JPS6135217B2 - - Google Patents
Info
- Publication number
- JPS6135217B2 JPS6135217B2 JP56103904A JP10390481A JPS6135217B2 JP S6135217 B2 JPS6135217 B2 JP S6135217B2 JP 56103904 A JP56103904 A JP 56103904A JP 10390481 A JP10390481 A JP 10390481A JP S6135217 B2 JPS6135217 B2 JP S6135217B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- corona discharge
- oxygen concentration
- fatty acid
- discharge treatment
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41M—PRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
- B41M5/00—Duplicating or marking methods; Sheet materials for use therein
- B41M5/0011—Pre-treatment or treatment during printing of the recording material, e.g. heating, irradiating
Landscapes
- Treatments Of Macromolecular Shaped Articles (AREA)
Description
本発明はポリプロピレンフイルムに付与された
帯電防止性を損なうことなく、印刷性を改良する
ための方法に関する。
ポリプロピレンフイルム(以下、PPフイルム
ともいう)は、機械的性質、化学的性質、透明
性、水蒸気遮断性等に優れているため、包装用材
料として広く使用されている。しかし、PPフイ
ルムはその表面特性により印刷性が悪く、汎用の
印刷用インク、例えばセロフアン用インク、水性
インク等による印刷がほとんど不可能であるとい
う欠点を有する。かかる欠点を解消する方法とし
て、本発明者等は既に脂肪酸アミドを含有してな
るPPフイルムを低酸素濃度の窒素ガス雰囲気下
でコロナ放電処理する方法を提案した。上記方法
においては、窒素ガス中の酸素濃度を低くする程
印刷性の優れたPPフイルムを得ることができる
が、該酸素濃度が0.2容量%未満と極めて低くな
つた場合には、帯電防止剤の添加によつてPPフ
イルムに付与された帯電防止性が損なわれるとい
う問題を生ずる。
本発明者等は、上記問題を防止しながら、PP
フイルムの印刷性を改良する方法を開発すべく更
に研究を重ねた。その結果、脂肪酸アミド及び帯
電防止剤を含有するPPフイルムを酸素濃度が0.2
容量%未満の窒素ガス雰囲気下でコロナ放電処理
した場合には、次いで特定の酸素濃度を有する窒
素ガス雰囲気下でコロナ放電処理することにより
所期の目的を達成できることを見い出し、本発明
を完成するに至つた。
即ち、本発明は脂肪酸アミド及び帯電防止剤を
含有するポリプロピレンフイルムの少なくとも片
面を、酸素濃度0.2容量%未満の窒素ガス雰囲気
下でコロナ放電処理した後、酸素濃度0.2〜1.0容
量%の窒素ガス雰囲気下でコロナ放電処理するこ
とを特徴とするポリプロピレンフイルムの処理方
法である。
本発明において、PPフイルムは一軸延伸PPフ
イルム、二軸延伸PPフイルム、及び上記PPフイ
ルムを少なくとも片面に有する複合フイルムの総
称である。また、ポリプロピレンはプロピレンの
ホモポリマー:プロピレンとエチレン、ブテン―
1,4―メチルペンテン―1等のプロピレン以外
のα―オレフインとのコポリマー:ポリプロピレ
〓〓〓〓〓
ンにポリエチレン、アイオノマー、ポリブテン―
1,エチレン―酢酸ビニルコポリマー、無水マレ
イン酸グラフトポリエチレン、アクリル酸グラフ
トポリエチレン、アクリル酸グラフトポリプロピ
レン、無水マレイン酸グラフトポリプロピレン、
テルペン樹脂類、石油樹脂類、ロジン類、クマロ
ン樹脂類、可塑剤等のポリマーや変性剤をポリプ
ロピレンの特性を損なわない範囲内で添加してな
るポリプロピレン組成物が一般に使用される。
本発明において、PPフイルムは脂肪酸アミド
