JPH01263138A - Polypropylene resin composition - Google Patents

Polypropylene resin composition

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Publication number
JPH01263138A
JPH01263138A JP9016988A JP9016988A JPH01263138A JP H01263138 A JPH01263138 A JP H01263138A JP 9016988 A JP9016988 A JP 9016988A JP 9016988 A JP9016988 A JP 9016988A JP H01263138 A JPH01263138 A JP H01263138A
Authority
JP
Japan
Prior art keywords
propylene
resin composition
copolymer
polypropylene resin
crystalline
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
JP9016988A
Other languages
Japanese (ja)
Other versions
JP2823861B2 (en
Inventor
Tadashi Asanuma
正 浅沼
Yoshiko Tokura
十倉 由子
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP9016988A priority Critical patent/JP2823861B2/en
Publication of JPH01263138A publication Critical patent/JPH01263138A/en
Application granted granted Critical
Publication of JP2823861B2 publication Critical patent/JP2823861B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain a crystalline polypropylene resin composition, containing a reaction product of a specific crystalline propylene copolymer with cyclohexyl alcohol (derivative) and capable of providing molded products excellent in physical properties. CONSTITUTION:A polypropylene resin composition containing (A) a reaction product prepared by reacting a crystalline polypropylene copolymer obtained by polymerizing an alkenylsilane (e.g., vinylsilane) with propylene in the presence of a stereoregular catalyst (preferably a catalyst system consisting of a titanium halide and an organometallic compound) with cyclohexyl alcohol (derivative) in an equimolar amount or more based on Si units in the above-mentioned copolymer preferably in the presence of an alkaline (earth) metal (oxide) and (B) crystalline polypropylene (random or block copolymer, etc., of propylene with other olefins).

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は特定の化合物を含有してなる結晶性ポリプロピ
レン樹脂組成物に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a crystalline polypropylene resin composition containing a specific compound.

〔従来の技術〕[Conventional technology]

ポリプロピレンは剛性に優れた重合体であるが、比較的
成形物の結晶化度が低く本来期待される物性に比べ通常
の成形物の物性は劣るという問題がある。これに対して
は、通常種々の核剤を添加する方法が行われており、剛
性に優れた成形体、或いは透明性に優れた成形体が得ら
れている。
Although polypropylene is a polymer with excellent rigidity, there is a problem in that the degree of crystallinity of molded products is relatively low, and the physical properties of ordinary molded products are inferior to the originally expected physical properties. To solve this problem, a method of adding various nucleating agents is usually used, and a molded product with excellent rigidity or transparency is obtained.

〔発明が解決すべき問題点〕[Problems to be solved by the invention]

核剤を添加する方法は簡便でしかも効果的であるが、比
較的多量の核を添加する必要がありそのため、核剤の分
散不良による成形物の物性のばらつきとか、添加した核
剤がブリードする問題があった。これに対しては、特定
の高分子化合物を添加することが知られているが更に効
果的な化合物が望まれる。
The method of adding a nucleating agent is simple and effective, but it requires the addition of a relatively large amount of nucleating agents, which may cause variations in the physical properties of the molded product due to poor dispersion of the nucleating agent, or bleeding of the added nucleating agent. There was a problem. For this purpose, it is known to add a specific polymer compound, but a more effective compound is desired.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らはより効果的な化合物について鋭意探索し本
発明に到達した。
The present inventors have diligently searched for more effective compounds and have arrived at the present invention.

即ち、本発明は、アルケニルシランとプロピレンを立体
規則性触媒を用いて得た結晶性プロピレン共重合体とシ
クロヘキシルアルコールまたはその誘導体との反応物を
含有してなる結晶性ポリプロピレン樹脂組成物である。
That is, the present invention is a crystalline polypropylene resin composition containing a reaction product of a crystalline propylene copolymer obtained from alkenylsilane and propylene using a stereoregular catalyst and cyclohexyl alcohol or a derivative thereof.

