JPS61152754A - Modification of polypropylene - Google Patents

Modification of polypropylene

Info

Publication number
JPS61152754A
JPS61152754A JP27507484A JP27507484A JPS61152754A JP S61152754 A JPS61152754 A JP S61152754A JP 27507484 A JP27507484 A JP 27507484A JP 27507484 A JP27507484 A JP 27507484A JP S61152754 A JPS61152754 A JP S61152754A
Authority
JP
Japan
Prior art keywords
polypropylene
organic peroxide
weight
heat
parts
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
JP27507484A
Other languages
Japanese (ja)
Other versions
JPH0559143B2 (en
Inventor
Takeshi Kobayashi
猛 小林
Fumihiro Tone
刀禰 文廣
Koji Akiyama
秋山 剛二
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP27507484A priority Critical patent/JPS61152754A/en
Publication of JPS61152754A publication Critical patent/JPS61152754A/en
Publication of JPH0559143B2 publication Critical patent/JPH0559143B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Graft Or Block Polymers (AREA)

Abstract

PURPOSE:Small amounts of an organic peroxide and a crosslinking agent area added to polypropylene so that they keep a prescribed ratio, then they are heat-treated at a specific temperature to improve melt tension and toughness without any adversely effecting shock resistance. CONSTITUTION:(A) 100pts.wt. of a polypropylene with a melt index of 0.5-30, preferably 2-20g/10min are combined with (B) 0.01-0.2, preferably 0.02-0.1pt.wt. of an organic peroxide, preferably whose decomposition temperature is 150-270 deg.C, when its half life is set to 1min, such as 1,3-bis(t- butylperoxisopropyl)benzene and (C) 0.05-1.5, preferably 0.06-1.2pt.wt. of a crossing agent, preferably a divinyl compound, maleimide or quinone dioxime so that the weight ratio of C/B becomes 3-12, preferably 4-10 and the resultant composition is heat-treated at 180-270 deg.C.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、ポリプロピレンの改質方法に関し、更に詳し
くは、ポリプロピレンを、衝撃強度の低下を伴わずに溶
融張力が飛躍的に向上すると共に剛性も向上したポリプ
ロピレンに改質する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for modifying polypropylene, and more particularly, the present invention relates to a method for modifying polypropylene, and more specifically, it improves polypropylene by dramatically improving melt tension and increasing rigidity without reducing impact strength. The present invention relates to a method for modifying polypropylene to improved polypropylene.

〔舛明の技術的背景とその問題点〕[Technical background of Masumei and its problems]

ポリオレフィンのうちで、ポリプロピレンは他の重合体
に比較して透明性、剛性2表面光沢、耐熱性の点におい
て優れている。
Among polyolefins, polypropylene is superior to other polymers in terms of transparency, rigidity, surface gloss, and heat resistance.

しかしながら、このようなポリプロピレンは、溶融張力
が小さいため、中空成形法に適用した場合その成形性が
低下する。
However, since such polypropylene has a low melt tension, its moldability decreases when it is applied to a blow molding method.

ポリプロピレンの溶融張力を向上させる方法としてポリ
プロピレンに高圧法で得た低密度ポリエチレンを配合す
る方法などが知られているが、これらの方法を適用した
場合、溶融張力を向上させようとすると透明性、剛性な
どの他の物性が悪くなるという問題を生じる。したがっ
て、このような問題に対処するため、例えば剛性の向上
を目的として、アルミ、マイカ、メルク等の無機充填剤
を添加することが知られているが、この方法によると成
形後衝撃強度が低下したシ、比重が増加するという問題
が発生する。さらに、有機過酸化物と架橋助剤を多量に
配合して、三次元的構造にして耐熱性を向上させること
も知られているが、溶融張力、衝撃強度、剛性が共にバ
ランスよく満足するものとはならず、これらのバランス
のとれた改質方法は未だ開発されていない。
A known method for improving the melt tension of polypropylene is to blend polypropylene with low-density polyethylene obtained by a high-pressure method, but when these methods are applied, trying to improve the melt tension results in problems with transparency, A problem arises in that other physical properties such as rigidity deteriorate. Therefore, in order to deal with such problems, it is known to add inorganic fillers such as aluminum, mica, Merck, etc. for the purpose of improving rigidity, but this method reduces the impact strength after molding. However, a problem arises in that the specific gravity increases. Furthermore, it is known that a large amount of organic peroxide and cross-linking aid are blended to form a three-dimensional structure to improve heat resistance; However, a well-balanced modification method has not yet been developed.

