JPS60149434A - Biaxially stretched polypropylene film - Google Patents

Biaxially stretched polypropylene film

Info

Publication number
JPS60149434A
JPS60149434A JP552484A JP552484A JPS60149434A JP S60149434 A JPS60149434 A JP S60149434A JP 552484 A JP552484 A JP 552484A JP 552484 A JP552484 A JP 552484A JP S60149434 A JPS60149434 A JP S60149434A
Authority
JP
Japan
Prior art keywords
less
boiling
hexane
component
biaxially stretched
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
JP552484A
Other languages
Japanese (ja)
Other versions
JPH0425134B2 (en
Inventor
Takeo Inoue
武夫 井上
Keigo Suehiro
末広 啓吾
Hiroyuki Doi
博之 土井
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 JP552484A priority Critical patent/JPS60149434A/en
Publication of JPS60149434A publication Critical patent/JPS60149434A/en
Publication of JPH0425134B2 publication Critical patent/JPH0425134B2/ja
Granted legal-status Critical Current

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  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain a biaxially stretched polypropylene film which is greatly improved in rigidity, transparency, and oil resistance from a polypropylene resin composition having a specific solvent solubility, a specific viscosity, and a specific molecular weight distribution. CONSTITUTION:A polypropylene resin composition, containing 1.0wt% or less soluble in component A with 1.0wt% or less soluble in component B of insoluble in the component A, and 0.8wt% or less soluble in the component C of insoluble in the component B when boiling diethylether (A), boiling n-hexane (B), and boiling n-heptane (C) are used for a consecutive extraction, where the solubles have each intrinsic viscosities of 0.5dl/g or less, 0.4dl/g or less, and 0.3dl/g or less and a molecular weight distribution MW/MN is less than a given value, is molded into the desired film.

Description

【発明の詳細な説明】 本発明は、剛性、透明性、耐油性に優れたポリプロピレ
ンニ軸延伸フィルムに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a biaxially stretched polypropylene film having excellent rigidity, transparency, and oil resistance.

ポリプロピレンニ軸延伸フィルムは、引張強度、剛性、
透明性に優れ、耐油性、電気的性質にも優れているため
、各種包装用フィルムとして、またコンデンサーなどの
電気部品などの用途に広く使用されている。
Polypropylene biaxially stretched film has high tensile strength, stiffness,
Because it has excellent transparency, oil resistance, and electrical properties, it is widely used as a variety of packaging films and for electrical parts such as capacitors.

一方、最近では、上述したポリプロピレンニ軸延伸フィ
ルムの優れた物性を一段と向上させたいという要望が強
く、例えば煙草包装分野ではセロハンからポリプロピレ
ンニ軸延伸フィルムに切り替えるに当り、更に、剛性、
透明性の改良が要望されている。また、例えばコンデン
サーフィルムとしても一段と耐油性の向上が望まれてい
る。
On the other hand, recently there has been a strong desire to further improve the excellent physical properties of the above-mentioned polypropylene biaxially oriented film. For example, in the cigarette packaging field, when switching from cellophane to polypropylene biaxially oriented film, there has been a strong desire to further improve the physical properties of polypropylene biaxially oriented film.
Improvements in transparency are requested. Further, it is desired to further improve oil resistance, for example, as a capacitor film.

本発明者らは、かかる点に鑑み鋭意検討した結果、特定
の物性を有するポリプロピレン樹脂組成物を使用したな
らば、得られるポリプロピレンニ軸延伸フィルムが剛性
、透明性、耐油性に一段とすぐれたものになることを見
出し、本発明に到達した。
The inventors of the present invention have made extensive studies in view of these points, and have found that if a polypropylene resin composition having specific physical properties is used, the resulting biaxially stretched polypropylene film will have even better rigidity, transparency, and oil resistance. The present invention was achieved by discovering that

