rate 500 sec-'
-3. The amount of oligomer nails contained was 4.2% as a result of 12-hour THF extraction using a Soxhlet extractor.

この未架(、t、Hp p sをPP5(A)とした。This unframed (, t, Hp ps) was designated as PP5 (A).

PP5(A)を+1iび151オートクレーブにもどし
81のトルエンを加えリフラックス状態で3時間撹拌、
抽出を行った。冷却後トルエンとPPSをろ過により分
離、さらにトルエンによって十分洗浄を行い得られた粉
末は真空乾燥機によって十分乾燥を行った。得られたP
PSの溶融粘度は60Pa・sであり、オリゴマー含有
量は0. 2%であった。この洗浄抽出を行ったPPS
をPPS (B)とした。
Return PP5(A) to +1i and 151 autoclave, add toluene from 81 and stir in reflux state for 3 hours.
Extraction was performed. After cooling, toluene and PPS were separated by filtration, and the resulting powder was thoroughly washed with toluene and thoroughly dried in a vacuum dryer. Obtained P
The melt viscosity of PS is 60 Pa·s, and the oligomer content is 0. It was 2%. PPS subjected to this washing extraction
was designated as PPS (B).

(PPS樹脂の製造−2) 151容量のオートクレーブにN a 2 S・2.8
H2014,8モル、N−メチル−2−ピロリドン4.
91を入れN2気流下撹拌して210℃まで昇温し、4
41gの主に水からなる留出液を留去した。系を170
℃まで冷却した後、p−ジクロルベンゼン14.8モル
及びトリクロルベンゼン0.07モルを添加し、N2気
流下に系を封入し、昇温しで250 ℃にて3時間重合
した。冷却後内容物を水中にあけ温水で3回洗浄、ろ過
を繰り返した後、120°Cの熱風乾燥機にて5時間乾
燥を行った。得られたPPSは収量1469 gx収率
が94%であり、300℃における溶融粘度は86Pa
・sであった。又オリゴマー含有量は4.7%であった
。このポリマーをPPS (C)とした。
(Manufacture of PPS resin-2) Na2S・2.8 in a 151 capacity autoclave
H2014, 8 mol, N-methyl-2-pyrrolidone 4.
91, stirred under N2 stream, heated to 210℃, and heated to 210℃.
41 g of a predominantly water distillate were distilled off. 170 system
After cooling to .degree. C., 14.8 mol of p-dichlorobenzene and 0.07 mol of trichlorobenzene were added, the system was sealed under a N2 stream, and the temperature was raised to 250.degree. C. for 3 hours to polymerize. After cooling, the contents were poured into water, washed three times with warm water, filtered repeatedly, and then dried in a hot air dryer at 120°C for 5 hours. The obtained PPS has a yield of 1469 g x 94% and a melt viscosity of 86 Pa at 300°C.
・It was s. Moreover, the oligomer content was 4.7%. This polymer was designated as PPS (C).

PPS (C)を再び151オートクレーブにもどし8
(のアセトンを加えリフラックス状態で3時間撹拌、抽
出を行った。冷却後アセトンをろ過により分離、さらに
アセトンによって十分洗浄を行った。得られた粉末は真
空乾燥機によって十分乾燥を行った。得られたPPSの
溶融粘度は97Passであり、オリゴマー含有量は0
. 3%であった。このPPSをPP5(D)とした。
Return PPS (C) to the 151 autoclave 8
After cooling, the acetone was separated by filtration and thoroughly washed with acetone. The obtained powder was thoroughly dried in a vacuum dryer. The melt viscosity of the obtained PPS was 97Pass, and the oligomer content was 0.
.. It was 3%. This PPS was designated as PP5(D).

