JPS5911357A - Polyphenylene sulfide resin molding material - Google Patents
Polyphenylene sulfide resin molding materialInfo
- Publication number
- JPS5911357A JPS5911357A JP11849182A JP11849182A JPS5911357A JP S5911357 A JPS5911357 A JP S5911357A JP 11849182 A JP11849182 A JP 11849182A JP 11849182 A JP11849182 A JP 11849182A JP S5911357 A JPS5911357 A JP S5911357A
- Authority
- JP
- Japan
- Prior art keywords
- molding material
- flow rate
- melt flow
- molding
- 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.)
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- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は圧縮圧形相あるいは射出Iフシ形用のポリフェ
ニレンサルファイド4i4脂成形材料に関するものであ
シ、特にポリフェニレンサルファイド樹脂がメルトフロ
ーレイトの異なる2林類からなり、無機質充填剤及びガ
ラス繊維を含有するホリフエニレンサルファイド樹脂成
形制料に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polyphenylene sulfide 4i4 resin molding material for compression molding type or injection I-shaped molding. The present invention relates to a holophenylene sulfide resin molding material containing an agent and glass fiber.
ポリフェニレンサルファイド樹脂(以下、pps樹脂と
称する)は熱可塑性樹脂でありながら、加熱等によジ榮
橋しうる熱硬化性樹脂の性質を有しており、ポリカーボ
ネート、ナイロン、飽和ポリエステル、その他のエンジ
ニアリングプラスチックと比較して剛性が極めて高く、
耐熱性、側薬品性、耐燃性、電気的性質などの優れたエ
ンジニアリングプラスチックとして知られている。pp
s樹脂は単独では伸びが少なく脆弱であるので成形材料
としての形態はガラス繊維を充填して強化をはかったp
ps樹脂樹脂成形材上て種々の成形用途に供されている
。Although polyphenylene sulfide resin (hereinafter referred to as pps resin) is a thermoplastic resin, it has the properties of a thermosetting resin that can be cured by heating, etc., and can be used with polycarbonate, nylon, saturated polyester, and other engineering materials. Extremely high rigidity compared to plastic
It is known as an engineering plastic with excellent heat resistance, chemical resistance, flame resistance, and electrical properties. pp
Since S resin alone has low elongation and is brittle, it is used as a molding material in the form of P, which is reinforced by filling it with glass fiber.
PS resin resin molding materials are used for various molding purposes.
しかしながら、かかるガラス繊維を充填したpps樹脂
成形材料は、圧縮成形あるいけ射出成形の際、fik、
彫金型中において成形材料の流tの伯九点であるウェル
ド部での融層が不児全とカリ易く、そのため成形品は熱
応力や機械的応力によりウェルド部から破壊する、いわ
ゆるウェルド強贋が低いという欠点を有している。特に
榛雑な形状の成形品を超音波溶着などの二次加工により
製造する場合、ウェルド部分からの破壊が著るしく増加
するという問題がある。However, during compression molding or injection molding, such glass fiber-filled pps resin molding materials cannot be used for fik,
In the engraving mold, the melt layer at the weld part, which is the ninth point of the flow of molding material, is easily damaged and the molded product breaks from the weld part due to thermal stress and mechanical stress, so-called weld failure. It has the disadvantage of being low. In particular, when manufacturing a molded article with a rough shape by secondary processing such as ultrasonic welding, there is a problem that breakage from the weld portion increases significantly.
従来から、ウェルド強度の低下に対しては、圧縮成形摩
・るいは射出成形に使用する金型の設計に改良を加えて
、この欠点を回避する手段がとられてきた。しかし、P
PS樹脂の優れた特性は、更に多様な、しかも複雑な形
状の成形品への対応が求められ、金型の改良による欠点
の回避という手段では対処しえなくなっている。Conventionally, measures have been taken to avoid this drawback by improving the design of molds used for compression molding or injection molding. However, P
The excellent properties of PS resin require support for molded products with even more diverse and complex shapes, and it is no longer possible to overcome the drawbacks by improving molds.
