JP3259588B2 - Heat and moisture proof film - Google Patents

Heat and moisture proof film

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Publication number
JP3259588B2
JP3259588B2 JP09791595A JP9791595A JP3259588B2 JP 3259588 B2 JP3259588 B2 JP 3259588B2 JP 09791595 A JP09791595 A JP 09791595A JP 9791595 A JP9791595 A JP 9791595A JP 3259588 B2 JP3259588 B2 JP 3259588B2
Authority
JP
Japan
Prior art keywords
film
heat
resin
moisture
layer
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
JP09791595A
Other languages
Japanese (ja)
Other versions
JPH08269213A (en
Inventor
文雄 緒方
茂 田中
伸夫 鈴井
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.)
Toray Industries Inc
Original Assignee
Toray Industries 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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP09791595A priority Critical patent/JP3259588B2/en
Publication of JPH08269213A publication Critical patent/JPH08269213A/en
Application granted granted Critical
Publication of JP3259588B2 publication Critical patent/JP3259588B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Wrappers (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Laminated Bodies (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、耐熱性と防湿性を合わ
せ持った、包装用に好適な耐熱防湿フイルムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat and moisture resistant film having both heat resistance and moisture resistance and suitable for packaging.

【0002】[0002]

【従来の技術】従来、ポリプロピレンに石油樹脂および
テルペン樹脂を添加すると、ヤング率や防湿性を向上さ
せることが知られている(特公平1−25503号、特
公平3−31347号公報等)。またポリプロピレンに
石油樹脂およびテルペン樹脂を添加したフイルム上に金
属蒸着およびポリ塩化ビニリデン系樹脂が積層して、防
湿性をさらに向上させることが知られている(特公平2
−27940号、特公平5−1138号公報等)。
2. Description of the Related Art It has been known that the addition of petroleum resin and terpene resin to polypropylene improves Young's modulus and moisture resistance (Japanese Patent Publication No. 1-25033, Japanese Patent Publication No. 3-31347). It is also known that metal vapor deposition and polyvinylidene chloride-based resin are laminated on a film obtained by adding a petroleum resin and a terpene resin to polypropylene to further improve the moisture-proof property (Japanese Patent Publication No. Hei 2 (1994)).
-27940, Japanese Patent Publication No. 5-1138, etc.).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、ポリプ
ロピレンに石油樹脂およびテルペン樹脂を添加するとヤ
ング率や防湿性は向上するが、石油樹脂やテルペン樹脂
が低軟化点であるため、これらを添加したフイルムは寸
法安定性に劣り、フイルムをロール状に巻いた時に巻締
まりが起こって平面性が悪化する。また熱収縮率が大き
いために加工時の工程安定性に劣るという問題があっ
た。
However, when a petroleum resin and a terpene resin are added to polypropylene, the Young's modulus and moisture resistance are improved. However, since the petroleum resin and the terpene resin have a low softening point, the film to which these are added cannot be used. It is inferior in dimensional stability, and when the film is wound into a roll, tightening occurs and the flatness deteriorates. In addition, there is a problem that the process stability during processing is inferior due to a large heat shrinkage.

【0004】また、該フイルムに金属を蒸着してさらに
防湿性を付与させようとしたときに、蒸着時の熱でフイ
ルムが収縮して金属蒸着面にクラックが入り、防湿性が
上がらないという問題があった。
Further, when a metal is vapor-deposited on the film to give it a further moisture-proof property, the film is shrunk by heat at the time of vapor deposition, cracks are formed on the metal-deposited surface, and the moisture-proof property is not improved. was there.

【0005】さらに、ポリ塩化ビニリデン系樹脂をコー
ティングしてさらに防湿性を付与させようとしたとき
に、コーティング後の乾燥時の熱でフイルムが収縮して
コーティング樹脂層に亀裂が入ったり、またポリプロピ
レンフイルムとの界面接着力が低下して、防湿性が上が
らないという問題があった。
Further, when a polyvinylidene chloride-based resin is coated to further impart moisture-proof properties, the film shrinks due to the heat of drying after coating, causing cracks in the coating resin layer, and polypropylene. There was a problem that the interfacial adhesive strength with the film was lowered and the moisture resistance was not improved.

【0006】本発明は、上記従来の欠点を解消すべくな
されたものであり、耐熱性と防湿性および製膜時の厚み
むらに優れ、かつ印刷および蒸着加工時の寸法安定性に
も優れたフイルムを提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned conventional disadvantages, and has excellent heat resistance, moisture resistance and thickness unevenness during film formation, and excellent dimensional stability during printing and vapor deposition. The purpose is to provide a film.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の耐熱防湿フイルムは、125℃での等温結
晶化時間が3.5分以下、アイソタクチックインデック
スが98.5%以上、メルトフローインデックスが2〜
4g/10分の結晶性ポリプロピレン70〜95重量%
に、極性基を実質的に含まない石油樹脂および極性基を
実質的に含まないテルペン樹脂の1種以上が5〜30重
量%混合されたフイルムであって、120℃、15分加
熱での長手方向の熱収縮率が5%以下であり、水蒸気透
過率が1.0(g/m2 ・24hr/0.1mm)以下
であることを特徴とするものからなる。
In order to achieve the above object, the heat and moisture resistant film of the present invention has an isothermal crystallization time at 125 ° C. of 3.5 minutes or less and an isotactic index of 98.5% or more. , Melt flow index is 2
4 g / 10 minutes of crystalline polypropylene 70 to 95% by weight
A film in which at least one kind of a petroleum resin substantially free of a polar group and a terpene resin substantially free of a polar group is mixed at 5 to 30% by weight, and heated at 120 ° C. for 15 minutes. The thermal contraction rate in the direction is 5% or less, and the water vapor transmission rate is 1.0 (g / m 2 · 24 hr / 0.1 mm) or less.

【0008】また、本発明に係る耐熱防湿フイルムは、
上記の耐熱防湿フイルム(以下、A層と言うこともあ
る。)の少なくとも片面に、アイソタクチックインデッ
クスが98%以下の結晶性ポリプロピレンを積層(以
下、B層と言うこともある。)してなることを特徴とす
るものからなる。
Further, the heat and moisture resistant film according to the present invention comprises:
A crystalline polypropylene having an isotactic index of 98% or less is laminated on at least one surface of the heat-resistant and moisture-proof film (hereinafter sometimes referred to as a layer A) (hereinafter sometimes referred to as a layer B). Characterized by the following.

