JPH0225935B2 - - Google Patents
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- JPH0225935B2 JPH0225935B2 JP57108219A JP10821982A JPH0225935B2 JP H0225935 B2 JPH0225935 B2 JP H0225935B2 JP 57108219 A JP57108219 A JP 57108219A JP 10821982 A JP10821982 A JP 10821982A JP H0225935 B2 JPH0225935 B2 JP H0225935B2
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C59/00—Surface shaping of articles, e.g. embossing; Apparatus therefor
- B29C59/10—Surface shaping of articles, e.g. embossing; Apparatus therefor by electric discharge treatment
- B29C59/12—Surface shaping of articles, e.g. embossing; Apparatus therefor by electric discharge treatment in an environment other than air
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Description
本発明は、コロナ放電処理効果を実生産レベル
において十分満足し得る程度迄改善向上させる方
法に関するものである。
プラスチツク成形物の放電処理は古くから行な
われている技術であり、特にポリエチレンフイル
ムやポリプロピレンフイルム等のプラスチツクフ
イルム(シートを含む、以下同様)の表面改質に
は欠くことのできない技術となつている。又後述
する種々のプラスチツク成形物についても、品質
改善の為の有用な手段と考えられており、今後益
益適用範囲が拡大していくものと期待されてい
る。しかしその為にはコロナ放電処理による処理
効率自体を向上し、その可能性を探求する必要が
ありこれ迄にも広範囲に亘る改善研究が展開され
ているが、未だ十分とは言えない。
例えば特公昭48−17747には、有機溶剤を放電
部に供給することによつて放電面における化学変
化を促進する技術が記載されているが、プラスチ
ツク成形物中への残留溶剤が問題とされる現今の
状況にはそぐわない。又JOURNAL OF
APPLIED POLYMER SCIENCE VOL15
PP1365〜1375(1971)には、不活性ガス雰囲気下
でコロナ放電処理を行なうことが記載され、プラ
スチツク成形物の表面に対する活性化又は劣化等
の影響が示唆されるに及び大気雰囲気を例えば低
酸素雰囲気に置き換えてコロナ放電処理を行なう
技術も提案される様になつたが、従来の方法、例
えば特公昭56−18381号の方法では、大量の不活
性ガスが必要になつてコスト高を招くという問題
があり、又特開昭57−23634号の方法(走行フイ
ルムに対する不活性雰囲気下のコロナ放電技術)
では、フイルムに随伴して巻込まれる大気を遮断
する為に特殊なシールド構造が要求されて装置ま
わりが複雑になるが、それでも不活性ガスの送給
量は不必要に多くなり、なおかつ完全若しくは略
完全な不活性雰囲気は形成されず、低処理レベル
に甘んじなければならなかつた。その為、フイル
ムを例にとつて説明すれば、高速処理ができない
為に生産性が著じるしく低下するという欠点があ
り、他方低速処理にして処理効果を高めようとす
れば表面損傷による外観不良が発生したりブロツ
キングの増大を招く等の欠陥が現われ、実生産の
レベルにおいては全く不満足なものと言う他な
い。
本発明はこの様な状況に着目してなされたもの
であつて、特殊且つ大がかりな装置が要求されず
又シールド用に大量のガスを消費しなくとも良い
様な技術の開発をめざし鋭意研究の結果完成され
たものである。しかして本発明に係るコロナ放電
処理法とは、少なくとも1対の対向電極が配設さ
れてなるコロナ放電処理装置に、プラスチツク成
形物を連続的に搬入してコロナ放電処理を行なう
方法において、放電側電極の側壁面又は底面から
プラスチツク成形物の処理面に空気組成よりも酸
素濃度の低い単独又は混合気体[具体的には空気
組成から酸素の一部を適当量除いたものや、空気
へ酸素以外のガスを適当量追加したもの、更には
B2、H2、Ar、CO2等の単独又は混合ガス等を包
含するが、以下、低酸素濃度ガスと言う]を吹付
けながらコロナ放電処理を行なうものであり、し
かもこの吹付速度を、上記プラスチツク成形物搬
入速度の1%以上と定めた点に要旨を有するもの
である。
本発明方法が適用されるプラスチツク成形物と
しては、上述のフイルムやシートの他に繊維、パ
イプ、テープ、織物、不織布等の長尺物が挙げら
れ、これら長尺物をコロナ放電処理装置に対して
長手方向に搬入し且つ通過させてコロナ放電処理
を行なう場合に本発明を適用すれば、その効果は
もつとも劇的に発揮されるが、その他の成形物で
あつても、一定の速度で移行させながらコロナ放
電処理を加えるものであれば、本発明を適用する
ことによつて多大の技術的効果を得ることができ
る。又該成形物を構成するポリマーとしては、ポ
リアミド、線状ポリエステル、ポリオレフイン、
ポリカーボネート、ポリ塩化ビニル、ポリ塩化ビ
ニリデン、ポリアクリロニトリル、ポリスチレ
ン、ポリビニルアルコール等の熱可塑性樹脂;フ
エノール樹脂、尿素樹脂、メラミン樹脂、不飽和
ポリエステル樹脂、フラン樹脂等の熱硬化性樹脂
が用いられる。尚これらの樹脂を用いてなる成形
物中には、安定剤、滑剤、耐ブロツキング剤、防
曇剤、紫外線吸収剤、難燃剤、透明化剤、酸化防
止剤、耐光剤、帯電防止剤、染料、顔料等の添加
剤が含有されていても良く、コロナ放電の実施に
悪影響を及ぼさない素材は単独及び複合の如何を
問わず全て本発明の対象として含まれる。
以下実施例図面に準拠しつつ本発明の構成及び
作用効果を明らかにしていくが、図面に示す放電
側電極の構造や配列、更にはカバーの形状等は代
表例であるに過ぎず、又図面ではプラスチツクフ
イルムへの適用例を示したに過ぎないから、これ
らの説明の趣旨に反しないという条件の下では設
計を変更することは本発明の技術的範囲に含まれ
る。
第1図は本発明の実施概念を示す要部断面図、
第2図は放電側電極の一部を示す斜視図であつ
て、図中の1は金属ドラム、2は電極カバー3は
放電側電極、4はガス供給管、5はガス噴出口、
6は走行フイルムを示す。即ちフイルム6は矢印
A方向に回転する金属ドラム1に対して矢印B方
向から導入され、更に矢印C方向へ引出されて行
くが、図示しない高電圧発生機に接続されている
放電側電極3と、ポリエステル、エポキシ樹脂、
セラミツク、クロルスルホン化ポリ界エチレン、
EPラバー等でカバーされた金属ドラム1との間
に数百KC/Sの高周波で数千ないし数万Vの高