一方、PPS樹脂成形材料の改良が行なわれ、配合剤あ
るいは充填剤の検討が進み、配合剤とi〜てFe2O2
を用いた成形材料が市販されているが、該桐料による成
形品はウェルド強度は向上したにもかかわらす引張強度
は低く、かつFe2O2は置屋゛の影響によ多変色する
という欠点かあり、湿度の高い場所での使用には適して
いない。−士だ、充填剤としてのカラス繊維の径につい
て、径を小さくすることによりウェルド強度を向−卜せ
しめるという掟案もあるが、海老な効果は認められ々い
。On the other hand, improvements have been made to PPS resin molding materials, and studies on compounding agents or fillers have progressed, and the compounding agents are Fe2O2
Molding materials using paulownia materials are commercially available, but although molded products made of paulownia materials have improved weld strength, they have low tensile strength, and Fe2O2 has the disadvantage that it discolors many times due to the influence of heating. Not suitable for use in humid locations. Regarding the diameter of the glass fiber used as a filler, there is a proposal to improve the weld strength by reducing the diameter, but it has not been found to have any significant effect.
本発明者は、かかる問題点の認識にもとすいて梅々研死
、検削を行なった。その結果、PPS欄脂′がメルトフ
ローレイトを異VCする2種類からなり、無機質充填剤
及びガラス繊維を含有するPPS樹脂成形材料は成形時
の流動性が改良さ扛ることによυ成形品のウェルド強唐
が向上し、しかもPPS樹脂特有の性質を損なうことな
く、前記問題点を解決しうることを見い出した。The present inventor conducted Umeme grinding and inspection in order to recognize such problems. As a result, PPS resin is composed of two types with different melt flow rates, and PPS resin molding materials containing inorganic fillers and glass fibers have improved fluidity during molding, resulting in υ molded products. It has been found that the above-mentioned problems can be solved by improving the weld strength and without impairing the properties peculiar to PPS resin.
即ち、本発明は、圧縮成形用ああいは射出成形用のポリ
フェニレンサルファイド樹脂成形材料において、該成形
材料中のポリフェニレンザルファイト樹脂がメルトフロ
ーレイト(300℃、荷重5ooor)5〜】00と5
00以上の2種類からなシ、無機質充填剤及びガラス繊
維を含有するポリフェニレンサルファイド樹脂成形材料
に関するものである。本発明のpps樹脂成形材料にお
いて、PPS樹脂はASTMD 1238−70Tで定
めるメルトインデクサ−にて300℃、荷重5000F
の条件で測定したメルトフローレイトが5〜100 (
y/10分)(以下、PP5−Aと称する)と5oo(
r/]0分)以上(以下、PP5−Bと称する)の2釉
類からなるものである。メルトフローレイトの前記範、
囲にある2種類のPPS樹脂の配合は、後に示す実施例
と比較例の対比からも明らかなように、成形時の加工性
、即ち、流動性が改良されるため、ウェルド部における
樹脂の融着が完全に行なわれ、充填剤の配合による効果
とともに、成形品のウェルド強度など機械的強度を向上
せしめることができる。2種類のPPS樹脂のメルトフ
ローレイトが前記の範囲を逸脱すると成形時の流動性は
改良されず、従って成形品の機械的強度の向上は認めら
れない。That is, the present invention provides a polyphenylene sulfide resin molding material for compression molding or injection molding, in which the polyphenylene sulfite resin in the molding material has a melt flow rate (300°C, load 5ooor) of 5 to 00 and 5.
The present invention relates to a polyphenylene sulfide resin molding material containing two types of 0.00 or more, an inorganic filler, and glass fiber. In the pps resin molding material of the present invention, the PPS resin is tested at 300°C and a load of 5000F using a melt indexer specified in ASTM D 1238-70T.
Melt flow rate measured under the conditions of 5 to 100 (
y/10 min) (hereinafter referred to as PP5-A) and 5oo (
r/]0 minutes) or above (hereinafter referred to as PP5-B). The above range of melt flow rate,
As is clear from the comparison between Examples and Comparative Examples shown later, the formulation of the two types of PPS resins shown in the box improves the processability during molding, that is, the fluidity, so the melting of the resin in the weld part is improved. The adhesion is completed completely, and the mechanical strength such as the weld strength of the molded article can be improved in addition to the effect of the filler compounding. If the melt flow rates of the two types of PPS resins deviate from the above range, the fluidity during molding will not be improved, and therefore the mechanical strength of the molded product will not be improved.
pps樹脂は市販品か入手できる。即ち、pps樹脂は
米国フィリップスペトローリアム社より1ライドン’P
PSという商標名で製造収光されているものが広く知ら
れている。7ライトン’PPSにはその架橋度に応じて
各種のタイプのものがあり、本発明のPP5−AはP−
4(粉体)りL/−ト、p P S −B r6: v
−1、P−2、P−3、P−6(いずわも粉体)グレ
ードが使用できる。PPS resins are commercially available. That is, the pps resin is 1 Rydon'P from Phillips Petroleum Company of the United States.