及び帯電防止剤を含有してなる。脂肪酸アミドは
公知のものが特に制限なく使用される。例えば、
オクチルアミド、ノニルアミド、デシルアミド、
ウンデシルアミド、ラウリルアミド、トリデシル
アミド、ミリスチルアミド、パーミチルアミド、
オレイルアミド、ヘキサンシルアミド、オクタコ
シルアミド等が一般に使用される。該脂肪酸アミ
ドのPPフイルム中の含有量は0.01〜0.5重量%、
好ましくは0.05〜0.3重量%の範囲とすることが
後述するコロナ放電処理によりPPフイルムに優
れた印刷性を付与することができ好ましい。また
帯電防止剤も公知のものが何等制限なく使用され
る。代表的な帯電防止剤を例示すれば、グリセリ
ン脂肪酸エステル、ペンタエリスリトール脂肪酸
エステル、アルキルジエタノールアミン、ソルビ
タン脂肪酸エステル、ポリエチレングリコール脂
肪酸エステル、アルキルジエタノールアミン脂肪
酸エステル、アルキルベンゼンスルホン酸塩等が
挙げられる。該帯電防止剤のPPフイルム中の含
有量はPPフイルムに帯電防止性を付与するため
に通常使用されている量とすればよい。一般に、
PPフイルム中に0.1〜3.0重量%、好ましくは、
0.2〜2.0重量%含有させることが好ましい。更
に、本発明においてPPフイルムは通常PPフイル
ム製造時に添加されるその他の添加剤、例えば酸
化防止剤、滑剤、耐ブロツキング剤、紫外線吸収
剤、着色剤等を含有してもよい。
本発明の最大の特徴は前記PPフイルムの少な
くとも片面を、酸素濃度0.2容量%未満の窒素ガ
ス雰囲気下でコロナ放電処理した(以下第1段処
理ともいう)後、酸素濃度0.2〜1.0容量%の窒素
ガス雰囲気下でコロナ放電処理する(以下第2段
処理ともいう)ことである。上記特定の条件下で
コロナ放電処理することにより、帯電防止剤によ
つて付与されたPPフイルムの帯電防止性を損な
うことなく、しかも前記脂肪酸アミドとの作用に
より優れた印刷性を該PPフイルムに付与するこ
とが可能である。即ち、第1段処理と第2段処理
の順序を変えても、また第1段処理及び第2段処
理の酸素濃度の範囲を外れても本発明の効果を発
揮することができない。該第1段処理において酸
素濃度は0.2容量%未満であれば何等制限されな
いが特に0.1容量%未満とすることが好ましい。
また、第2段処理において酸素濃度は0.2〜1.0容
量%の範囲内であれば何等制限されないが、特に
0.3〜0.8容量%の範囲内とすることが好ましい。
本発明において、第1段処理と第2段処理の割
合は特に限定されないが、一般に第1段処理が全
体の30〜90%、好ましくは40〜80%となる如く行
なうのがよい。また、第1段処理及び第2段処理
は合計してPPフイルム1m2当り20〜300W・分、
好ましくは40〜150W・分となるようコロナ放電
処理を行なうことが好ましい。即ち、コロナ放電
処理が上記範囲より弱いと印刷性の付与効果が少
なく、上記範囲より強いとPPフイルムが放電電
撃により損傷を受ける傾向がある。第1段処理と
第2段処理は夫々独立して行なつてもよいし、連
続して行なつてもよい。また、PPフイルムを所
定の酸素濃度を有する窒素ガス雰囲気下でコロナ
放電処理する態様は特に制限されない。例えば、
PPフイルムの表面に所定の酸素濃度を有する窒
素ガスを吹き付けながらコロナ放電処理する態
様、該窒素ガスを存在させた槽内でコロナ放電処
理する態様等が一般的である。
本発明の処理方法において、他の処理条件は公
知のコロナ放電処理における条件が特に制限なく
適用される。例えば、コロナ放電処理と被処理フ
イルムとの間隔は0.5〜3mm程度が一般に採用さ
れる。また、該コロナ放電電極も公知のものが何
等制限なく使用される。
以上の説明より理解される如く、本発明の処理
方法はPPフイルムに付与された帯電防止性を損
なうことなく優れた印刷性を付与することがで
き、汎用性が高いPPフイルムを得ることができ
る。
以下実施例により本発明を説明するが、本発明
はこれらの実施例に限定されるものではない。
尚、実施例中に示した特性値は下記の方法によ
〓〓〓〓〓
り測定した。
1 メルト・インデツクス
ASTMD―1238に従い、宝工業株式会社製メ
ルト・インデクサーを用いて測定した。
2 酸素濃度
日立製作所製ガスクロマトグラフ636050型を
用い、キヤリヤーガスHe、カラム長さ2m、
充填剤モレキユラーシーブ5A(ガスクロ工業
製)で室温にて測定した。
3 透明性(ヘイズ)
