JPH07138471A - Polyamide resin composition and packaging film prepared therefrom - Google Patents

Polyamide resin composition and packaging film prepared therefrom

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Publication number
JPH07138471A
JPH07138471A JP29073293A JP29073293A JPH07138471A JP H07138471 A JPH07138471 A JP H07138471A JP 29073293 A JP29073293 A JP 29073293A JP 29073293 A JP29073293 A JP 29073293A JP H07138471 A JPH07138471 A JP H07138471A
Authority
JP
Japan
Prior art keywords
polyamide resin
film
silica
talc
resin composition
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.)
Pending
Application number
JP29073293A
Other languages
Japanese (ja)
Inventor
Hiroshi Urabe
宏 浦部
Katsuhiko Sugiura
克彦 杉浦
Morio Tsunoda
守男 角田
Tomoaki Kanemasa
智亮 金政
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP29073293A priority Critical patent/JPH07138471A/en
Publication of JPH07138471A publication Critical patent/JPH07138471A/en
Pending legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain the subject composition excellent in the oxygen barrier resistance, transparency and slipperiness under high humidity of the film prepared therefrom, useful for packaging films for high water content foods, etc., by incorporating a polyamide resin with each specified amount of silica and talc. CONSTITUTION:This resin composition is obtained by incorporating (A) 100 pts.wt. of a polyamide resin such as nylon 6 or nylon 6-66 copolymer resin with (B) 0.03-0.5 pts.wt. of silica pref. 80-350ml/100g in oil absorption and (C) 0.01-0.07 pts.wt. of talc pref. 30-50ml/100g in oil absorption.

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、フィルム成形用ポリア
ミド樹脂組成物に関する。詳しくは、特定のシリカとタ
ルクを組み合わせて配合してなる、特に高湿度下での滑
り性に優れたポリアミドフィルム成形用ポリアミド樹脂
組成物に関するものである。
FIELD OF THE INVENTION The present invention relates to a polyamide resin composition for film forming. More specifically, the present invention relates to a polyamide resin composition for forming a polyamide film, which is prepared by combining specific silica and talc and is particularly excellent in slipperiness under high humidity.

【0002】[0002]

【従来の技術】ポリアミドフィルムは、二軸延伸ポリプ
ロピレンフィルムや二軸延伸ポリエステルフィルムなど
に比べて優れた酸素バリアー性、強靱な強度と柔軟性、
耐熱性、透明性や広い温度範囲で使用可能なことなどの
特徴があるため、これらの特徴を利用して、主に食品包
装材料として利用されている。
2. Description of the Related Art Polyamide films are superior in oxygen barrier properties, tough strength and flexibility to biaxially oriented polypropylene films and biaxially oriented polyester films.
Because of its features such as heat resistance, transparency, and that it can be used in a wide temperature range, it is mainly used as a food packaging material by utilizing these features.

【0003】かかるポリアミドフィルムの技術分野にお
いては、フィルムの滑り性が悪いと製袋時にフィルムが
引っかかったり、多色印刷時にインクの印刷ズレが生じ
たりすることがあるため、フィルムの滑り性はフィルム
の生産性や品質、商品価値の点からきわめて重要な特性
である。特に、こんにゃく、漬物などの水分を多量に含
む食品の包装材料分野においては、高湿度下の滑り性が
悪いと、給袋不良が発生して、かかる水分を多く含む内
容物の充填を円滑に行うことができず、安定した連続運
転が困難となる。
In the technical field of such a polyamide film, if the film has poor slipperiness, the film may be caught during bag making, or ink misalignment may occur during multicolor printing. It is a very important characteristic in terms of productivity, quality and commercial value. In particular, in the packaging material field of foods containing a large amount of water such as konjac and pickles, poor slipperiness under high humidity causes bag feeding failure and facilitates filling of such water-rich contents. It cannot be performed and stable continuous operation becomes difficult.