電圧をかけることによつて発生する高圧コロナの
影響を受け、例えば自然の大気中であればオゾン
や酸化窒素が生成してフイルム6の表面にカルボ
ニル基やカルボキシル基を生ぜしめることにより
表面が極性化される。しかし本図例においてはコ
ロナ放電の雰囲気全体を電極カバー2によつて大
気から遮断すると共に、放電側電極3にガス噴出
口5を設けフイルム6の表面に向けて低酸素濃度
ガスを吹付ける様に構成しているので、低酸素濃
度ガスの種類に応じた種々の効果(例えばN2ガ
スであれば窒素含有基の形成による接着性、特に
含窒素物体との接着性の向上および放電々極の有
効放電面積拡大による処理効率の向上CO2ガスで
あればコロナ放電効率の改善による接着性の一層
の向上等)を得ることができる。尚図示した放電
側電極3は、その概念を第2図に示す如く放電面
側に向けて開口するガス噴出口5が、該電極3の
長手方向(被処理フイルムの幅方向)に沿つてス
リツト状に形成され、且つ該スリツト底部には適
当間隔を置いてガス供給管4が連通されている。
従つてガス供給管4を通して加圧下に供給された
低酸素濃度ガスはスリツト部内で長手方向に分散
されガス噴出口5からほぼ均等に噴出されるの
で、コロナ放電部の雰囲気が低酸素濃度ガスに置
換される。尚スリツトの長手方向両側(図の手前
側及び向う側、但し向う側は図に現われていな
い。)には、該端面からのガス拡散を防止する目
的で適当な蓋板を取付けることもある。
しかし矢印B方向に沿つて相当の高速度で進入
してくるフイルム6の表面には、若干ながら随伴
空気層が形成されており、コロナ放電部の雰囲気
が低酸素濃度ガスによつて置換されても、フイル
ム6の表面自体は相変らず大気雰囲気を保持した
ままになつており、低酸素濃度ガスをただ漫然と
噴出させるだけのときは、本発明の効果を享受す
ることができない。そこで低酸素濃度ガスを第3
図に示す如く強く噴出させ随伴空気層7を噴気流
8によつて破壊分散させれば、コロナ放電部の雰
囲気を低酸素濃度ガスによつてほぼ完全に置換さ
せることができるのではないかと考え種々検討し
た。その結果随伴空気層7の進入速度が重要な因
子であることを見出し、該空気層7の移動速度
(プラスチツク成形物の搬入速度)に対して少な
くとも1%以上、好ましくは10%以上、更に好ま
しくは40%以上の速度で噴気流8を形成すれば、
随伴空気層を実用上の不都合がない程度に迄破壊
分散することができるということを見出した。尚
プラスチツク成形物の搬入速度は、一般に1〜
500m/分である。
この様な条件を採用することによつて随伴空気
層を破壊分散させることができる様になり、且つ
同時にコロナ放電部の近傍を低酸素濃度ガス雰囲
気で保護することが可能となるので、第1図に示
した電極カバー2は、雰囲気保持用としての機能
よりも、むしろ電極3を機械的な衝撃から保護す
るという機能と随伴流を少しでも抑制する機能の
方が強く期待される様になる。従つて本発明の実
施に当つては、時に電極カバー2を取外すことも
あり得るが、低酸素濃度ガスの消費量を抑制する
為には、雰囲気保持用としての機能を改めて見直
すことが望ましく、例えば第4図に示す如くカバ
ー2の下端(フイルム側)を絞ると同時に、導管
10から低酸素濃度ガスをカバー2内へ導入すれ
ば、該ガスは斜面9の内面に沿つて収束される様
に矢印方向へ流れ、カバー2の入口においてガス
カーテン効果が発揮される。即ち随伴空気層の侵
入が入口側で遮断され、電極カバー2の価値が一
段と向上する。但しフイルム6の出口側(第4図
の右側)についてはカバー2内のガスが走行フイ
ルム6に随伴して排出されていくので、シール性
ないし大気侵入遮断性については入口側ほどの配
慮をする必要性は無いが、前述の様に低酸素濃度
ガス消費量を少なくするという意味においては入
口側と同様の配慮を払うことは有意義である。尚
カバー2の入口側及び出口側における上述のシー
ル機能を最低限度において発揮する為には、フイ
ルムの走行速度に対して少なくとも0.2%以上、
好ましくは10%以上の速度でフイルム面に放出さ
せることが望まれる。尚低酸素濃度ガスの噴出速
度については、ガス噴出口5及びカバー2の出入
口のいずれについても下限側のみを述べたが上限
については実質上制限を設ける必要はなく、せい
ぜい噴出量と噴出効果の見合い並びに経済性か
ら、前者については走行速度の10倍以下、好まし
くは5倍以下、又後者については走行速度の10倍
以下、好ましくは5倍以下を一応の目安と考えれ
ば良い。
第5〜25図は本発明において用いられる放電
側電極の各種構造例及び該構造における噴出ガス
の挙動を示す説明図で、実施例を網羅的に示すも
のではないから、これらを適当に組合わせること
は本発明を実施する者の自由に委ねられる。
第5図は前に示した電極と同一構造のもので、
低酸素濃度ガス(以下単にガスという)は矢印の
様に噴出されていく。第6図の例ではガス噴出口
5を、フイルム進入方向と対向する様に、換言す
ればフイルム上の随伴空気層の進入に対してガス
を真向から吹付ける様に、入口側(図では左側)
へ偏向されている。又電極3の入口側及び出口側
(図では右側)側面に沿つて矢印D及びEで示す
様にガスを流すことも有意義である。第7図は電
極3の先端に、導電性を有する金属焼結体スチー
ルウールあるいは金網の様な多孔質のガス拡散材
料で形成されたガス拡散電極(以下単に拡散電極
という)3′を付加した例である。この場合ガス
噴出口5は拡散電極3′に対するガス供給口とし
ての機能を発揮するものであり、ガスは電極の先
端全体から噴出される。従つてガスの噴出は滑ら
かとなり、コロナ放電部におけるガス雰囲気が安
定するという効果が得られる。第8図は、第7図
の例に対して電極に沿うガス流の形成を付加した
例である。第9図は電極を前後(図の左右、以下
同じ)に分割し、前方側に第7図と同一構成から
なるガス噴出電極を配すると共に後方側にガス噴
出機能の無い通常電極を設け、これらを一体化し
たものである。この例は、随伴空気層を進入の初
期に破壊拡散させようという考えに基づいて設計
されたものである。第10図は電極を3分割し、
中央部に第7図のガス噴出電極を設け、前後の両
端に通常電極を配置した例、第11図は中央に通
常電極を配すると共に前後の両端にガス噴出電極
を配置した例で、その構成は全く逆である。しか
しいずれも随伴空気層を破壊拡散しコロナ放電部
の雰囲気を保護するという効果は同程度に発揮す
る。第12図は、第11図における中央の通常電
極に、第5図と同一構成のガス噴出口5を設けた
例であり、上記効果は更に顕著に発揮される。第
13図は電極3の前後上方にガス噴出パイプ11
を配置した例で、パイプ11から真下に噴出され
たガスは電極に沿つて下降し、第6図について述
べたのと同様の効果を発揮する。尚第6,8図及
び第13図例ではパイプ11によつて集中的にガ
スを噴出させているので少量のガスを効果的に利
用することができる。
第14〜22図は、一方でガスの噴出を行ない
他方でこれを吸引するという方式の例であり、ガ
スを噴出するという面から見る限り既述の例と異
なるところは無いが、このガスを他の部分から吸
引する為、1つには噴出後のガスが強制的に特定
