JP2737786B2 - Method for producing highly transparent stretched polypropylene film - Google Patents

Method for producing highly transparent stretched polypropylene film

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Publication number
JP2737786B2
JP2737786B2 JP63130437A JP13043788A JP2737786B2 JP 2737786 B2 JP2737786 B2 JP 2737786B2 JP 63130437 A JP63130437 A JP 63130437A JP 13043788 A JP13043788 A JP 13043788A JP 2737786 B2 JP2737786 B2 JP 2737786B2
Authority
JP
Japan
Prior art keywords
sheet
highly transparent
polypropylene film
film
intensity
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.)
Expired - Fee Related
Application number
JP63130437A
Other languages
Japanese (ja)
Other versions
JPH01301720A (en
Inventor
建世 佐々木
孝行 山田
一彦 山本
浅沼  正
武夫 井上
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 Chemicals Inc
Original Assignee
Mitsui Chemicals Inc
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Filing date
Publication date
Application filed by Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Priority to JP63130437A priority Critical patent/JP2737786B2/en
Publication of JPH01301720A publication Critical patent/JPH01301720A/en
Application granted granted Critical
Publication of JP2737786B2 publication Critical patent/JP2737786B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、高透明ポリプロピレン延伸フイルムの製造
方法に関する。詳しくは、特定の特性を有するシートを
延伸してなる高透明ポリプロピレン延伸フイルムの製造
方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for producing a highly transparent stretched polypropylene film. More specifically, the present invention relates to a method for producing a highly transparent stretched polypropylene film formed by stretching a sheet having specific characteristics.

〔従来の技術〕[Conventional technology]

ポリプロピレンは比較的透明性に優れたポリマーであ
るが、結晶性のポリマーであり、成形条件により種々の
程度の透明性のものが得られる。さらに透明性を向上さ
せる目的でエチレン等の他のオレフィンと共重合して結
晶化度、あるいは球晶の大きさをコントロールする方
法、あるいは核剤を添加して球晶を小さくする方法、成
形物の冷却速度を上げて球晶を小さくする方法等が知ら
れている。これらの方法は一定の効果があり、特に球晶
の大きさをコントロールする方法は有用である。
Polypropylene is a polymer having relatively excellent transparency, but is a crystalline polymer, and can have various degrees of transparency depending on molding conditions. Method of controlling crystallinity or spherulite size by copolymerizing with other olefins such as ethylene for the purpose of further improving transparency, or method of reducing spherulite by adding nucleating agent, molded product There are known methods for increasing the cooling rate of spherulites to reduce spherulites. These methods have a certain effect, and a method of controlling the size of spherulite is particularly useful.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

球晶の大きさをコントロールする方法は有用である
が、延伸フイルムの場合には、もとのシートの透明性が
同じように良好であっても延伸すると透明性に差が生
じ、場合によっては極めて不透明なフイルムになる場合
もある。
It is useful to control the size of spherulites, but in the case of stretched films, even if the transparency of the original sheet is equally good, there is a difference in transparency when stretched. The film may be extremely opaque.

本発明は、前記問題点を解決した高透明ポリプロピレ
ン延伸フイルムの製造方法を提供することを課題とす
る。
An object of the present invention is to provide a method for producing a highly transparent stretched polypropylene film that has solved the above-mentioned problems.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者らは、従来の前記透明性に差のあるフイルム
について厳密な解析を行ったところ、得られた延伸フイ
ルムはX線回折スペクトルでは殆ど差が無く、また球晶
の大きさにも差がなくても、透明性が大きく異なること
があり、その原因は延伸フイルムの表面の滑らかさが大
きく異なっていることによることを見出した。
The present inventors have conducted a rigorous analysis on the conventional film having a difference in transparency, and found that the obtained stretched film has almost no difference in the X-ray diffraction spectrum, and also has a difference in the size of the spherulite. Even without the film, the transparency may be largely different, and it has been found that the cause is that the surface smoothness of the stretched film is largely different.

本発明者らは、この発見に基づき鋭意検討した結果、
特定の条件を満足するシートを延伸することで従来知ら
れていなかった極めて、透明性に優れた延伸フイルムを
得られることを見出し本発明を完成した。
The present inventors have conducted intensive studies based on this finding,
The present inventors have found that stretching a sheet satisfying specific conditions can provide a stretched film excellent in transparency, which was not conventionally known, and completed the present invention.

