JPS5986646A - Reinforced polyolefin resin composition - Google Patents

Reinforced polyolefin resin composition

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Publication number
JPS5986646A
JPS5986646A JP19695682A JP19695682A JPS5986646A JP S5986646 A JPS5986646 A JP S5986646A JP 19695682 A JP19695682 A JP 19695682A JP 19695682 A JP19695682 A JP 19695682A JP S5986646 A JPS5986646 A JP S5986646A
Authority
JP
Japan
Prior art keywords
polyolefin
weight
butylperoxy
organic
peroxide
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
JP19695682A
Other languages
Japanese (ja)
Other versions
JPH0359934B2 (en
Inventor
Isao Sasaki
笹木 勲
Hiroshi Mori
弘 森
Yasuaki Ii
井伊 康明
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP19695682A priority Critical patent/JPS5986646A/en
Publication of JPS5986646A publication Critical patent/JPS5986646A/en
Publication of JPH0359934B2 publication Critical patent/JPH0359934B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To provide a reinforced polyolefin resin compsn. which is excellent in mechanical and electrical properties and water repellency and has low specific gravity, by blending a reinforcing org. fiber, a reinforcing inorg. fiber or an inorg. filler with a specified modified polyolefin. CONSTITUTION:A reinforcing org. fiber, a reinforcing inorg. fiber or an inorg. filler is blended with a modified polyolefin or a mixture thereof with an unmodified polyolefin or other thermoplastic resin, said modified polyolefin being obtd. by reacting 0.05-0.8pts.wt. unsaturated carboxylic acid with 100pts.wt. polyolefin in the presence of benzoyl peroxide and 0.03-3pts.wt. org. peroxide derived from a dialkyl compd. or ketal having a decomposition temp. of 80 deg.C or higher to obtain a half life period of 10hr.

Description

【発明の詳細な説明】 を有し、かつ低比重でしかも撥水性に優れた強化ポリオ
レフイン系樹脂組成物に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reinforced polyolefin resin composition having the following properties, low specific gravity, and excellent water repellency.

熱可塑性複合材料の工業用途への利用は最近めざましい
ものがあり、材料も種々特徴を生かして数多く用いられ
てい乙。中でもポリエチレン.ポリプロピレンなどに代
表されるポリオレフィン系樹脂は、低比重で成形加工性
および耐薬品性に優力、シかも安価であるため、各分野
で多量に使用されている。しかし、ポリオレフィン系樹
脂は機械的性質,耐熱性などが要求される工業制料の用
途においては、物性が十分でなく、各種の強化剤や充填
剤を配合することが試みられたが、無極性樹脂であるた
め.各種の強化剤や充填剤との親和性に乏しく、補強効
果が低いものしか得られなかった。そこでその対策とし
て、ポリオレフィンに極性基を導入し、強化剤または充
填剤との親和性を改良する方法が種々報告されており、
補強効果の高いものが得られるようになった。
Recently, the use of thermoplastic composite materials for industrial purposes has been remarkable, and many materials are being used that take advantage of their various characteristics. Among them, polyethylene. Polyolefin resins such as polypropylene are used in large quantities in various fields because they have low specific gravity, excellent moldability and chemical resistance, and are inexpensive. However, polyolefin resins do not have sufficient physical properties for industrial applications that require mechanical properties, heat resistance, etc., and attempts have been made to incorporate various reinforcing agents and fillers, but Because it is resin. It has poor affinity with various reinforcing agents and fillers, and only those with low reinforcing effects were obtained. As a countermeasure against this, various methods have been reported to introduce polar groups into polyolefins to improve their affinity with reinforcing agents or fillers.
It is now possible to obtain items with a high reinforcing effect.

