JPH0356170B2 - - Google Patents
Info
- Publication number
- JPH0356170B2 JPH0356170B2 JP1785782A JP1785782A JPH0356170B2 JP H0356170 B2 JPH0356170 B2 JP H0356170B2 JP 1785782 A JP1785782 A JP 1785782A JP 1785782 A JP1785782 A JP 1785782A JP H0356170 B2 JPH0356170 B2 JP H0356170B2
- Authority
- JP
- Japan
- Prior art keywords
- polypropylene
- weight
- stretching
- boiling heptane
- stretched film
- 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
Links
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 40
- -1 polypropylene Polymers 0.000 claims description 34
- 239000004743 Polypropylene Substances 0.000 claims description 25
- 229920001155 polypropylene Polymers 0.000 claims description 25
- 238000009835 boiling Methods 0.000 claims description 19
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 238000000034 method Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 3
- 229920002521 macromolecule Polymers 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229920000298 Cellophane Polymers 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 description 1
- FTQWRYSLUYAIRQ-UHFFFAOYSA-N n-[(octadecanoylamino)methyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCNC(=O)CCCCCCCCCCCCCCCCC FTQWRYSLUYAIRQ-UHFFFAOYSA-N 0.000 description 1
- SLZWSYPJQQIDJB-UHFFFAOYSA-N n-[6-(octadecanoylamino)hexyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCCCCCNC(=O)CCCCCCCCCCCCCCCCC SLZWSYPJQQIDJB-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は剛性の優れたポリプロピレン延伸フイ
ルムの製造方法に関する。
ポリプロピレン延伸フイルム、特に二軸延伸フ
イルムは透明性、光沢等の光学的性質に優れ、か
つ引張強度、剛性等の機械的性質が比較的良好で
あるがゆえに食品包装、繊維包装その他広範囲な
用途に使用されている。
しかしながら用途によつてはこれらの性質が十
分に満足されている訳ではなく、特にフイルム剛
性の点でセロハン、ポリエステル延伸フイルム等
に劣るため、使用分野が大幅に制限されているの
が実情である。
このようなことからポリプロピレン延伸フイル
ムの剛性を改良すべく従来から種々の検討がなさ
れているが延伸加工性とフイルム剛性共に満足で
きる方法は見い出されていない。
例えば延伸加工において延伸倍率を高める方法
が試みられているが延伸加工時の膜破れが発生し
易くなり、生産性が悪化するため剛性改良には限
度がある。
またポリプロピレンとして高結晶性ポリプロピ
レンを用いる方法があるが、延伸加工時に膜破れ
や延伸ムラを生じ正常な製膜が困難であるため適
用可能なポリプロピレンの高結晶化には限度があ
り、また延伸温度、延伸倍率等の延伸条件変更に
より延伸加工性を改良しようとする延伸フイルム
の剛性低下を生じるため高結晶性ポリプロピレン
による剛性改良には限度がある。
本発明者らはかかる実情にかんがみ上記の如き
延伸加工性に問題のない剛性に優れたポリプロピ
レン延伸フイルムの製造方法を得るべく種々検討
した結果、特定の構造を有する高結晶性ポリプロ
ピレンにビスアマイド化合物を添加してなる配合
物を用いて延伸することにより、延伸加工性の低
下をきたすことなく剛性の優れた延伸フイルムが
得られることを見い出し、本発明に到達した。
すなわち、沸騰ヘプタン不溶部のアイソタクチ
ツクペンタツド分率が0.955以上でかつ沸騰ヘプ
タン可溶部の含有率が9.0重量%以下である高結
晶性ポリプロピレン100重量部に対して、一般式
RCONH(CH2)nNHCOR
(ここでRは炭素数11〜21の脂肪族炭化水素基、
nは1〜10の整数を表わす。)で表わされるビス
アマイド化合物を0.5〜5重量部を添加してなる
配合物を少なくとも一軸方向に延伸することを特
徴とする剛性の優れたポリプロピレン延伸フイル
ムの製造方法である。
本発明で使用するポリプロピレンは沸騰ヘプタ
ン不溶部のアイソタクチツクペンタツド分率と沸
騰ヘプタン可溶部の含有量で規定されるがこれら
は次のように決定される。
ポリプロピレン5gを沸騰キシレン500mlに完全
溶解させた後、20℃に降温し4時間放置する。そ
の後、別し20℃キシレン可溶部と不溶部に分離
する。次いで、20℃キシレン不溶部をさらに沸騰
n−ヘプタンで8時間ソツクスレー抽出して抽出
残渣と抽出物に分離する。この抽出残渣を沸騰ヘ
プタン不溶部とする。沸騰ヘプタン可溶部とは20
℃キシレン可溶部と先の沸騰n−ヘプタン抽出物
とを足し合わせたものである。この沸騰ヘプタン
可溶部の重量と測定に供した全ポリプロピレン重