本発明においてアルケニルシランとプロピレンを立体規
則性触媒を用いて得た結晶性プロピレン共重合体の製造
方法としては例誕ば米国特許3223686号に開示さ
れておりその方法がそのまま使用できるが、アルケニル
シランとしては少なくとも1つの5i−H結合を有する
ものが用いられ、ビニルシラン、アリルシラン、ブテニ
ルシラン、ペンテニルシランの他に該モノマーの5i−
1(結合の1〜2個がアルキル基で置換された物も例示
できる。立体規則性触媒としてはその後多くの性能の改
良された触媒が開示されておりそれらを使用することが
でき、また重合法としても不活性溶媒を使用する溶媒法
の他に塊状重合法、気相重合法も採用できる。ここで立
体規則性触媒としては遷移金属触媒と有機金属化合物か
らなる触媒系が好ましく例示でき、遷移金属触媒として
はハロゲン化チタンが好ましく用いられ、例えば四塩化
チタンを金属アルミニウム、水素或いは有機アルミニウ
ムで還元して得た三塩化チタン又はそれらを電子供与性
化合物で変性処理したものと有機アルミニウム化合物さ
らに必要に応じ含酸素有機化合物などの立体規則性向上
剤からなる触媒系、或いはハロゲン化マグネシウム等の
担体或いはそれらを電子供与性化合物で処理したものに
ハロゲン化チタンを担持してえた遷移金属触媒と有機ア
ルミニウム化合物、必要に応じ含酸素有機化合物などの
立体規則性向上剤からなる触媒系が例示される。(例え
ば以下の文献に種々の例が記載されている。Ziegl
er−Natta Catalysts and Po
lymerization by JohnBoor 
Jr<Academrc Press>+Journa
I of Macromorecular Sienc
e−Reviews in Macromolecul
ar Chemistry and Physics 
C24,(3)355−385(1984)、同C2こ
こで立体規則性向上剤、或いは電子供与性化合物として
は通常エーテル、エステル、オルソエステル、アルコキ
シ硅素化合物などの含酸素化合物が好ましく例示でき、
電子供与性化合物としてはさらにアルコール、アルデヒ
ド、水なども使用可能である。
In the present invention, as a method for producing a crystalline propylene copolymer obtained by using alkenylsilane and propylene using a stereoregular catalyst, for example, the method disclosed in U.S. Pat. No. 3,223,686 can be used as is. As the monomer, those having at least one 5i-H bond are used, and in addition to vinylsilane, allylsilane, butenylsilane, and pentenylsilane, the 5i-
1 (one or two of the bonds are substituted with an alkyl group can also be exemplified.As stereoregular catalysts, many catalysts with improved performance have since been disclosed, and these can be used. Even if it is legal, in addition to the solvent method using an inert solvent, bulk polymerization method and gas phase polymerization method can also be adopted.Here, as the stereoregular catalyst, a catalyst system consisting of a transition metal catalyst and an organometallic compound can be preferably exemplified. As the transition metal catalyst, titanium halides are preferably used, such as titanium trichloride obtained by reducing titanium tetrachloride with metallic aluminum, hydrogen, or organoaluminum, or titanium trichloride obtained by modifying these with an electron-donating compound, and organoaluminum compounds. Furthermore, if necessary, a catalyst system consisting of a stereoregularity improver such as an oxygen-containing organic compound, or a transition metal catalyst obtained by supporting titanium halide on a carrier such as magnesium halide, or a carrier treated with an electron-donating compound. An example is a catalyst system consisting of a stereoregularity improver such as an organoaluminum compound and, if necessary, an oxygen-containing organic compound. (For example, various examples are described in the following literature.
er-Natta Catalysts and Po
lymerization by JohnBoor
Jr<Academrc Press>+Journa
I of Macromorecular Science
e-Reviews in Macromolecules
ar Chemistry and Physics
C24, (3) 355-385 (1984), C2, where the stereoregularity improver or electron-donating compound is usually preferably exemplified by oxygen-containing compounds such as ethers, esters, orthoesters, and alkoxy silicon compounds;
Further, alcohols, aldehydes, water, etc. can also be used as electron-donating compounds.

有機アルミニウム化合物としては、トリアルキルアルミ
ニウム、ジアルキルアルミニウムハライド、アルキルア
ルミニウムセスキハライド、アルキルアルミニウムシバ
ライドが使用でき、アルキル基としてはメチル基、エチ
ル基、プロピル基、ブチル基、ヘキシル基などが例示さ
れ、ハライドとしては塩素、臭素、沃素が例示される。
As the organoaluminum compound, trialkylaluminum, dialkylaluminum halide, alkylaluminum sesquihalide, alkyl aluminum civalide can be used, and examples of the alkyl group include methyl group, ethyl group, propyl group, butyl group, hexyl group, etc. Examples of halides include chlorine, bromine, and iodine.