しかし、成形加工性については問題点が残されており、
とりわけ薄肉成形品または大型成形品については補強剤
または充填剤の配合により薄肉部分の肉厚および面稍.
また大型成形品では大きさ、形状によっては成形困難で
あることが多い。本発明者らはこの点の改良に関して検
討を加え、ポリオレフィンに極性基を導入する過程、す
なわち、ポリオレフィンへの不飽和カルボン酸グラフト
時に反応開始剤としてケタール類またはジアルキル類に
属するもので、しかも半減期10時間を得るための分解
温度が80℃以上の有機過酸化物を用いると、流動性の
よい成形加工性に優れた材料が得られることを見出した
(特願昭57−112428号)。しかし、該方法によ
って得られる成形品でも耐衝撃性が必らずしも満足でき
る水準に到っていなかった。そこで本発明者等はさらに
鋭意検討を行なった結果、ポリオレフィンに不飽和カル
ボン酸をグラフトするにあたり、反応開始剤として特定
二種類以上の有機過酸化物を併用することにより、成形
加工性に優れ、しかも機械的物性。
However, problems remain regarding moldability.
Especially for thin-walled molded products or large-sized molded products, the thickness and surface roughness of thin-walled parts can be improved by adding reinforcing agents or fillers.
Furthermore, it is often difficult to mold large molded products depending on their size and shape. The present inventors conducted studies to improve this point, and found that in the process of introducing polar groups into polyolefins, that is, during the grafting of unsaturated carboxylic acids onto polyolefins, a reaction initiator belonging to ketals or dialkyl groups was used, and the reduction was reduced by half. It has been found that when an organic peroxide having a decomposition temperature of 80 DEG C. or higher to obtain a 10-hour period is used, a material with good fluidity and excellent moldability can be obtained (Japanese Patent Application No. 112428/1982). However, even the molded articles obtained by this method did not necessarily have a satisfactory impact resistance. Therefore, the present inventors conducted further intensive studies and found that when grafting an unsaturated carboxylic acid onto a polyolefin, by using two or more specific organic peroxides together as a reaction initiator, excellent molding processability can be achieved. Moreover, mechanical properties.

特に耐衝撃性の改良された組成物が得られることを見い
出し本発明に到達した。すなわち、本発明の要旨とする
ところは、ベンゾイルパーオル類またはジアルキル類に
属する有機過酸化物の存在下でポリオレフィンに不飽和
カルボン酸を反応せしめて得られる変性ポリオレフィン
または該変性ポリオレフィンと未変性ポリオレフィンま
たは他の熱可塑性樹脂との混合物に、有機繊維状強化剤
.無機繊維状強化剤または無機充填剤の少々くとも一種
を配合してなる強化ボリオレフイン系樹脂組成物にある
In particular, it has been discovered that a composition with improved impact resistance can be obtained, and the present invention has been achieved. That is, the gist of the present invention is to provide a modified polyolefin obtained by reacting a polyolefin with an unsaturated carboxylic acid in the presence of an organic peroxide belonging to benzoylperols or dialkyls, or a modified polyolefin and an unmodified polyolefin. Or organic fibrous reinforcement in a mixture with other thermoplastic resins. A reinforced polyolefin resin composition containing at least one type of inorganic fibrous reinforcing agent or inorganic filler.

本発明を実施するに際して用いられる変性ポリオレフィ
ンの変性方法については、不飽和カルボン酸とポリオレ
フィンを有機過酸化物の存在下に溶融混練する方法、溶
媒中にポリオレフィンを溶解して行なう溶液反応法など
があげられるが、前者は主としてポリオレフィンの着色
Methods for modifying the modified polyolefin used in carrying out the present invention include a method in which an unsaturated carboxylic acid and a polyolefin are melt-kneaded in the presence of an organic peroxide, and a solution reaction method in which the polyolefin is dissolved in a solvent. The former is mainly used to color polyolefins.

分子量の著しい低下を招き、後者は反応時間が長くポリ
マーの回収工程が煩雑なため作業性が悪いという欠点を
有しているが、前者の方法は特定条件で反応させる事に
よりポリオレフィンの着色1分子量の著しい低下を起こ
さずに変性することができ、とくに、押出様を用いて反
応させる方法が優れている。このように押出機中での反
応には次に示す3つの有利な点がある。
The latter method has the drawback of poor workability due to the long reaction time and complicated polymer recovery process, while the former method has the disadvantage of causing a significant decrease in the molecular weight of the polyolefin by reacting it under specific conditions. In particular, extrusion-based reaction methods are excellent because they can be modified without causing a significant decrease in their properties. The reaction in the extruder has the following three advantages.