The one produced under the trade name PS is widely known. There are various types of 7 Ryton' PPS depending on the degree of crosslinking, and the PP5-A of the present invention is P-
4 (powder) L/-t, p P S -B r6: v
-1, P-2, P-3, and P-6 (Izuwamo powder) grades can be used.
PP5−AとPP5−Bを配合することにより、流動性
が改良されるため、充填剤を多量に1合1−ることか可
能となる。かかる充填剤としては無機質充填剤が好適に
用いられる。無機質充填剤は特に限定されないが、成形
時の加熱により分解あるいは発煙を伴なわず、吸湿性あ
るいは経時変化などによシ成形品に影響を与えないもの
が好ましい。無機質充填剤を例示すれば、炭鯵カルシウ
ム、炭酸マグネシウム、硫酸バリウム、硫酸カルシウム
のような炭酸塩類、硫酸均類あるいは酸化銅、酸化亜鉛
、酸化チタン、酸化マグネシウム、アルミナのような金
桐酸化物、更に、シリカ、クラファイト、ホロンナイト
ライド、クルジ、クレーなどが革けられる。By blending PP5-A and PP5-B, fluidity is improved, so it becomes possible to mix a large amount of filler. Inorganic fillers are preferably used as such fillers. The inorganic filler is not particularly limited, but it is preferably one that does not decompose or emit smoke when heated during molding, and does not affect the molded product due to hygroscopicity or deterioration over time. Examples of inorganic fillers include carbonates such as calcium charcoal, magnesium carbonate, barium sulfate, and calcium sulfate, sulfuric acids, and metal tung oxides such as copper oxide, zinc oxide, titanium oxide, magnesium oxide, and alumina. In addition, silica, graphite, holonitride, cruzi, clay, etc. can be used.
無機質充填剤は、細かく粉砕されフy粉床状σ)もの、
あるいd、鱗片状のものが、流動性、機械的強度力どの
点で好すしい。無機質充填剤は1朴扛に1[(定でれる
ものでになく、2S類以上台併用することもできる。The inorganic filler is finely pulverized into a powder bed shape (σ),
Alternatively, scale-like materials are preferable in terms of fluidity and mechanical strength. The number of inorganic fillers is not limited to one per unit, and it is also possible to use 2S or more in combination.
本発明のPPS樹脂成形材料はPP5−A、P1?S−
B、無機質充填剤の配合物にカラス繊維が充填される。The PPS resin molding material of the present invention is PP5-A, P1? S-
B. The inorganic filler formulation is filled with glass fibers.
ガラスゆ糺は熱可塑性位j脂成形制狛によって成形され
゛る成形品の機械的強度の向上のために必塘である。か
かるカラス神維けP p s 樹脂の強化に通常使用さ
れるものでよく、市販のEガラス、0カラス、Sカラス
、Aガラスなど各種のカラス繊維を使用することができ
る。カラス繊維の形態はチョツプドストランド、ロービ
ング、ミルドファイバーなどいずれでもよいが、長い線
維や過剰に使用するととtit成形材料の流動性を低下
させるので適当でない。配合時のカラス繊維は、好管し
く1l−1直径5〜2 (1ミクロン、長で)05〜1
0筋程)kのもの、慣に好管しく(づ肉径13ミクロン
、長さ3關のチョツフトストラントで葎〕る。カラス輸
緬σビニノドシラン、ブミノシラン、エポキシシラン、
メルカフトシランなどの公知のシランカップリング剤あ
るいは集束剤で着面処理を施してもよく、こnらの処理
は成形時の加工性を優朴たものとし、しかも成形品の面
j*性、Tr+ 5特性を白土させる。Glass glue is essential for improving the mechanical strength of molded products formed by thermoplastic resin molding. Any glass fiber that is commonly used for reinforcing such Karasujin fiber P ps resin may be used, and various types of glass fibers such as commercially available E glass, 0 glass, S glass, and A glass can be used. The form of the glass fibers may be chopped strands, rovings, milled fibers, etc., but if they are long fibers or are used in excess, the fluidity of the tit molding material will be reduced, so it is not suitable. The glass fiber at the time of compounding is preferably 1l-1 diameter 5-2 (1 micron, length) 05-1
(approximately 0 strands) k, with a fine tube (with a wall diameter of 13 microns and a length of 3 mm).
Surface bonding treatment may be performed using a known silane coupling agent or sizing agent such as mercaftosilane, and these treatments improve workability during molding and improve the surface properties of the molded product. , Tr+ 5 characteristics are made white clay.