JIS K―6714に従い、東洋精機製作所製ヘイ
ズメーターを用いて測定した。この数値が小さ
い程、透明性の良いことを示す。
4 滑り性(動摩擦係数)
上島製作所製摩擦係数測定器を用い、2枚の
フイルムの表裏を重ねて、45mm×45mmの200グ
ラムウエイトを載せフイルムの一方を固定し他
方を30mm/minで引つ張つた時の動摩擦係数を
測定した。
5 耐ブロツキング性
120mm×120mmフイルムのコロナ放電処理を重
ねて1Kgウエイトを載せ、40℃、90%RH条件
下に24時間放置した後、30mm巾サンプルを切出
して引張セン断剥離強度を測定した。
6 濡れ指数
JIS K―6768に従い測定した。
7 着臭
官能テストによりコロナ放電処理面を三段階
判定した。
○:全く臭わない。
△:少し臭う。
×:強く臭う。
8 帯電防止効果(表面固有抵抗)
横河ヒユーレツト・パツカード社製微少電位
差計及びフイルム用電極を用い、23℃、50%
RH雰囲気下に、500Vの直流電圧を印加し、2
分後のコロナ放電処理面の表面固有抵抗を測定
した。
9 印刷性
PPフイルムのコロナ放電処理面に、市販セ
ロフアン用印刷インキ セロカラーST「白」
(東洋インキ製造株式会社製)及び市販水性イ
ンキ デイツクセーフLS#4「白」(大日本イ
ンキ化学工業株式会社製)をマイヤーバーによ
つて塗布し、80℃オーブンで1分間乾燥した
後、23℃、50%RH下に24時間放置した。
イ セロテープ剥離テスト
印刷PPフイルムに18mm巾セロテープ(ニ
チバン株式会社製)を貼付して強く引き剥
し、インキ剥離面積により下表の通り5段階
評価した。
The present invention relates to a method for improving printability without impairing the antistatic properties imparted to polypropylene films. Polypropylene film (hereinafter also referred to as PP film) is widely used as a packaging material because of its excellent mechanical properties, chemical properties, transparency, water vapor barrier properties, etc. However, PP film has poor printability due to its surface characteristics, and has the disadvantage that printing with general-purpose printing inks such as cellophane ink, water-based ink, etc. is almost impossible. As a method to eliminate such drawbacks, the present inventors have already proposed a method in which a PP film containing a fatty acid amide is subjected to a corona discharge treatment in a nitrogen gas atmosphere with a low oxygen concentration. In the above method, a PP film with better printability can be obtained as the oxygen concentration in the nitrogen gas is lowered, but if the oxygen concentration becomes extremely low, less than 0.2% by volume, the antistatic agent may be Addition causes a problem in that the antistatic property imparted to the PP film is impaired. The present inventors have solved the above problem while preventing PP.