第一に溶液反応法と違って少量の変性側および少量の過
酸化物を添加することによって、短時間に反応を進める
ことができること、第二に経済的であること、第三にグ
ラフト率が高くすることができ、従ってホモポリマーが
少くなり、物性が良く成形品の外観が良いことである。
Firstly, unlike the solution reaction method, the reaction can proceed in a short time by adding a small amount of modified side and a small amount of peroxide, secondly, it is economical, and thirdly, the grafting rate is low. Therefore, the homopolymer content is reduced, and the physical properties are good and the appearance of the molded product is good.

本発明の組成物を得る際に用いられる方法は特に制限さ
hないが、工業的実用価値の点から特定条件下押出機中
で反応させるのが望ましい。
The method used to obtain the composition of the present invention is not particularly limited, but from the viewpoint of industrial practical value, it is desirable to carry out the reaction in an extruder under specific conditions.

即ちポリオレフィンの粉末に不飽和カルボン酸と有機過
酸化物を少量の低沸点溶媒に溶解して添加し、ヘンシェ
ルミキサーなど適当な混合機によって充分混合した後、
押出機に通して反応させて得る方法である。
That is, an unsaturated carboxylic acid and an organic peroxide are dissolved in a small amount of a low-boiling solvent and added to polyolefin powder, and the mixture is sufficiently mixed using a suitable mixer such as a Henschel mixer.
This method involves passing it through an extruder and reacting it.

まで広範囲のものが適用できる。オなポリプロピレン単
独系以外に他のポリオレフィン、すなわちポリエチレン
、ポリ(4−メチル−ペンテン−1)、エチレン−酢酸
ビニル共重合樹脂(PTA)、エチレン−エチルアクリ
レート共重合樹脂(EEA)、エチレン−プロピレンゴ
ム(EPR)。
A wide range of things can be applied. In addition to the single polypropylene system, other polyolefins are used, namely polyethylene, poly(4-methyl-pentene-1), ethylene-vinyl acetate copolymer resin (PTA), ethylene-ethyl acrylate copolymer resin (EEA), ethylene-propylene. Rubber (EPR).

エチレン−プロピレン−ジエンゴム(gpoM)などを
併用することも可能である。また不飽和カルボン酸とし
てはビニル基を有するカルボン酸であれば%に限定はな
いが、具体的にはマレイン酸、フマル酸、アクリル酸、
メタクリル酸。
It is also possible to use ethylene-propylene-diene rubber (gpoM) in combination. There is no limit to the percentage of unsaturated carboxylic acids as long as they have a vinyl group, but specific examples include maleic acid, fumaric acid, acrylic acid,
methacrylic acid.

イタコン酸ならびにこれらの酸無水物などがあげられ、
特にアクリル酸、無水マレイン酸が好適である。この不
飽和カルボ/酸の配合量は、ポリオレフィン100重量
部に対して0.05〜o、all郡部適当で、0.1〜
0.6重量部が特に好ましい。次に反応触媒として用い
られる有機過酸化物はベンゾイルパーオキサイドC以下
、BPOと呼ぶ)およびパーオキシケタール類、ジアル
キルパーオキサイド類に属し、しかも半減期10時間を
得るための分解温度が80℃以上のものである。
Examples include itaconic acid and these acid anhydrides.
Particularly suitable are acrylic acid and maleic anhydride. The blending amount of this unsaturated carboxylic acid/acid is 0.05 to 0.0, per 100 parts by weight of the polyolefin, and 0.1 to
Particularly preferred is 0.6 parts by weight. Next, the organic peroxide used as a reaction catalyst belongs to benzoyl peroxide (hereinafter referred to as BPO), peroxyketals, and dialkyl peroxides, and the decomposition temperature to obtain a half-life of 10 hours is 80°C or higher. belongs to.

本発明の実施にあたっては、BPOを併用することは必
須条件となる。その理由とは、各種有機過酸化物中、B
POのみがポリオレフィンの球晶を微細化する特異的効
果を有する点にある。
In carrying out the present invention, it is an essential condition to use BPO in combination. The reason is that among various organic peroxides, B
Only PO has the specific effect of making the spherulites of polyolefin fine.