PP5−A、PP5−B、無?l仙充埴剤及びツノラス
繊維の配合割合は牛与に限定されるものでれ1ノ(いが
、圧縮酸形あるいし射出成形におけるR形時のaiPI
I性及び成形品の機誠的弥暦などの面から、好脣しい態
様けPP5−A99〜60重隼襲、PP5−Bo、5〜
20重i= %、無機質)1)埴剤05〜207ii
%%であり、かかる配合物95〜30箆匍チに対しカラ
ス細#15〜70重444%の配合が適当でめる。特に
PP61−A、PP5−B、無機質充填剤から々る配も
物55〜65重量−に対しガラス繊維35〜451[間
係であるのが好ましい。これらの配合剤41Jは1済性
の面C・−おいて無機質充填剤を多量とし、カラス繊維
を少がとするのが針管しいが、成形品の肪妄!ii j
Jj、との関係において、必要かつ充分な紹を越え庁い
方がよい。PP5-A, PP5-B, nothing? The blending ratio of the senjiro agent and the tunorasu fiber is limited to the one used in beef.
From the viewpoint of I characteristics and the integrity of the molded product, the appearance is unfavorable.
20 weight i = %, inorganic) 1) Clay agent 05-207ii
%%, and it is appropriate to mix 444% by weight of Crow Thin #15-70 for 95-30 weight. In particular, it is preferable that the weight of the glass fibers be 35 to 451% by weight for the weight of PP61-A, PP5-B, and the inorganic filler. In terms of convenience, C.--, these compounded preparations 41J contain a large amount of inorganic filler and a small amount of glass fiber. ii j
In your relationship with JJ, it is better to go beyond the necessary and sufficient introduction.
これらの混合方法は、公知の方法が採用づれる。たとえ
ば、PP5−A、PP5−B、無機質充填剤をヘンシェ
ルミキサーなどの混合棒(Cより機械的に均一に混合し
7て予備混合物とし、次いで該予備混合物とガラス給維
どケスクリユ一式の単ill捷たけ2軸の混練押出し根
に投入し、300〜4()0℃に加熱、溶融、混線を紅
て冷却(11、ベレット化することにより成形相料とす
ることがてきる。A known method can be used for mixing these. For example, PP5-A, PP5-B, and an inorganic filler are mechanically mixed uniformly using a mixing rod (C) such as a Henschel mixer to obtain a premix, and then the premix is mixed with a glass fiber feeder in a single unit. The mixture is put into a kneading extruder with two screws, heated to 300 to 40°C, melted, mixed, and cooled (11) It can be made into a molding phase material by pelletizing.
本発明の成形制料は、本発明の目的を逸脱しない範囲で
PPS征脂に対して他の熱可塑性樹脂すたVJ熱熱化化
性樹脂併用することかできる。The molding material of the present invention can be used in combination with other thermoplastic resins or VJ thermothermizable resins in addition to PPS resin without departing from the purpose of the present invention.
かかる樹脂としては、たとえば、ポリエチレン、ホリプ
ロビレン、ポリスチレン、ポリ塩化ビニル、メタクリル
樹脂、・丁すウレタン、ポリアミド、ポリカーホネート
、フッ素樹脂、ホリアミト−イミド、エポキシ樹脂、シ
リコーン樹脂などの公知の棒j脂が¥けられる。まだ、
カフス懺給以夕1の強化剤、たとえば、炭素締紐、チタ
ン酸カリウム、アスベスト、炭化ケイ素などを使用して
もよく、更に、潤滑剤、滑剤、着色剤、W〜安定剤、4
;泡剤、離型剤、酸化防止剤などを使用すること力・で
きる。Examples of such resins include known resins such as polyethylene, polypropylene, polystyrene, polyvinyl chloride, methacrylic resin, polyurethane, polyamide, polycarbonate, fluororesin, polyamitoimide, epoxy resin, and silicone resin. You can get rid of the fat. still,
In addition, reinforcing agents such as carbon cord, potassium titanate, asbestos, silicon carbide, etc. may be used in the cuff supply, and in addition, lubricants, lubricants, coloring agents, stabilizers, etc.
It is possible to use foaming agents, mold release agents, antioxidants, etc.
本発明の成形材料は無機質充填剤及びカラス繊維が適度
に配合されていることにより、ベレットや成形品の外観
は従来の成形材料に与らねない美味さを崩していイ、。Since the molding material of the present invention contains an appropriate amount of inorganic filler and glass fiber, the appearance of pellets and molded products does not lose the deliciousness that conventional molding materials lack.