【0004】このようなポリアミドフィルムの滑り性改
良のために従来から種々の方法が試みられてきた。例え
ば無機フィラーを配合する方法(特公昭54ー474
1)や、ポリエチレンを配合する方法(特公昭53ー4
5226)などが提案されてい
Various methods have heretofore been tried to improve the slipperiness of such a polyamide film. For example, a method of adding an inorganic filler (Japanese Patent Publication No. 54-474).
1) and a method of blending polyethylene (Japanese Patent Publication No. 53-4)
5226) etc. have been proposed

【0005】る。[0005]

【発明が解決しようとする課題】しかし、前者の無機フ
ィラーを配合する方法では、ポリアミドフィルムの特徴
である透明性が低下し、商品価値がなくなってしまう恐
れがある。そのため添加量は大幅に制限され、十分な滑
り性を発現せしめることはできない。特に、高湿度下で
の滑り性の改良は不十分であった。
However, in the former method of incorporating the inorganic filler, there is a possibility that the transparency, which is a characteristic of the polyamide film, is lowered and the commercial value is lost. Therefore, the addition amount is significantly limited, and sufficient slipperiness cannot be exhibited. In particular, the improvement of slipperiness under high humidity was insufficient.

【0006】また、無機粒子の表面活性が高いと、ポリ
アミド樹脂の熱安定性が不良になり、フィッシュアイや
ダイラインが生じやすく、外観不良となって連続安定生
産性に問題が生じる。特に、シリカ系粒子はこの傾向が
強く、ダイラインやフィッシュアイなどの外観不良が生
じやすく、使用する際には注意が必要であった。一方、
ポリエチレンを配合する方法では、やはりフィルムの透
明性が大幅に低下することが認められており、また同時
に強度の低下も招くという欠点がある。
Further, when the surface activity of the inorganic particles is high, the thermal stability of the polyamide resin becomes poor, fish eyes and die lines are apt to occur, the appearance becomes poor, and continuous stable productivity becomes a problem. In particular, silica-based particles have such a strong tendency that the appearance defects such as die lines and fish eyes are liable to occur, and therefore care must be taken when using them. on the other hand,
The method of blending polyethylene is also recognized to greatly reduce the transparency of the film, and at the same time, it has the drawback of causing a decrease in strength.

【0007】よって、透明性低下、強度低下、外観不良
等を招くことなく滑り性の優れたポリアミドフィルムを
工業的に得ることは、未だ容易でないのが実情であっ
た。
Therefore, it has not been easy to industrially obtain a polyamide film having excellent slipperiness without causing deterioration of transparency, deterioration of strength, poor appearance and the like.

【0008】[0008]

【課題を解決するための手段】そこで発明者らは、ポリ
アミドフィルムの透明性を確保しつつ、滑り性、特に高
湿度下での滑り性に優れたフィルムを開発すべく鋭意検
討を行った結果、ポリアミド系樹脂に一定量のシリカと
タルクを配合すること、特に特定の吸油量を有するシリ
カとタルクを併用することによって、かかる目的が達成
できることを見いだし、本発明に到達した。
[Means for Solving the Problems] As a result, the inventors have conducted earnest studies to develop a film having excellent slipperiness, particularly slipperiness under high humidity, while ensuring the transparency of the polyamide film. The inventors have found that such an object can be achieved by blending a certain amount of silica and talc in a polyamide resin, and particularly by using silica and talc having a specific oil absorption amount together, and arrived at the present invention.