【0009】本発明のA層の結晶性ポリプロピレンは、
125℃での等温結晶化時間(以下t−1/2と略称す
ることもある。)は3.5分以下で、かつアイソタクチ
ックインデックス(以下IIと略称することもある。)
が98.5%以上であることが必要である。t−1/2
が3.5分を越え、IIが98.5%未満ではフイルム
の結晶化度が上がらず、120℃、15分加熱での長手
方向の熱収縮率が5%以上になるので好ましくなく、ま
た耐有機溶剤性も悪化するので好ましくない。またメル
トフローインデックス(MFI)を2〜4g/10分の
範囲とすることにより、石油樹脂および/またはテルペ
ン樹脂の分散性が良くなり、製膜性および防湿性も良く
なる。また、プロピレン以外の第2成分、例えばエチレ
ン、ブテン、ヘキセンなどを少量ランダムに共重合させ
てもよい。また、公知の添加剤、例えば結晶核剤、酸化
防止剤、熱安定剤、すべり剤、帯電防止剤、ブロッキン
グ防止剤、充填剤、粘度調整剤、着色防止剤などを適量
含有させてもよい。
The crystalline polypropylene of the layer A of the present invention comprises:
The isothermal crystallization time at 125 ° C. (hereinafter sometimes abbreviated as t- /) is 3.5 minutes or less, and the isotactic index (hereinafter sometimes abbreviated as II).
Should be 98.5% or more. t-1 / 2
If it exceeds 3.5 minutes and II is less than 98.5%, the crystallinity of the film does not increase, and the heat shrinkage in the longitudinal direction at 120 ° C. for 15 minutes becomes 5% or more, which is not preferable. It is not preferable because the organic solvent resistance is also deteriorated. When the melt flow index (MFI) is in the range of 2 to 4 g / 10 minutes, the dispersibility of the petroleum resin and / or the terpene resin is improved, and the film forming property and the moisture resistance are also improved. Further, a small amount of a second component other than propylene, for example, ethylene, butene, hexene or the like may be randomly copolymerized. In addition, known additives such as a crystal nucleating agent, an antioxidant, a heat stabilizer, a slipping agent, an antistatic agent, an antiblocking agent, a filler, a viscosity modifier, and a coloring inhibitor may be contained in appropriate amounts.

【0010】本発明において、結晶性ポリプロピレンに
混合される極性基を実質的に含まない石油樹脂とは、水
酸基、カルボキシル基、ハロゲン基、スルホン基および
それらの変成体などからなる極性基を有さない石油樹
脂、即ち石油系不飽和炭化水素を直接原料とするシクロ
ペンタジエン系、或は高級オレフィン系炭化水素を主原
料とする樹脂である。
In the present invention, the petroleum resin which does not substantially contain a polar group and is mixed with the crystalline polypropylene has a polar group comprising a hydroxyl group, a carboxyl group, a halogen group, a sulfone group and a modified product thereof. No petroleum resin, that is, a resin that is mainly made of a cyclopentadiene-based hydrocarbon or a higher olefin-based hydrocarbon directly using a petroleum unsaturated hydrocarbon as a raw material.

【0011】かかる極性基を実質的に含まない石油樹脂
のガラス転移点温度(以下、Tgと略称する)は、60
℃以上であることが好ましい。Tgが60℃未満では、
防湿性の向上効果が小さい。
The glass transition temperature (hereinafter abbreviated as Tg) of a petroleum resin substantially free of such a polar group is 60
It is preferable that the temperature is not lower than ° C. When Tg is less than 60 ° C,
The effect of improving the moisture resistance is small.

【0012】また、かかる石油樹脂に水素を添加し、そ
の水素添加率を90%以上、好ましくは99%以上とし
た水添石油樹脂が本発明の耐熱防湿フイルムに特に望ま
しい。代表的な水素添加石油樹脂としては、例えばTg
70℃以上で水添率99%以上のポリジシクロペンタジ
エン等の高Tg完全水添脂環族石油樹脂を挙げることが
できる。
A hydrogenated petroleum resin obtained by adding hydrogen to such a petroleum resin and having a hydrogenation ratio of 90% or more, preferably 99% or more, is particularly desirable for the heat and moisture resistant film of the present invention. Typical hydrogenated petroleum resins include, for example, Tg
High Tg completely hydrogenated alicyclic petroleum resins such as polydicyclopentadiene having a hydrogenation ratio of 99% or more at 70 ° C. or more can be given.

【0013】また、極性基を実質的に含まないテルペン
樹脂とは、水酸基、アルデヒド基、ケトン基、カルボキ
シル基、ハロゲン基、スルホン基およびそれらの変成体
などからなる極性基を有さないテルペン樹脂、即ち(C
5 8 )nの組成の炭化水素およびこれから導かれる変
性化合物である。nは2〜20程度の自然数である。
The term "terpene resin containing substantially no polar group" refers to a terpene resin having no polar group, such as a hydroxyl group, an aldehyde group, a ketone group, a carboxyl group, a halogen group, a sulfone group or a modified form thereof. , Ie (C
5 H 8) is a hydrocarbon and now modified compound derived composition of n. n is a natural number of about 2 to 20.

【0014】テルペン樹脂のことをテルペノイドと呼ぶ
こともあり、代表的な化合物としては、ピネン、ジペン
テン、カレン、ミルセン、オシメン、リモネン、テレピ
ノレン、テルピネン、サビネン、トリシクレン、ビサボ
レン、ジンギペレン、サンタレン、カンホレン、ミレ
ン、トタレン等があり、本発明のフイルムの場合、水素
を添加し、その水素添加率を90%以上、好ましくは9
9%以上とするのが望ましく、特にβ−ピネン、水素β
−ピネン、水添β−ジペンテン等が好ましい。
The terpene resin is sometimes referred to as a terpenoid, and typical compounds include pinene, dipentene, karen, myrcene, osimene, limonene, terpinolene, terpinene, sabinene, tricyclene, bisabolene, zingiperene, santalen, camphorene, There are millen and totalene, and in the case of the film of the present invention, hydrogen is added and the hydrogenation rate is 90% or more, preferably 9%.
9% or more, particularly β-pinene, hydrogen β
-Pinene, hydrogenated β-dipentene and the like are preferred.

【0015】このように、極性基を実質的に含まない石
油樹脂および極性基を実質的に含まないテルペン樹脂の
1種以上の使用が本発明の場合重要であり、臭素価とし
て10以下、好ましくは5以下、更に好ましくは1以下
のものが良い。
As described above, the use of at least one of a petroleum resin substantially free of a polar group and a terpene resin substantially free of a polar group is important in the present invention. Is preferably 5 or less, more preferably 1 or less.