量から、沸騰ヘプタン可溶部の重量百分率を決定
する。
アイソタクチツクペンタツド分率とは、A・
ZambelliらによつてMacromolecules6925
(1978)に発表されている方法、すなわち 13C−
NMRを使用して測定されるポリプロピレン分子
鎖中のペンタツド単位でのアイソタクチツク分率
である。ただし、ピークの帰属に関しては、
Macromolecules8,687(1975)に
Macromolecules6,925(1973)の訂正版が記載
されているのでこれに基づいて行なうものであ
る。
本発明で使用する高結晶性ポリプロピレンは沸
騰ヘプタン不溶部のアイソタクチツクペンタツド
分率が0.955以上、好ましくは0.960以上でかつ沸
騰ヘプタン可溶部の含有量が9.0重量%以下、好
ましくは2.0〜8.0重量%のものでなくてはならな
い。すなわち沸騰ヘプタン不溶部のアイソタクチ
ツクペンタツド分率が0.955に満たないか、ある
いは沸騰ヘプタン不溶部のアイソタクチツクペン
タツド分率が0.955以上であつても沸騰ヘプタン
可溶部の含有量が9.0重量%を越えるポリプロピ
レンでは本発明の目的とする剛性の優れた延伸フ
イルムを得ることはできない。
本発明において用いられるかかるポリプロピレ
ンは、例えば、本願と同一の出願人による出願で
あり、本願出願日以前に公知である特開昭53−
33289号に記載の方法により得ることができる。
本発明におけるビスアマイド化合物の例として
はメチレンビスステアロアマイド、エチレンビス
ステアロアマイド、ヘキサメチレンビスステアロ
アマイド等が挙げられる。
ビスアマイド化合物のメチレン数nが10を越え
ると相溶性、発煙、臭気の点で問題が生じるので
使用できない。
ビスアマイド化合物の添加量は0.5〜5重量部、
好ましくは1.0〜3.0重量部である。
本発明に使用するポリプロピレンには種々の添
加剤、例えば酸化防止剤、滑剤、帯電防止剤、抗
ブロツキング剤等を適宜配合することができる。
本発明における延伸加工は通常工業的に用いら
れる方法、例えばロール延伸、テンター延伸、チ
ユーブラー延伸等の延伸方法により実施すること
ができる。
本発明で規定された高結晶性ポリプロピレンを
用いて延伸フイルムを製造した場合、通常のポリ
プロピレンを用いた場合に較べて著るしく剛性の
高いフイルムが得られるが、延伸加工性が低下す
るという問題がある。しかるに驚くべきことには
本発明におけるビスアマイド化合物を添加するこ
とによりフイルム剛性の低下をきたすことなく延
伸加工性を大幅に改善することができるのであ
る。
以下に実施例を挙げて本発明の効果を説明する
が本発明はこれらの限定されるものではない。
実施例におけるフイルム物性は下記の試験法に
より測定した。
ヤング率:幅20mmの試験片を縦方向(MD)及び
横方向(TD)より採取し引張試験機によりチ
ヤツク間隔60mm、引張速度5mm/分でS−S曲
線をとり、初期弾性率を測定した。
実施例 1
メルトインデツクスが2.2g/10分、沸騰ヘプタ
ン不溶部のアイソタクチツクペンタツド分率が
0.967、沸騰ヘプタン可溶部の含有量が4.5重量%
の高結晶性ポリプロピレン100重量部に対してビ
スアマイド化合物としてエチレンビスステアロア
マイドを2.0重量部添加混合し、造粒機によりペ
レツト化した後、樹脂温度280℃で溶融押出を行
ない、30℃の冷却ロールにて急冷することにより
厚さ0.8mmのシートとした。得られたシートをテ
ンター式逐次二軸延伸装置にて所定の延伸速度で
縦方向に延伸温度140℃で4倍、横方向に延伸温
度155℃で10倍延伸を行ない、つづいて140℃で熱
処理を行なうことにより厚さ約20μの二軸延伸フ
イルムとした。
比較例 1
実施例1における高結晶性ポリプロピレンにビ
スアマイド化合物を添加せずに実施例1と同様の
方法により二軸延伸フイルムとした。
比較例 2
ポリプロピレンとしてメルトインデツクスが
2.4g/10分、沸騰ヘプタン不溶部のアイソタクチ
ツクペンタツド分率が0.940沸騰ヘプタン可溶部
の含有率が7.5重量%であるポリプロピレンを用
い、ビスアマイド化合物を添加しない他は実施例
1と同様の方法により二軸延伸フイルムとした。
以上の実施例1及び比較例1,2における延伸
加工性及びフイルム物性を第1表に示す。
The present invention relates to a method for producing a polypropylene stretched film with excellent rigidity. Polypropylene stretched film, especially biaxially stretched film, has excellent optical properties such as transparency and gloss, and relatively good mechanical properties such as tensile strength and rigidity, making it suitable for a wide range of applications such as food packaging and textile packaging. It is used. However, depending on the application, these properties are not fully satisfied, and in particular, the film is inferior to cellophane, polyester stretched film, etc. in terms of film rigidity, so the field of use is greatly restricted. . For this reason, various studies have been made to improve the rigidity of stretched polypropylene films, but no method has been found that satisfies both stretchability and film rigidity. For example, attempts