即ち、本発明は、プロピレンの単独重合体、或いは少
量の他のα−オレフィンとの共重合体からなりポリアリ
ルトリメチルシランを含有する高結晶性ポリプロピレン
樹脂組成物を押出成形してダイより取り出したシート
を、少なくともその表面においてX−線回折スペクトル
で測定して得られるα晶とβ晶に帰属される回折線の強
度の総和に対するβ晶に帰属される回折線の強度の割合
が0.02以下となるように冷却して得たシートを延伸する
ことを特徴とする高透明ポリプロピレン延伸フィルムの
製造方法である。
That is, in the present invention, a high-crystalline polypropylene resin composition comprising a homopolymer of propylene or a copolymer with a small amount of another α-olefin and containing polyallyltrimethylsilane was extruded and taken out from a die. The ratio of the intensity of the diffraction line attributed to the β-crystal to the total sum of the intensity of the diffraction line attributed to the α- and β-crystals obtained by measuring the X-ray diffraction spectrum on at least the surface thereof is 0.02 or less. This is a method for producing a highly transparent stretched polypropylene film, comprising stretching a sheet obtained by cooling the film.

以下に本発明のフイルムの製造方法について詳細に説
明する。本発明の延伸フイルムの製造方法はその前段の
シートの特性によって特徴づけられ、シートが少なくと
もその表面においてX−線回折スペクトルで測定して得
られるα晶とβ晶に帰属される回折線の強度の総和に対
するβ晶に帰属される回折線の強度の割合が0.02以下で
あることが必要である。β晶に帰属される回折線の強度
の割合(以下単にβ晶の割合という)は小さければ小さ
い程よく、好ましくは0であることが最も望ましい。
Hereinafter, the method for producing a film of the present invention will be described in detail. The method for producing a stretched film of the present invention is characterized by the properties of the sheet at the preceding stage, and the intensity of the diffraction lines attributed to α- and β-crystals obtained by measuring the sheet at least on its surface with an X-ray diffraction spectrum. It is necessary that the ratio of the intensity of the diffraction line attributed to the β crystal to the sum of The smaller the ratio of the intensity of the diffraction line attributed to the β crystal (hereinafter, simply referred to as the ratio of the β crystal), the better, preferably 0.

このようなシートの製造には種々の方法があり、ポリ
アリルトリメチルシランを多く添加すること。シートを
成形する際にダイより押し出されてきたシートを比較的
急冷すること。出来るだけ薄いシートから延伸するこ
と。これらの条件を組み合わせることにより、β晶の割
合を0.02以下とすることが可能である。必要条件として
は、用いるポリプロピレンによっても異なるが、実験室
的には、結晶化温度を高める添加剤を加え、シートを急
冷するだけでもβ晶の割合を実質的に0とすることも可
能であるが、工業的には、ポリアリルトリメチルシラン
を添加したポリプロピレンを用い、しかも比較的シート
を急冷できるような条件で成形することにより達成でき
る。
There are various methods for producing such a sheet, and a large amount of polyallyltrimethylsilane must be added. The relatively rapid cooling of the sheet extruded from the die when forming the sheet. Stretch from the thinnest sheet possible. By combining these conditions, it is possible to reduce the ratio of β crystals to 0.02 or less. The requirements vary depending on the polypropylene used, but in the laboratory, it is also possible to add an additive for increasing the crystallization temperature and rapidly cool the sheet to make the ratio of β crystals substantially zero. However, industrially, it can be attained by using polypropylene to which polyallyltrimethylsilane is added, and by molding under conditions that allow relatively rapid cooling of the sheet.

本発明において用いるポリプロピレンとしては、高結
晶性であるかぎり特に制限はなく、プロピレンの単独重
合体のみならず、エチレン、ブテン、ヘキセン等との統
計的共重合体も使用でき、通常プロピレン1に対して0.
1モル比程度以下の他のオレフィンを含有するものが利
用できる。また分子量としては230℃で測定した、メル
トフローレートとして好ましくは0.1〜10程度の分子量
のものが利用できる。
The polypropylene used in the present invention is not particularly limited as long as it is highly crystalline. Not only a propylene homopolymer but also a statistical copolymer with ethylene, butene, hexene, etc. can be used. 0.
Those containing other olefins of about 1 mole ratio or less can be used. The melt flow rate measured at 230 ° C. and preferably having a molecular weight of about 0.1 to 10 can be used.