一般に結晶性ポリマーにおわては成型過程で球晶が形成
されるが球晶が大きい場合強度物性は全般的に低下する
傾向があり、とりわけ耐衝撃(9) 性に大きな影響を及ぼす。しかるにBPOは顕著にポリ
オレフィン成形品の球晶を微細化させ、もって耐衝撃性
の優れた成形品を得ることができるもので、これは本発
明者らによって見出された新規事実である。ただしBP
Oは分解温度が低いため、ポリオレフィンの低分子量化
に伴なう成形品の流動性、加工性改良には大きな効果を
発現しない。そこでこの点の改良に対して前記の分解温
度の高いケタール類またはジアルキル類に属する有機過
酸化物の併用配合が有効となる。BPOと併用する有機
過酸化物としてケタールMまたはジアルキル類の特定化
合物への限定は、BPOの持つ特異な核剤効果を阻害す
ることなくポリオレフィンの低分子量化効果を同時に最
大限発揮せしめる。
Generally, in crystalline polymers, spherulites are formed during the molding process, but if the spherulites are large, the strength and physical properties tend to decrease overall, and in particular impact resistance (9) is greatly affected. However, BPO significantly refines the spherulites of polyolefin molded products, thereby making it possible to obtain molded products with excellent impact resistance, which is a new fact discovered by the present inventors. However, B.P.
Since O has a low decomposition temperature, it does not have a large effect on improving the fluidity and processability of molded products that accompany the reduction of the molecular weight of polyolefins. Therefore, to improve this point, it is effective to combine organic peroxides belonging to the ketals or dialkyl groups, which have a high decomposition temperature. Limiting the organic peroxide used in combination with BPO to a specific compound such as ketal M or dialkyl allows the polyolefin to have a lower molecular weight effect to the maximum extent at the same time without inhibiting the unique nucleating agent effect of BPO.

本発明において併用するケタール類またはジアルキル類
に属する有機過酸化物の具体例としては1.1−ビス(
t−ブチルパーオキシ)3,3゜5−トリメチルシクロ
ヘキサン、1.1−ビス(1−ブチルパーオキシ)シク
ロヘキサン、n−プhr* チル4.4−ビス(1−ブチルパーオキシ)バレレート
、2.2−ビス(t−ブチルパーオキシ)ブタン、2.
2−ビス(1−ブチルパーオキシ)オクタン、ジ−t−
ブチルパーオキサイド、を−ブチルクミルパーオキサイ
ド、ジクミルパーオキサイド、α、α′−ビス(t−ブ
チルパーオキシインプロピル)ベンゼン、2.5−ジメ
チル−2,5−ジ(1−ブチルパーオキシ)ヘキサン。
Specific examples of organic peroxides belonging to ketals or dialkyls used in the present invention include 1,1-bis(
t-butylperoxy) 3,3゜5-trimethylcyclohexane, 1.1-bis(1-butylperoxy)cyclohexane, n-phr* thyl 4.4-bis(1-butylperoxy)valerate, 2 .2-bis(t-butylperoxy)butane, 2.
2-bis(1-butylperoxy)octane, di-t-
Butyl peroxide, -butylcumyl peroxide, dicumyl peroxide, α,α'-bis(t-butylperoxyinpropyl)benzene, 2,5-dimethyl-2,5-di(1-butylperoxy) ) hexane.