【0009】すなわち本発明の要旨は、ポリアミド系樹
脂100重量部に対してシリカ0.03〜0.5重量部
とタルク0.01〜0.07重量部を配合してなる樹脂
組成物よりなることを特徴とするポリアミドフィルムに
関する。以下本発明を詳細に説明する。本発明において
使用するポリアミド系樹脂とは、3員環以上のラクタ
ム、重合可能なω−アミノ酸、二塩基酸とジアミンなど
の重縮合によって得られるポリアミド樹脂を用いること
ができる。具体的にはε−カプロラクタム、アミノカプ
ロン酸、エナントラクタム、7−アミノヘプタン酸、1
1−アミノウンデカン酸、9−アミノノナン酸、α−ピ
ロリドン、α−ピペリドンなどの重合体、ヘキサメチレ
ンジアミン、ノナメチレンジアミン、ウンデカメチレン
ジアミン、ドデカメチレンジアミン、メタキシレンジア
ミンなどのジアミン類とテレフタル酸、イソフタル酸、
アジピン酸、セバシン酸、ドデカン二塩基酸、グルター
ル酸などのジカルボン酸類とを宿重合させて得られる重
合体、または共重合体であり例えば、ナイロン4、6、
7、8、11、12、6・6、6・10、6・11、6
・12、6T、6/6・6、6/12、6/6T、6I
/6Tなどが挙げられる。
That is, the gist of the present invention is a resin composition obtained by mixing 0.03 to 0.5 part by weight of silica and 0.01 to 0.07 part by weight of talc with 100 parts by weight of a polyamide resin. The present invention relates to a polyamide film. The present invention will be described in detail below. As the polyamide resin used in the present invention, a polyamide resin obtained by polycondensation of a lactam having 3 or more membered rings, a polymerizable ω-amino acid, a dibasic acid and a diamine, or the like can be used. Specifically, ε-caprolactam, aminocaproic acid, enanthlactam, 7-aminoheptanoic acid, 1
Polymers such as 1-aminoundecanoic acid, 9-aminononanoic acid, α-pyrrolidone and α-piperidone, diamines such as hexamethylenediamine, nonamethylenediamine, undecamethylenediamine, dodecamethylenediamine and metaxylenediamine, and terephthalic acid , Isophthalic acid,
Polymers or copolymers obtained by subjecting dicarboxylic acids such as adipic acid, sebacic acid, dodecane dibasic acid, glutaric acid, etc. to polymerisation, for example nylon 4, 6,
7, 8, 11, 12, 6/6, 6/10, 6/11, 6
・ 12, 6T, 6/6 ・ 6, 6/12, 6 / 6T, 6I
/ 6T and the like.

【0010】これらのうちでは、得られるフィルムの熱
的、機械的特性の面から、特にナイロン6、またはナイ
ロン6/6・6共重合樹脂の使用が適している。使用す
るポリアミド樹脂の相対粘度(ηrel)については、
JIS−K−6810に従って98%硫酸中濃度1%、
温度25℃で測定した値で2〜6、好ましくは2〜5の
範囲が適している。相対粘度が低すぎると得られたフィ
ルムの機械的強度が低く、使用に耐えない。また、相対
粘度が高すぎると押出圧力やトルクが高すぎて成形が不
可能となる。
Of these, nylon 6 or nylon 6/6/6 copolymer resin is particularly suitable in terms of the thermal and mechanical properties of the obtained film. Regarding the relative viscosity (ηrel) of the polyamide resin used,
According to JIS-K-6810, 98% sulfuric acid concentration 1%,
A range of 2 to 6, preferably 2 to 5 as a value measured at a temperature of 25 ° C. is suitable. If the relative viscosity is too low, the mechanical strength of the obtained film is low and it cannot be used. On the other hand, if the relative viscosity is too high, the extrusion pressure and torque are too high, and molding becomes impossible.

【0011】本発明のポリアミド樹脂については、更
に、JIS−K−6810に規定する低分子量物の含有
量の測定方法に準じて測定した水抽出量が1%以下、好
ましくは0.5%以下になるようにするのが好ましい。
水抽出量が多いと、ダイス付近へのオリゴマー成分の付
着が著しく、これら付着物によるダイラインやフィッシ
ュアイの発生により工業的連続生産性が悪化する。
The polyamide resin of the present invention has a water extraction amount of 1% or less, preferably 0.5% or less, which is measured according to the method for measuring the content of low molecular weight substances specified in JIS-K-6810. Is preferred.
When the amount of water extracted is large, the oligomer component is remarkably attached to the vicinity of the die, and the die continuous line and fish eyes are generated by these adhered substances, so that the industrial continuous productivity is deteriorated.