実施例l PP5 (B)1.4kg(35wt%)、ガラス繊維
(直径13μ、カット長3mmのチョツプドストランド
)1.4kg(35νt%)、炭酸カルシウム1、 1
2kg (28wt%)、顔料(群青)80g(2wt
%)をヘンシェルミキサーによって予備混合した後シリ
ンダ一温度310℃に設定した45mm二輔押出し機に
フィードし、スクリュー回転数100 rpmで混練し
、ホットカッターによりペレット化した。得られたペレ
ットは2オンス射出成形機(横型、型締カフ5Ton)
によって曲げ試験用短冊(3X25X120mm)及び
l zod衝撃強度測定用短In)(3,2X12. 
7X63. 5mm)を金型温度130℃で成形した。
Example l PP5 (B) 1.4 kg (35 wt%), glass fiber (chopped strand with a diameter of 13 μm and a cut length of 3 mm) 1.4 kg (35 νt%), calcium carbonate 1, 1
2kg (28wt%), pigment (ulmarine blue) 80g (2wt%)
%) were premixed using a Henschel mixer, then fed to a 45 mm Nisuke extruder set at a cylinder temperature of 310° C., kneaded at a screw rotation speed of 100 rpm, and pelletized using a hot cutter. The obtained pellets were molded using a 2-ounce injection molding machine (horizontal type, mold clamping cuff 5Ton).
A strip for bending test (3X25X120mm) and a strip for measuring impact strength (3,2X12.
7X63. 5 mm) was molded at a mold temperature of 130°C.

得られた試験片はくすみのない色調に優れたものであっ
た。又機械的強度を測定した結果、曲げ強度180MP
a、アイゾツト衝撃はノツチ側で41 J/m 、環ノ
ツチ側で146 J/mあった。
The obtained test piece was free from dullness and had an excellent color tone. Also, as a result of measuring the mechanical strength, the bending strength was 180MP.
a. The Izot impact was 41 J/m on the notch side and 146 J/m on the ring notch side.

比較例l PP5 (B)をPP5(A)に代えて実施例1と同様
の操作を行った。得られた試験片は、光沢が劣りゲート
部の反対側には著しい肌荒れを起していた。機械的強度
は曲げ強度が145MPa、アイゾツト衝撃強度はノツ
チ側で32J/[11,環ノツチ側で98J/mあり実
施例1に比べて大きく劣ったものであった。
Comparative Example 1 The same operation as in Example 1 was performed except that PP5 (B) was replaced with PP5 (A). The resulting test piece had poor gloss and significant roughness on the side opposite the gate. As for the mechanical strength, the bending strength was 145 MPa, the isot impact strength was 32 J/[11 on the notch side, and 98 J/m on the ring notch side, which were significantly inferior to Example 1.

比較例2 PPS (B)をステンレスバットに入れ250℃に加
熱した熱風循環式オーブン中で1時間加熱硬化させた。
Comparative Example 2 PPS (B) was placed in a stainless steel vat and cured by heating for 1 hour in a hot air circulation oven heated to 250°C.

得られたPPS樹脂の溶融粘度は80Pa−8であった
。又オリゴマーの含有量は1.8wt%であった。この
PPS樹脂をPP5(E)とした。
The melt viscosity of the obtained PPS resin was 80 Pa-8. Further, the oligomer content was 1.8 wt%. This PPS resin was designated as PP5(E).

PPS (E)を用い実施例1と同一の操作を行った。The same operation as in Example 1 was performed using PPS (E).

得られた試験片はくすんだ青色を呈し、実施例1に比べ
はるかに劣ったものであった。又機械的強度は曲げ強度
176MPa、アイゾツト衝撃強度はノツチ側で38 
J/m 、環ノツチ側で135J/mあった。
The obtained test piece exhibited a dull blue color and was far inferior to Example 1. In addition, the mechanical strength is bending strength 176MPa, and the isot impact strength is 38MPa on the notch side.
J/m, and it was 135 J/m on the ring notch side.

実施例2 PPS(D)を用い実施例1と同一の操作を行った。得
られた試験片はくすみのない色調に優れたものであった
。又機械的強度を/l111定した結果、曲げ強度17
6MPa、アイゾツト衝撃強度はノツチ側で40 J/
m 1反ノツチ側で129 J/mあった。
Example 2 The same operation as in Example 1 was performed using PPS (D). The obtained test piece was free from dullness and had an excellent color tone. In addition, as a result of determining the mechanical strength by /l111, the bending strength was 17
6MPa, Izotsu impact strength is 40 J/ on the notch side
There was 129 J/m on the anti-notch side.