し、かも成形時の流動1=j:力−1好のため、従来、
神々のトラブルの原因どなる充填剤、配合剤あるいは強
化剤の偏在を起すことがない。而して、本発明の成形材
料により成形された成形品の機械的強度、即ち、ウェル
ド強射、引張強度は後に示す比較例からも明らかなよう
に従来のpps樹脂成形材相にない強度を有するもので
ある。However, because the flow during molding 1 = j: force - 1, conventionally,
There will be no uneven distribution of fillers, compounding agents, or reinforcing agents, which causes trouble for the gods. As is clear from the comparative examples shown later, the mechanical strength of the molded product molded with the molding material of the present invention, that is, the weld blast strength and tensile strength, is higher than that of the conventional pps resin molding material phase. It is something that you have.
本発明の成形材料は通常の圧縮成形あるいは射出成形に
よって成形することができる。成形条件は牲に限定され
ることなく、通常の条件で行なわれる。本発明の成形材
料は、従来、機械的強度が低く、pps樹脂成形材料の
使用が困難であった複雑影状の成形品、/ことえは、超
音波溶層による二次加工を必要とする成形品の製ガ1を
可能とする。本発明の成形材料は1車輛用様制、電気機
械器具、電子機械器具、事務機械器具、化学機械器具、
あるいけその他の機械器具の部品、たとえば、板、棒、
管、容器、歯車などエンジニアリングプラスチックとし
て広い用途に使用できる。The molding material of the present invention can be molded by conventional compression molding or injection molding. The molding conditions are not particularly limited, and the molding is carried out under normal conditions. The molding material of the present invention can be used to create molded products with complex shadow shapes, which have conventionally had low mechanical strength and made it difficult to use PPS resin molding materials. Enables the production of molded products. The molding material of the present invention can be used for vehicle applications, electrical machinery appliances, electronic machinery appliances, office machinery appliances, chemical machinery appliances,
Parts of boats and other mechanical equipment, such as plates, rods,
It can be used in a wide range of applications as engineering plastics such as pipes, containers, and gears.
本発明の成形材料の評価方法は次の辿りである。即ち、
浴融粘度は高化式フローテスター(島津製作所製)を使
用し、温度300℃における粘度を測定した。成形品の
機械的強度はJIS−に7 ] 131/C従つ−r試
験片をPA製し、′テンシロン1引張試験機(東洋ホー
ルドウィン社製)を用いて引張ウェルド強度及び引張強
度を測定した。試験用成形品の成形は射出成形により行
ない、その条件は成形温度340°C1平均滞留時間2
.5分である。The method for evaluating the molding material of the present invention is as follows. That is,
The bath melt viscosity was measured at a temperature of 300° C. using a Koka type flow tester (manufactured by Shimadzu Corporation). The mechanical strength of the molded product is determined according to JIS-7] 131/C-r test piece was made of PA, and the tensile weld strength and tensile strength were measured using a Tensilon 1 tensile tester (manufactured by Toyo Holdwin Co., Ltd.). did. The test molded product was molded by injection molding, and the conditions were: molding temperature: 340°C, average residence time: 2
.. It's 5 minutes.
以下に本発明を実施例により具体的に駅、明するか、杢
−発明はとgら実施例のみに限定さねるもので1ない。The present invention will now be explained in more detail with reference to Examples, but the invention is not limited to these Examples.
実施例1
PPS−Aとして”ライドン’PP5P−4グレード(
メルトフローレイト実測値100以−ト)、PP5−B
として1ライドン”PP5V−1グレード(メルトフロ
ーレイト実測値約1500)(いずれも米国フィリップ
スベトローリアム社製)及び無機質充填剤として炭酸カ
ルシウムを52 / 5 / 3各重量部の割合に配合
しヘンシェルミキサーにて混合し予備混合物を得た。こ
の予備混合物にカラス繊維としてチョップドヌトラント
O8−03−λ4A−497゛(長さ3諭、旭ファイバ
ーグラス社製)40重量部を加えて、スクリュー径40
tmnlの単軸混練押出機に投入し、シリンダー及びダ
イス温度320℃、スクリュー回転毎分30回転で押出
し、ペレットを作成した。このペレットを射出成形機を
使用してシリンダー渦層340℃、金型温度120℃で
成形を行ない成形品を得た。得られた成形品をJIS−
に7]13に従った強度試験片に調製し、引張試験機に
て引張ウェルド強度及び引張強)基を測定した。別に溶
融粘度苓「フローテスターにて測定した。Example 1 "Rydon' PP5P-4 grade (
Melt flow rate actual value 100 or more), PP5-B
1 Rydon" PP5V-1 grade (measured melt flow rate approx. 1500) (all manufactured by Phillips Vetroleum, Inc. in the United States) and calcium carbonate as an inorganic filler at a ratio of 52/5/3 parts by weight. A premix was obtained by mixing in a mixer. To this premix, 40 parts by weight of chopped nutrant O8-03-λ4A-497゛ (length 3, manufactured by Asahi Fiberglass Co., Ltd.) was added as glass fiber, and the screw diameter was adjusted. 40
The mixture was put into a tmnl single-screw kneading extruder and extruded at a cylinder and die temperature of 320°C and a screw rotation of 30 revolutions per minute to create pellets. This pellet was molded using an injection molding machine at a cylinder swirl layer of 340°C and a mold temperature of 120°C to obtain a molded product. The obtained molded product is JIS-
A strength test piece was prepared according to 7] 13, and the tensile weld strength and tensile strength were measured using a tensile tester. Separately, melt viscosity was measured using a flow tester.