【0012】本発明において使用するシリカは、特に限
定はなく、市販のもの等が使用できるが、好ましくは、
JIS−K−5101法に従って測定した吸油量が80
〜350ml/100gの範囲にあるものを用いる。吸
油量が大きすぎると、ポリアミドフィルム中でのシリカ
の分散性が悪くなり、また、2次凝集物によるフィッシ
ュアイの発生もしやすくなるので好ましくない。一方、
吸油量が小さすぎると、延伸時のボイドの発生や延伸切
れが多くなり、好ましくない。本発明では、更に、粒径
10μm以上の粒子を分級して除いたものを用いるのが
好ましい。
The silica used in the present invention is not particularly limited, and commercially available ones can be used, but preferably,
The oil absorption measured according to JIS-K-5101 is 80.
What is in the range of up to 350 ml / 100 g is used. If the amount of oil absorption is too large, the dispersibility of silica in the polyamide film becomes poor, and fish eyes are easily generated due to secondary aggregates, which is not preferable. on the other hand,
If the oil absorption is too small, voids and stretching breakage during stretching increase, which is not preferable. In the present invention, it is preferable to use particles obtained by classifying and removing particles having a particle diameter of 10 μm or more.

【0013】本発明に好適なシリカは、いわゆる湿式シ
リカ及び乾式シリカのどちらでもかまわない。また、シ
ランカップリング剤や、チタンカップリング剤など公知
の方法で表面処理をすることにより、更に良好な分散性
が得られると同時に、フィルムの透明性も改良される。
なお、この表面処理の方法は特に限定しないが、例えば
特開昭63−251460に記載されている方法が使用
できる。
The silica suitable for the present invention may be so-called wet silica or dry silica. Further, by subjecting the surface to a known method such as a silane coupling agent or a titanium coupling agent, better dispersibility can be obtained, and at the same time, the transparency of the film is improved.
The method of this surface treatment is not particularly limited, but for example, the method described in JP-A-63-251460 can be used.

【0014】シリカの配合量は、ポリアミド樹脂100
重量部に対して0.03〜0.5重量部であり、特に好
ましくは0.1〜0.25重量部である。添加量が少な
いとフィルムの滑り性の改良が不十分となり、好ましく
ない。一方、添加量が多すぎると透明性の低下やフィッ
シュアイの原因となる。タルクについても、特に限定は
なく、市販のもの等が使用できるが、JIS−K−51
01法に従って測定した吸油量が30〜50ml/10
0gの範囲にあるものが好ましい。吸油量が大きすぎる
とシリカ同様に分散不良となり、小さすぎるとボイドや
延伸破断の原因となる。本発明では、更に、10μm以
上の粒子を分級して除いたものを用いるのが好ましい。
The silica content is 100% polyamide resin.
The amount is 0.03 to 0.5 part by weight, and particularly preferably 0.1 to 0.25 part by weight. If the amount added is too small, the improvement of the slipperiness of the film becomes insufficient, which is not preferable. On the other hand, if the addition amount is too large, it may cause deterioration of transparency and fish eyes. The talc is not particularly limited, and commercially available ones can be used, but JIS-K-51
Oil absorption measured according to method 01 is 30 to 50 ml / 10
Those in the range of 0 g are preferable. If the oil absorption is too large, the dispersion will be poor like silica, and if it is too small, voids and stretch breaks will occur. In the present invention, it is preferable to use particles obtained by classifying particles of 10 μm or more and removing them.

【0015】タルクの配合量は、ポリアミド樹脂100
重量部に対して0.01〜0.07重量部であり、特に
好ましくは0.01〜0.06重量部である。添加量が
少ないと高湿度下(85%RH)での滑り性が改良され
ず、逆に多すぎると透明性が悪化し、高湿度下の滑りも
悪化する。本発明においては、上述した特定量のシリカ
とタルクを併用する点に特徴がある。これは、透明性を
確保しつつ、滑り性、特に高湿度下での滑り性を確保す
るためである。即ち、シリカ単独またはタルク単独で高
湿度下の滑りを改良するためには、それぞれ例えば0.
5重量部または0.08重量部以上もの大量の添加が必
要となるが、かかる大量を添加すると、透明性低下やフ
ィッシュアイ発生といった問題が生じ、実用的でない。
The blending amount of talc is 100% polyamide resin.
The amount is 0.01 to 0.07 part by weight, and particularly preferably 0.01 to 0.06 part by weight. If the amount added is small, the slipperiness under high humidity (85% RH) is not improved, and conversely, if it is too large, the transparency deteriorates and the slipperiness under high humidity also deteriorates. The present invention is characterized in that the specific amount of silica and talc described above are used together. This is for ensuring the slipperiness, particularly the slipperiness under high humidity, while ensuring the transparency. That is, in order to improve slippage under high humidity with silica alone or talc alone, for example, each of them can be reduced to, for example, 0.
It is necessary to add a large amount of 5 parts by weight or 0.08 parts by weight or more, but if such a large amount is added, problems such as deterioration of transparency and generation of fish eyes occur, which is not practical.