Further research was conducted to develop a method to improve the printability of the film. As a result, the oxygen concentration of PP film containing fatty acid amide and antistatic agent was 0.2.
It has been discovered that when corona discharge treatment is performed in a nitrogen gas atmosphere of less than % by volume, the desired objective can be achieved by subsequent corona discharge treatment in a nitrogen gas atmosphere having a specific oxygen concentration, and the present invention has been completed. It came to this. That is, in the present invention, at least one side of a polypropylene film containing a fatty acid amide and an antistatic agent is subjected to a corona discharge treatment in a nitrogen gas atmosphere with an oxygen concentration of less than 0.2% by volume, and then treated with a nitrogen gas atmosphere with an oxygen concentration of 0.2 to 1.0% by volume. This is a method for processing polypropylene film, which is characterized by subjecting it to corona discharge treatment. In the present invention, the PP film is a general term for a uniaxially stretched PP film, a biaxially stretched PP film, and a composite film having the above-mentioned PP film on at least one side. Polypropylene is a homopolymer of propylene: propylene, ethylene, and butene.
Copolymer with α-olefin other than propylene such as 1,4-methylpentene-1: polypropylene
polyethylene, ionomer, polybutene.
1, ethylene-vinyl acetate copolymer, maleic anhydride grafted polyethylene, acrylic acid grafted polyethylene, acrylic acid grafted polypropylene, maleic anhydride grafted polypropylene,
Polypropylene compositions are generally used in which polymers and modifiers such as terpene resins, petroleum resins, rosins, coumaron resins, and plasticizers are added within the range that does not impair the properties of polypropylene. In the present invention, the PP film contains a fatty acid amide and an antistatic agent. Any known fatty acid amide can be used without any particular restriction. for example,
octylamide, nonylamide, decylamide,
undecylamide, laurylamide, tridecylamide, myristylamide, permitylamide,
Oleylamide, hexanecylamide, octacosylamide, etc. are commonly used. The content of the fatty acid amide in the PP film is 0.01 to 0.5% by weight,
Preferably, the content is in the range of 0.05 to 0.3% by weight because it can impart excellent printability to the PP film by the corona discharge treatment described below. Also, known antistatic agents can be used without any restrictions. Typical antistatic agents include glycerin fatty acid ester, pentaerythritol fatty acid ester, alkyl diethanolamine, sorbitan fatty acid ester, polyethylene glycol fatty acid ester, alkyl diethanolamine fatty acid ester, and alkylbenzene sulfonate. The content of the antistatic agent in the PP film may be the amount normally used to impart antistatic properties to the PP film. in general,
0.1-3.0% by weight in PP film, preferably
It is preferable to contain it in an amount of 0.2 to 2.0% by weight. Furthermore, in the present invention, the PP film may contain other additives that are normally added during the production of PP films, such as antioxidants, lubricants, antiblocking agents, ultraviolet absorbers, colorants, and the like. The greatest feature of the present invention is that at least one side of the PP film is subjected to corona discharge treatment in a nitrogen gas atmosphere with an oxygen concentration of less than 0.2% by volume (hereinafter also referred to as first stage treatment), and then Corona discharge treatment is performed in a nitrogen gas atmosphere (hereinafter also referred to as second stage treatment). By performing corona discharge treatment under the above specific conditions, the PP film has excellent printability due to the action with the fatty acid amide, without impairing the antistatic properties of the PP film imparted by the antistatic agent. It is possible to grant. That is, even if the order of the first stage treatment and the second stage treatment is changed, or even if the oxygen concentration is outside the range of the first stage treatment and the second stage treatment, the effects of the present invention cannot be exhibited. In the first stage treatment, the oxygen concentration is not particularly limited as long as it is less than 0.2% by volume, but it is particularly preferably less than 0.1% by volume.