測定結果f第1表に示しだ。The measurement results are shown in Table 1.
実施例2〜4
実施例1におけるPP5−A、−B及び炭酸カルシウム
の配合割合を第1表に示す配合割合に変えた他は実施例
1と同様の方法でペレット及び成形品を作成し、引張ウ
ェルド強度、引張強度及び浩融粘度を測定した。Examples 2 to 4 Pellets and molded products were created in the same manner as in Example 1, except that the blending ratios of PP5-A, -B and calcium carbonate in Example 1 were changed to the blending ratios shown in Table 1. Tensile weld strength, tensile strength and bulk melt viscosity were measured.
測定結果11表に示した。The measurement results are shown in Table 11.
実施例5〜12
実施例】における無核質充填剤としての炭酸カルシウム
を第2衣に示す無機質充填剤に変えた他は実施例1と同
様の方法でベレット及び成形品全作成し、引張ウェルド
強度、引張強度及び電融粘度を測定した。Examples 5 to 12 All pellets and molded products were prepared in the same manner as in Example 1, except that the calcium carbonate as the non-nuclear filler in Example was changed to the inorganic filler shown in the second layer, and tensile welding was performed. Strength, tensile strength and melt viscosity were measured.
測定結果を第2表に示した。The measurement results are shown in Table 2.
比較例1〜5
組3表に示す配合物及び配合割合で、実施例と同様の方
法によシペレット及び成形品を作成し、引張ウコールド
強度、引張強度及び溶融粘度を測定した。Comparative Examples 1 to 5 Pellets and molded articles were prepared in the same manner as in Examples using the formulations and proportions shown in Table 3, and their tensile cold strength, tensile strength, and melt viscosity were measured.
測定結果を第3表に示した。The measurement results are shown in Table 3.
flり1 361−flri1 361-
Claims (2)
レンプルファイト樹脂成形材料において、該成形材料中
のポリフェニレンサルファイド樹脂がメルトフローレイ
ト(300℃、荷重5000f)5〜100と500以
上の2棟類からなり、無機質充填剤及びガラス繊維を含
有するポリフェニレンサルファイド樹脂成形材料。(1) In a polyphenylene pulfite resin molding material for compression molding or injection molding, the polyphenylene sulfide resin in the molding material has two types of melt flow rate (300°C, load 5000 f): 5 to 100 and 500 or more. , a polyphenylene sulfide resin molding material containing an inorganic filler and glass fiber.