方向へ移動されてコロナ放電部の保護が強化さ
れ、2つには噴出ガスの一部が回収され、場合に
よつてはその一部をそのまま噴出ガス中に混合再
使用することもできるのでガスコストの低減を図
ることができる、等の効果が得られる。但し吸引
側が大気圧以下になると随伴空気層をそのまま電
極の下端側迄引込む恐れがあるので大気圧以上に
保持する必要がある。まず第14図は一方をガス
噴出口5、他方をガス吸引口5′とした例であり、
前者から噴出されたガスの一部は随伴空気層の破
壊分散の為に消費され、残部はフイルム上を伴走
してコロナ放電部の雰囲気を形成した後ガス吸引
口5′から回収されていく。第15図は噴出口5、
吸引口5′に焼結金属を添装した例、第16,1
7図は第11,12図に対応し夫々図の様にガス
を噴出及び吸引させた例であり、いずれも前述の
各効果が十分に発揮される。
第18図は電極3の前後にプレート12,12
を接近配設した例であり、プレート12の下端部
に膨みを持たせると共にガス噴出パイプ11を配
設する。そして電極3とプレート12の間隙内を
上方から吸引して上方へのガス流を形成する様に
しながらパイプ11よりガスを噴出させると、噴
出ガスの一部は前述の膨み部から放出され、特に
入口側では随伴空気層を破壊拡散する。そして残
部は電極3の下面を覆つた後、又は垂直上方へ吸
引されていく。第19図は電極3の中央に第14
図と同様のガス吸引口5′を形成した例、第20
図はその前面に焼結金属を添設した例、第21図
は入口側にのみプレート12を設け、プレート1
2の電極3の間隙からガスを噴出させると共に電
極3の底部全面からもガスを噴出させ、一方プレ
ート12の膨み部にガス吸引管14を臨ませて噴
出ガスを吸引させる例で、この例では随伴空気層
の一部が吸引管14内へ押込まれていく。第22
図は第12,17図の変形例で、元々一体のガス
電極3の先端に焼結金属を添装し、中央のガス噴
出口5については焼結金属の先端まで貫通させて
形成し、両脇のガス吸引口5′は焼結金属の手前
で止めている。そして噴出口5を出たガスは矢印
の様に流れて吸引口5′から回収されていくが、
遂に吸引口5′側からガスを噴出させ噴出口5側
からガスを吸引する様に変更しても良い。
第23〜25図は電極2本を夫々独立させて併
設した例を示し、第5〜22図に示した様な電極
を2本又は3本以上近接して併設するか、複数電
極の相互関係を利用することによつて前述の各効
果を更に顕著なものとすることが推奨できる。ま
ず第23図は無加工の電極を2本近接して併設
し、その近接隙間をスリツトに代わるものとして
下向きにガスを流し、図の如くガスを噴出させる
例であり、第24図は第21,23図の考えを応
用し第21図におけるガス吸引口管14を電極の
両脇に配設したものである。最後に第25図は第
7図の電極と第6図の電極を、ガス吸引間隙15
を残す様に2本並べた例であり、噴出ガスは矢印
で示す方向に流れる。
上記各実施例では電極の下端を平担なものとし
て説明したが、鋭角又は鈍角状に尖らせたもの、
半球状に丸味をもたらせたもの、あるいはこれら
をフイルム通過方向へ2段以上に繰返えさせたも
の(例えば鋸歯状等……)であつてもよく、要は
通過するプラスチツク成形物のコロナ放電処理面
に対して低酸素濃度ガスを吹付ける上で不都合の
ない構成であればどの様な電極構造であつても良
い。
本発明の構成は上述の通りであるが、コロナ放
電処理効果を高める為の手段を別途付加すること
は自由である。この様な手段としては、プラスチ
ツク成形物をコロナ放電と同時期、又は前もつて
加温することが例示され、具体的には火炎によつ
て予備処理を施すことや、プラスチツク成形物が
フイルムの様な長尺物である場合に予め調温ロー
ルを通して長尺物を予熱したり、金属ドラムその
ものを温めておくことが推奨される。もつとも本
発明においては、吹付けるべき低酸素濃度ガスが
電極との接触によつて十分予熱されているので、
上記の手段を付加しなくともコロナ放電処理効果
は極めて高いものが得られる。
次に本発明の実施例及び比較例を説明する。
第1図の装置を用いてアイソタクテイツクポリ
プロピレン(但しポリオキシエチレンアルキルア
ミン:0.6重量%混合)の2軸延伸フイルム(厚
さ20μm)のコロナ放電処理を行なつた。処理条
件及び結果は第1表に示す。尚比較例1として大
気中でコロナ放電処理(窒素ガス吹付けなし)を
行ない、又比較例2として電極カバー内に窒素ガ
スを注入しつつ(但し窒素ガス吹付けを行なわな
いで)コロナ放電処理を行なつた。夫々の処理条
件及び結果は第1表に併記した。
The present invention relates to a method for improving the corona discharge treatment effect to a degree that is sufficiently satisfactory at the actual production level. Electric discharge treatment of plastic molded products is a technology that has been used for a long time, and is indispensable for surface modification of plastic films (including sheets, hereinafter the same), such as polyethylene films and polypropylene films. . The various plastic molded products described below are also considered to be a useful means for improving quality, and the range of benefits and applications is expected to expand in the future. However, for this purpose, it is necessary to improve the processing efficiency itself by corona discharge treatment and explore its possibilities.Although extensive improvement research has been carried out so far, it cannot be said to be sufficient. For example, Japanese Patent Publication No. 48-17747 describes a technique for promoting chemical changes on the discharge surface by supplying an organic solvent to the discharge section, but residual solvent in the plastic molding is a problem. It doesn't suit the current situation. Mata JOURNAL OF