In addition, in the second stage treatment, there are no restrictions on the oxygen concentration as long as it is within the range of 0.2 to 1.0% by volume, but in particular
It is preferably within the range of 0.3 to 0.8% by volume. In the present invention, the ratio of the first stage treatment to the second stage treatment is not particularly limited, but it is generally preferred that the first stage treatment accounts for 30 to 90% of the total, preferably 40 to 80%. In addition, the total of the first stage treatment and second stage treatment is 20 to 300 W/min per 1 m2 of PP film.
It is preferable to perform the corona discharge treatment so that the power is preferably 40 to 150 W·min. That is, if the corona discharge treatment is weaker than the above range, the effect of imparting printability will be small, and if the corona discharge treatment is stronger than the above range, the PP film tends to be damaged by electric discharge shock. The first stage processing and the second stage processing may be performed independently or consecutively. Furthermore, there are no particular limitations on the manner in which the PP film is subjected to the corona discharge treatment in a nitrogen gas atmosphere having a predetermined oxygen concentration. for example,
Common methods include performing corona discharge treatment while spraying nitrogen gas having a predetermined oxygen concentration onto the surface of the PP film, and performing corona discharge treatment in a tank in which the nitrogen gas is present. In the treatment method of the present invention, other treatment conditions may be those in known corona discharge treatment without particular limitation. For example, the distance between the corona discharge treatment and the film to be treated is generally about 0.5 to 3 mm. Furthermore, any known corona discharge electrode may be used without any restriction. As can be understood from the above explanation, the processing method of the present invention can impart excellent printability without impairing the antistatic property imparted to the PP film, and can obtain a highly versatile PP film. . The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples. In addition, the characteristic values shown in the examples were obtained by the following method.
was measured. 1 Melt Index Measured using a melt indexer manufactured by Takara Kogyo Co., Ltd. according to ASTMD-1238. 2 Oxygen concentration Using a gas chromatograph model 636050 manufactured by Hitachi, carrier gas He, column length 2 m,
It was measured at room temperature using the filler Molecular Sieve 5A (manufactured by Gascro Industries). 3 Transparency (Haze) Measured using a haze meter manufactured by Toyo Seiki Seisakusho in accordance with JIS K-6714. The smaller this number is, the better the transparency is. 4 Slip property (coefficient of dynamic friction) Using a friction coefficient measuring device made by Uejima Seisakusho, stack two films front and back, place a 200-gram weight measuring 45 mm x 45 mm, and fix one side of the film while pulling the other at 30 mm/min. The coefficient of dynamic friction was measured when it was stretched. 5. Blocking resistance A 120 mm x 120 mm film was repeatedly subjected to corona discharge treatment, a 1 kg weight was placed on it, and the film was left at 40°C and 90% RH for 24 hours. A 30 mm wide sample was cut out and its tensile shear peel strength was measured. 6 Wetting index Measured according to JIS K-6768. 7. Odor The corona discharge treated surface was evaluated in three grades by a sensory test. ○: No odor at all. △: Slight odor. ×: Strong odor. 8 Antistatic effect (surface specific resistance) Using a micropotentiometer and film electrode manufactured by Yokogawa Heuretsu Packard, 23℃, 50%
Apply 500V DC voltage under RH atmosphere,
The surface resistivity of the corona discharge treated surface was measured after 5 minutes. 9 Printability Commercial cellophane printing ink Cellocolor ST “White” was applied to the corona discharge treated surface of PP film.
(manufactured by Toyo Ink Mfg. Co., Ltd.) and commercially available water-based ink Deitskusafe LS #4 "White" (manufactured by Dainippon Ink & Chemicals Co., Ltd.) were applied using a Mayer bar, dried in an oven at 80°C for 1 minute, and then dried at 23°C. , and left under 50% RH for 24 hours. B. Cellotape Peeling Test A 18 mm wide cellophane tape (manufactured by Nichiban Co., Ltd.) was attached to a printed PP film, and it was strongly peeled off, and the ink peeled area was evaluated in five grades as shown in the table below.