〔発明の目的〕[Purpose of the invention]

本発明は、上記した問題点を解消し、ポリプロピレンを
、衝撃強度の低下を伴わずに溶融張力が飛躍的に向上す
ると共に剛性も向上したポリプロピレンに改質する方法
の提供を目的とする。
The present invention aims to solve the above-mentioned problems and provide a method for modifying polypropylene into polypropylene that has dramatically improved melt tension and improved rigidity without reducing impact strength.

〔発明の概要〕[Summary of the invention]

本発明者らは、上記した目的を達成すべく鋭意研究を重
ねた結果、後述するポリプロピレンに後述する極めて少
量の有機過酸化物と架橋助剤とを両者が所定の配合比と
なるように配合して後述する温度で熱処理することによ
シ、該ポリプロピレンが衝撃強度の低下を伴わずに溶融
張力が飛躍的に向上し剛性も向上したものに改質される
という事実を見出し本発明を完成するに到った。
As a result of intensive research to achieve the above-mentioned objective, the present inventors have found that polypropylene, which will be described later, is blended with a very small amount of an organic peroxide and a crosslinking aid, which will be described later, in a predetermined mixing ratio. The present invention was completed by discovering the fact that by heat-treating the polypropylene at the temperature described below, the polypropylene can be modified into a material with dramatically improved melt tension and improved rigidity without a decrease in impact strength. I came to the conclusion.

すなわち、本発明のポリプロピレンの改質方法は、メル
トインデックスが0.5〜30 t710分のポリプロ
ピレン100重量部に対し、有機過酸化物囚0.01〜
0.2重量部及び架橋助剤(B) 0.05〜1.5重
量部を、該有機過酸化物(A)と該架橋助剤(B)との
配合比中)/(ト)が重量比で3〜12となるように配
合し、180〜270℃で熱処理することを特徴とする
That is, in the method for modifying polypropylene of the present invention, 0.01 to 0.01 to 0.01 to 100 parts by weight of polypropylene having a melt index of 0.5 to 30 t and 710 minutes of polypropylene is added.
0.2 parts by weight and 0.05 to 1.5 parts by weight of the crosslinking aid (B) in the blending ratio of the organic peroxide (A) and the crosslinking aid (B). It is characterized in that it is blended in a weight ratio of 3 to 12 and heat treated at 180 to 270°C.

まず、本発明におけるポリプロピレンは、メルトインデ
ックスが0.5〜30 f/10分好ましくは2.0〜
20 f/10分のポリプロピレンである。ポリプロピ
レンの種類は、格別限定されるものではなく、ホモポリ
マーまたはエチレン含有率20%までのプロピレン−エ
チレン共重合体などがあげられる。
First, the polypropylene in the present invention has a melt index of 0.5 to 30 f/10 minutes, preferably 2.0 to 30 f/10 minutes.
20 f/10 min polypropylene. The type of polypropylene is not particularly limited, and examples include homopolymers and propylene-ethylene copolymers with an ethylene content of up to 20%.

メルトインデックスが上記した範囲を外れて0.5f/
10分未満の場合改質時のポリプロピレンの流動性が低
下し、302/10分を超えると架橋が充分に行われず
、溶融張力の向上が不充分である。
The melt index is outside the above range and is 0.5f/
If it is less than 10 minutes, the fluidity of the polypropylene during modification will decrease, and if it exceeds 302/10 minutes, crosslinking will not be sufficiently performed and the improvement in melt tension will be insufficient.