APPLIED POLYMER SCIENCE VOL15
PP1365-1375 (1971) describes that corona discharge treatment is performed in an inert gas atmosphere, and it is suggested that the influence of activation or deterioration on the surface of plastic molded products may occur. Techniques for performing corona discharge treatment in place of the atmosphere have also been proposed, but conventional methods, such as the method disclosed in Japanese Patent Publication No. 18381/1983, require a large amount of inert gas, leading to high costs. There are some problems, and the method of JP-A-57-23634 (corona discharge technology under inert atmosphere for running film)
In this case, a special shield structure is required to block the atmosphere that is entrained by the film, which complicates the equipment. A completely inert atmosphere was not created and low treatment levels had to be settled. For this reason, taking film as an example, it has the disadvantage that high-speed processing is not possible, resulting in a significant drop in productivity.On the other hand, if you try to increase the processing effect by using low-speed processing, the appearance of the film due to surface damage. Defects such as defects and increased blocking occur, and it can only be said to be completely unsatisfactory at the level of actual production. The present invention has been made with attention to this situation, and is the result of intensive research aimed at developing a technology that does not require special and large-scale equipment and does not require the consumption of large amounts of gas for shielding. The result is complete. However, the corona discharge treatment method according to the present invention is a method in which a plastic molded article is continuously carried into a corona discharge treatment apparatus provided with at least one pair of opposing electrodes and subjected to corona discharge treatment. From the side wall surface or bottom surface of the side electrode to the treated surface of the plastic molding, a single or mixed gas with an oxygen concentration lower than that of the air [specifically, a gas from which an appropriate amount of oxygen has been removed from the air composition, or a gas containing oxygen from the air] Those with an appropriate amount of other gases added, and even
The corona discharge treatment is performed while spraying gases such as B 2 , H 2 , Ar, CO 2 , etc. alone or in combination (hereinafter referred to as low oxygen concentration gas), and this spraying speed is The gist of this is that it is set at 1% or more of the above-mentioned plastic molded article conveyance speed. Plastic molded articles to which the method of the present invention is applied include, in addition to the above-mentioned films and sheets, long articles such as fibers, pipes, tapes, woven fabrics, and nonwoven fabrics. If the present invention is applied to corona discharge treatment by transporting the molded product in the longitudinal direction and passing it through, the effect will be dramatically exhibited, but even with other molded products, the process can be carried out at a constant speed. As long as the corona discharge treatment is applied while the process is being carried out, great technical effects can be obtained by applying the present invention. Polymers constituting the molded product include polyamide, linear polyester, polyolefin,