【表】
ロ 揉みテスト
印刷PPフイルムを20回強く揉んでセロテ
ープ剥離強度と同様に5段階評価した。
実施例 1
メルトインデツクス0.8dg/minの粉末状ポリ
プロピレンに、表1に示した種類及び添加量の脂
肪酸アミド及び帯電防止剤をそれぞれ添加してス
ーパーミキサーで混合した後、二軸押出機を用い
て230℃で造粒した。この配合ポリプロピレンペ
レツトを、Tダイを装着した65mmφ一軸押出機を
用いて300℃に加熱溶融させ、40℃の冷却ロール
上に押出し冷却固化させて1.25mm厚さの未延伸シ
ートを作成した。該未延伸シートをロール表面温
度を155℃に調節したロール式縦延伸機を用い縦
方向に5倍、次いで雰囲気温度を160℃に設定し
たオーブン式横延伸機を用いて横方向に10倍延伸
して厚さ25μの二軸延伸PPフイルムを得た。更
に、二軸延伸PPフイルムを30m/分の速度で走
行させながら表1記載の酸素濃度を有する窒素ガ
スを順次フイルム表面に吹き付けながら表1に示
す強度で連続的にコロナ放電処理を行つた。得ら
れたPPフイルムを30℃,50%RH下に3日間熟成
した後、帯電防止性、ヘイズ、滑り性、耐ブロツ
キング性、ぬれ指数、着臭、印刷性を評価し、そ
の結果を表1に示した。
〓〓〓〓〓
[Table] B. Rub test The printed PP film was rubbed vigorously 20 times and evaluated on a 5-grade scale in the same manner as the cellophane tape peel strength. Example 1 To powdered polypropylene with a melt index of 0.8 dg/min, fatty acid amide and antistatic agent of the type and amount shown in Table 1 were added and mixed in a super mixer, and then mixed using a twin screw extruder. and granulated at 230°C. The blended polypropylene pellets were heated and melted at 300°C using a 65mmφ single-screw extruder equipped with a T-die, extruded onto a cooling roll at 40°C, and cooled and solidified to produce an unstretched sheet with a thickness of 1.25mm. The unstretched sheet was stretched 5 times in the machine direction using a roll longitudinal stretching machine with a roll surface temperature adjusted to 155°C, and then 10 times in the transverse direction using an oven type horizontal stretching machine with an ambient temperature of 160°C. A biaxially stretched PP film with a thickness of 25μ was obtained. Further, while the biaxially stretched PP film was traveling at a speed of 30 m/min, nitrogen gas having the oxygen concentration shown in Table 1 was sequentially sprayed onto the film surface, and corona discharge treatment was continuously performed at the intensity shown in Table 1. After the obtained PP film was aged for 3 days at 30°C and 50% RH, its antistatic properties, haze, slipperiness, blocking resistance, wetting index, odor, and printability were evaluated, and the results are shown in Table 1. It was shown to. 〓〓〓〓〓
【表】【table】
【表】
実施例 2
メルトインデツクス7dg/min、エチレン含量
2.5重量%の粉末状エチレンプロピレンランダム
コポリマーに、エルシルアミド0.10重量%及びペ
ンタエリスリトール脂肪酸エステル(第一工業製
薬社:レヂスタツトPE―139)0.3重量%を夫々
添加してスーパーミキサーで混合した後、一軸押
出機を用いて210℃で造粒した。この配合ペレツ
トをTダイを有する65mmφ押出機により240℃で
加熱溶融させ、内部に20℃の冷水を貫流させた、
鏡面仕上硬質クロームメツキを施した冷却ロール
上に40m/minの製膜速度で押出し冷却固化さ
せ、厚さ30μのPPフイルムを作成した。このPP
フイルムを40m/minで走行させ、酸素濃度0.04
〓〓〓〓〓
容積%の窒素ガスをフイルム表面に吹付けなが
ら、処理強度40W・分/m2で第1段処理を、次い
で酸素濃度0.7容積%の窒素ガスをフイルム表面
に吹付けながら処理強度38W・分/m2で第2段処
理を連続的に実施した。得られたPPフイルムは
ヘイズ2.8%、滑り性0.25,耐ブロツキング性10
>,ぬれ指数44dyne/cm、表面固有抵抗2.2×
1011Ω、着臭なし、セロフアン用インキ、水性イ
ンキに対するセロテープ剥離、揉み強度はいずれ
も“5”とすぐれた特性を示した。
〓〓〓〓〓
[Table] Example 2 Melt index 7dg/min, ethylene content
0.10% by weight of erucylamide and 0.3% by weight of pentaerythritol fatty acid ester (Daiichi Kogyo Seiyaku Co., Ltd.: Registat PE-139) were added to 2.5% by weight of powdered ethylene propylene random copolymer, mixed in a super mixer, and then uniaxially extruded. The mixture was granulated using a machine at 210°C. This blended pellet was heated and melted at 240°C using a 65mmφ extruder equipped with a T-die, and cold water at 20°C was flowed through the inside.