比較例3 PPS (C)を用い実施例2と同一の操作を行った。Comparative example 3 The same operation as in Example 2 was performed using PPS (C).

得られた試験片は光沢が劣りゲート部の反対側には肌荒
れが認められた。機械的強度は、曲げ強度126MPa
、アイゾツト衝撃強度はノツチ側で27 J/m 、環
ノツチ側で89J/mであり、実施例2に比べ大きく劣
ったものであった。
The resulting test piece had poor gloss and rough skin was observed on the opposite side of the gate area. Mechanical strength is bending strength 126MPa
The Izo impact strength was 27 J/m on the notch side and 89 J/m on the ring notch side, which was significantly inferior to Example 2.

PPS−35wt%              O:
良好ガラス繊維−35vt%            
 △:ややくすむ炭酸カルシウム−28νt%    
       X:不良顔料(群青)−2wt%
PPS-35wt% O:
Good glass fiber - 35vt%
△: Slightly dull calcium carbonate - 28νt%
X: Defective pigment (ulmarine blue) -2wt%

Claims (1)

【特許請求の範囲】 1、300℃における溶融粘度がせん断速度500se
c^−^1において30Pa・s以上100Pa・s以
下である未架橋ポリフェニレンサルファイド樹脂を有機
溶剤によって洗浄抽出したオリゴマー含有量が1.0w
t%以下の樹脂80〜30重量%、ガラス繊維10〜5
0重量%、無機フィラー0〜40重量%、顔料0.1〜
5重量%からなるポリフェニレンサルファイド樹脂組成
物。 2、ポリフェニレンサルファイド樹脂がp−ジクロルベ
ンゼンとトリクロルベンゼンの共重合体である特許請求
の範囲第1項記載の組成物。
[Claims] 1. Melt viscosity at 300°C at shear rate of 500 se
An oligomer content of 1.0w is obtained by washing and extracting an uncrosslinked polyphenylene sulfide resin with an organic solvent of 30 Pa-s or more and 100 Pa-s or less at c^-^1.
t% or less resin 80-30% by weight, glass fiber 10-5%
0% by weight, inorganic filler 0~40% by weight, pigment 0.1~
A polyphenylene sulfide resin composition consisting of 5% by weight. 2. The composition according to claim 1, wherein the polyphenylene sulfide resin is a copolymer of p-dichlorobenzene and trichlorobenzene.
JP60287959A 1985-12-23 1985-12-23 Polyphenylene sulfide resin composition Granted JPS62148567A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60287959A JPS62148567A (en) 1985-12-23 1985-12-23 Polyphenylene sulfide resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60287959A JPS62148567A (en) 1985-12-23 1985-12-23 Polyphenylene sulfide resin composition

Publications (2)

Publication Number Publication Date
JPS62148567A true JPS62148567A (en) 1987-07-02
JPH0548784B2 JPH0548784B2 (en) 1993-07-22

Family

ID=17723957

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60287959A Granted JPS62148567A (en) 1985-12-23 1985-12-23 Polyphenylene sulfide resin composition

Country Status (1)

Country Link
JP (1) JPS62148567A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108064A (en) * 1986-10-23 1988-05-12 Denki Kagaku Kogyo Kk Polyphenylene sulfide resin composition
JPH01228815A (en) * 1988-03-09 1989-09-12 Toray Ind Inc Polyphenylene sulfide injection molding material
US5258442A (en) * 1989-10-31 1993-11-02 Tosoh Corporation Polyphenylene sulfide resin composition
JPH0649356A (en) * 1992-11-30 1994-02-22 Toray Ind Inc Polyphenylene sulfide resin composition
KR100419990B1 (en) * 2000-08-31 2004-03-03 주식회사 삼양사 A manufacturing of polyphenylene sulfide based thermoplastic resin composition
JP2017088690A (en) * 2015-11-06 2017-05-25 東ソー株式会社 Polyarylene sulfide-based composition