【0016】シリカ及びタルクのポリアミド樹脂への配
合方法としては、ポリアミド樹脂の重合時に添加する重
合時添加法、予め高濃度でポリアミド樹脂に1軸または
二軸の押出機を使用して練り込み、これを成形時に希釈
して使用するいわゆるマスターバッチ法、成形に使用す
る添加剤濃度で予めポリアミド樹脂に練り込み使用する
練り混み法、成形時にポリアミド樹脂に所定量を添加す
るドライブレンド法などが可能であり、このとき必要に
応じて公知の展着剤を使用しても差し支えない。また、
シリカとタルクを各々別の方法により添加してもかまわ
ない。
The silica and talc may be added to the polyamide resin by adding during polymerization of the polyamide resin, or by kneading the polyamide resin in high concentration in advance using a uniaxial or biaxial extruder. A so-called masterbatch method in which this is diluted at the time of molding is used, a kneading method in which it is kneaded into a polyamide resin in advance at the additive concentration used in molding, and a dry blending method in which a predetermined amount is added to the polyamide resin during molding At this time, a known spreading agent may be used if necessary. Also,
Silica and talc may be added by different methods.

【0017】これら無機フィラーを添加したポリアミド
樹脂には、フィルムとしての性質を損なわない範囲でビ
スアミド化合物をはじめとする各種滑剤、ヒンダートフ
ェノール系やリン酸エステル、亜リン酸エステル系をは
じめとする酸化防止剤、耐候性改良剤、離型剤、帯電防
止剤、ブロッキング防止剤、染料、顔料などの添加剤を
配合して使用してもよい。特に有機系滑剤としてビスア
ミド化合物は効果があり有用である。
Polyamide resins containing these inorganic fillers include various lubricants such as bisamide compounds, hindered phenols, phosphoric acid esters, and phosphorous acid ester-based materials as long as the properties of the film are not impaired. You may mix and use additives, such as an antioxidant, a weather resistance improving agent, a mold release agent, an antistatic agent, an antiblocking agent, a dye, and a pigment. Bisamide compounds are particularly effective and useful as organic lubricants.

【0018】本発明のポリアミドフィルムは、公知の方
法で成形することができる。たとえば前記樹脂原料の溶
融体を連続的にT−ダイより押出し、キャスティングロ
ールにて冷却しながらフィルム状に成形するT−ダイ
法、環状のダイスより連続的に押出し、水を接触させて
冷却する水冷インフレーション法、同じく環状のダイス
より押出し、空気によって冷却する空冷インフレーショ
ン法などが用いられる。
The polyamide film of the present invention can be formed by a known method. For example, a melt of the resin raw material is continuously extruded from a T-die and is formed into a film while being cooled by a casting roll, a T-die method is continuously extruded from an annular die, and water is contacted and cooled. A water-cooled inflation method, an air-cooled inflation method of extruding from an annular die and cooling with air is also used.