A PP film with a thickness of 30 μm was produced by extrusion at a film forming speed of 40 m/min onto a cooling roll coated with mirror-finished hard chrome plating and cooling and solidifying it. This PP
The film was run at 40 m/min, and the oxygen concentration was 0.04.
〓〓〓〓〓
The first stage treatment was carried out at a treatment intensity of 40 W min/m 2 while spraying nitrogen gas at a concentration of 0.7 volume % onto the film surface, and then at a treatment intensity of 38 W min/m 2 while spraying nitrogen gas at a concentration of 0.7 volume % on the film surface. The second stage treatment was carried out continuously in m 2 . The resulting PP film has a haze of 2.8%, slipperiness of 0.25, and blocking resistance of 10.
>, Wetting index 44dyne/cm, surface specific resistance 2.2×
10 11 Ω, no odor, cellophane ink, cellophane ink peeling strength against water-based ink, and rubbing strength were all "5", showing excellent properties. 〓〓〓〓〓
Claims (1)
プロピレンフイルムの少なくとも片面を、酸素濃
度0.2容量%未満の窒素ガス雰囲気下でコロナ放
電処理した後、酸素濃度0.2〜1.0容量%の窒素ガ
ス雰囲気下でコロナ放電処理することを特徴とす
るポリプロピレンフイルムの処理方法。 2 ポリプロピレンフイルムが脂肪酸アミドを
0.01〜0.5重量%含有する特許請求の範囲第1項
記載の方法。[Scope of Claims] 1 At least one side of a polypropylene film containing a fatty acid amide and an antistatic agent is subjected to corona discharge treatment in a nitrogen gas atmosphere with an oxygen concentration of less than 0.2% by volume, and then treated with nitrogen having an oxygen concentration of 0.2 to 1.0% by volume. A method for processing polypropylene film, characterized by corona discharge treatment in a gas atmosphere. 2 Polypropylene film absorbs fatty acid amide
The method according to claim 1, containing 0.01 to 0.5% by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56103904A JPS587429A (en) | 1981-07-04 | 1981-07-04 | How to process polypropylene film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56103904A JPS587429A (en) | 1981-07-04 | 1981-07-04 | How to process polypropylene film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS587429A JPS587429A (en) | 1983-01-17 |
| JPS6135217B2 true JPS6135217B2 (en) | 1986-08-12 |
Family
ID=14366407
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56103904A Granted JPS587429A (en) | 1981-07-04 | 1981-07-04 | How to process polypropylene film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS587429A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63180717U (en) * | 1987-05-14 | 1988-11-22 |
-
1981
- 1981-07-04 JP JP56103904A patent/JPS587429A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63180717U (en) * | 1987-05-14 | 1988-11-22 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS587429A (en) | 1983-01-17 |
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