【0016】本発明のフイルム中に含まれる前記極性基
を実質的に含まない石油樹脂および極性基を実質的に含
まないテルペン樹脂の1種以上の混合量は、前記結晶性
ポリプロピレン70〜95重量%に対して、5〜30重
量%であることが必要である。特に10〜20重量%で
あることが好ましい。該樹脂の混合量が5重量%未満で
は防湿性の向上がみられず、30重量%を超えると、耐
熱性が悪化するのみならず、表層にブリードアウトし
て、積層樹脂の接着力および金属蒸着の密着力が低下す
るので好ましくない。
The amount of at least one of the petroleum resin substantially free of the polar group and the terpene resin substantially free of the polar group contained in the film of the present invention is 70 to 95% by weight of the crystalline polypropylene. % To 5% by weight. In particular, it is preferably from 10 to 20% by weight. If the amount of the resin is less than 5% by weight, the moisture-proof property is not improved, and if it exceeds 30% by weight, not only the heat resistance is deteriorated, but also the resin bleeds out to the surface layer, and the adhesive strength of the laminated resin and metal It is not preferable because the adhesion of the deposition is reduced.

【0017】また、本発明のフイルムは、120℃、1
5分加熱での長手方向の熱収縮率が5%以下であること
が必要であり、好ましくは3%以下である。長手方向の
熱収縮率が5%を超えると、フイルムをロール状に巻い
た時に巻締まりが起こって平面性が悪化し、また熱収縮
率が大きいために、印刷後の印字のピッチずれや、粘着
剤塗布やラミネート加工時にシワが発生して工程安定性
に劣る。
The film of the present invention has a temperature of 120.degree.
The heat shrinkage in the longitudinal direction after heating for 5 minutes needs to be 5% or less, preferably 3% or less. When the heat shrinkage in the longitudinal direction exceeds 5%, when the film is wound into a roll, the film is tightened and the flatness is deteriorated. Also, since the heat shrinkage is large, the pitch deviation of the print after printing, Wrinkles occur during application of the adhesive or lamination, resulting in poor process stability.

【0018】また、該フイルムに金属を蒸着してさらに
防湿性を付与させようとしたときに、蒸着時の熱でフイ
ルムが収縮し、また金属蒸着面に押出ラミネートした際
に熱でフイルムが収縮して、金属蒸着面にクラックが入
り、防湿性が上がらない。
Further, when a film is deposited on the film to give a further moisture-proof property, the film shrinks due to the heat during the deposition, and the film shrinks due to the heat when extruded and laminated on the metal deposition surface. As a result, cracks are formed on the metal-deposited surface, and the moisture resistance is not improved.

【0019】さらに、ポリ塩化ビニリデン系樹脂をコー
ティングしてさらに防湿性を付与させようとしたとき
に、コーティング後の乾燥時の熱でフイルムが収縮して
コーティング樹脂層に亀裂が入ったり、またポリプロピ
レンフイルムとの界面接着力が低下して、防湿性が上が
らない。
Furthermore, when a polyvinylidene chloride-based resin is coated to further impart moisture-proof properties, the film shrinks due to the heat of drying after the coating, causing cracks in the coating resin layer and / or polypropylene. The interfacial adhesion to the film is reduced, and the moisture resistance is not improved.

【0020】また本発明のフイルムは、水蒸気透過率が
1.0(g/m2 ・24hr/0.1mm)以下である
必要がある。水蒸気透過率が1.0(g/m2 ・24h
r/0.1mm)を超えると、本フイルムを乾物やポテ
トチップスなどの防湿性を必要とする防湿包装用として
用いたときに、内容物が湿気って内容物保護性に劣る。
さらに防湿性を必要とする用途においては、金属蒸着の
膜厚やポリ塩化ビニリデン系樹脂のコーティング厚みを
厚くする必要があり、価格上昇や着色することが避けら
れない。
The film of the present invention must have a water vapor transmission rate of 1.0 (g / m 2 · 24 hr / 0.1 mm) or less. Water vapor transmission rate of 1.0 (g / m 2 · 24h
(r / 0.1 mm), when the film is used for moisture-proof packaging that requires moisture-proof properties such as dry matter and potato chips, the content is moist and the content-protection is poor.
Further, in applications requiring moisture resistance, it is necessary to increase the film thickness of metal vapor deposition and the coating thickness of polyvinylidene chloride resin, which inevitably leads to an increase in price and coloring.

【0021】本発明のフイルムは、未延伸、一軸延伸、
二軸延伸フイルムのいずれでもよいが、機械的性質、光
学的性質、熱的性質および防湿性などの点から二軸延伸
フイルムが好ましい。
The film of the present invention is unstretched, uniaxially stretched,
Although any of biaxially stretched films may be used, biaxially stretched films are preferred from the viewpoints of mechanical properties, optical properties, thermal properties, moisture resistance and the like.

【0022】次に、本発明の耐熱防湿フイルム(A層)
の少なくとも片面に積層されるB層の樹脂は、アイソタ
クチックインデックス(II)が98%以下の結晶性ポ
リプロピレンである。B層の結晶性ポリプロピレンのI
Iが98%を越えると結晶化が高くなって、フイルム表
面の粗さが大きくなり、外部ヘイズが高くなって透明性
が悪化する。また金属蒸着およびポリ塩化ビニリデン系
樹脂などの密着性も悪化する。
Next, the heat- and moisture-proof film of the present invention (layer A)
Is a crystalline polypropylene having an isotactic index (II) of 98% or less. I of crystalline polypropylene in layer B
When I exceeds 98%, the crystallization is increased, the roughness of the film surface is increased, the external haze is increased, and the transparency is deteriorated. In addition, adhesion of metal vapor deposition and polyvinylidene chloride-based resin is also deteriorated.

【0023】また、該B層の結晶性ポリプロピレンに
は、プロピレン以外の第2成分、例えばエチレン、ブテ
ン、ヘキセンなどを少量ランダムに共重合させてもよ
い。また、公知の添加剤、例えば結晶核剤、酸化防止
剤、熱安定剤、すべり剤、帯電防止剤、ブロッキング防
止剤、充填剤、粘度調整剤、着色防止剤などを含有させ
てもよい。
Further, a small amount of a second component other than propylene, for example, ethylene, butene, hexene or the like may be randomly copolymerized with the crystalline polypropylene of the layer B. Further, known additives such as a crystal nucleating agent, an antioxidant, a heat stabilizer, a sliding agent, an antistatic agent, an antiblocking agent, a filler, a viscosity modifier, and a coloring inhibitor may be contained.