なお、本発明においてβ晶の割合は以下の様な定義に
従いK−Cu線を用いて測定した。例えば比較例1のシー
ト面の広角X−線回折スペクトル第2図で説明すると、
広角X−線回折スペクトルの2θの値が約13.8℃、16.6
℃、18.3℃のピークをα晶と定義し、その強度はそのピ
ーク高さで表される。また同じく2θの他が約15.8のピ
ークをβ晶と定義し、強度は同様にそのピーク高さで表
される。(TURNER JORESらMakromol.Chemie vol.75,134
(1964)によった。)。
In the present invention, the ratio of β crystals was measured using a K-Cu line according to the following definition. For example, a wide-angle X-ray diffraction spectrum of the sheet surface of Comparative Example 1 will be described with reference to FIG.
The value of 2θ in the wide-angle X-ray diffraction spectrum is about 13.8 ° C., 16.6 ° C.
The peaks at 18.3 ° C. and 18.3 ° C. are defined as α crystals, and the intensity is represented by the peak height. Similarly, a peak of about 15.8 other than 2θ is defined as a β crystal, and the intensity is similarly represented by the peak height. (TURNER JORES et al. Makromol. Chemie vol. 75, 134
According to (1964). ).

〔実施例〕〔Example〕

以下に実施例を示し、本発明を更に説明する。 Hereinafter, the present invention will be further described with reference to Examples.

実施例1 直径12mmの鋼球2.2kgの入った内容積0.97の粉砕用
ポットを2個装備した振動ミルを用意し、各ポットに窒
素雰囲気下で塩化マグネシウム20g、テトラエトキシシ
ラン4mlおよびα,α,α−トリクロロトルエン3mlを加
え、40時間粉砕した。こうして得た共粉砕物のうち15g
を200mlのフラスコに入れ、四塩化チタン80mlとトルエ
ン80mlを加え、100℃で30分間撹拌処理した。その後上
澄液を除き、同様に四塩化チタン80mlとトルエン80mlを
加え、100℃で30分間撹拌処理し、上澄液を除去して得
た固形分を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1.9wt%であった。
Example 1 A vibration mill equipped with two crushing pots having an inner volume of 0.97 and containing 2.2 kg of steel balls having a diameter of 12 mm was prepared. , Α-trichlorotoluene (3 ml) was added, and the mixture was ground for 40 hours. 15g of the co-ground product thus obtained
Was placed in a 200 ml flask, 80 ml of titanium tetrachloride and 80 ml of toluene were added, and the mixture was stirred at 100 ° C. for 30 minutes. Thereafter, the supernatant was removed, 80 ml of titanium tetrachloride and 80 ml of toluene were added in the same manner, and the mixture was stirred at 100 ° C. for 30 minutes, and the solid obtained by removing the supernatant was repeatedly washed with n-hexane to prepare a transition metal. A catalyst slurry was obtained. When a part was sampled and the titanium content was analyzed, it was 1.9 wt%.

内容積200mlのフラスコに、窒素雰囲気下トルエン40m
l、上記遷移金属触媒10.0g、ジエチルアルミニウムクロ
ライド24.0ml、p−トルイル酸メチル14mlおよびトリエ
チルアルミニウム20mlを加え混合した後、この触媒スラ
リーを充分に脱気したn−ヘプタン1を入れた内容積
300のオートクレーブに入れ、プロピレンで気相部を
置換した後、水素20Nを入れ、次いでプロピレンを入
れて圧力が5kg/cm2ゲージとなるようにプロピレンを追
加し、内温70℃でプロピレンの装入量が50kgとなるまで
重合した。次いで未反応のプロピレンをパージし、メタ
ノール20を加え、90℃で撹拌処理し、得られたスラリ
ーを水で洗浄して精製した。スラリーを濾過し、パウダ
ーを分離し、80℃、60mmHgで12時間乾燥した。
In a flask with an inner volume of 200 ml, toluene 40 m under a nitrogen atmosphere
l, 10.0 g of the above-mentioned transition metal catalyst, 24.0 ml of diethylaluminum chloride, 14 ml of methyl p-toluate and 20 ml of triethylaluminum were added and mixed.
After placing the autoclave in a 300 g autoclave and replacing the gas phase with propylene, 20 N of hydrogen was added, then propylene was added, and propylene was added to a pressure of 5 kg / cm 2 gauge. The polymerization was continued until the amount of the mixture reached 50 kg. Then, unreacted propylene was purged, methanol 20 was added, the mixture was stirred at 90 ° C., and the obtained slurry was purified by washing with water. The slurry was filtered, the powder was separated and dried at 80 ° C., 60 mmHg for 12 hours.