have been made to increase the stretching ratio during stretching, but there is a limit to the improvement in rigidity because membrane tearing tends to occur during stretching, which reduces productivity. In addition, there is a method of using highly crystalline polypropylene as the polypropylene, but there is a limit to the high crystallization of polypropylene that can be applied because film tearing and stretching unevenness occur during stretching, making normal film formation difficult. However, there is a limit to the improvement in rigidity by highly crystalline polypropylene because the rigidity of the stretched film that is attempted to be improved by changing the stretching conditions, such as the stretching ratio, decreases. In view of these circumstances, the present inventors conducted various studies in order to obtain a method for producing a polypropylene stretched film with excellent rigidity and no problem with the above-mentioned stretching processability. It has been discovered that a stretched film with excellent rigidity can be obtained without deteriorating the stretching processability by stretching using a blend formed by adding the above-mentioned compounds, and the present invention has been achieved based on this discovery. That is, the general formula RCONH (CH 2 ) nNHCOR (where R is an aliphatic hydrocarbon group having 11 to 21 carbon atoms,
n represents an integer from 1 to 10. This is a method for producing a polypropylene stretched film with excellent rigidity, which comprises stretching in at least one direction a blend obtained by adding 0.5 to 5 parts by weight of a bisamide compound represented by the following formula. The polypropylene used in the present invention is defined by the isotactic pentad fraction of the boiling heptane insoluble portion and the content of the boiling heptane soluble portion, which are determined as follows. After completely dissolving 5 g of polypropylene in 500 ml of boiling xylene, the temperature was lowered to 20°C and left for 4 hours. Thereafter, it is separated into a xylene soluble part and an insoluble part at 20°C. Next, the xylene-insoluble portion at 20° C. is further subjected to Soxhlet extraction with boiling n-heptane for 8 hours to separate it into an extraction residue and an extract. This extraction residue is used as the boiling heptane insoluble part. What is boiling heptane soluble part?20
It is the sum of the xylene soluble portion and the boiled n-heptane extract. The weight percentage of the boiling heptane soluble portion is determined from the weight of the boiling heptane soluble portion and the total weight of the polypropylene subjected to measurement. Isotactic pentad fraction is A.
Macromolecules 6 925 by Zambelli et al.