ここでアルケニルシランとプロピレンの重合割合として
は、得られる重合体が結晶性を保っているかぎり特に制
限は無いが通常アルケニルシランが30モルχ〜0.0
1モルχとするのが重合時の触媒活性、或いは、混合さ
れる結晶性ポリプロピレンとの混合のため及び物性の改
良効果が充分であるために好ましい。重合体の分子量と
しては特に制限はないが極めて高い分子量、例えば13
5°Cテトラリン溶液で測定した極限粘度として10以
上にならないようすべきである。
Here, the polymerization ratio of alkenylsilane and propylene is not particularly limited as long as the resulting polymer maintains crystallinity, but usually alkenylsilane is 30 mol χ to 0.0 mol.
It is preferable to set the amount to 1 mol χ for the catalytic activity during polymerization, for mixing with the crystalline polypropylene to be mixed, and for the effect of improving physical properties to be sufficient. There is no particular limit to the molecular weight of the polymer, but extremely high molecular weights, such as 13
The intrinsic viscosity measured with a 5°C tetralin solution should not exceed 10.

本発明においては、上記プロピレンとアルケニルシラン
の共重合体は、ついでシクロヘキシルアルコールあるい
はその誘導体、具体的にはシクロヘキシル基の1〜それ
以上の水素が、アルキル基、ハロゲンアルコキシ基など
で置換されたものと反応する。ここでシクロヘキシルア
ルコールあるいは、その誘導体の使用量はプロピレンと
アルケニルシランの共重合体中のSi単位に対し等モル
以上であるのが一般的であり、反応に際し、アルカリ金
属、アルカリ土類金属あるいはその水酸化物を存在せし
めると効果的であり、反応温度は室温で充分であるが、
加熱しても良い。また場合によっては、混合して用いる
後述のポリプロピレンと混合した後にシクロヘキシルア
ルコールと反応しても良い。
In the present invention, the copolymer of propylene and alkenylsilane is cyclohexyl alcohol or a derivative thereof, specifically, one in which one or more hydrogen atoms of the cyclohexyl group are substituted with an alkyl group, a halogen alkoxy group, etc. reacts. Here, the amount of cyclohexyl alcohol or its derivative used is generally at least equimolar to the Si unit in the copolymer of propylene and alkenylsilane. The presence of hydroxide is effective, and room temperature is sufficient for the reaction temperature, but
May be heated. In some cases, the mixture may be mixed with polypropylene, which will be described later, and then reacted with cyclohexyl alcohol.

本発明において上記アルケニルシランとプロピレンを立
体規則性触媒を用いて得た結晶性プロピレン共重合体と
シクロヘキシルアルコールとの反応物と混合される結晶
性ポリプロピレンとしては特に制限は無く必要に応じ種
々の分子量の重合体、あるいはエチレン、ブテン、ヘキ
セン等の他のオレフィンとのランダム或いはブロック共
重合体が利用できる。本発明の目的はこのアルケニルシ
ランとプロピレンを立体規則性触媒を用いて得た結晶性
プロピレン共重合体と混合される結晶性ポリプロピレン
の物性向上にあり、その組成は間はない。
In the present invention, the crystalline polypropylene to be mixed with the reaction product of the crystalline propylene copolymer obtained by using the above-mentioned alkenylsilane and propylene using a stereoregular catalyst and cyclohexyl alcohol is not particularly limited, and various molecular weights may be used as necessary. or random or block copolymers with other olefins such as ethylene, butene, hexene, etc. can be used. The object of the present invention is to improve the physical properties of crystalline polypropylene in which alkenylsilane and propylene are mixed with a crystalline propylene copolymer obtained using a stereoregular catalyst, and the composition thereof is wide-ranging.

該結晶性のポリプロピレンを得るには重合に際して上記
触媒、及び重合法を利用すれば良く共重合体の製造方法
としてはすでに多くの方法が提案されており、必要に応
じ、他のオレフィンとのランダム共重合、あるいは始め
にプロピレンのみを重合し次いで他のオレフィンとプロ
ピレンを重合する所謂ブロック共重合、また重合反応を
不活性媒体中、液状の単量体中、あるいは気相状態で行
うこともできる。
To obtain the crystalline polypropylene, it is sufficient to use the above-mentioned catalyst and polymerization method during polymerization.Many methods have already been proposed for producing copolymers, and if necessary, random copolymers with other olefins may be used. Copolymerization, or so-called block copolymerization, in which only propylene is first polymerized and then other olefins and propylene are polymerized, and the polymerization reaction can also be carried out in an inert medium, in liquid monomers, or in the gas phase. .