【0019】また、これらの成形法で他の原料を同時に
押し出す共押出法で多層のフィルムを得ることもでき
る。延伸フィルム用原反の成形法としては特にT−ダイ
法、水冷インフレーション法が連続延伸性の点で優れて
いる。さらに本発明のポリアミドフィルムは延伸するこ
とも可能であり、延伸方法についても公知の方法が応用
できる。例えば、T−ダイ法にて成形したフィルムにつ
いては縦延伸はロール方式を用い、さらに横方向に延伸
する際にはテンター方式を使用したいわゆる逐次二軸延
伸法、環状ダイより成形したチューブ状フィルムについ
ては上記の逐次二軸法以外に縦横同時に延伸できるチュ
ーブラー延伸法が用いられる。
Further, a multilayer film can be obtained by a coextrusion method in which other raw materials are simultaneously extruded by these molding methods. As a method for forming a raw material for a stretched film, a T-die method and a water-cooled inflation method are particularly excellent in continuous stretchability. Further, the polyamide film of the present invention can be stretched, and a known method can be applied as a stretching method. For example, a film formed by the T-die method uses a roll method for longitudinal stretching, and a so-called sequential biaxial stretching method using a tenter method when stretching in the transverse direction, a tubular film formed by an annular die. In addition to the above-mentioned sequential biaxial method, a tubular drawing method that allows simultaneous drawing in the machine and transverse directions is used.

【0020】本発明のポリアミドフィルムは、他のフィ
ルム、例えばポリオレフィンフィルムなどと積層して用
いることもできる。積層の方法についても特に限定され
ないが、共押出しする場合は、共押出フィルムについて
も同様の方法で各層を同時に延伸(共延伸)する事がで
きる。このようにして得られた本発明のポリアミドフィ
ルムは、印刷性の改良やラミ性の改良のために片面また
は両面にコロナ処理した後使用することもできる。
The polyamide film of the present invention can be used by laminating it with another film such as a polyolefin film. The method for laminating is not particularly limited, but when coextruding, each layer can be simultaneously stretched (costretched) in the same manner for a coextruded film. The polyamide film of the present invention thus obtained can be used after corona treatment on one side or both sides for improving printability and laminating property.

【0021】[0021]

【実施例】以下、本発明を実施例を挙げて更に詳細に説
明するが、本発明はその要旨を越えない限りこれらの実
施例に限定されるものではない。なお、以下の実施例に
おける各種物性の評価は次のように行った。 (1)透明性 東京電色株式会社製ヘーズメーターを使用してヘーズ値
で評価した。 (2)滑り性 23℃、相対湿度65%および85%の条件下、平行移
動式で静止摩擦係数を測定した。 (3)フィルム外観 フィルムを300mm×300mmの正方形に切り取
り、その部分を目視観察によってダイラインの発生の有
無、および40μm以上の大きさのフィッシュアイ
(F.E.)の数を測定した。
The present invention will be described in more detail below with reference to examples, but the present invention is not limited to these examples as long as the gist thereof is not exceeded. In addition, evaluation of various physical properties in the following examples was performed as follows. (1) Transparency The haze value was evaluated using a haze meter manufactured by Tokyo Denshoku Co., Ltd. (2) Sliding property The static friction coefficient was measured by a parallel displacement method under the conditions of 23 ° C. and relative humidity of 65% and 85%. (3) Appearance of Film The film was cut into a square of 300 mm × 300 mm, and the portion was visually observed to determine whether a die line was generated and the number of fish eyes (FE) having a size of 40 μm or more.

【0022】実施例1〜3、5、比較例1、3 200リットルのオートクレーブ中にε−カプロラクタ
ム60Kgと水1.2KgとJIS−K−5101法に
よる吸油量が310ml/100gの非晶性湿式合成シ
リカを、ポリアミド樹脂チップとしたとき表2に示す添
加量になるように仕込んだ。
Examples 1 to 3 and 5 and Comparative Examples 1 and 3 60 kg of ε-caprolactam, 1.2 kg of water, and 200 ml of an autoclave in an amorphous wet type having an oil absorption of 310 ml / 100 g according to the JIS-K-5101 method. Synthetic silica was charged so as to have the addition amount shown in Table 2 when polyamide resin chips were used.