Thermoplastic resins such as polycarbonate, polyvinyl chloride, polyvinylidene chloride, polyacrylonitrile, polystyrene, and polyvinyl alcohol; thermosetting resins such as phenolic resin, urea resin, melamine resin, unsaturated polyester resin, and furan resin are used. In addition, molded products made using these resins contain stabilizers, lubricants, anti-blocking agents, antifogging agents, ultraviolet absorbers, flame retardants, clarifying agents, antioxidants, light stabilizers, antistatic agents, and dyes. All materials that may contain additives such as pigments and do not adversely affect the implementation of corona discharge are included as objects of the present invention, whether alone or in combination. The structure and effects of the present invention will be clarified below based on the drawings of the embodiments, but the structure and arrangement of the discharge side electrodes and the shape of the cover shown in the drawings are only representative examples. Since the above is merely an example of application to plastic film, it is within the technical scope of the present invention to change the design as long as it does not go against the spirit of these descriptions. FIG. 1 is a sectional view of the main parts showing the implementation concept of the present invention,
FIG. 2 is a perspective view showing a part of the discharge side electrode, in which 1 is a metal drum, 2 is an electrode cover 3 is a discharge side electrode, 4 is a gas supply pipe, 5 is a gas outlet,
6 indicates a running film. That is, the film 6 is introduced from the direction of arrow B into the metal drum 1 rotating in the direction of arrow A, and is further pulled out in the direction of arrow C. , polyester, epoxy resin,
Ceramic, chlorosulfonated polyethylene,
Under the influence of high-pressure corona generated by applying a high voltage of several thousand to tens of thousands of V at a high frequency of several hundred KC/S between the metal drum 1 covered with EP rubber etc. If it is inside, ozone and nitrogen oxide are generated to generate carbonyl groups and carboxyl groups on the surface of the film 6, thereby polarizing the surface. However, in this example, the entire corona discharge atmosphere is isolated from the atmosphere by the electrode cover 2, and a gas outlet 5 is provided on the discharge side electrode 3 to blow low oxygen concentration gas toward the surface of the film 6. Since the structure is composed of Improved processing efficiency by expanding the effective discharge area of CO 2 gas, it is possible to obtain further improvements in adhesion by improving corona discharge efficiency. The concept of the illustrated discharge side electrode 3 is that, as shown in FIG. Gas supply pipes 4 are connected to the bottom of the slit at appropriate intervals.