得られたパウダーを分析したところ、沸騰n−ヘプタ
ン抽出残率97.7%、135℃のテトラリン溶液で測定した
極限粘度1.72(以下、ηと略記する)であった。
Analysis of the obtained powder showed a boiling n-heptane extraction residual ratio of 97.7% and an intrinsic viscosity of 1.72 (hereinafter abbreviated as η) measured with a tetralin solution at 135 ° C.

一方、上記遷移金属触媒を用い、アリルトリメチルシ
ランの重合体を含有するマスターパウダーを製造した。
300mlのフラスコ中で遷移金属触媒5g、ジエチルアルミ
ニウムクロライド5mlをアリルトリメチルシラン10ml、
トルエン10mlに加え60℃で2時間撹拌し、次いてこのス
ラリーを内容積3のオートクレーブに入れ、ヘプタン
1、p−トルイル酸メチル0.6ml、トリメチルアルミ
ニウム5ml加え、水素0.2N、プロピレンを装入して圧
力5kg/cm2ゲージととし、次いで内温60℃でプロピレン
の装入量が500gとなるまで圧力一定で重合した。上記方
法と同様に処理してアリルトルメチルシランの重合体を
12000ppm含有するマスターパウダーを得た。
On the other hand, a master powder containing a polymer of allyltrimethylsilane was produced using the above transition metal catalyst.
In a 300 ml flask, 5 g of a transition metal catalyst, 5 ml of diethylaluminum chloride and 10 ml of allyltrimethylsilane,
The slurry was added to 10 ml of toluene and stirred at 60 ° C. for 2 hours. Then, the slurry was placed in an autoclave having an internal volume of 3, and then heptane 1, methyl p-toluate (0.6 ml) and trimethylaluminum (5 ml) were added. The pressure was adjusted to 5 kg / cm 2 gauge, and then the polymerization was carried out at an internal temperature of 60 ° C. at a constant pressure until the charged amount of propylene became 500 g. By treating in the same manner as in the above method, a polymer of allyltolumethylsilane is obtained.
A master powder containing 12000 ppm was obtained.

次いで、公知の酸化防止剤と上記共重合体とマスター
パウダーを押出機で混合し、アリルトリメチルシランの
重合体を10ppm含有する組成物を得た。この組成物を40m
mΦの押出機で押出温度250℃、シート冷却温度(チルロ
ール表面温度)80℃の条件で厚さ550μのシートに成形
した。次いでTMロング社製の2軸延伸機で155℃で5×
7倍に延伸して延伸フイルムを得た、このシートのβ晶
の割合及びフイルムの物性を表に示す。表中、透明性は
ヘイズ及び目視での評価結果で表示した。
Next, the known antioxidant, the above copolymer and master powder were mixed by an extruder to obtain a composition containing 10 ppm of a polymer of allyltrimethylsilane. 40 m of this composition
The sheet was formed into a sheet having a thickness of 550 μm using an extruder having an mΦ at an extrusion temperature of 250 ° C. and a sheet cooling temperature of 80 ° C. Next, 5 × at 155 ° C. using a biaxial stretching machine manufactured by TM Long.
The film was stretched 7 times to obtain a stretched film. The ratio of β crystal in this sheet and the physical properties of the film are shown in the table. In the table, transparency is indicated by haze and visual evaluation results.

ヘイズ ASTM D1003に準拠した。 Haze Compliant with ASTM D1003.

比較列1 シート厚みを1300μとした他は、実施例1と同様とし
た。評価結果は表に示す。
Comparative Row 1 The procedure was the same as in Example 1 except that the sheet thickness was 1300 μm. The evaluation results are shown in the table.

比較例2 実施例1で得たプロピレンの単独重合体を用い、酸化
防止剤のみ添加した他は、実施例1と同様にした。結果
は表に示す。
Comparative Example 2 The procedure of Example 1 was repeated, except that the propylene homopolymer obtained in Example 1 was used and only an antioxidant was added. The results are shown in the table.

実施例2 シート冷却温度(チルロール表面温度)20℃とし、シ
ート厚み1300μとした他は、実施例1と同様とした。結
果は表に示す。
Example 2 Same as Example 1 except that the sheet cooling temperature (chill roll surface temperature) was 20 ° C. and the sheet thickness was 1300 μm. The results are shown in the table.