【0023】オートクレーブを窒素雰囲気にして密封
し、260℃に昇温し、撹拌しながら2時間加圧下にて
反応を行った後、徐々に法圧して100Toorまで減
圧し、更に2時間減圧下にて反応を行った。その後、オ
ートクレーブ中に窒素を導入して上圧に吹く圧した後撹
拌をやめ、ポリアミド樹脂をストランドとして抜き出
し、チップ化した。
The autoclave was sealed in a nitrogen atmosphere, the temperature was raised to 260 ° C., the reaction was carried out under pressure for 2 hours while stirring, then the pressure was gradually reduced to 100 Toor, and the pressure was further reduced for 2 hours. The reaction was carried out. Then, nitrogen was introduced into the autoclave to blow it to an upper pressure, stirring was stopped, and the polyamide resin was extracted as a strand and made into chips.

【0024】次いで、得られたポリアミド樹脂チップを
沸騰水中に投入して未反応のモノマーを抽出除去した
後、真空乾燥した。得られたポリアミド樹脂の相対粘度
を測定したところ、4.5であった。このポリアミド樹
脂100重量部に対して表1の組み合わせのタルクを表
2に示した添加量添加し、水冷インフレーション法にて
厚み135μmの延伸原反を得た。得られたフィルム
は、ロング社製二軸延伸機を用いて80℃で熱固定して
厚み約15μmの二軸延伸フィルムとした。
Then, the obtained polyamide resin chips were put into boiling water to extract and remove unreacted monomers, and then vacuum dried. The relative viscosity of the obtained polyamide resin was measured and found to be 4.5. Talc of the combination shown in Table 1 was added to 100 parts by weight of this polyamide resin, and the addition amount shown in Table 2 was added to obtain a stretched raw fabric having a thickness of 135 μm by a water-cooled inflation method. The obtained film was heat-set at 80 ° C. using a biaxial stretching machine manufactured by Long Co. to obtain a biaxially stretched film having a thickness of about 15 μm.

【0025】実施例4、6、比較例2、4、5 市販のナイロン6樹脂(三菱化成株式会社製、ノバミッ
ド1020:ノバミッドは登録商標)100重量部に、
表1に示す無機フィラーを表2に示す量添加し、水冷イ
ンフレーション法にて厚み135μmの延伸原反を成形
した。次いで、得られたフィルムをロング社製二軸延伸
機を用いて80℃の条件下、歪速度20000%/分で
同時二軸延伸し、さらに210℃で熱固定して厚み約1
5μmの二軸延伸フィルムを得た。得られたフィルムに
ついて、各種物性の評価結果を、表2に示す。
Examples 4, 6 and Comparative Examples 2, 4, 5 100 parts by weight of commercially available nylon 6 resin (Novamid 1020: Novamid is a registered trademark, manufactured by Mitsubishi Kasei Co., Ltd.),
The inorganic fillers shown in Table 1 were added in the amounts shown in Table 2, and a stretched raw fabric having a thickness of 135 μm was formed by a water cooling inflation method. Then, the obtained film was simultaneously biaxially stretched at a strain rate of 20000% / min under a condition of 80 ° C. using a biaxial stretching machine manufactured by Long Co., and further heat set at 210 ° C. to have a thickness of about 1
A 5 μm biaxially stretched film was obtained. Table 2 shows the evaluation results of various physical properties of the obtained film.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【表2】 [Table 2]

【0028】[0028]

【発明の効果】本発明によれば、酸素バリアー性に優れ
たポリアミドフィルムの透明性を確保しつつ、特に高湿
度下での滑り性に優れたフィルムを得ることができる。
よって、本発明は、特に水分を多量に含む食品の包装材
料分野において非常に有用な技術である。
According to the present invention, it is possible to obtain a film having excellent slipperiness especially under high humidity while ensuring the transparency of the polyamide film having excellent oxygen barrier property.
Therefore, the present invention is a very useful technique especially in the field of packaging materials for foods containing a large amount of water.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 金政 智亮 神奈川県茅ヶ崎市円蔵370番地 三菱化成 株式会社茅ヶ崎事業所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tomoaki Kinmasa 370 Enzo, Chigasaki City, Kanagawa Mitsubishi Kasei Co., Ltd. Chigasaki Plant