【0024】かかる積層されるB層の厚さとしては、1
〜50μmが好ましく、さらに好ましくは2〜30μm
である。この厚さが1μmに満たないと、防湿性および
表層に該水添石油樹脂や水添テルペン樹脂がブリードア
ウトして、金属蒸着およびポリ塩化ビニリデン系樹脂な
どの密着力が低下するのみならず、油物包装時に油のし
みだしを防止する耐油性が低下するので好ましくない。
一方、厚さが50μmを超えると、熱収縮率が大きくな
って耐熱性が悪化し、防湿性も悪化する。
The thickness of the laminated B layer is 1
To 50 μm, more preferably 2 to 30 μm
It is. If the thickness is less than 1 μm, not only the moisture resistance and the hydrogenated petroleum resin or hydrogenated terpene resin bleed out to the surface layer, but also the adhesion of metal vapor deposition and polyvinylidene chloride resin decreases, It is not preferable because oil resistance for preventing oil seepage at the time of packaging of oils is reduced.
On the other hand, when the thickness exceeds 50 μm, the heat shrinkage increases, heat resistance deteriorates, and moisture resistance deteriorates.

【0025】また積層されるB層は、未延伸、一軸延
伸、二軸延伸のいずれでもよいが、機械的性質、光学的
性質、熱的性質および防湿性などの点から、該耐熱防湿
フイルム(A層)の樹脂と共押出して、二軸延伸フイル
ムとするのが好ましい。
The layer B to be laminated may be any of unstretched, uniaxially stretched and biaxially stretched. However, from the viewpoint of mechanical properties, optical properties, thermal properties and moisture resistance, the heat and moisture resistant film ( The biaxially stretched film is preferably co-extruded with the resin of layer A).

【0026】また本発明のフイルムに、印刷、塗工、蒸
着などをするときに、接着力を高めるために、フイルム
表面にコロナ放電処理あるいはプラズマ処理を行なうこ
とが好ましい。コロナ放電処理は公知の方法を用いるこ
とができるが、処理を施す時の雰囲気ガスとして、空
気、炭酸ガス、窒素ガスおよびこれらの混合ガスが好ま
しい。またプラズマ処理は、種々の気体をプラズマ状態
におき、フイルム表面を化学変成させる方法、例えば特
開昭59−98140号公報記載の方法などがある。
When the film of the present invention is printed, coated, vapor-deposited, or the like, it is preferable to perform a corona discharge treatment or a plasma treatment on the film surface in order to increase the adhesive strength. A known method can be used for the corona discharge treatment, but air, carbon dioxide gas, nitrogen gas, and a mixed gas thereof are preferable as the atmosphere gas at the time of the treatment. The plasma treatment includes a method in which various gases are kept in a plasma state to chemically modify the film surface, for example, a method described in JP-A-59-98140.

【0027】さらに、本発明の耐熱防湿フイルム上に金
属蒸着およびポリ塩化ビニリデン系樹脂性をコーティン
グしてさらに防湿性を向上させるときは、通常のフロピ
レンフイルムに比べ、蒸着膜厚およびコーティング厚み
を薄くすることができ、低価格な超防湿フイルムとする
ことができる。
Further, when the metal vapor deposition and the polyvinylidene chloride-based resin are coated on the heat- and moisture-proof film of the present invention to further improve the moisture-proof property, the film thickness and the coating thickness of the vapor-deposited film and the coating thickness are reduced as compared with ordinary propylene film. It can be made thin and can be a low-cost ultra-moisture-proof film.

【0028】蒸着される金属は、アルミニウム、亜鉛、
ケイ素、金、銀などの金属およびこれらの1種以上の金
属化合物およびこれらの金属酸化物である。中でもアル
ミニウムが低価格で経済性がよく好ましい。
The metals to be deposited are aluminum, zinc,
Metals such as silicon, gold, silver and the like, and one or more metal compounds thereof and metal oxides thereof. Among them, aluminum is preferable because of its low cost and good economy.

【0029】ポリ塩化ビニリデン系樹脂としては、特に
限定されるものではなく、塩化ビニリデン単独重合体お
よび塩化ビニリデンの共重合体が含まれる。
The polyvinylidene chloride-based resin is not particularly limited, and includes a homopolymer of vinylidene chloride and a copolymer of vinylidene chloride.

【0030】次に、本発明の耐熱防湿フイルムの製造方
法の一例について述べる。125℃でのt−1/2が
3.5分以下で、IIが98.5%以上、かつ、メルト
フローインデックスが2〜4g/10分の結晶性ポリプ
ロピレンに極性基を実質的に含まない石油樹脂および極
性基を実質的に含まないテルペン樹脂のそれぞれ特定範
囲の混合物からなるA層樹脂を押出機に供給し、樹脂温
度200℃以上、好ましくは220℃〜280℃の温度
で溶融混合した後、T型口金からシート状に押出成形
し、ドラフト比(口金リップ間隙/フイルム厚み)が
1.2以上、好ましくは1.5〜3.0で該シートを2
0〜100℃、好ましくは50〜80℃の温度のドラム
に巻き付けて冷却固化し、次いで、該シートを100〜
150℃に保たれたオーブン中に通して予熱し、引き続
き該シートを80℃〜150℃の温度に保ち周速差を設
けたロール間に通し、長手方向に2〜6倍に延伸し、た
だちに室温に冷却する。引き続き該延伸フイルムをテン
ターに導いて、170℃以下の温度、好ましくは140
〜165℃の温度で幅方向に5〜10倍に延伸し、次い
で幅方向に2〜20%の弛緩を与えつつ、160〜17
0℃の温度で熱固定して巻取る。また、IIが98%以
下の結晶性ポリプロピレンのB層樹脂の積層は、B層の
樹脂をもう1台の押出機に供給して220〜280℃の
温度で溶融した後、多層成形口金にてB層/A層または
B層/A層/B層の構成となるように口金内で合流させ
た後、積層シート状に成形する。また、別の積層方法と
しては、口金の上流の短管内でA層樹脂とB層樹脂とを
合流せしめた後、T型口金でシート状に成形するか、ま
たは上記製膜工程で長手方向に延伸された延伸フイルム
にB層の樹脂を押出ラミネートし、該積層フイルムをテ
ンターに導き、幅方向に延伸される方法が用いられる。
具体的には、B層の樹脂を押出機に供給し、260〜2
80℃の温度で溶融した後、カラス口型の口金にてシー
ト状に溶融押出をし、その溶融シートを5〜50℃の温
度の冷却ロールとゴムロールの間で該長手方向に延伸し
たフイルムと貼り合わせ圧着する。
Next, an example of the method for producing the heat and moisture resistant film of the present invention will be described. The crystalline polypropylene at 125 ° C. has a t-1 / 2 of 3.5 minutes or less, II of 98.5% or more, and a melt flow index of 2 to 4 g / 10 minutes. An A-layer resin composed of a mixture of a specific range of a petroleum resin and a terpene resin substantially free of a polar group was supplied to an extruder and melt-mixed at a resin temperature of 200 ° C or higher, preferably 220 ° C to 280 ° C. Thereafter, the sheet is extruded from a T-shaped die into a sheet, and the sheet is subjected to a draft ratio (lip gap of die / thickness of film) of 1.2 or more, preferably 1.5 to 3.0.
It is wound around a drum at a temperature of 0 to 100 ° C., preferably 50 to 80 ° C., cooled and solidified.
The sheet is preheated by passing it through an oven kept at 150 ° C., and then the sheet is kept at a temperature of 80 ° C. to 150 ° C. and passed between rolls provided with a peripheral speed difference, and stretched 2 to 6 times in the longitudinal direction. Cool to room temperature. Subsequently, the stretched film is guided to a tenter, and a temperature of 170 ° C. or less, preferably 140 ° C.
The film is stretched 5 to 10 times in the width direction at a temperature of 16165 ° C., and then relaxed by 2 to 20% in the width direction,
It is heat-set at a temperature of 0 ° C. and wound. In addition, for lamination of the B layer resin of crystalline polypropylene having II of 98% or less, the resin of the B layer is supplied to another extruder and melted at a temperature of 220 to 280 ° C., and then is formed by a multilayer molding die. After merging in a die so as to have a structure of B layer / A layer or B layer / A layer / B layer, it is formed into a laminated sheet. Further, as another laminating method, after the A-layer resin and the B-layer resin are merged in a short pipe upstream of the die, they are formed into a sheet shape with a T-type die, or in the longitudinal direction in the film forming step. A method is used in which the resin of layer B is extrusion-laminated on the stretched stretched film, the laminated film is guided to a tenter, and stretched in the width direction.
Specifically, the resin of layer B is supplied to an extruder, and
After being melted at a temperature of 80 ° C., it is melt-extruded into a sheet by a crow mouth-type die, and the molten sheet is stretched in the longitudinal direction between a cooling roll and a rubber roll at a temperature of 5 to 50 ° C. Bond and crimp.