本発明において上記2成分の混合方法については特に制
限は無くヘンシェルミキサーで前混合しついで押し出し
機で溶融混合し造粒するといった一般的な方法で十分混
合できる。この際公知の種々の安定剤などの添加剤を混
合することは勿論可能である。
In the present invention, there is no particular restriction on the method of mixing the two components, and they can be sufficiently mixed by a general method such as pre-mixing with a Henschel mixer, followed by melt-mixing with an extruder and granulation. At this time, it is of course possible to mix various known additives such as stabilizers.

〔実施例〕〔Example〕

以下に実施例を示しさらに本発明を説明する。 The present invention will be further explained with reference to Examples below.

実施例1 直径12mの鋼球9Kgの入った内容積41の粉砕用ポ
ットを4個装備した振動ミルを用意する。各ポットに窒
素雰囲気下で塩化マグネシウム300g、テトラエトキ
シシラン60m1.α、α、α−トリクロロトルエン4
5m1を加え40時間粉砕した。こうして得た共粉砕物
300gを51のフラスコに入れ四塩化チタン1,51
、トルエン1.51を加え100 @Cで30分間撹拌
処理し次いで上澄液を除き同様に四塩化チタン1.51
、トルエン1.51を加え100 ” Cで30分間撹
拌処理し次いで上澄液を除去し固形分をn−ヘキサンで
繰り返し洗浄して遷移金属触媒スラリーを得た。一部を
サンプリングしチタン分を分析したところ1.9wtχ
であった。
Example 1 A vibratory mill equipped with four grinding pots each having an internal volume of 41 and containing 9 kg of steel balls each having a diameter of 12 m was prepared. 300 g of magnesium chloride and 60 ml of tetraethoxysilane were placed in each pot under a nitrogen atmosphere. α, α, α-Trichlorotoluene 4
5ml was added and pulverized for 40 hours. 300 g of the co-pulverized material obtained in this way was put into a 51 flask and titanium tetrachloride 1,51
, 1.51% of toluene was added, stirred at 100 @C for 30 minutes, the supernatant was removed, and 1.51% of titanium tetrachloride was added in the same manner.
, 1.51 g of toluene was added, and the mixture was stirred at 100"C for 30 minutes. The supernatant liquid was removed, and the solid content was washed repeatedly with n-hexane to obtain a transition metal catalyst slurry. A portion was sampled to remove the titanium content. According to the analysis, it was 1.9wtχ
Met.

内容積200m1 の耐圧ガラスオートクレーブに窒素
雰囲気下トルエン40m1、上記遷移金属触媒20mg
、ジエチルアルミニウムクロライド0.128m1 、
p−トルイル酸メチル0.06m1、)ジエチルアルミ
ニウム0.b 、次いでプロピレンを5 kg/cm”になるまで装入
し70″Cで圧カ一定で2時間重合した。その後スラリ
ーを取り出し濾過乾燥して29gのパウダーを得た。
In a pressure-resistant glass autoclave with an internal volume of 200 m1, 40 m1 of toluene and 20 mg of the above transition metal catalyst were placed in a nitrogen atmosphere.
, diethylaluminum chloride 0.128ml,
Methyl p-toluate 0.06 ml,) Diethylaluminium 0. b) Next, propylene was charged to a concentration of 5 kg/cm" and polymerization was carried out at 70"C for 2 hours at a constant pressure. Thereafter, the slurry was taken out, filtered and dried to obtain 29 g of powder.

135°Cのテトラリン溶液で測定した極限粘度(以下
ηと略記する。)示差熱分析装置を用い10°C/+*
inで昇温或いは降温することで融点及び結晶化温度を
最大ピーク温度として測定した所、ηは1゜39、融点
152°C1結晶化温度108°Cであり結晶性のポリ
プロピレンであった。尚元素分析によればビニルシラン
単位を1.6wtχ含有していた。
Intrinsic viscosity (hereinafter abbreviated as η) measured with a tetralin solution at 135°C using a differential thermal analyzer at 10°C/+*
When the melting point and crystallization temperature were measured as the maximum peak temperature by increasing or decreasing the temperature in increments, η was 1°39, melting point was 152°C, crystallization temperature was 108°C, and it was found to be crystalline polypropylene. According to elemental analysis, it contained 1.6wtχ of vinylsilane units.

ついで、この共重合体を10gをシクロヘキシルアルコ
ール100m1 に分散し、金属ナトリウムO,Igを
加え常温で10時間反応した。スラリーを濾過しパウダ
ーをトルエンで充分に洗浄したのち乾燥した。このポリ
マーは赤外吸収スペクトルによれば5i−Hに帰属され
る吸収(2150cn+−’)が消失しておりエーテル
結合に帰属される吸収(1100cm ”付近)が観測
された。
Next, 10 g of this copolymer was dispersed in 100 ml of cyclohexyl alcohol, metal sodium O and Ig were added, and the mixture was reacted at room temperature for 10 hours. The slurry was filtered, and the powder was thoroughly washed with toluene and then dried. According to the infrared absorption spectrum of this polymer, the absorption attributed to 5i-H (2150cn+-') disappeared, and the absorption attributed to ether bonds (near 1100cm'') was observed.