2.5−ジメチル−2,5−ジ(t−ブチルパーオキシ
)ヘキシン−3等があげられる。有機過酸化物の総記合
量はポリオレフィン100重量部に対して0.03〜3
重量部が適当で、好ましくは0.05〜1.0重量部で
ある。また反応開始剤として使用するBPOとケタール
類またはジアルキル類に属する有機過酸化物との併用重
量比は1:10〜10:1の範囲が適当で、好ましくは
1;6〜6:1の範囲である。またこれらの反応におい
ては、温度は150〜280℃1反応時間は1〜20分
とするのが好ましい。上記の設定範囲外では、ポリマー
の着色1分子量の著しい低下、あるいけ未反応不飽和カ
ルボン酸の残存等が起こるのであまり好甘しくない、尚
、反応機は特に押出機に限定するものではなく、上記の
条件を満足する溶融混線機であれば形状の如伺を問わず
使用できる。また本発明に用いられる有機捷たけ無機繊
維状強化剤としては具体的には、ガラス繊維、芳香族ポ
リアミド繊維。
Examples include 2,5-dimethyl-2,5-di(t-butylperoxy)hexyne-3. The total amount of organic peroxide is 0.03 to 3 parts by weight per 100 parts by weight of polyolefin.
The weight part is appropriate, preferably 0.05 to 1.0 weight part. In addition, the combined weight ratio of BPO and organic peroxide belonging to ketals or dialkyls used as a reaction initiator is suitably in the range of 1:10 to 10:1, preferably in the range of 1:6 to 6:1. It is. In these reactions, the temperature is preferably 150 to 280°C and the reaction time is preferably 1 to 20 minutes. Outside the above setting range, it is not very preferable because the polymer will be colored, the molecular weight will be markedly reduced, and unreacted unsaturated carboxylic acid will remain.The reactor is not particularly limited to an extruder. , any fusion crosstalk machine that satisfies the above conditions can be used regardless of its shape. Further, specific examples of the organic and inorganic fibrous reinforcing agent used in the present invention include glass fiber and aromatic polyamide fiber.

炭化ケイ素繊維、ビニロン繊維、金属繊維などが適用で
きる。これらは単独もしくけ併用の形で使用することが
できるが、その配合量は本発明の組成物の成形性の面か
ら60重重量板下が好ましく、また補強性の点からl′
i5重量係以上が好ましい。無機充填剤とこれら繊維状
強化剤を併用した場合においても、その総量が5〜60
重量係が好ましい、1 次に本発明に用いられる無機充填剤としては、ガラス箔
、タルク、マイカ、クレー、炭酸カルシウム、硫酸カル
シウム、酸化マグネシウム。
Silicon carbide fibers, vinylon fibers, metal fibers, etc. can be used. These can be used alone or in combination, but from the viewpoint of moldability of the composition of the present invention, it is preferable that the blending amount is 60% by weight, and from the viewpoint of reinforcing properties, it is preferable to use l'
i5 weight ratio or higher is preferable. Even when inorganic fillers and these fibrous reinforcing agents are used together, the total amount is 5 to 60%.
Weight ratio is preferred.1 Next, inorganic fillers used in the present invention include glass foil, talc, mica, clay, calcium carbonate, calcium sulfate, and magnesium oxide.

カーボンブラック、酸化チタン、ホワイトカーボン、三
酸化アンチモン等があげられる。これらは単独もしくは
併用の形で使用できるがその配合量は全組成物中5〜6
0重量係の範囲である。好ましくは無機充填剤と有機繊
維状強化剤または無機繊維状強化剤との総量が全樹脂組
成物中5〜60重量係である場合である。また本発明の
強化ポリオレフィン系樹脂組成物におけるマトリックス
としては、該変性ポリオレフィンに樹脂成分100重量
部中40重量部以下であれば未変性ポリオレフィンまた
はポリオレフィン以外の熱可塑性樹脂、例えばナイロン
66゜ナイロン6、PBTなどとブレンドすることがで
きる。
Examples include carbon black, titanium oxide, white carbon, and antimony trioxide. These can be used alone or in combination, but the amount added is 5 to 6 in the total composition.
It is in the range of 0 weight. Preferably, the total amount of the inorganic filler and the organic fibrous reinforcing agent or the inorganic fibrous reinforcing agent is 5 to 60% by weight in the entire resin composition. The matrix in the reinforced polyolefin resin composition of the present invention may be an unmodified polyolefin or a thermoplastic resin other than polyolefin, such as nylon 66°, nylon 6, if the modified polyolefin is 40 parts by weight or less in 100 parts by weight of the resin component. It can be blended with PBT etc.

また本発明の強化樹脂組成物には必要に応じて光または
熱に対する安定剤等の種々の添加剤を加えることができ
る。
Furthermore, various additives such as stabilizers against light or heat can be added to the reinforced resin composition of the present invention, if necessary.