次に有機過酸化物に)としては、半減期を1分にする分
解温度が150〜270℃の範囲にあるようなものが好
ましく、具体的には、ベンゾイルパーオキシド、ジクロ
ルベンゾイルパーオキシド。
Next, as for organic peroxides, those having a decomposition temperature in the range of 150 to 270° C. to give a half-life of 1 minute are preferable, and specifically, benzoyl peroxide and dichlorobenzoyl peroxide.

ジクミルパーオキシド、ジ−t−ブチルパーオキシド、
2.5−ジメチル−2,5−ジ(パーオキシドベンゾエ
ート)ヘキシン−3,1,3−ビス(t−ブチルパーオ
キシイソプロビル)ベンゼン、ラウロイルパーオキシド
、製−ブチルパーアセテート。
dicumyl peroxide, di-t-butyl peroxide,
2.5-Dimethyl-2,5-di(peroxide benzoate)hexyne-3,1,3-bis(t-butylperoxyisopropyl)benzene, lauroyl peroxide, -butyl peracetate.

2.5−ジメチル−λ5−ジ(魯−ブチルパーオキシ)
ヘキシン−3,2,5−ジメチル−2,5−ジ(i−ブ
チルパーオキシ)ヘキサン、t−ブチルパーベンゾエー
ト、t−ブチルパーフェニルアセテート。
2.5-dimethyl-λ5-di(butylperoxy)
Hexyne-3,2,5-dimethyl-2,5-di(i-butylperoxy)hexane, t-butyl perbenzoate, t-butyl perphenylacetate.

t−ブチルバーインブチレート、t−ブチルパー膳ea
−オクテート、t−ブチルパービバレート。
t-butyl burnin butyrate, t-butyl parzen ea
-Octate, t-butyl pervivalate.

/ ミA/パーピバレート、t−プチルパージエテール
アセテートなどをあげることができる。これらのうち、
1.3−ビス(t−ブチルパーオキシイソプロビル)ベ
ンゼン、ジクミルパーオキシド、ジ−t−ブチルパーオ
キシド、λ5−ジメチルー2.5−ジ(−一プデルパー
オキシ)ヘキシン−3,2,5−ジメチル−λ5−ジ(
i−ブチルパーオキシ)ヘキサンなどく好ましいもので
ある。
/ MiA/perpivalate, t-butyl perdiethyl acetate, and the like. Of these,
1.3-bis(t-butylperoxyisopropyl)benzene, dicumyl peroxide, di-t-butyl peroxide, λ5-dimethyl-2.5-di(-1-pudelperoxy)hexyne-3,2,5- Dimethyl-λ5-di(
Preferred examples include i-butylperoxy)hexane.

これら有機過酸化物(8)は、前記したポリプロピレン
100重量部に対して0.01−0.2重量部好ましく
は0.02〜0.1重量部配合されると同時に後述する
架橋助剤中)との配合比CB)/(A)を満たすことが
必要である。この配合量が0.01重量部未満の場合は
、反応性が劣シ優れた物性は得られず、また0、 2重
量部を超えると反応性が高くなシすぎて流動性は劣って
くる。
These organic peroxides (8) are added in an amount of 0.01 to 0.2 parts by weight, preferably 0.02 to 0.1 parts by weight, per 100 parts by weight of the polypropylene mentioned above, and at the same time are added to the crosslinking aid described below. ) is required to satisfy the blending ratio CB)/(A). If the amount is less than 0.01 parts by weight, the reactivity will be poor and excellent physical properties will not be obtained, and if it exceeds 0.2 parts by weight, the reactivity will be too high and the fluidity will be poor. .