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ポリアミド系樹脂100重量部に対して
シリカ0.03〜0.5重量部とタルク0.01〜0.
07重量部を含有してなることを特徴とする、フィルム
成形用ポリアミド樹脂組成物。
1. To 100 parts by weight of a polyamide resin, 0.03 to 0.5 parts by weight of silica and 0.01 to 0.
A polyamide resin composition for film forming, comprising 07 parts by weight.
【請求項2】 ポリアミド系樹脂100重量部に対して
吸油量が80〜350ml/100gのシリカ0.03
〜0.5重量部と吸油量が30〜50ml/100gの
タルク0.01〜0.07重量部を含有してなることを
特徴とする、フィルム成形用ポリアミド樹脂組成物。
2. A silica 0.03 having an oil absorption of 80 to 350 ml / 100 g with respect to 100 parts by weight of a polyamide resin.
To 0.5 parts by weight and 0.01 to 0.07 parts by weight of talc having an oil absorption of 30 to 50 ml / 100 g, a polyamide resin composition for film molding.
【請求項3】 請求項1または2記載のポリアミド樹脂
組成物よりなる、滑り性の優れた包装用フィルム。
3. A packaging film having excellent slipperiness, which comprises the polyamide resin composition according to claim 1 or 2.
JP29073293A 1993-11-19 1993-11-19 Polyamide resin composition and packaging film prepared therefrom Pending JPH07138471A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29073293A JPH07138471A (en) 1993-11-19 1993-11-19 Polyamide resin composition and packaging film prepared therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29073293A JPH07138471A (en) 1993-11-19 1993-11-19 Polyamide resin composition and packaging film prepared therefrom

Publications (1)

Publication Number Publication Date
JPH07138471A true JPH07138471A (en) 1995-05-30

Family

ID=17759812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29073293A Pending JPH07138471A (en) 1993-11-19 1993-11-19 Polyamide resin composition and packaging film prepared therefrom

Country Status (1)

Country Link
JP (1) JPH07138471A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997003113A1 (en) * 1995-07-11 1997-01-30 W.R. Grace & Co.-Conn. Film having modified surface characteristics through use of combination of spherical and lamellar particulates
KR100233425B1 (en) * 1995-09-12 1999-12-01 구광시 Polyamide resin composition for film uses
JP2002309014A (en) * 2001-04-12 2002-10-23 Toray Ind Inc Mat polyester film and method for producing the same
JP2006111763A (en) * 2004-10-15 2006-04-27 Ube Ind Ltd Polyamide film
FR3006318A1 (en) * 2013-06-03 2014-12-05 Rhodia Operations CHARGES AS AN AGENT FOR REDUCING THE DETERIORATION OF BARRIER PROPERTIES
KR20240031359A (en) 2021-08-31 2024-03-07 도요보 가부시키가이샤 Release film for resin sheet molding

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997003113A1 (en) * 1995-07-11 1997-01-30 W.R. Grace & Co.-Conn. Film having modified surface characteristics through use of combination of spherical and lamellar particulates
US5925454A (en) * 1995-07-11 1999-07-20 W.R. Grace & Co.-Conn. Film having modified surface characteristics through use of combination of spherical and lamellar particulates
JPH11509254A (en) * 1995-07-11 1999-08-17 ダブリユ・アール・グレイス・アンド・カンパニー−コネテイカツト Film with improved surface properties by using a combination of spherical and layered fine particles
KR100233425B1 (en) * 1995-09-12 1999-12-01 구광시 Polyamide resin composition for film uses
JP2002309014A (en) * 2001-04-12 2002-10-23 Toray Ind Inc Mat polyester film and method for producing the same
JP2006111763A (en) * 2004-10-15 2006-04-27 Ube Ind Ltd Polyamide film
FR3006318A1 (en) * 2013-06-03 2014-12-05 Rhodia Operations CHARGES AS AN AGENT FOR REDUCING THE DETERIORATION OF BARRIER PROPERTIES
WO2014195328A1 (en) * 2013-06-03 2014-12-11 Rhodia Operations Fillers used as an agent making it possible to reduce deterioration of barrier properties
KR20240031359A (en) 2021-08-31 2024-03-07 도요보 가부시키가이샤 Release film for resin sheet molding

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