以下、実施例により本発明を具体的に説明する0 実施例1〜6.比較例1〜6 極限粘度1.5(135℃、テトラリン)のポリフロピ
レン粉末100重量部に不飽和カルボン酸および有機過
酸化物として表1に示す化合物を同じく表1に示す割合
で加え、ヘンシェルミキサーでよく混合したのち、30
φ押出機(t、10 = 25 )  に供給し230
℃で7分間の滞在条件で押出を行ないペレットを得た。
Hereinafter, the present invention will be specifically explained with reference to Examples 0 Examples 1 to 6. Comparative Examples 1 to 6 To 100 parts by weight of polypropylene powder having an intrinsic viscosity of 1.5 (135°C, tetralin), the compounds shown in Table 1 as unsaturated carboxylic acids and organic peroxides were added in the proportions shown in Table 1, and the mixture was heated using a Henschel mixer. After mixing well with
φ extruder (t, 10 = 25) 230
Pellets were obtained by extrusion under conditions of residence at ℃ for 7 minutes.

この場合ペント部分より脱気して未反応の不飽和カルボ
ン酸を除去した。得られた変性ポリプロピレン混合物を
樹脂成分としてこれに少なくとも一種の有機繊維状強化
剤、無機繊維状強化剤または無機充填剤を表1VC示す
割合でタンブラ−で充分混合し、上記の押出機を用いて
220℃で押出してベレットとなし、5オンススクリユ
一インライン式射出成形機により、シリンダ一温度22
0℃、金型温度60℃の成形条件で成形品を得た。成形
品のうち1号ダンベルと125×12.5X3.2m+
および125×12.5X6.4閣の角棒の3種類を物
性測定のための試験片として用い、その評価結果を表1
に示す。表中の曲げ強度6曲げ弾性率はASTM −D
 790 、アイゾツト衝撃強度はASTM−D25/
+、  流動性(MFI”) FiA8TM−D123
8 Kよりそれぞれ測定した値である。また比較として
本発明以外の組成物を同様の方法で成形評価した結果を
併せて表2に示す。
In this case, the pento portion was degassed to remove unreacted unsaturated carboxylic acid. The obtained modified polypropylene mixture was used as a resin component, and at least one organic fibrous reinforcing agent, inorganic fibrous reinforcing agent, or inorganic filler was thoroughly mixed in a tumbler in the proportions shown in Table 1VC, and the mixture was mixed using the extruder described above. It was extruded into pellets at 220°C and molded using a 5-ounce screw in-line injection molding machine at a cylinder temperature of 22°C.
A molded article was obtained under molding conditions of 0°C and mold temperature of 60°C. Among the molded products, No. 1 dumbbell and 125 x 12.5 x 3.2 m +
and 125 x 12.5 x 6.4 square bars were used as test pieces for measuring physical properties, and the evaluation results are shown in Table 1.
Shown below. The bending strength 6 bending modulus in the table is ASTM-D
790, Izod impact strength is ASTM-D25/
+, Fluidity (MFI”) FiA8TM-D123
These are the values measured at 8K. For comparison, Table 2 also shows the results of molding evaluations of compositions other than those of the present invention using the same method.

以上水したように反応開始剤としてBPOおよびケター
ル類またはジアルキル類に属し、しかも半減期10時間
を得るための分解温度が80℃以上の有機過酸化物の併
用系を用いた本発明の組成物は、成形加工性1機械的物
性に優れた特に耐衝撃性を改良したものであることがわ
かる。
As mentioned above, the composition of the present invention uses a combined system of BPO and an organic peroxide belonging to ketals or dialkyls as a reaction initiator and having a decomposition temperature of 80°C or higher to obtain a half-life of 10 hours. It can be seen that the material has excellent moldability, excellent mechanical properties, and particularly improved impact resistance.