架橋助剤中)としては、例えば、イオウ;ジビニルベン
ゼンのようなジビニル化合物;ジアリルフタレートのよ
うなジアリル化合物;p−ギノンジオキシム+  PN
P’−ジベンゾイルキノンジオキシムのようなオキシム
化合物;フェニルマレイミドのようなマレイミド化合物
;の外に、トリアリルシアヌレート、トリアリルイソシ
アヌレート、エチレングリコールメタクリレート、ポリ
エチレングリコールメタクリレート、1,3.5−)リ
アクリロイルへキサヒドロ−5−)リアジン、液状の1
.2−ポリブタジェンなどの主鎖又は側鎖に二重結合ヲ
有スるオリゴマー、シンジオタクチック−1,2−ポリ
ブタジェンなどの主鎖又は側鎖に二重結合を有するポリ
マーをあげることができる。これらのうち、好ましくは
、ジビニル化合物、?レイミド化合物、キノンジオキシ
ム化合物である。
(in the crosslinking aid), for example, sulfur; divinyl compounds such as divinylbenzene; diallyl compounds such as diallyl phthalate; p-ginone dioxime + PN
Oxime compounds such as P'-dibenzoylquinone dioxime; maleimide compounds such as phenylmaleimide; as well as triallyl cyanurate, triallylisocyanurate, ethylene glycol methacrylate, polyethylene glycol methacrylate, 1,3.5- ) lyacryloylhexahydro-5-) riazine, liquid 1
.. Examples include oligomers having double bonds in the main chain or side chains such as 2-polybutadiene, and polymers having double bonds in the main chain or side chains such as syndiotactic-1,2-polybutadiene. Among these, divinyl compounds, ? They are leimide compounds and quinone dioxime compounds.

これら架橋助剤(B)は、前記したポリプロピレン10
0重量部に対して0.05〜1.5重量部好ましくは0
.06〜1.2重量部配合されると同時に前述した有機
過酸化物(A)との後述する配合比(]1/(6)を満
たすことが必要である。この配合量が0.05重量部未
満の場合は分解反応が優先して物性が劣化し、1.5重
量部を超えると物性の更なる向上は認められないので無
意味である。
These crosslinking aids (B) are the polypropylene 10 described above.
0.05 to 1.5 parts by weight, preferably 0 parts by weight
.. 06 to 1.2 parts by weight, and at the same time, it is necessary to satisfy the later-described blending ratio (]1/(6) with the organic peroxide (A) mentioned above.This blending amount is 0.05 parts by weight. If the amount is less than 1 part by weight, the decomposition reaction will take priority and the physical properties will deteriorate, and if it exceeds 1.5 parts by weight, no further improvement in the physical properties will be observed, so it is meaningless.

有機過酸化物(6)と架橋助剤(B)との配合比は、(
6)/(A)が重量比で3〜12好ましくは4〜10と
なるように設定する。この値が、3未満の場合には分解
反応が優先して物性が劣化し、12を超えると物性の更
なる向上は認められないので無意味である。
The blending ratio of the organic peroxide (6) and the crosslinking aid (B) is (
6)/(A) is set at a weight ratio of 3 to 12, preferably 4 to 10. If this value is less than 3, the decomposition reaction takes precedence and the physical properties deteriorate; if it exceeds 12, no further improvement in the physical properties is observed, which is meaningless.

本発明のポリプロピレンの改質は、例えば次のようKし
て行われる。まず、上記したポリプロピレンと有機過酸
化物と架橋助剤とを1所定量混合例えばトライブレンド
したのち、単軸押出機や二軸混練機などを用いて後述す
る温度で熱処理を行い混合物を溶融混練してベレットを
得る。
The modification of polypropylene of the present invention is carried out, for example, as follows. First, a predetermined amount of the above-mentioned polypropylene, organic peroxide, and crosslinking aid are mixed, for example, tri-blended, and then heat-treated at the temperature described below using a single-screw extruder or twin-screw kneader, and the mixture is melt-kneaded. and get a beret.