比較例3 実施例1で得たプロピレンの単独重合体を用いて、ポ
リアリルトリメチルシランに代えて、核剤として1 2,3
4−ジ(エチルベンジリデン)ソルビトールをポリプロ
ピレン100重量部に対し0.1重量部添加し、シート冷却温
度(チルロール表面温度)90℃とし、シート厚さ1300μ
とした他は、実施例1と同様にした。結果を表に示す。
Comparative Example 3 Using the homopolymer of propylene obtained in Example 1, instead of polyallyltrimethylsilane, 12
0.1 part by weight of 4-di (ethylbenzylidene) sorbitol is added to 100 parts by weight of polypropylene, the sheet cooling temperature (chill roll surface temperature) is 90 ° C., and the sheet thickness is 1300 μm.
Other than the above, the procedure was the same as in Example 1. The results are shown in the table.

本発明の延伸シートを製造する際に用いたシートの一
面の広角X−線回折スペクトルを第1図に示したが、β
晶は観測されない。参考のため比較例1のシートのロー
ルに接触していない面の広角X−線回折スペクトルを第
2図に示したが、β晶がかなり観測される。
FIG. 1 shows a wide-angle X-ray diffraction spectrum of one surface of the sheet used for producing the stretched sheet of the present invention.
No crystals are observed. For reference, the wide-angle X-ray diffraction spectrum of the surface of the sheet of Comparative Example 1 which is not in contact with the roll is shown in FIG. 2, but considerable β crystals are observed.

〔発明の効果〕 本発明の方法を実施することにより、極めて透明性に
優れ、種々の用途に利用可能な延伸フィルムを得ること
ができ極めて工業的に価値のあるものである。
[Effects of the Invention] By carrying out the method of the present invention, a stretched film which is extremely excellent in transparency and can be used for various applications can be obtained, and is extremely industrially valuable.

【図面の簡単な説明】[Brief description of the drawings]

第1図は、本発明の延伸シートを製造する際に用いたシ
ートの一面の広角X−線回折スペクトルを示し、第2図
は、比較例1のシートのロールに接触していない面の広
角X−線回折スペクトルを示す。
FIG. 1 shows a wide-angle X-ray diffraction spectrum of one surface of a sheet used for producing a stretched sheet of the present invention, and FIG. 2 shows a wide-angle of a surface of a sheet of Comparative Example 1 which is not in contact with a roll. 3 shows an X-ray diffraction spectrum.

───────────────────────────────────────────────────── フロントページの続き 合議体 審判長 小野 新次郎 審判官 仁木 由美子 審判官 喜納 稔 (56)参考文献 特開 昭58−87024(JP,A) 特開 昭59−198122(JP,A) ──────────────────────────────────────────────────の Continuing from the front page Judge of the colleague Jinro Ono Judge Yumiko Niki Judge Minoru Kina (56) References JP-A-58-87024 (JP, A) JP-A-59-198122 (JP, A)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】プロピレンの単独重合体、或いは少量の他
のα−オレフィンとの共重合体からなりポリアリルトリ
メチルシランを含有する高結晶性ポリプロピレン樹脂組
成物を押出成形してダイより取り出したシートを、少な
くともその表面においてX−線回折スペクトルで測定し
て得られるα晶とβ晶に帰属される回折線の強度の総和
に対するβ晶に帰属される回折線の強度の割合が0.02以
下となるように冷却して得たシートを延伸することを特
徴とする高透明ポリプロピレン延伸フィルムの製造方
法。
1. A sheet obtained by extruding a highly crystalline polypropylene resin composition comprising a homopolymer of propylene or a copolymer with a small amount of another α-olefin and containing polyallyltrimethylsilane, and taking out from a die. The ratio of the intensity of the diffraction line attributed to the β-crystal to the total sum of the intensity of the diffraction line attributed to the α- and β-crystals obtained by measuring at least the surface with an X-ray diffraction spectrum is 0.02 or less. A method for producing a stretched highly transparent polypropylene film, comprising stretching a sheet obtained by cooling as described above.
JP63130437A 1988-05-30 1988-05-30 Method for producing highly transparent stretched polypropylene film Expired - Fee Related JP2737786B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63130437A JP2737786B2 (en) 1988-05-30 1988-05-30 Method for producing highly transparent stretched polypropylene film

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JP63130437A JP2737786B2 (en) 1988-05-30 1988-05-30 Method for producing highly transparent stretched polypropylene film

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JPH01301720A JPH01301720A (en) 1989-12-05
JP2737786B2 true JP2737786B2 (en) 1998-04-08

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Publication number Priority date Publication date Assignee Title
JPS5887024A (en) * 1981-11-19 1983-05-24 Sumitomo Chem Co Ltd Polypropylene stretched film
JPS59198122A (en) * 1983-04-25 1984-11-09 Tokuyama Soda Co Ltd Manufacture of roughened polypropylene film

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