【0031】次いで本発明の耐熱防湿フイルムに金属蒸
着をしたフイルムは、例えば真空蒸着機により金属を所
望の膜厚に積層することにより得られる。
Next, a film obtained by vapor-depositing a metal on the heat-resistant and moisture-proof film of the present invention can be obtained, for example, by laminating a metal to a desired film thickness using a vacuum vapor deposition machine.

【0032】また、ポリ塩化ビニリデン系樹脂のコーテ
ィングは、ロールコーター、グラビアロール、ロッドコ
ーター、スプレイコーターなどの通常の方法が使用さ
れ、乾燥はライン速度にもよるが、60℃〜120℃の
オーブンに通して乾燥される。
The coating of the polyvinylidene chloride resin is carried out by a usual method such as a roll coater, a gravure roll, a rod coater, a spray coater and the like. Drying depends on the line speed. And dried.

【0033】本発明のフイルムは、目的に応じて帯電防
止剤、耐候剤、防曇剤、滑り剤などの添加剤を添加、ま
たはコーティングしてもよい。また、表面改質の目的で
空気雰囲気中、不活性ガス雰囲気中等でコロナ放電処理
などの公知の処理を施してもよい。
The film of the present invention may be coated with additives such as an antistatic agent, a weathering agent, an antifogging agent, a slipping agent, etc., depending on the purpose. Further, a known treatment such as a corona discharge treatment may be performed in an air atmosphere, an inert gas atmosphere, or the like for the purpose of surface modification.

【0034】また本発明のフイルムは、目的に応じてエ
ンボス加工、印刷、押出ラミネーション加工、他の樹脂
フイルム、紙、布などと張り合わせ加工を行なって用い
ることもできる。
The film of the present invention can be used after embossing, printing, extrusion lamination, laminating with another resin film, paper, cloth or the like according to the purpose.

【0035】〔特性の測定方法並びに効果の評価方法〕
本発明の特性値の測定方法、並びに効果の評価方法は次
のとおりである。 (1)極限粘度[η] 試料0.1gを135℃のテトラリン100mlに完全
溶解させ、この溶液を粘度計で135℃の恒温槽中で測
定して、比粘度Sにより次式に従って極限粘度を求め
る。単位はdl/gとする。 [η]=(S/0.1)×(1+0.22×S)
[Method of measuring characteristics and method of evaluating effects]
The method for measuring the characteristic values and the method for evaluating the effects of the present invention are as follows. (1) Intrinsic viscosity [η] 0.1 g of a sample was completely dissolved in 100 ml of tetralin at 135 ° C., and this solution was measured in a thermostat at 135 ° C. with a viscometer. Ask. The unit is dl / g. [Η] = (S / 0.1) × (1 + 0.22 × S)

【0036】(2)アイソタクチックインデックス(I
I) 原料の状態では個々に測定すればよいが、複合フイルム
においては、まず試料を60℃以下の温度のn−ヘプタ
ンで2時間抽出し、プロピレンへの添加物を除去する。
その後130℃で2時間真空乾燥する。これから重量W
(mg)の試料をとり、ソックスレー抽出器に入れ沸騰
n−ヘプタンで12時間抽出する。次に、この試料を取
り出しアセトンで十分洗浄した後、130℃で6時間真
空乾燥しその後常温まで冷却し、重量W′(mg)を測
定し、次式で求める。 II(%)=(W′/W)×100 なお複合層については、表層を削りとり、上記と同じ方
法にて測定すればよい。
(2) Isotactic index (I
I) The measurement may be performed individually in the raw material state. In the case of the composite film, the sample is first extracted with n-heptane at a temperature of 60 ° C. or less for 2 hours to remove additives to propylene.
Thereafter, vacuum drying is performed at 130 ° C. for 2 hours. From now on weight W
Take (mg) sample, place in Soxhlet extractor and extract with boiling n-heptane for 12 hours. Next, the sample is taken out, sufficiently washed with acetone, vacuum-dried at 130 ° C. for 6 hours, and then cooled to room temperature, the weight W ′ (mg) is measured, and it is determined by the following equation. II (%) = (W ′ / W) × 100 For the composite layer, the surface layer may be scraped off and measured by the same method as described above.