また別途プロピレンを重合しηは1.65、ソックスレ
、−抽出器で抽出した時の抽出残率(以下IIと略記、
抽出後パウダー重量/抽出前パウダー重量を100分率
で表示)が97.1χのポリプロピレンを得、上記反応
物Logとポリプロピレン1000g 、フェノール系
の安定剤10/ 10000重量比(対ポリプロピレン
)、及びステアリン酸カルシウムを15/10000重
量比加え造粒し組成物を得た。
Separately, propylene was polymerized and η was 1.65, and the extraction residual rate when extracted with a Soxhlet extractor (hereinafter abbreviated as II),
Polypropylene with a ratio of powder weight after extraction/powder weight before extraction (expressed as a 100 fraction) of 97.1χ was obtained, and the above reactant Log and 1000 g of polypropylene, a phenolic stabilizer at a weight ratio of 10/10000 (to polypropylene), and a steer. Calcium phosphate was added in a weight ratio of 15/10000 and granulated to obtain a composition.

ついでこの組成物を用いメルトフローインデックスを測
定しさらに厚さIIのインジェクションシートを作り、
曲げ剛性度を測定した。
Next, the melt flow index was measured using this composition, and an injection sheet with a thickness of II was made.
Bending stiffness was measured.

メルトフローインデックス    (Ml)  AST
M  01238(230’  C)曲げ剛性度   
  657M D747−63(20″’ c>比較例
1 ビニルシランとプロピレンの共重合体とシクロヘキシル
アルコールとの反応物を用いなかった他は実施例1と同
様にして物性を測定した、結果は表に示す。
Melt flow index (Ml) AST
M 01238 (230' C) Bending rigidity
657M D747-63 (20''c> Comparative Example 1 The physical properties were measured in the same manner as in Example 1 except that the reaction product of the copolymer of vinylsilane and propylene and cyclohexyl alcohol was not used. The results are shown in the table. .

実施例2 ビニルシランに変えアリルシランを用いた他は実施例1
と同様にした、ここで共重合体はアリルシラ72.9w
t%含み、ηは1.34、融点146°ct’あった。
Example 2 Example 1 except that allylsilane was used instead of vinylsilane
The copolymer was allyl sila 72.9w.
t%, η was 1.34, and the melting point was 146°ct'.

結果は表に示す。The results are shown in the table.

〔効果〕〔effect〕

本発明の組成物は極めて物性に優れており工業的に極め
て価値がある。
The composition of the present invention has extremely excellent physical properties and is extremely valuable industrially.

特許出願人 三井東圧化学株式会社Patent applicant: Mitsui Toatsu Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)アルケニルシランとプロピレンを立体規則性触媒
を用いて得た結晶性プロピレン共重合体とシクロヘキシ
ルアルコールまたはその誘導体との反応物を含有してな
る結晶性ポリプロピレン樹脂組成物。
(1) A crystalline polypropylene resin composition containing a reaction product of a crystalline propylene copolymer obtained from alkenylsilane and propylene using a stereoregular catalyst and cyclohexyl alcohol or a derivative thereof.
JP9016988A 1988-04-14 1988-04-14 Polypropylene resin composition Expired - Lifetime JP2823861B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9016988A JP2823861B2 (en) 1988-04-14 1988-04-14 Polypropylene resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9016988A JP2823861B2 (en) 1988-04-14 1988-04-14 Polypropylene resin composition

Publications (2)

Publication Number Publication Date
JPH01263138A true JPH01263138A (en) 1989-10-19
JP2823861B2 JP2823861B2 (en) 1998-11-11

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0249048A (en) * 1988-02-09 1990-02-19 Mitsui Toatsu Chem Inc Polypropylene resin composition and use thereof
JPH0297541A (en) * 1988-10-03 1990-04-10 Mitsui Toatsu Chem Inc Crystalline polypropylene resin composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0249048A (en) * 1988-02-09 1990-02-19 Mitsui Toatsu Chem Inc Polypropylene resin composition and use thereof
JPH0297541A (en) * 1988-10-03 1990-04-10 Mitsui Toatsu Chem Inc Crystalline polypropylene resin composition

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