ローレイト5〜100が99〜60重量%、メルトフロ
ーレイト500以上が05〜20重量%、無機質充填剤
05〜20重匍・チとからなる配合物95〜30重都チ
とガラス繊維5〜70篇葉チを含有する特許請求の範囲
第1項記載の成形材料。(2) A blend of polyphenylene sulfide resin with a melt flow rate of 5 to 100 in an amount of 99 to 60%, a melt flow rate of 500 or more in an amount of 05 to 20% by weight, and an inorganic filler of 05 to 20% by weight, 95 to 30%. 2. The molding material according to claim 1, which contains heavy fibers and 5 to 70 glass fibers.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11849182A JPS5911357A (en) | 1982-07-09 | 1982-07-09 | Polyphenylene sulfide resin molding material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11849182A JPS5911357A (en) | 1982-07-09 | 1982-07-09 | Polyphenylene sulfide resin molding material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5911357A true JPS5911357A (en) | 1984-01-20 |
JPS6367503B2 JPS6367503B2 (en) | 1988-12-26 |
Family
ID=14737980
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11849182A Granted JPS5911357A (en) | 1982-07-09 | 1982-07-09 | Polyphenylene sulfide resin molding material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5911357A (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60229949A (en) * | 1984-04-16 | 1985-11-15 | 東レ株式会社 | Reinforced polyarylene sulfide forming composition and formed product |
JPS6187752A (en) * | 1984-10-06 | 1986-05-06 | Tdk Corp | Resin composition |
JPS6281450A (en) * | 1985-10-04 | 1987-04-14 | Toray Ind Inc | Polyphenylene sulfide resin composition |
EP0237006A2 (en) * | 1986-03-11 | 1987-09-16 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thioether compositions |
JPS63108064A (en) * | 1986-10-23 | 1988-05-12 | Denki Kagaku Kogyo Kk | Polyphenylene sulfide resin composition |
EP0286298A2 (en) * | 1987-03-30 | 1988-10-12 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thioether composition for molding |
JPS63273665A (en) * | 1987-05-06 | 1988-11-10 | Sumitomo Bakelite Co Ltd | Polyphenylene sulfide resin composition |
US4785057A (en) * | 1984-06-29 | 1988-11-15 | Kureha Kagawa Kogyo Kabushiki Kaisha | Para-phenylene sulfide block copolymer, process for the production of the same |
US4820759A (en) * | 1986-09-09 | 1989-04-11 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thiother composition |
JPH0287487A (en) * | 1988-09-26 | 1990-03-28 | Sumitomo Wiring Syst Ltd | Connector |
JPH02107666A (en) * | 1988-10-17 | 1990-04-19 | Idemitsu Petrochem Co Ltd | Polyarylene sulfide resin composition |
JPH02180962A (en) * | 1988-12-30 | 1990-07-13 | Toopuren:Kk | Polyphenylene sulfide resin composition |
US5015686A (en) * | 1987-02-24 | 1991-05-14 | Phillips Petroleum Company | Coatings of arylene sulfide polymers |
EP0445985A2 (en) * | 1990-03-05 | 1991-09-11 | Kureha Kagaku Kogyo Kabushiki Kaisha | Process of production of poly(arylene thioether) resin compositions |
JPH06256653A (en) * | 1993-03-09 | 1994-09-13 | Dainippon Ink & Chem Inc | Polyarylene sulfide resin composition |
JPH06350284A (en) * | 1993-06-10 | 1994-12-22 | Murata Mfg Co Ltd | Chip coil element |
EP1159344A1 (en) * | 1998-12-18 | 2001-12-05 | Phillips Petroleum Company | Poly(arylene sulfide) compositions and their use |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5128145A (en) * | 1974-09-04 | 1976-03-09 | Hodogaya Chemical Co Ltd | HORIFUENIRE NSARUFUAIDOJUSHISOSEIBUTSU |
JPS5216214A (en) * | 1975-07-29 | 1977-02-07 | Hodogaya Chem Co Ltd | Composite material for finger board of string instrument |
JPS5322363A (en) * | 1976-08-13 | 1978-03-01 | Asahi Glass Co Ltd | Method of sealing electronic parts |
JPS5398356A (en) * | 1977-02-10 | 1978-08-28 | Asahi Glass Co Ltd | Polyphenylene sulfide resin molding material and its production |
JPS5447752A (en) * | 1977-09-19 | 1979-04-14 | Phillips Petroleum Co | Method of improving processability of arylenesulfide polymer composition |
JPS5543120A (en) * | 1978-09-22 | 1980-03-26 | Dainippon Ink & Chem Inc | Preparation of improved resin composition |
JPS55127002A (en) * | 1979-03-26 | 1980-10-01 | Kanegafuchi Chem Ind Co Ltd | Electric wave absorbing material with high heat resistance |
JPS5654025A (en) * | 1979-10-09 | 1981-05-13 | Murata Manufacturing Co | Grain boundary insulating type semiconductor porcelain composition |