即ち、本発明は、 ■ 沸騰ジエチルエーテル、沸騰n−ヘキサン及び沸騰
n−へブタンによる逐次抽出において、沸騰ジエチルエ
ーテル可溶物が1.0重量%以下、沸騰ジエチルエーテ
ル不溶物中の沸騰n−ヘキサン可溶物が10重量%以下
、沸騰n−ヘキサン不溶物中の沸騰n−へブタン可溶物
が08重量%以下であり、 ■ 前記■の可溶物の極限粘度〔η〕がそれぞれ0、5
 d l/jJ以下、0.4 dl/、9以下、及び0
.3dl 7g以下であり、 ■ 分子量分布Mw/I屯が5以下 であるポリプロピレン樹脂組成物を使用してなるポリプ
ロピレンニ軸延伸フィルムである。
That is, in the present invention, (1) In sequential extraction with boiling diethyl ether, boiling n-hexane, and boiling n-hexane, boiling diethyl ether soluble matter is 1.0% by weight or less, boiling diethyl ether insoluble matter contains boiling n- The hexane soluble matter is 10% by weight or less, the boiling n-hebutane soluble matter in the boiling n-hexane insoluble matter is 08% by weight or less, and the intrinsic viscosity [η] of the soluble material in (2) above is 0. ,5
d l/jJ or less, 0.4 dl/, 9 or less, and 0
.. It is a polypropylene biaxially stretched film made using a polypropylene resin composition having a molecular weight distribution Mw/I ton of 5 or less.

本発明における沸騰ジエチルエーテル、沸騰n−ヘキサ
ン、及び沸騰n−へブタンによる逐次抽出法とは次のと
おりである。
The sequential extraction method using boiling diethyl ether, boiling n-hexane, and boiling n-hebutane in the present invention is as follows.

ポリプロピレン樹脂組成物試料5gを160℃のテトラ
リン500m1に完全に溶解したのち、6時間をかけて
徐々に20℃まで冷却し、次いでアセトン1.57を加
え、ポリプロピレンを完全に析出させ、沢過、乾燥する
After completely dissolving 5 g of a polypropylene resin composition sample in 500 ml of tetralin at 160°C, it was gradually cooled to 20°C over 6 hours, and then 1.57 g of acetone was added to completely precipitate the polypropylene. dry.

得られたポリプロピレン粉末をまずジエチルエーテル1
20m1で6時間ソックスレー抽出し、不溶分と可溶分
に分離する。次いで沸騰ジエチルエーテル不溶分をη、
−ヘキサン120m1で13時間ソックスレー抽出し、
不溶分と可溶分に分離する。
The obtained polypropylene powder was first diluted with diethyl ether 1
Soxhlet extraction was performed using 20ml for 6 hours to separate insoluble and soluble components. Then boiling diethyl ether insoluble matter is η,
- Soxhlet extraction with 120 ml hexane for 13 hours,
Separate into insoluble and soluble components.

最後に沸騰n−へキサン不溶分をn−へブタン120m
Aで13時間ソックスレー抽出して不溶分と可溶分に分
離する。
Finally, remove the insoluble matter from boiling n-hexane with 120ml of n-hebutane.
A Soxhlet extraction was performed for 13 hours to separate insoluble and soluble components.

本発明(Cおいては、上記各種沸騰溶剤可溶物の割合お
よび165℃テトラリン中で測定した極限粘度〔η〕(
以下、単に〔η〕と記す。)が特定の範囲にあることが
必要である。
In the present invention (C), the ratio of the above-mentioned various boiling solvent soluble substances and the intrinsic viscosity [η] (
Hereinafter, it will be simply written as [η]. ) must be within a certain range.

即ち、可溶物の割合については、沸騰ジエチルエーテル
可溶物は1.0重量%以下、沸騰ジエチルエーテル不溶
物中の沸騰n−ヘキサン可溶物は10重量%以下、沸騰
n−ヘキサン不溶物中の沸騰n−へブタン可溶物は08
重量%以下である。
That is, regarding the proportion of soluble matter, boiling diethyl ether soluble matter is 1.0% by weight or less, boiling n-hexane soluble matter in boiling diethyl ether insoluble matter is 10% by weight or less, boiling n-hexane insoluble matter The boiling n-hebutane solubles in it are 08
% by weight or less.

これらの範囲をはずれる場合は、二軸延伸フィルムの剛
性及び耐油性が充分でない。
If it is outside these ranges, the biaxially stretched film will not have sufficient rigidity and oil resistance.

また、各可溶物の〔η〕は、沸騰ジエチルエーテル可溶
分で0.5 dl /ji以下、沸騰n−ヘキサン可溶
分でo4dn/、!i’以下、沸騰n−へブタン可溶分
で0.3 dl/ji以下である。これらの範囲をはず
れる場合は、二軸延伸フィルムの透明性が充分でない。
Moreover, [η] of each soluble substance is 0.5 dl/ji or less for boiling diethyl ether soluble content, and o4dn/ for boiling n-hexane soluble content! i' or less, boiling n-hebutane soluble content is 0.3 dl/ji or less. If it is outside these ranges, the biaxially stretched film will not have sufficient transparency.