(1978), i.e. 13 C−
It is the isotactic fraction in pentad units in a polypropylene molecular chain measured using NMR. However, regarding peak attribution,
Macromolecules 8 , 687 (1975)
The revised version of Macromolecules 6 , 925 (1973) has been described, so this will be used as the basis. The highly crystalline polypropylene used in the present invention has an isotactic pentad fraction in the boiling heptane insoluble part of 0.955 or more, preferably 0.960 or more, and a content of the boiling heptane soluble part of 9.0% by weight or less, preferably 2.0 to Must be 8.0% by weight. That is, the isotactic pentad fraction of the boiling heptane insoluble portion is less than 0.955, or even if the isotactic pentad fraction of the boiling heptane insoluble portion is 0.955 or more, the content of the boiling heptane soluble portion is 9.0. If the amount of polypropylene exceeds the weight percentage, it is impossible to obtain a stretched film with excellent rigidity, which is the object of the present invention. Such polypropylene used in the present invention is, for example, JP-A No. 53-1989, which is filed by the same applicant as the present application and is known before the filing date of the present application.
It can be obtained by the method described in No. 33289. Examples of the bisamide compound in the present invention include methylene bis stearamide, ethylene bis stearamide, hexamethylene bis stearamide, and the like. If the methylene number n of the bisamide compound exceeds 10, problems will occur in terms of compatibility, smoke generation, and odor, so it cannot be used. The amount of bisamide compound added is 0.5 to 5 parts by weight,
Preferably it is 1.0 to 3.0 parts by weight. Various additives such as antioxidants, lubricants, antistatic agents, antiblocking agents, etc. can be appropriately added to the polypropylene used in the present invention. The stretching process in the present invention can be carried out by a method commonly used in industry, such as roll stretching, tenter stretching, tubular stretching, and the like. When a stretched film is produced using the highly crystalline polypropylene specified in the present invention, a film with significantly higher rigidity can be obtained compared to when ordinary polypropylene is used, but there is a problem in that the stretching processability is reduced. There is. However, surprisingly, by adding the bisamide compound of the present invention, stretching processability can be significantly improved without causing a decrease in film stiffness. The effects of the present invention will be explained below with reference to Examples, but the present invention is not limited to these. The physical properties of the films in the Examples were measured by the following test methods. Young's modulus: A test piece with a width of 20 mm was taken from the longitudinal direction (MD) and the transverse direction (TD), and an S-S curve was taken using a tensile tester at a chuck interval of 60 mm and a tensile speed of 5 mm/min to measure the initial elastic modulus. . Example 1 The melt index was 2.2 g/10 min, and the isotactic pentad fraction of the insoluble part of boiling heptane was
0.967, the content of boiling heptane soluble part is 4.5% by weight
2.0 parts by weight of ethylene bisstearoamide as a bisamide compound is added and mixed to 100 parts by weight of highly crystalline polypropylene, and after pelletizing with a granulator, melt extrusion is performed at a resin temperature of 280°C, and then cooled to 30°C. A sheet with a thickness of 0.8 mm was obtained by rapidly cooling with a roll. The obtained sheet was stretched 4 times in the longitudinal direction at a stretching temperature of 140°C and 10 times in the transverse direction at a stretching temperature of 155°C at a predetermined stretching speed using a tenter-type sequential biaxial stretching device, followed by heat treatment at 140°C. By doing this, a biaxially stretched film with a thickness of about 20 μm was obtained. Comparative Example 1 A biaxially stretched film was prepared in the same manner as in Example 1 without adding a bisamide compound to the highly crystalline polypropylene in Example 1. Comparative example 2 Melt index as polypropylene
2.4 g/10 minutes, using polypropylene with an isotactic pentad fraction of boiling heptane insoluble part of 0.940 and a boiling heptane soluble part content of 7.5% by weight, and the same as Example 1 except that no bisamide compound was added. A biaxially stretched film was prepared by the method described in the following. Table 1 shows the stretchability and film properties in Example 1 and Comparative Examples 1 and 2 above.