【0037】(3)ガラス転移点温度(Tg)、等温結
晶化時間(t−1/2) 原料の状態では個々に測定すればよいが、複合フイルム
においては、まず試料を60℃以下の温度のn−ヘプタ
ンで2時間抽出し、プロピレンと石油樹脂およびテルペ
ン樹脂を分割する。次いでプロピレンは130℃、石油
樹脂およびテルペン樹脂は60℃で2時間真空乾燥す
る。その後、各試料について示差走査熱量計(DSC−
2型、パーキンエルマー社製)を用い、サンプル5mg
を室温より、20℃/分の昇温速度で昇温していった際
に、二次転移形に伴う比熱の変化をガラス転移点温度
(Tg)とし、ついで、280℃の溶融保持温度まで昇
温し、5分間保持した後に20℃/分の冷却速度にて冷
却していき、125℃で保持した時に、結晶化に伴う潜
熱のピークの始めの時間と終わりの時間を記録し、その
半分の時間を等温結晶化時間(t−1/2)とした。な
お複合層については、表層を削りとり、上記と同じ方法
にて測定すればよい。
(3) Glass transition temperature (Tg) and isothermal crystallization time (t-1 / 2) In the state of the raw material, the measurement may be performed individually. In the case of the composite film, the sample is first heated to a temperature of 60 ° C. or less. For 2 hours to separate propylene from petroleum resin and terpene resin. Then, propylene is vacuum dried at 130 ° C. and petroleum resin and terpene resin are dried at 60 ° C. for 2 hours. Then, for each sample, a differential scanning calorimeter (DSC-
2 type, manufactured by PerkinElmer Co., Ltd.)
When the temperature was raised from room temperature at a rate of 20 ° C./min, the change in specific heat accompanying the second-order transition type was defined as the glass transition temperature (Tg), and then to the melting holding temperature of 280 ° C. After raising the temperature and holding for 5 minutes, the mixture was cooled at a cooling rate of 20 ° C./min. When the temperature was held at 125 ° C., the start time and end time of the peak of the latent heat accompanying crystallization were recorded. Half the time was taken as the isothermal crystallization time (t-1 / 2). In addition, about a composite layer, what is necessary is just to scrape a surface layer, and to measure by the same method as the above.

【0038】(4)メルトフローインデックス(MF
I) ASTM−D−1238に準じて、230℃、2.16
kgの条件で測定した。
(4) Melt flow index (MF)
I) 230 ° C., 2.16 according to ASTM-D-1238
It was measured under the condition of kg.

【0039】(5)臭素価 JIS−K2543−1979によって測定した。試料
油100g中の不飽和成分に付加される臭素のg数で表
わされる。
(5) Bromine value Measured according to JIS-K2543-1979. It is represented by the number of g of bromine added to the unsaturated component in 100 g of the sample oil.

【0040】(6)熱収縮率 熱収縮率は、試長260mm、幅10mmにサンプリン
グし、原寸(L0 )として200mmの位置にマークを
入れる。このサンプルの下端に3gの荷重をかけ、12
0℃のオーブン中で15分間熱処理し、この後サンプル
にマークした長さ(L1 )を測定する。この熱収縮率
(R)は次式により求められる。 熱収縮率(R)(%)=[(L0 −L1 )/L0 ]×1
00
(6) Heat Shrinkage The heat shrinkage is sampled at a test length of 260 mm and a width of 10 mm, and a mark is placed at a position of 200 mm as the original size (L 0 ). A load of 3 g was applied to the lower end of the sample, and 12
Heat treatment is performed for 15 minutes in an oven at 0 ° C., after which the length (L 1 ) marked on the sample is measured. This heat shrinkage (R) is obtained by the following equation. Heat shrinkage (R) (%) = [(L 0 −L 1 ) / L 0 ] × 1
00

【0041】(7)水蒸気透過率 JIS−Z0208に従い、40℃・90%RHの条件
で測定した値で、g/m2 ・24hr/0.1mm単位
で表わす。
(7) Water Vapor Permeability A value measured under the conditions of 40 ° C. and 90% RH in accordance with JIS-Z0208 and expressed in g / m 2 · 24 hr / 0.1 mm.

【0042】(8)フイルム厚み ダイヤルゲージ式厚み計(JIS−B7509)を用い
て測定した。
(8) Film thickness The film thickness was measured using a dial gauge type thickness meter (JIS-B7509).

【0043】(9)積層厚み 電界放射形走査電子顕微鏡(FE−SEM)を用いてフ
イルム断面構成観察を行ない、厚みを測定した。
(9) Lamination Thickness The film cross-sectional structure was observed using a field emission scanning electron microscope (FE-SEM), and the thickness was measured.

【0044】(10)光沢度(JIS−Z8741、方
法2 60°鏡面光沢) 光沢度計(日本電色工業(株)製、VG107型)を用
いて、60°反射の時の光沢度を測定して求めた。
(10) Gloss (JIS-Z8741, Method 2, 60 ° Mirror Gloss) Gloss at 60 ° reflection is measured using a gloss meter (Model VG107, manufactured by Nippon Denshoku Industries Co., Ltd.). I asked.

【0045】(11)印刷加工性 フイルム厚み20μm、長さ1000mをグラビア印刷
した時に、フイルムの収縮による印字のピッチずれや、
フイルムのシワ等の発生の有無を評価した。
(11) Printing processability When gravure printing is performed on a film having a thickness of 20 μm and a length of 1000 m, a printing pitch shift due to shrinkage of the film,
The occurrence of wrinkles and the like of the film was evaluated.

【0046】(12)耐有機溶剤性 試長200mm、幅10mmにサンプリングし、原寸
(l0 )として100mmの位置にマークを入れる。こ
のサンプルを25℃のトルエンに1分浸漬し、その後サ
ンプルの下端に3gおよび100gの荷重をかけ、80
℃のオーブン中で1分間熱処理し、この後サンプルにマ
ークした長さ(l1 )を測定する。このときの寸法変化
(L)を次式により求める。 寸法変化率(L)(%)=[(l0 −l1 )/l0 ]×
100 この寸法変化率(L)が±2%未満のものを耐有機溶剤
性:○、±2%以上のものを耐有機溶剤性:×として評
価した。
(12) Resistance to Organic Solvents A sample was sampled at a test length of 200 mm and a width of 10 mm, and a mark was placed at a position of 100 mm as the original size (l 0 ). This sample was immersed in toluene at 25 ° C. for 1 minute, and thereafter, a load of 3 g and 100 g was applied to the lower end of the sample, and 80 g of
Heat treatment in an oven at 1 ° C. for 1 minute, and then measure the length (l 1 ) marked on the sample. The dimensional change (L) at this time is obtained by the following equation. Dimensional change rate (L) (%) = [(l 0 −l 1 ) / l 0 ] ×
100 Those having a dimensional change (L) of less than ± 2% were evaluated as organic solvent resistance: ○, and those having ± 2% or more were evaluated as organic solvent resistance: x.

【0047】(13)蒸着加工性 フイルム厚み20μm、長さ1000mを真空蒸着機に
て、約1.33×10-5Paの真空度で、アルミニウム
を厚さ60nm程度に蒸着して巻とり、その後この蒸着
面を電界放射形走査電子顕微鏡(FE−SEM)を用い
て観察し、蒸着面のクラックの発生状態をみた。
(13) Evaporation processability Aluminum was evaporated to a film thickness of about 60 nm with a film thickness of 20 μm and a length of 1000 m at a degree of vacuum of about 1.33 × 10 −5 Pa using a vacuum evaporation machine, and was wound. Thereafter, the deposited surface was observed using a field emission scanning electron microscope (FE-SEM), and the occurrence of cracks on the deposited surface was observed.