本発明においては、分子量分布+Vlψ感はゲルパーミ
ェーションクロマトグラフィーにより、単分散ポリエチ
レン分子量基準で分子量校正を行なってめた。
In the present invention, the molecular weight distribution + Vlψ feeling was determined by gel permeation chromatography, and the molecular weight was calibrated using a monodisperse polyethylene molecular weight standard.

本発明ではこの否/嘉の値が5以下であることが必要で
あり、この値が5を越える場合は透明性が不充分となる
In the present invention, it is necessary that the value of the ratio is 5 or less, and if this value exceeds 5, the transparency will be insufficient.

メルトフローインデックスMI (ASTM D−12
38−65Tに準じ、温度230℃、荷重216に9で
測定した値)については、特に限定されないが、好まし
くは05〜10!9/10分、特に好ましくは1.0〜
4.o、9/1o分である。MIの値が0.5g710
分未満の場合は、製膜性が不良であり、MIの値が10
g710分をこえると、二軸延伸フィルムの強度が不充
分となる。
Melt Flow Index MI (ASTM D-12
38-65T, at a temperature of 230°C and a load of 216 to 9) is not particularly limited, but is preferably 05 to 10!9/10 minutes, particularly preferably 1.0 to
4. o, 9/1o minutes. MI value is 0.5g710
If it is less than 10 minutes, the film forming property is poor and the MI value is 10 minutes.
If the time exceeds 710 minutes, the strength of the biaxially stretched film will be insufficient.

本発明に使用するポリプロピレンの製造方法は、以上述
べた物性を満足すれば特に限定されないが、−例として
、四塩化チタンをジエチルアルミニウムクロライドで遣
元したのち、ジイソアミルエーテルで処理し、更に四塩
化チタンで処理した三塩化チタン組成物触媒と有機アル
ミニウム化合物(例えばジエチルアルミニウムクロライ
ド)及び必要により第3成分(例えばエーテル、エステ
ル、ホスファイト化合物等)とからなる組み合せの触媒
系で重合したポリプロピレンを分子量減成する方法があ
げられる。
The method for producing polypropylene used in the present invention is not particularly limited as long as it satisfies the physical properties described above, but as an example, titanium tetrachloride is treated with diethylaluminum chloride, then treated with diisoamyl ether, and then Polypropylene polymerized with a catalyst system consisting of a titanium trichloride composition catalyst treated with titanium chloride, an organoaluminum compound (e.g. diethylaluminum chloride) and optionally a third component (e.g. ether, ester, phosphite compound, etc.) One example is a method of reducing molecular weight.

本発明では、ポリプロピレン樹脂組成物に通常使用され
る酸化防止剤、紫外線吸収剤、アンチブロッキング剤、
スリップ剤、帯電防止剤、着色剤等を添加し、Tダイ等
でフィルムにされたのち、通常行なわれる2段延伸ある
いは二軸同時延伸などにより、二軸延伸フィルムとされ
る。
In the present invention, antioxidants, ultraviolet absorbers, anti-blocking agents, commonly used in polypropylene resin compositions,
After adding a slip agent, an antistatic agent, a coloring agent, etc., the film is made into a film using a T-die or the like, and then a biaxially stretched film is obtained by conventional two-stage stretching or simultaneous biaxial stretching.

以下、実施例により本発明を更に詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

フィルム物性は下記により測定した。The physical properties of the film were measured as follows.

ヘイズ : A、STM D−1003−53に準する
Haze: A, according to STM D-1003-53.

ヤング率 :幅2Qmmの試験片を、縦方向(MD)及
び横方向(TD)よりサンプリング し、引張り試験機にてチャック間隔 示す。
Young's modulus: A test piece with a width of 2 Qmm was sampled from the longitudinal direction (MD) and the transverse direction (TD), and the chuck interval was measured using a tensile tester.

引張強さ : A、STM D−882−64Tによる
Tensile strength: A, according to STM D-882-64T.

耐油性 : 5cm×5Cmx 2 fkμのフィルム
をJIS 1号オイルに80℃X 24 hr浸漬した
後に取り出し、JIS 1号オイルで洗浄、乾燥する。
Oil resistance: A film of 5 cm x 5 cm x 2 fkμ is immersed in JIS No. 1 oil at 80°C for 24 hours, then taken out, washed with JIS No. 1 oil, and dried.

その時の重量 増加率で示す。weight at that time Expressed as an increase rate.