熱処理の温度は180〜270℃好ましくは190〜2
50℃である。熱処理温度が、180℃未満の場合は有
機過酸化物が完全に分解せず、270℃を超えると分解
反応が優先してしまい物性の劣化が起る。
The temperature of heat treatment is 180-270℃, preferably 190-2
The temperature is 50°C. If the heat treatment temperature is less than 180°C, the organic peroxide will not be completely decomposed, and if it exceeds 270°C, the decomposition reaction will take priority and the physical properties will deteriorate.

〔発明の実施例〕[Embodiments of the invention]

実施例1〜8.比較例1〜4 ポリプロピレンとして表IK示すポリプロピレン1〜5
を用意した。なお、これらポリプロピレンのメルトイン
デックス(MI))及び諸物性(曲げ強さ1曲げ弾性率
、溶融張力、アイゾツト衝撃強度)を下記の仕様で測定
して表1に併記した。
Examples 1-8. Comparative Examples 1 to 4 Polypropylenes 1 to 5 shown in Table IK as polypropylenes
prepared. The melt index (MI) and various physical properties (flexural strength 1 flexural modulus, melt tension, Izod impact strength) of these polypropylenes were measured according to the following specifications and are also listed in Table 1.

メルトインデックス: JISK7210 に準拠。Melt index: Compliant with JISK7210.

曲げ強度: JIS  K7203に準拠。Bending strength: Based on JIS K7203.

曲げ弾性率: JIS  K7203に準拠。Flexural modulus: Based on JIS K7203.

溶融張カニ東洋精機社製のメルトテンションテスターを
用いて、口径2.09m、長 さ8−のオリフィスから230℃に 加熱された溶融樹脂を20m/分の速 度で押出し、該押出物を張力検出用 プーリーに移送させ、20r、p9m、で回転する該プ
ーリーが該押出物を巻 取るときの張力の値である。
Using a melt tension tester manufactured by Toyo Seiki Co., Ltd., molten resin heated to 230°C was extruded from an orifice with a diameter of 2.09 m and a length of 8 mm at a speed of 20 m/min, and the extrudate was subjected to tension detection. This is the value of the tension when the extrudate is transferred to a commercial pulley and rotated at 20 r, p9 m, and the pulley winds up the extrudate.

アイゾツト衝撃強度: JIS  K7110に準拠。Izotsu impact strength: Compliant with JIS K7110.

試験片にノツチを設けた。A notch was provided in the test piece.

表1 有機過酸化物(8)としては%a:L3’−ビス(を−
7’チルパーオキシイソプロピル)ベンゼンとbニジク
ミルパーオキサイドを用意した。
Table 1 Organic peroxide (8) %a:L3'-bis(-
7' (peroxyisopropyl)benzene and (b) dicumyl peroxide were prepared.

架橋助剤(6)としては、aニジビニルベンゼンとb=
パラキノンジオキシムを用意した。
As the crosslinking aid (6), a-nidivinylbenzene and b=
Paraquinone dioxime was prepared.

上記した各ポリプロピレン100重量部に対して、有機
過酸化物(A)と架橋助剤(B)とを表2に示す配合量
で配合してトライブレンドしたのち、単軸押出機を用い
て表2に示し良熱処理温度で溶融混線を行いペレット化
した。
100 parts by weight of each of the polypropylenes described above was triblended with the organic peroxide (A) and crosslinking aid (B) in the amounts shown in Table 2, and then subjected to a tri-blend using a single-screw extruder. The mixture was melted and mixed at a good heat treatment temperature as shown in step 2, and then pelletized.