JPS5770157A (en) * | 1980-10-21 | 1982-04-30 | Dainippon Ink & Chem Inc | Glass fiber-reinforced polyarylane sulfide resin composition |
-
1982
- 1982-07-09 JP JP11849182A patent/JPS5911357A/en active Granted
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5128145A (en) * | 1974-09-04 | 1976-03-09 | Hodogaya Chemical Co Ltd | HORIFUENIRE NSARUFUAIDOJUSHISOSEIBUTSU |
JPS5216214A (en) * | 1975-07-29 | 1977-02-07 | Hodogaya Chem Co Ltd | Composite material for finger board of string instrument |
JPS5322363A (en) * | 1976-08-13 | 1978-03-01 | Asahi Glass Co Ltd | Method of sealing electronic parts |
JPS5398356A (en) * | 1977-02-10 | 1978-08-28 | Asahi Glass Co Ltd | Polyphenylene sulfide resin molding material and its production |
JPS5447752A (en) * | 1977-09-19 | 1979-04-14 | Phillips Petroleum Co | Method of improving processability of arylenesulfide polymer composition |
JPS5543120A (en) * | 1978-09-22 | 1980-03-26 | Dainippon Ink & Chem Inc | Preparation of improved resin composition |
JPS55127002A (en) * | 1979-03-26 | 1980-10-01 | Kanegafuchi Chem Ind Co Ltd | Electric wave absorbing material with high heat resistance |
JPS5654025A (en) * | 1979-10-09 | 1981-05-13 | Murata Manufacturing Co | Grain boundary insulating type semiconductor porcelain composition |
JPS5770157A (en) * | 1980-10-21 | 1982-04-30 | Dainippon Ink & Chem Inc | Glass fiber-reinforced polyarylane sulfide resin composition |
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60229949A (en) * | 1984-04-16 | 1985-11-15 | 東レ株式会社 | Reinforced polyarylene sulfide forming composition and formed product |
US4785057A (en) * | 1984-06-29 | 1988-11-15 | Kureha Kagawa Kogyo Kabushiki Kaisha | Para-phenylene sulfide block copolymer, process for the production of the same |
JPS6187752A (en) * | 1984-10-06 | 1986-05-06 | Tdk Corp | Resin composition |
JPH0550545B2 (en) * | 1984-10-06 | 1993-07-29 | Tdk Electronics Co Ltd | |
JPS6281450A (en) * | 1985-10-04 | 1987-04-14 | Toray Ind Inc | Polyphenylene sulfide resin composition |
EP0237006A2 (en) * | 1986-03-11 | 1987-09-16 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thioether compositions |
JPS62240359A (en) * | 1986-03-11 | 1987-10-21 | Kureha Chem Ind Co Ltd | Polyarylene thioether composition |
JPH0548786B2 (en) * | 1986-03-11 | 1993-07-22 | Kureha Chemical Ind Co Ltd | |
US4820759A (en) * | 1986-09-09 | 1989-04-11 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thiother composition |
JPS63108064A (en) * | 1986-10-23 | 1988-05-12 | Denki Kagaku Kogyo Kk | Polyphenylene sulfide resin composition |
US5015686A (en) * | 1987-02-24 | 1991-05-14 | Phillips Petroleum Company | Coatings of arylene sulfide polymers |
EP0286298A2 (en) * | 1987-03-30 | 1988-10-12 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thioether composition for molding |
US4956499A (en) * | 1987-03-30 | 1990-09-11 | Kureha Kagaku Kogyo Kabushiki Kaisha | Polyarylene thioether composition for molding |
JPS63273665A (en) * | 1987-05-06 | 1988-11-10 | Sumitomo Bakelite Co Ltd | Polyphenylene sulfide resin composition |
JPH041477B2 (en) * | 1988-09-26 | 1992-01-13 | Sumitomo Wiring Systems | |
JPH0287487A (en) * | 1988-09-26 | 1990-03-28 | Sumitomo Wiring Syst Ltd | Connector |
JPH02107666A (en) * | 1988-10-17 | 1990-04-19 | Idemitsu Petrochem Co Ltd | Polyarylene sulfide resin composition |
JPH02180962A (en) * | 1988-12-30 | 1990-07-13 | Toopuren:Kk | Polyphenylene sulfide resin composition |
EP0445985A2 (en) * | 1990-03-05 | 1991-09-11 | Kureha Kagaku Kogyo Kabushiki Kaisha | Process of production of poly(arylene thioether) resin compositions |
US5256743A (en) * | 1990-03-05 | 1993-10-26 | Kureha Kagaku Kogyo K.K. | Poly(arylene thioether) resin compositions and extruded products thereof |
JPH06256653A (en) * | 1993-03-09 | 1994-09-13 | Dainippon Ink & Chem Inc | Polyarylene sulfide resin composition |
JPH06350284A (en) * | 1993-06-10 | 1994-12-22 | Murata Mfg Co Ltd | Chip coil element |
EP1159344A1 (en) * | 1998-12-18 | 2001-12-05 | Phillips Petroleum Company | Poly(arylene sulfide) compositions and their use |
EP1159344A4 (en) * | 1998-12-18 | 2002-11-06 | Phillips Petroleum Co | Poly(arylene sulfide) compositions and their use |
Also Published As
Publication number | Publication date |
---|---|
JPS6367503B2 (en) | 1988-12-26 |
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