【0048】(14)PVDCコーティング性 厚み20μm、長さ1000mのフイルムに、PVDC
を厚さ3μmコーティングした後、80℃のオーブンに
通して乾燥させ巻き取った。このコーティング面を電界
放射形走査電子顕微鏡(FE−SEM)を用いて観察
し、コーティング面のクラックの発生状態をみた。
(14) PVDC coating property PVDC is applied to a film having a thickness of 20 μm and a length of 1000 m.
Was coated in a thickness of 3 μm, dried in an oven at 80 ° C. and wound up. The coated surface was observed using a field emission scanning electron microscope (FE-SEM) to check the occurrence of cracks on the coated surface.

【0049】[0049]

【実施例】以下に、本発明を実施例、比較例に基づいて
説明する。 実施例1、2、比較例1、2 結晶性ポリプロピレン(PP)(t−1/2:97se
c、II:98.7%、MFI:3.5g/10分)樹
脂に、特定の水添無極性石油樹脂を表1に示した割合に
混合したA層樹脂組成を押出機に供給して240℃の温
度で溶融し、一方B層の積層樹脂として、II:97.
0%の結晶性ポリプロピレンを別の押出機(II)に供給
して260℃の温度で溶融し、B層/A層/B層からな
る多層口金にて3層に共押出してシート状に押出成形
し、ドラフト比2.0で60℃の温度のドラムに巻き付
けてシート状に冷却固化した。該シートを140℃に保
たれたオーブン中に通して予熱し、引き続き130℃に
保ち周速差を設けた4本のロールに通して長手方向に
5.0倍延伸し、ただちに40℃に冷却した。次に該延
伸シートをテンターに導き、165℃の温度に予熱し、
引き続き155℃の温度で幅方向に10倍延伸し、次い
で幅方向に5%の弛緩を与えつつ165℃の温度で熱処
理をした後、冷却し巻き取った。フイルム特性は表2の
とおりであった。本発明の範囲のフイルムは熱収縮率が
小さくて耐熱性に優れ、また水蒸気透過率も小さくて防
湿性に優れ、印刷性や耐有機溶剤性および蒸着性などの
二次加工性にも優れたフイルムであった。また、本発明
の範囲をはずれたフイルムは、耐熱性および防湿性のい
ずれかに劣り、また印刷性や耐有機溶剤性および蒸着性
などの二次加工性にも劣り、本発明の目的とするフイル
ムは得られなかった。
The present invention will be described below based on examples and comparative examples. Examples 1 and 2, Comparative Examples 1 and 2 Crystalline polypropylene (PP) (t-1 / 2: 97 sec.)
c, II: 98.7%, MFI: 3.5 g / 10 min), and the extruder was supplied with a layer A resin composition in which a specific hydrogenated nonpolar petroleum resin was mixed with the resin in the ratio shown in Table 1. Melted at a temperature of 240 ° C., while as a laminated resin of layer B, II: 97.
0% crystalline polypropylene is supplied to another extruder (II), melted at a temperature of 260 ° C., and co-extruded into three layers by a multilayer die composed of B layer / A layer / B layer and extruded into a sheet. It was molded, wound around a drum at a draft ratio of 2.0 and at a temperature of 60 ° C., and cooled and solidified into a sheet. The sheet is preheated by passing it through an oven maintained at 140 ° C., then stretched 5.0 times in the longitudinal direction through four rolls maintained at 130 ° C. and provided with a peripheral speed difference, and immediately cooled to 40 ° C. did. Next, the stretched sheet is guided to a tenter and preheated to a temperature of 165 ° C.
Subsequently, the film was stretched 10 times in the width direction at a temperature of 155 ° C., then subjected to a heat treatment at a temperature of 165 ° C. while giving 5% relaxation in the width direction, and then cooled and wound up. The film properties were as shown in Table 2. The film in the range of the present invention has a small heat shrinkage and excellent heat resistance, and also has a small water vapor transmission rate and excellent moisture proofing property, and also has excellent secondary processing properties such as printability and organic solvent resistance and vapor deposition property. It was a film. Further, the film deviating from the scope of the present invention is inferior in either heat resistance or moisture resistance, and is inferior in secondary workability such as printability, organic solvent resistance and vapor deposition, and is an object of the present invention. No film was obtained.

【0050】比較例3、4 比較例3、4では、実施例1のA層の結晶性ポリプロピ
レンのMFIをそれぞれ、5.0g/10分、1.0g
/10分とした以外は実施例1と全く同様にしてフイル
ムを製造した。
Comparative Examples 3 and 4 In Comparative Examples 3 and 4, the MFI of the crystalline polypropylene of the layer A in Example 1 was 5.0 g / 10 min and 1.0 g, respectively.
A film was produced in exactly the same manner as in Example 1 except that the time was / 10 minutes.

【0051】実施例3、比較例5、6 実施例3では、結晶性ポリプロピレン(t−1/2:1
12sec、II:99.0%)樹脂に、特定の水添無
極性テルペン樹脂を15重量%混合して押出機(I)に
供給して240℃の温度で溶融し、T型口金に導きシー
ト状に押出成形した以外は実施例1と全く同様にしてフ
イルムを製造した。比較例5では、実施例1のA層の結
晶性ポリプロピレンの替わりに、t−1/2:225s
ec、II:97.3%の結晶性ポリプロピレンとし、
比較例6では、実施例1の特定の水添無極性石油樹脂の
替わりに、未水添で極性基(カルボキシル基−COO
H)を持った石油樹脂とし、B層の結晶性ポリプロピレ
ンを、II:98.5%の結晶性ポリプロピレンとした
以外は実施例1と全く同様にしてフイルムを製造した。
フイルム特性は表2のとおりであった。本発明の範囲の
フイルムは熱収縮率が小さくて耐熱性に優れ、また水蒸
気透過率も小さくて防湿性に優れ、印刷性や耐有機溶剤
性および蒸着性などの二次加工性にも優れたフイルムで
あった。また、本発明の範囲をはずれたフイルムは、耐
熱性および防湿性のいずれかに劣り、また印刷性や耐有
機溶剤性および蒸着性などの二次加工性にも劣り、本発
明の目的とするフイルムは得られなかった。
Example 3, Comparative Examples 5 and 6 In Example 3, crystalline polypropylene (t-1 / 2: 1) was used.
12 sec, II: 99.0%) A specific hydrogenated non-polar terpene resin is mixed with the resin in an amount of 15% by weight, supplied to the extruder (I), melted at a temperature of 240 ° C., and guided to a T-type die. A film was produced in exactly the same manner as in Example 1 except that the film was extruded. In Comparative Example 5, t-1 / 2: 225 s was used instead of the crystalline polypropylene of the layer A in Example 1.
ec, II: 97.3% crystalline polypropylene;
In Comparative Example 6, an unhydrogenated polar group (carboxyl group -COO) was used instead of the specific hydrogenated nonpolar petroleum resin of Example 1.
A film was produced in exactly the same manner as in Example 1 except that the petroleum resin having H) was used, and the crystalline polypropylene of the layer B was II: 98.5% crystalline polypropylene.
The film properties were as shown in Table 2. The film in the range of the present invention has a small heat shrinkage and excellent heat resistance, and also has a small water vapor transmission rate and excellent moisture proofing property, and also has excellent secondary processing properties such as printability and organic solvent resistance and vapor deposition property. It was a film. Further, the film deviating from the scope of the present invention is inferior in either heat resistance or moisture resistance, and is inferior in secondary workability such as printability, organic solvent resistance and vapor deposition, and is an object of the present invention. No film was obtained.