Therefore, the low oxygen concentration gas supplied under pressure through the gas supply pipe 4 is dispersed in the longitudinal direction within the slit section and is ejected almost uniformly from the gas outlet 5, so that the atmosphere in the corona discharge section becomes a low oxygen concentration gas. Replaced. In addition, appropriate cover plates may be attached to both sides of the slit in the longitudinal direction (the front side and the opposite side in the figure, however, the opposite side is not shown in the figure) for the purpose of preventing gas diffusion from the end face. However, a slight accompanying air layer is formed on the surface of the film 6 that enters at a considerably high speed in the direction of arrow B, and the atmosphere in the corona discharge area is replaced by low oxygen concentration gas. However, the surface of the film 6 itself still retains the atmospheric atmosphere, and the effects of the present invention cannot be enjoyed if the low oxygen concentration gas is simply spouted out aimlessly. Therefore, low oxygen concentration gas is used as a third
We believe that if the accompanying air layer 7 is destroyed and dispersed by the jet flow 8 by ejecting it strongly as shown in the figure, the atmosphere in the corona discharge area can be almost completely replaced by low oxygen concentration gas. Various considerations were made. As a result, it was found that the intrusion speed of the accompanying air layer 7 is an important factor, and it is at least 1% or more, preferably 10% or more, and more preferably If a jet stream 8 is formed at a speed of 40% or more,
It has been found that the accompanying air layer can be destroyed and dispersed to the extent that there is no practical problem. Furthermore, the conveyance speed of plastic moldings is generally 1~
500m/min. By adopting such conditions, it becomes possible to destroy and disperse the accompanying air layer, and at the same time, it becomes possible to protect the vicinity of the corona discharge part with a low oxygen concentration gas atmosphere. The electrode cover 2 shown in the figure is expected to have a function of protecting the electrode 3 from mechanical shock and suppressing the accompanying flow even slightly, rather than a function of maintaining the atmosphere. . Therefore, when implementing the present invention, the electrode cover 2 may be removed from time to time, but in order to suppress the consumption of low oxygen concentration gas, it is desirable to reconsider its function for maintaining the atmosphere. For example, as shown in FIG. 4, if the lower end (film side) of the cover 2 is squeezed and at the same time low oxygen concentration gas is introduced into the cover 2 from the conduit 10, the gas will be converged along the inner surface of the slope 9. The gas flows in the direction of the arrow, and a gas curtain effect is exerted at the inlet of the cover 2. That is, the intrusion of the entrained air layer is blocked on the inlet side, and the value of the electrode cover 2 is further improved. However, on the exit side of the film 6 (the right side in Fig. 4), the gas inside the cover 2 is discharged along with the traveling film 6, so the sealing performance or air infiltration barrier properties should be given the same consideration as on the entrance side. Although it is not necessary, it is meaningful to take the same consideration as on the inlet side in terms of reducing the amount of low oxygen concentration gas consumed as described above. In order to achieve the above-mentioned sealing function on the inlet and outlet sides of the cover 2 to the minimum extent, the pressure should be at least 0.2% or more relative to the film running speed.
It is desirable to release it onto the film surface preferably at a rate of 10% or more. Regarding the ejection speed of low oxygen concentration gas, only the lower limit side has been described for both the gas ejection port 5 and the inlet/outlet of the cover 2, but there is no practical need to set an upper limit on the ejection speed, and at most the ejection amount and ejection effect are limited. From the standpoint of budget and economy, the former should be 10 times or less, preferably 5 times or less, the traveling speed, and the latter should be 10 times or less, preferably 5 times or less, the traveling speed. Figures 5 to 25 are explanatory diagrams showing various structural examples of the discharge side electrode used in the present invention and the behavior of the ejected gas in the structures, and are not meant to exhaustively show the examples, so they may be combined appropriately. This is left to the discretion of the person implementing the invention. Figure 5 shows the same structure as the electrode shown previously.
Low oxygen concentration gas (hereinafter simply referred to as gas) is ejected in the direction of the arrow. In the example shown in FIG. 6, the gas outlet 5 is placed on the inlet side (in the figure) so as to face the direction in which the film enters, or in other words, to blow gas directly against the entry of the accompanying air layer on the film. left)
is biased towards. It is also useful to flow the gas along the inlet and outlet (right side in the figure) sides of the electrode 3 as shown by arrows D and E. Fig. 7 shows a gas diffusion electrode (hereinafter simply referred to as diffusion electrode) 3' made of a porous gas diffusion material such as conductive metal sintered steel wool or wire mesh added to the tip of the electrode 3. This is an example. In this case, the gas ejection port 5 functions as a gas supply port to the diffusion electrode 3', and gas is ejected from the entire tip of the electrode. Therefore, the gas is ejected smoothly and the gas atmosphere in the corona discharge section is stabilized. FIG. 8 is an example in which formation of a gas flow along the electrodes is added to the example of FIG. 7. In Fig. 9, the electrode is divided into front and rear (left and right in the figure, the same below), and a gas ejection electrode with the same configuration as Fig. 7 is placed on the front side, and a normal electrode without a gas ejection function is provided on the rear side. These are integrated. This example was designed based on the idea of destroying and diffusing the accompanying air layer at the beginning of the approach. Figure 10 shows the electrode divided into three parts.