Claims (1)

【特許請求の範囲】 80℃以上であるケタール類またはジアルキル類に属す
る有機過酸化物の存在下でポリオレフィンに不飽和カル
ボン酸を反応せしめて得られる変性ポリオレフィンまた
は該変性ポリオレフィンと未変性ポリオレフィンまたは
他の熱可塑性樹脂との混合物に、有機繊維状強化剤、無
機繊維状強化剤または無機充填剤の少なくとも一種を配
合してなる強化ポリオレフィン系樹脂組成物。 2、 変性ポリオレフィンとしてポリオレフィン100
重量部に対して、不飽和カルボン酸0.05〜0.8重
量部および過酸化物0.03〜3重量部よりなる混合物
を押出機を用いて溶融反応せしめることにより得られた
ものを用いることを特徴とする特許請求の範囲第1項記
載の強化ポリオレフィン系樹脂組成物。 五 ケタール類またはジアルキル類に属する有機過酸化
物が1.1−ビス(t−ブチルパーオキシ)5,3.5
−)リメチルシクロヘキサン、1.1−ビス(t−ブチ
ルパーオキシ)シクロヘキサン、n−ブチル4,4−ビ
ス(1−ブチルパーオキシ)バレレート、2.2−ビス
(t−プチチルーオキシ)ブタン、2.2−ビス(1−
プチルパーオキシ)オクタン、ジルt−ブチルパーオキ
サイド、t−ブチルクミルパーオキサイド、ジクミルバ
ーオキサイド、α、α′−ヒス(t−7”チルパーオキ
シインプロピル)ベンゼン、2.5−ジメチル−2,5
−ジ(1−ブチルパーオキシ)ヘキサン、2.5−ジメ
チル−2,5−ジ(1−ブチルパーオキシ)ヘキシン−
3の中から選ばれた少なくとも一種であることを特徴と
する特許請求の範囲第1項記載の強化ポリオレフィン系
樹脂組成物。 4、 ベンゾイルパーオキサイドと10時間の半減期を
得るための分解温度が80℃以上のケタール類またはジ
アルキル類に属する有機過酸化物との重量比が1:1o
〜1o:1であ5、 有機繊維状強化剤または無機繊維
状強化剤がガラス繊維、金属繊維、炭化ケイ素繊維。 芳香族ポリアミド繊維、ビニロン繊維の中から選ばれた
少なくとも一種で、しかも全組成物に対して割合が5〜
60重量%の範囲であり、かつ有機繊維状強化材または
無機繊維状強化剤と無機充填剤の総量が5〜60重量%
であることを特徴とする特許請求の範囲第1項記載の強
化ポリオレフィン系樹脂組成物。 6、 無機充填剤がガラス箔、メルク、炭酸カルシウム
、石責、ホワイトカーボン、三酸化アンチモン、酸化マ
グネシウム、クレー、マイカ、カーボンブラックおよび
酸化チタンの中から選ばれた少なくとも一種であす、シ
かも全組成物に対する割合が5〜60重量%の範囲にあ
り、無機充填剤と有機繊維状強化材または無機繊維状強
化剤との総量が5〜60重量%であることを特徴とする
特許請求の範囲第1項記載の強化ポリオレフィン系樹脂
組成物っ
[Scope of Claims] A modified polyolefin obtained by reacting a polyolefin with an unsaturated carboxylic acid in the presence of an organic peroxide belonging to ketals or dialkyls at a temperature of 80°C or higher, or the modified polyolefin and unmodified polyolefin, or others. A reinforced polyolefin resin composition comprising a mixture with a thermoplastic resin and at least one of an organic fibrous reinforcing agent, an inorganic fibrous reinforcing agent, or an inorganic filler. 2. Polyolefin 100 as modified polyolefin
Use a mixture obtained by melting and reacting a mixture of 0.05 to 0.8 parts by weight of an unsaturated carboxylic acid and 0.03 to 3 parts by weight of a peroxide based on parts by weight using an extruder. The reinforced polyolefin resin composition according to claim 1, characterized in that: (5) The organic peroxide belonging to ketals or dialkyl is 1,1-bis(t-butylperoxy)5,3.5
-) Limethylcyclohexane, 1,1-bis(t-butylperoxy)cyclohexane, n-butyl 4,4-bis(1-butylperoxy)valerate, 2,2-bis(t-butylperoxy)butane , 2.2-bis(1-
(butylperoxy)octane, di-t-butyl peroxide, t-butylcumyl peroxide, dicumyl peroxide, α, α′-his(t-7” thylperoxyinpropyl)benzene, 2,5-dimethyl- 2,5
-di(1-butylperoxy)hexane, 2,5-dimethyl-2,5-di(1-butylperoxy)hexane-
The reinforced polyolefin resin composition according to claim 1, characterized in that the reinforced polyolefin resin composition is at least one selected from the group consisting of: 4. The weight ratio of benzoyl peroxide to an organic peroxide belonging to ketals or dialkyls with a decomposition temperature of 80°C or higher to obtain a half-life of 10 hours is 1:1.
~1o:1 and 5, the organic fibrous reinforcing agent or the inorganic fibrous reinforcing agent is glass fiber, metal fiber, or silicon carbide fiber. At least one type selected from aromatic polyamide fibers and vinylon fibers, and the proportion of the total composition is 5 to 5.
60% by weight, and the total amount of organic fibrous reinforcement or inorganic fibrous reinforcement and inorganic filler is 5 to 60% by weight.
The reinforced polyolefin resin composition according to claim 1, characterized in that: 6. The inorganic filler is at least one selected from glass foil, Merck, calcium carbonate, stone oxide, white carbon, antimony trioxide, magnesium oxide, clay, mica, carbon black, and titanium oxide. Claims characterized in that the proportion of the inorganic filler and the organic or inorganic fibrous reinforcement in the composition is in the range of 5 to 60% by weight, and the total amount of the inorganic filler and the organic or inorganic fibrous reinforcement is 5 to 60% by weight. The reinforced polyolefin resin composition described in item 1
JP19695682A 1982-11-10 1982-11-10 Reinforced polyolefin resin composition Granted JPS5986646A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19695682A JPS5986646A (en) 1982-11-10 1982-11-10 Reinforced polyolefin resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19695682A JPS5986646A (en) 1982-11-10 1982-11-10 Reinforced polyolefin resin composition