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5212240A (en) * 1975-07-18 1977-01-29 Matsushita Electric Ind Co Ltd Process for preparing transparent coating compounds
US4025496A (en) * 1975-10-10 1977-05-24 Phillips Petroleum Company Sequenced addition of components in poly(arylene sulfide) production
JPS56136847A (en) * 1980-03-31 1981-10-26 Dainippon Ink & Chem Inc Polyarylenesulfide composition
JPS57121052A (en) * 1981-01-22 1982-07-28 Toray Ind Inc Polyphenylene sulfide sheet -like material
JPS57205425A (en) * 1981-06-12 1982-12-16 Toray Ind Inc Stabilized polyphenylene sulfide
JPS58152019A (en) * 1982-02-19 1983-09-09 バイエル・アクチエンゲゼルシヤフト Light color polyphenylene sulfide, manufacture and mixture thereof with thermoplastic polycarbonate and/or thermoplastic polyester
JPS591536A (en) * 1982-06-04 1984-01-06 フイリツプス・ペトロリユ−ム・コンパニ− Recovery of granular poly(arylene sulfide)
JPS59204657A (en) * 1983-05-09 1984-11-20 Toray Ind Inc Polyphenylene sulfide composition
JPS59219331A (en) * 1983-05-27 1984-12-10 Dainippon Ink & Chem Inc Purification of polyphenylene sulfide
JPS60115631A (en) * 1983-10-28 1985-06-22 バイエル・アクチエンゲゼルシヤフト Manufacture of optionally branch chained polyarylene sulfidewith decreased corrosivity

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5212240A (en) * 1975-07-18 1977-01-29 Matsushita Electric Ind Co Ltd Process for preparing transparent coating compounds
US4025496A (en) * 1975-10-10 1977-05-24 Phillips Petroleum Company Sequenced addition of components in poly(arylene sulfide) production
JPS56136847A (en) * 1980-03-31 1981-10-26 Dainippon Ink & Chem Inc Polyarylenesulfide composition
JPS57121052A (en) * 1981-01-22 1982-07-28 Toray Ind Inc Polyphenylene sulfide sheet -like material
JPS57205425A (en) * 1981-06-12 1982-12-16 Toray Ind Inc Stabilized polyphenylene sulfide
JPS58152019A (en) * 1982-02-19 1983-09-09 バイエル・アクチエンゲゼルシヤフト Light color polyphenylene sulfide, manufacture and mixture thereof with thermoplastic polycarbonate and/or thermoplastic polyester
JPS591536A (en) * 1982-06-04 1984-01-06 フイリツプス・ペトロリユ−ム・コンパニ− Recovery of granular poly(arylene sulfide)
JPS59204657A (en) * 1983-05-09 1984-11-20 Toray Ind Inc Polyphenylene sulfide composition
JPS59219331A (en) * 1983-05-27 1984-12-10 Dainippon Ink & Chem Inc Purification of polyphenylene sulfide
JPS60115631A (en) * 1983-10-28 1985-06-22 バイエル・アクチエンゲゼルシヤフト Manufacture of optionally branch chained polyarylene sulfidewith decreased corrosivity

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108064A (en) * 1986-10-23 1988-05-12 Denki Kagaku Kogyo Kk Polyphenylene sulfide resin composition
JPH01228815A (en) * 1988-03-09 1989-09-12 Toray Ind Inc Polyphenylene sulfide injection molding material
JPH0558374B2 (en) * 1988-03-09 1993-08-26 Toray Industries
US5258442A (en) * 1989-10-31 1993-11-02 Tosoh Corporation Polyphenylene sulfide resin composition
JPH0649356A (en) * 1992-11-30 1994-02-22 Toray Ind Inc Polyphenylene sulfide resin composition
KR100419990B1 (en) * 2000-08-31 2004-03-03 주식회사 삼양사 A manufacturing of polyphenylene sulfide based thermoplastic resin composition
JP2017088690A (en) * 2015-11-06 2017-05-25 東ソー株式会社 Polyarylene sulfide-based composition

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