An example in which a gas ejection electrode as shown in Fig. 7 is provided in the center and normal electrodes are arranged at both front and rear ends, and Fig. 11 is an example in which a normal electrode is arranged in the center and gas ejection electrodes are arranged at both front and rear ends. The composition is exactly the opposite. However, both methods exhibit the same effect of destroying and diffusing the accompanying air layer and protecting the atmosphere of the corona discharge section. FIG. 12 shows an example in which the central normal electrode in FIG. 11 is provided with a gas outlet 5 having the same configuration as that in FIG. 5, and the above effect is even more pronounced. FIG. 13 shows gas jet pipes 11 in front and above the electrode 3.
In this example, the gas ejected directly below from the pipe 11 descends along the electrodes, producing the same effect as described with reference to FIG. In the examples shown in FIGS. 6, 8, and 13, the gas is ejected in a concentrated manner through the pipe 11, so that a small amount of gas can be effectively utilized. Figures 14 to 22 show examples of a method in which gas is ejected on one side and sucked on the other side.As far as the gas is ejected, there is no difference from the previously described examples, but this gas is Since it is sucked in from other parts, firstly, the ejected gas is forcibly moved in a specific direction, which strengthens the protection of the corona discharge area, and secondly, a part of the ejected gas is recovered, and in some cases In addition, a part of the gas can be mixed and reused in the ejected gas as it is, so that effects such as reduction in gas cost can be obtained. However, if the pressure on the suction side falls below atmospheric pressure, there is a risk that the accompanying air layer will be drawn directly to the lower end of the electrode, so it is necessary to maintain the pressure above atmospheric pressure. First, Fig. 14 shows an example in which one side is a gas jet port 5 and the other side is a gas suction port 5'.
A part of the gas ejected from the former is consumed to destroy and disperse the accompanying air layer, and the remaining part travels on the film to form an atmosphere in the corona discharge area and is then recovered from the gas suction port 5'. Figure 15 shows the spout 5,
Example of adding sintered metal to the suction port 5', No. 16, 1
FIG. 7 corresponds to FIGS. 11 and 12 and is an example in which gas is ejected and sucked as shown in the figures, and each of the above-mentioned effects is fully exhibited in both cases. Figure 18 shows plates 12, 12 before and after the electrode 3.
This is an example in which the plates 12 are disposed close to each other, and the lower end of the plate 12 is bulged and the gas ejection pipe 11 is disposed. Then, when gas is ejected from the pipe 11 while sucking the space between the electrode 3 and the plate 12 from above to form an upward gas flow, a part of the ejected gas is released from the aforementioned bulge. Particularly on the inlet side, the accompanying air layer is destroyed and diffused. The remaining portion covers the lower surface of the electrode 3 or is sucked vertically upward. Figure 19 shows the 14th electrode in the center of electrode 3.
An example in which a gas suction port 5' similar to that shown in the figure is formed, No. 20
The figure shows an example in which sintered metal is attached to the front side, and Figure 21 shows an example in which a plate 12 is provided only on the inlet side.
In this example, gas is ejected from the gap between the two electrodes 3 and also from the entire bottom surface of the electrode 3, while the gas suction pipe 14 is exposed to the bulge of the plate 12 to suck the ejected gas. Then, a part of the entrained air layer is forced into the suction tube 14. 22nd
The figure shows a modification of FIGS. 12 and 17, in which a sintered metal is added to the tip of the gas electrode 3, which was originally integrated, and the gas outlet 5 in the center is formed by penetrating it to the tip of the sintered metal. The side gas suction port 5' is stopped in front of the sintered metal. The gas that exits the spout 5 flows as shown by the arrow and is recovered from the suction port 5'.
Finally, the gas may be ejected from the suction port 5' side and the gas may be sucked from the ejection port 5 side. Figures 23 to 25 show examples in which two electrodes are installed independently and side by side. It is recommended to make each of the above-mentioned effects even more remarkable by using the following. First, Fig. 23 shows an example in which two unprocessed electrodes are placed close together, and the gap between them is used as a slit to flow the gas downward, and the gas is ejected as shown in the figure. , 23 is applied, and the gas suction port pipes 14 in FIG. 21 are arranged on both sides of the electrode. Finally, FIG. 25 shows the electrodes in FIG. 7 and the electrodes in FIG. 6 in the gas suction gap 15.
This is an example of two pipes being lined up so as to leave a gap, and the ejected gas flows in the direction shown by the arrow. In each of the above embodiments, the lower end of the electrode was explained as being flat, but it may be pointed at an acute angle or an obtuse angle.