【表】
注(1) ○:延伸状態良好 △:延伸ムラ発生
×:膜破れ発生
第1表に示す如く、本発明による実施例1では
比較例2に比べ著るしく剛性の高い延伸フイルム
が得られており、また比較例1に較べ延伸加工性
が大幅に改善されていることがわかる。[Table] Note (1) ○: Good stretching condition △: Stretching unevenness occurred ×: Film tearing As shown in Table 1, in Example 1 according to the present invention, the stretched film had significantly higher rigidity than Comparative Example 2. It can also be seen that the stretchability is significantly improved compared to Comparative Example 1.
Claims (1)
タツド分率が0.955以上でかつ沸騰ヘプタン可溶
部の含有率が9.0重量%以下である高結晶性ポリ
プロピレン100重量部に対して、一般式 RCONH(CH2)nNHCOR (ここでRは炭素数11〜21の脂肪族炭化水素基、
nは1〜10の整数を表わす。) で表わされるビスアマイド化合物を0.5〜5重量
部添加してなる配合物を少なくとも一軸方向に延
伸することを特徴とする剛性の優れたポリプロピ
レン延伸フイルムの製造方法。[Scope of Claims] 1. Based on 100 parts by weight of highly crystalline polypropylene, the isotactic pentad fraction of the boiling heptane insoluble part is 0.955 or more and the content of the boiling heptane soluble part is 9.0% by weight or less, General formula RCONH(CH 2 ) nNHCOR (where R is an aliphatic hydrocarbon group having 11 to 21 carbon atoms,
n represents an integer from 1 to 10. 1. A method for producing a polypropylene stretched film with excellent rigidity, which comprises stretching in at least one direction a blend obtained by adding 0.5 to 5 parts by weight of a bisamide compound represented by the following formula.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1785782A JPS58134712A (en) | 1982-02-05 | 1982-02-05 | Manufacture of polypropylene drawing film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1785782A JPS58134712A (en) | 1982-02-05 | 1982-02-05 | Manufacture of polypropylene drawing film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58134712A JPS58134712A (en) | 1983-08-11 |
| JPH0356170B2 true JPH0356170B2 (en) | 1991-08-27 |
Family
ID=11955323
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1785782A Granted JPS58134712A (en) | 1982-02-05 | 1982-02-05 | Manufacture of polypropylene drawing film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58134712A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6114258A (en) * | 1984-06-29 | 1986-01-22 | Mitsubishi Petrochem Co Ltd | Resin composition with improved moldability |
-
1982
- 1982-02-05 JP JP1785782A patent/JPS58134712A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58134712A (en) | 1983-08-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6037417A (en) | Polypropylene composition useful for making solid state oriented film | |
| US6733898B2 (en) | Resin compositions for producing biaxially oriented polypropylene films | |
| US4514534A (en) | Modified polypropylene for film | |
| US3969304A (en) | Ethylene polymer films | |
| US4554321A (en) | Film compositions of butene polymers | |
| EP0343943A2 (en) | A composition comprising polymers of but-1-ene and propylene | |
| US20070167576A1 (en) | Resin compositions for producing biaxially oriented polypropylene films | |
| JPH08198913A (en) | Polypropylene film | |
| US6583254B2 (en) | Propylene-based polymer and film made of the same | |
| CA2600256C (en) | In-reactor produced polypropylene blends | |
| JPH0378250B2 (en) | ||
| JPH0356170B2 (en) | ||
| US5369181A (en) | Olefinic polymer blends for improving polyolefins | |
| EP4331800A1 (en) | Process for recycling propylene based polymers | |
| JPH0739517B2 (en) | Resin composition for shrink film | |
| JP3029483B2 (en) | Highly crystalline polypropylene biaxially stretched film | |
| JPH0356169B2 (en) | ||
| JPS63113059A (en) | Shrink packaging film | |
| JPH04361019A (en) | High crystalline polypropylene biaxially oriented film | |
| JPH08192462A (en) | Opaque stretched film | |
| JPS599207A (en) | Drawn tape | |
| JPS64988B2 (en) | ||
| JPS60149433A (en) | Biaxially stretched polypropylene film | |
| JPH01198650A (en) | Polypropylene resin composition | |
| JPS58134138A (en) | Drawn antistatic polypropylene film |