【0052】[0052]

【表1】 [Table 1]

【0053】[0053]

【表2】 [Table 2]

【0054】[0054]

【発明の効果】以上述べたように、本発明の耐熱防湿フ
イルムは、特定の高結晶性ポリプロピレンに特定の石油
樹脂および/または特定のテルペン樹脂を添加混合した
フイルムであって、次のような優れた効果を生じるもの
である。 (1)水蒸気透過率が小さくて防湿性に優れ、包装用
途、特に食品、医薬品等の包装用として好適である。 (2)二次加工で必要な耐熱性および耐有機溶剤性に優
れ、また印刷、粘着テープ、蒸着ベース用として良好な
特性を有する。 (3)耐熱性および防湿性に優れていることから、薄膜
化を図ることができ、包装材料のコスト低減となる。
As described above, the heat and moisture resistant film of the present invention is a film in which a specific petroleum resin and / or a specific terpene resin is added to a specific high crystalline polypropylene and mixed. It produces excellent effects. (1) It has a small water vapor transmission rate and excellent moisture resistance, and is suitable for use in packaging, particularly for packaging foods and pharmaceuticals. (2) It has excellent heat resistance and organic solvent resistance required for secondary processing, and has good properties for printing, adhesive tapes, and vapor deposition bases. (3) Since it is excellent in heat resistance and moisture resistance, it can be made thinner and the cost of the packaging material can be reduced.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI // C08L 23/12 C08L 23/12 B29K 23:00 B29K 23:00 55:00 55:00 B29L 7:00 B29L 7:00 9:00 9:00 (56)参考文献 特開 平7−157573(JP,A) 特開 昭58−213037(JP,A) 特開 平3−255137(JP,A) 特開 平4−272937(JP,A) 特開 平8−253633(JP,A) 特開 平7−76641(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08J 5/00 - 5/02 C08J 5/12 - 5/22 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI // C08L 23/12 C08L 23/12 B29K 23:00 B29K 23:00 55:00 55:00 B29L 7:00 B29L 7:00 9:00 9:00 (56) References JP-A-7-157573 (JP, A) JP-A-58-213037 (JP, A) JP-A-3-255137 (JP, A) JP-A-4-272937 (JP, A) JP-A-8-253633 (JP, A) JP-A-7-76641 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C08J 5/00-5 / 02 C08J 5/12-5/22

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 125℃での等温結晶化時間が3.5分
以下、アイソタクチックインデックスが98.5%以
上、メルトフローインデックスが2〜4g/10分の結
晶性ポリプロピレン70〜95重量%に、極性基を実質
的に含まない石油樹脂および極性基を実質的に含まない
テルペン樹脂の1種以上が5〜30重量%混合されたフ
イルムであって、120℃、15分加熱での長手方向の
熱収縮率が5%以下であり、水蒸気透過率が1.0(g
/m2 ・24hr/0.1mm)以下であることを特徴
とする耐熱防湿フイルム。
1. Isothermal crystallization time at 125 ° C. of 3.5 minutes or less, isotactic index of 98.5% or more, melt flow index of 2 to 4 g / 10 min. A film in which at least one kind of a petroleum resin substantially free of a polar group and a terpene resin substantially free of a polar group is mixed at 5 to 30% by weight, and heated at 120 ° C. for 15 minutes. Direction heat shrinkage is 5% or less and water vapor transmission rate is 1.0 (g
/ M 2 · 24 hr / 0.1 mm) or less.
【請求項2】 請求項1に記載の耐熱防湿フイルムの少
なくとも片面に、アイソタクチックインデックスが98
%以下の結晶性ポリプロピレンを積層してなることを特
徴とする耐熱防湿フイルム。
2. The heat- and moisture-proof film according to claim 1, wherein at least one surface has an isotactic index of 98.
% Or less of a crystalline polypropylene.
JP09791595A 1995-03-29 1995-03-29 Heat and moisture proof film Expired - Fee Related JP3259588B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09791595A JP3259588B2 (en) 1995-03-29 1995-03-29 Heat and moisture proof film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09791595A JP3259588B2 (en) 1995-03-29 1995-03-29 Heat and moisture proof film

Publications (2)

Publication Number Publication Date
JPH08269213A JPH08269213A (en) 1996-10-15
JP3259588B2 true JP3259588B2 (en) 2002-02-25

Family

ID=14205008

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Country Link
JP (1) JP3259588B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2372954C (en) * 2000-03-22 2009-05-26 Basell Technology Company Bv Multilayer heat-shrinkable sealable films
JP3581359B2 (en) * 2002-06-20 2004-10-27 ダイセル化学工業株式会社 Polypropylene-based laminated film, method for producing the same, and packaging material
JP6089463B2 (en) * 2012-06-25 2017-03-08 Dic株式会社 LAMINATE, MANUFACTURING METHOD THEREOF AND PACKAGE BODY USING THE SAME

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58213037A (en) * 1982-06-03 1983-12-10 Toray Ind Inc Polypropylene film
DE69018606T2 (en) * 1990-02-01 1995-09-07 Borden Inc Modified polyolefin film with stable insertion behavior, folding properties and blocking characteristics.
JPH04272937A (en) * 1991-02-28 1992-09-29 Toray Ind Inc Composite polymer sheet
JP3330733B2 (en) * 1993-07-16 2002-09-30 三井化学株式会社 Polypropylene resin composition and use thereof
JP3077482B2 (en) * 1993-12-03 2000-08-14 東レ株式会社 Heat and moisture proof film
JPH08253633A (en) * 1995-03-14 1996-10-01 Chisso Corp Drawn polypropylene film

Also Published As

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