Publications (2)

Publication Number Publication Date
JPS5986646A true JPS5986646A (en) 1984-05-18
JPH0359934B2 JPH0359934B2 (en) 1991-09-12

Family

ID=16366440

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19695682A Granted JPS5986646A (en) 1982-11-10 1982-11-10 Reinforced polyolefin resin composition

Country Status (1)

Country Link
JP (1) JPS5986646A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6160745A (en) * 1984-08-31 1986-03-28 Ube Ind Ltd Bondable polyolefin composition and laminate thereof
JPS6162543A (en) * 1984-09-03 1986-03-31 Chisso Corp Polypropylene composition
JPS6198758A (en) * 1984-10-22 1986-05-17 Chisso Corp Propylene resin composition

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55131031A (en) * 1979-03-31 1980-10-11 Idemitsu Petrochem Co Ltd Polypropylene resin composition
JPS5642621A (en) * 1979-09-17 1981-04-20 Mitsuboshi:Kk Method of joining together and fastening molded product made from thermoplastic synthetic resin
JPS578829A (en) * 1980-06-20 1982-01-18 Hitachi Ltd Input and output controller
JPS5980453A (en) * 1982-10-29 1984-05-09 Mitsubishi Rayon Co Ltd Carbon-fiber-reinforced polyolefin resin composition

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55131031A (en) * 1979-03-31 1980-10-11 Idemitsu Petrochem Co Ltd Polypropylene resin composition
JPS5642621A (en) * 1979-09-17 1981-04-20 Mitsuboshi:Kk Method of joining together and fastening molded product made from thermoplastic synthetic resin
JPS578829A (en) * 1980-06-20 1982-01-18 Hitachi Ltd Input and output controller
JPS5980453A (en) * 1982-10-29 1984-05-09 Mitsubishi Rayon Co Ltd Carbon-fiber-reinforced polyolefin resin composition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6160745A (en) * 1984-08-31 1986-03-28 Ube Ind Ltd Bondable polyolefin composition and laminate thereof
JPH0112783B2 (en) * 1984-08-31 1989-03-02 Ube Industries
JPS6162543A (en) * 1984-09-03 1986-03-31 Chisso Corp Polypropylene composition
JPS6198758A (en) * 1984-10-22 1986-05-17 Chisso Corp Propylene resin composition
JPS6411218B2 (en) * 1984-10-22 1989-02-23 Chisso Corp

Also Published As

Publication number Publication date
JPH0359934B2 (en) 1991-09-12

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