ベレットのメルトインデックス(MIりを測定したのち
、射出成形機を用いて各種試験片を作製し、上記した仕
様で曲げ強度2曲げ弾性率、溶融張九アイゾツト衝撃強
度を測定した。これらの値と改質する前のポリプロピレ
ンの値との比を°とり、この測定値比を表2に記載した
After measuring the melt index (MI) of the pellet, various test specimens were prepared using an injection molding machine, and the bending strength (2) flexural modulus and melt tensile (9) isot impact strength were measured according to the specifications described above. The ratio with the value of polypropylene before modification was calculated, and the measured value ratio is listed in Table 2.

〔発明の効果〕〔Effect of the invention〕

以上の説明で明らかなように、本発明方法によれば、ポ
リプロピレンを、衝撃強度の低下を伴わずに溶融張力が
飛躍的に向上すると共に剛性も向上したポリプロピレン
に改質することができる。
As is clear from the above description, according to the method of the present invention, polypropylene can be modified into polypropylene that has dramatically improved melt tension and improved rigidity without reducing impact strength.

したがって、メルトインデックスが大きくても中空成形
が可能となシ、自動車用材料1弱電関係の材料などの中
空成形品の製造に適用して有効である。
Therefore, even if the melt index is large, blow molding is possible, and it is effective when applied to the production of hollow molded products such as automobile materials 1 and materials related to low electric current.

Claims (1)

【特許請求の範囲】[Claims] メルトインデックスが0.5〜30g/10分のポリプ
ロピレン100重量部に対し、有機過酸化物(A)0.
01〜0.2重量部及び架橋助剤(B)0.05〜1.
5重量部を、該有機過酸化物(A)と該架橋助剤(B)
との配合比(B)/(A)が重量比で3〜12となるよ
うに配合し、180〜270℃で熱処理することを特徴
とするポリプロピレンの改質方法。
Organic peroxide (A) 0.0.
01 to 0.2 parts by weight and crosslinking aid (B) 0.05 to 1.
5 parts by weight of the organic peroxide (A) and the crosslinking aid (B)
A method for modifying polypropylene, which comprises blending the polypropylene so that the blending ratio (B)/(A) is 3 to 12 by weight, and heat-treating at 180 to 270°C.
JP27507484A 1984-12-26 1984-12-26 Modification of polypropylene Granted JPS61152754A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27507484A JPS61152754A (en) 1984-12-26 1984-12-26 Modification of polypropylene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27507484A JPS61152754A (en) 1984-12-26 1984-12-26 Modification of polypropylene

Publications (2)

Publication Number Publication Date
JPS61152754A true JPS61152754A (en) 1986-07-11
JPH0559143B2 JPH0559143B2 (en) 1993-08-30

Family

ID=17550465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27507484A Granted JPS61152754A (en) 1984-12-26 1984-12-26 Modification of polypropylene

Country Status (1)

Country Link
JP (1) JPS61152754A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6153710A (en) * 1997-02-18 2000-11-28 Chisso Corporation Preactivated catalyst for olefin (CO)polymer, catalyst for olefin (CO)polymerization, olefin (CO)polymer composition, and process for producing the same
US6231804B1 (en) 1997-04-02 2001-05-15 Chisso Corporation Modified olefin (co)polymer composition, process for preparing the same, and modified olefin (co)polymer composition molding
US6235845B1 (en) 1997-08-07 2001-05-22 Chisso Corporation Olefin (co)polymer composition
US6303696B1 (en) 1997-04-11 2001-10-16 Chisso Corporation Propylene (co)polymer composition using metallocene catalyst
US6313225B2 (en) 1995-10-18 2001-11-06 Chisso Corporation Catalyst for olefin (co-)polymerization and method for producing the same
JP2001524565A (en) * 1997-11-21 2001-12-04 アクゾ ノーベル ナムローゼ フェンノートシャップ Extrusion method for enhancing the melt strength of polypropylene
US6437048B1 (en) 1995-12-01 2002-08-20 Chisso Corporation Molded resin articles
US6444736B1 (en) 1998-04-24 2002-09-03 Chisso Corporation Flame retardant polyolefin composition
US6515037B2 (en) 2000-02-29 2003-02-04 Chisso Corporation Polypropylene base resin composition for foam-molding, foamed article using the same composition, production process for the same foamed article and foam-molded product using the foamed-article
US6710130B2 (en) 2001-03-30 2004-03-23 Chisso Corporation Propylene polymer composition and its foam moldings
US6780914B2 (en) 1999-12-30 2004-08-24 Samsung General Chemicals Co., Ltd. Flame retardant polypropylene resin composition
US7470727B2 (en) 2001-05-30 2008-12-30 Basell Poliolefine Italia S.P.A. Polypropylene resin composition
WO2010024286A1 (en) 2008-09-01 2010-03-04 三井化学株式会社 Ionomer resin, resin compositions containing same and uses of both
WO2011046103A1 (en) 2009-10-13 2011-04-21 株式会社カネカ Polypropylene resin, polypropylene resin composition, and foam-injection-molded article
CN104448536A (en) * 2013-09-18 2015-03-25 中国石油天然气股份有限公司 Polypropylene composition toughened by high-rigidity TPV and preparation method thereof