実施例1〜3、比較例1〜2 第1表に示す物性を有するポリプロピレン樹脂組成物を
Tダイ式製膜機を用い、250℃で押出し、50℃の冷
却ロールで冷却して、厚さ750μmのシートを作成し
た。このシートをTMロンク二軸延伸機により、150
℃で縦方向(MD)に5倍、次いで横方向(TD、) 
VC7倍延伸したのち、熱固定して厚さ25μmの二軸
延伸フィルムを得た。
Examples 1 to 3, Comparative Examples 1 to 2 A polypropylene resin composition having the physical properties shown in Table 1 was extruded at 250°C using a T-die film forming machine, and cooled with a cooling roll at 50°C to determine the thickness. A sheet of 750 μm was prepared. This sheet was processed by TM Ronc biaxial stretching machine to 150
5x in longitudinal direction (MD) then transverse direction (TD, ) at °C.
After stretching 7 times the VC, the film was heat-set to obtain a biaxially stretched film with a thickness of 25 μm.

このフィルムの物性を測定し、その結果を第1表に示す
The physical properties of this film were measured and the results are shown in Table 1.

Claims (1)

【特許請求の範囲】 ■ 沸騰ジエチルエーテル、沸騰n−ヘキサン及び沸騰
n−へブタンによる逐次抽出において、沸騰ジエチルエ
ーテル可溶物が10重量%以下、沸騰ジエチルエーテル
不溶物中の沸騰n−ヘキサン可溶物が1.0重t%以下
、沸騰n−ヘキサン不溶物中の沸騰n−へブタン可溶物
が08重量%以下であり、 ■ 前記■の可溶物の極限粘度〔η〕がそれぞれ0.5
dl1717以下、0.4 dn /17以下、及び0
3dl1g以下であり、 ■ 分子量分布& /r6が5以下 であるポリプロピレン樹脂組成物を使用してなるポリプ
ロピレンニ軸延伸フィルム。
[Claims] ■ In sequential extraction with boiling diethyl ether, boiling n-hexane and boiling n-hexane, boiling diethyl ether soluble matter is 10% by weight or less, boiling n-hexane in boiling diethyl ether insoluble matter is possible. The dissolved material is 1.0% by weight or less, the boiling n-hebutane soluble material in the boiling n-hexane insoluble material is 0.8% by weight or less, and the intrinsic viscosity [η] of the soluble material in (2) above is respectively 0.5
dl1717 or less, 0.4 dn /17 or less, and 0
3dl1g or less, and (1) a biaxially stretched polypropylene film using a polypropylene resin composition having a molecular weight distribution &/r6 of 5 or less.
JP552484A 1984-01-18 1984-01-18 Biaxially stretched polypropylene film Granted JPS60149434A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP552484A JPS60149434A (en) 1984-01-18 1984-01-18 Biaxially stretched polypropylene film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP552484A JPS60149434A (en) 1984-01-18 1984-01-18 Biaxially stretched polypropylene film

Publications (2)

Publication Number Publication Date
JPS60149434A true JPS60149434A (en) 1985-08-06
JPH0425134B2 JPH0425134B2 (en) 1992-04-30

Family

ID=11613574

Family Applications (1)

Application Number Title Priority Date Filing Date
JP552484A Granted JPS60149434A (en) 1984-01-18 1984-01-18 Biaxially stretched polypropylene film

Country Status (1)

Country Link
JP (1) JPS60149434A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6369501A (en) * 1986-09-09 1988-03-29 Mitsui Toatsu Chem Inc Device for successively extracting and separating crystalline polymer
EP0298730A1 (en) * 1987-07-08 1989-01-11 COURTAULDS FILMS & PACKAGING (HOLDINGS) LTD. Oriented polypropylene films
EP0298731A1 (en) * 1987-07-08 1989-01-11 COURTAULDS FILMS & PACKAGING (HOLDINGS) LTD. Voided polypropylene films

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6369501A (en) * 1986-09-09 1988-03-29 Mitsui Toatsu Chem Inc Device for successively extracting and separating crystalline polymer
EP0298730A1 (en) * 1987-07-08 1989-01-11 COURTAULDS FILMS & PACKAGING (HOLDINGS) LTD. Oriented polypropylene films
EP0298731A1 (en) * 1987-07-08 1989-01-11 COURTAULDS FILMS & PACKAGING (HOLDINGS) LTD. Voided polypropylene films
WO1989000105A1 (en) * 1987-07-08 1989-01-12 Courtaulds Films & Packaging (Holdings) Ltd Voided polypropylene films
WO1989000104A1 (en) * 1987-07-08 1989-01-12 Courtaulds Films & Packaging (Holdings) Ltd Oriented polypropylene films

Also Published As

Publication number Publication date
JPH0425134B2 (en) 1992-04-30

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