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JPS59223740A (en) * 1983-06-02 1984-12-15 Mitsui Petrochem Ind Ltd Production of polypropylene composition

Patent Citations (1)

* Cited by examiner, † Cited by third party
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JPS59223740A (en) * 1983-06-02 1984-12-15 Mitsui Petrochem Ind Ltd Production of polypropylene composition

Cited By (16)

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US6313225B2 (en) 1995-10-18 2001-11-06 Chisso Corporation Catalyst for olefin (co-)polymerization and method for producing the same
US6437048B1 (en) 1995-12-01 2002-08-20 Chisso Corporation Molded resin articles
US6153710A (en) * 1997-02-18 2000-11-28 Chisso Corporation Preactivated catalyst for olefin (CO)polymer, catalyst for olefin (CO)polymerization, olefin (CO)polymer composition, and process for producing the same
US6231804B1 (en) 1997-04-02 2001-05-15 Chisso Corporation Modified olefin (co)polymer composition, process for preparing the same, and modified olefin (co)polymer composition molding
US6303696B1 (en) 1997-04-11 2001-10-16 Chisso Corporation Propylene (co)polymer composition using metallocene catalyst
US6235845B1 (en) 1997-08-07 2001-05-22 Chisso Corporation Olefin (co)polymer composition
JP2001524565A (en) * 1997-11-21 2001-12-04 アクゾ ノーベル ナムローゼ フェンノートシャップ Extrusion method for enhancing the melt strength of polypropylene
US6444736B1 (en) 1998-04-24 2002-09-03 Chisso Corporation Flame retardant polyolefin composition
US6780914B2 (en) 1999-12-30 2004-08-24 Samsung General Chemicals Co., Ltd. Flame retardant polypropylene resin composition
US6515037B2 (en) 2000-02-29 2003-02-04 Chisso Corporation Polypropylene base resin composition for foam-molding, foamed article using the same composition, production process for the same foamed article and foam-molded product using the foamed-article
US6710130B2 (en) 2001-03-30 2004-03-23 Chisso Corporation Propylene polymer composition and its foam moldings
US7470727B2 (en) 2001-05-30 2008-12-30 Basell Poliolefine Italia S.P.A. Polypropylene resin composition
WO2010024286A1 (en) 2008-09-01 2010-03-04 三井化学株式会社 Ionomer resin, resin compositions containing same and uses of both
WO2011046103A1 (en) 2009-10-13 2011-04-21 株式会社カネカ Polypropylene resin, polypropylene resin composition, and foam-injection-molded article
US8552116B2 (en) 2009-10-13 2013-10-08 Kaneka Corporation Polypropylene resin, polypropylene resin composition, and foam-injection-molded article
CN104448536A (en) * 2013-09-18 2015-03-25 中国石油天然气股份有限公司 Polypropylene composition toughened by high-rigidity TPV and preparation method thereof

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