It may be a hemispherical shape with a rounded shape, or a shape in which these are repeated in two or more stages in the film passing direction (for example, a sawtooth shape, etc.), in short, the shape of the plastic molded object passing through Any electrode structure may be used as long as it does not cause any inconvenience in spraying the low oxygen concentration gas onto the corona discharge treated surface. Although the structure of the present invention is as described above, it is free to add additional means for enhancing the effect of corona discharge treatment. Examples of such means include heating the plastic molding at the same time as the corona discharge or in advance of the corona discharge. If the object is a long object, it is recommended to preheat it through a temperature control roll or warm the metal drum itself. However, in the present invention, since the low oxygen concentration gas to be sprayed is sufficiently preheated by contact with the electrode,
An extremely high corona discharge treatment effect can be obtained even without adding the above-mentioned means. Next, examples and comparative examples of the present invention will be described. A biaxially stretched film (thickness: 20 μm) of isotactic polypropylene (mixed with 0.6% by weight of polyoxyethylene alkylamine) was subjected to corona discharge treatment using the apparatus shown in FIG. The treatment conditions and results are shown in Table 1. As Comparative Example 1, corona discharge treatment was performed in the atmosphere (without nitrogen gas spraying), and as Comparative Example 2, corona discharge treatment was performed while nitrogen gas was injected into the electrode cover (but without nitrogen gas spraying). I did this. The respective treatment conditions and results are also listed in Table 1.
【表】
又ESCA分析(化学分析用電子分光法)によつ
て未処理フイルム及び処理フイルムの表面分析を
行なつたところ第2表に示す結果が得られた。
ESCA法による(N/C)比及び(O/C)比の
測定
ESCAスペクトロメーター(ES−200型:国際
電気株式会社製)を用い、フイルム表面の炭素の
1s軌道スペクトルから求めた積分強度と、窒素の
1s軌道スペクトルから有機性窒素の結合エネルギ
ーに対応するピークより求めた積分強度との比を
算出し、その積分比に基づいて炭素数100個当り
の窒素数を求め、この値を(N/C)比と定義し
て表わした。又フイルム表面の炭素と酸素の比に
ついても、同様に炭素数100個当りの酸素数を
(O/C)比として表わした。[Table] In addition, surface analysis of the untreated film and the treated film was performed by ESCA analysis (electron spectroscopy for chemical analysis), and the results shown in Table 2 were obtained. Measurement of (N/C) ratio and (O/C) ratio by ESCA method Using an ESCA spectrometer (ES-200 model: manufactured by Kokusai Denki Co., Ltd.), carbon on the film surface was measured.
The integrated intensity obtained from the 1s orbital spectrum and the nitrogen
Calculate the ratio of the integrated intensity obtained from the peak corresponding to the binding energy of organic nitrogen from the 1s orbital spectrum, calculate the number of nitrogen per 100 carbons based on the integral ratio, and calculate this value as (N/C ) ratio. The ratio of carbon to oxygen on the film surface was similarly expressed as the number of oxygen per 100 carbon atoms as the (O/C) ratio.
【表】
第2表に示される様に比較例1、2で(O/
C)比が高くフイルム表面からの大気除去が不十
分であるのに対し、実施例では(O/C)比は大
幅に低下している。そして実施例では処理後の
(N/C)比が効果的に上昇すると共に[Δ(O/
C)/Δ(N/C)]も1.09と低い値となつている
(優れた接着性を示すことになる)。即ち第2表の
結果へからフイルム表面への低酸素濃度ガス吹付
けを行なつて始めてフイルム表面の随伴大気を除
去することができ、単に電極カバー内を低酸素濃
度ガス雰囲気とした(比較例2)だけでは随伴空
気の除去は達成されないことが確認された。
かくして第1、2表に示される様に実施例にお
いては、比較例1、2と同一電圧であつても高電
流が得られており又接着特性においても極だつて
優秀な結果が得られた。特に比較例2(単なる低
酸素雰囲気)よりも明らかに良好な結果が得られ
た。
尚電極カバー内の酸素濃度を1%に高めて実施
例及び比較例2を両実験したところ、比較例2で
は比較例1並みの結果になつたが、実施例では良
好な結果が持続された。
本発明の構成は以上述べた通りであるから、以
下要約して述べる様な種々の効果が得られる。
(1) プラスチツク成形物の表面に随伴してコロナ
放電処理部に搬入されてくる大気層が、該表面
へ吹付けられる低酸素濃度ガスによつて確実に
破壊分散される。従つてコロナ放電部の雰囲気
中に大気が混入することは極めて少なくなり、
ガス量が少なくても確実に所望雰囲気が形成さ
れる。
(2) 一方吹付けガスは大気よりも酸素濃度の低い
ガスであるから、コロナ放電雰囲気からは大気
が放遂され、且つ残素濃度が低いものとなり、
放電雰囲気中の酸素濃度が低くなる。
(3) 従つて放電が電極の全面に亘つて均一に行な
われることにより、有効電極面積が拡大される
と共に、単位面積当りの電流値及び電力値が増
大する。換言すれば同一電圧の下でも電流が飛
躍的に増大し、実効電力密度の増加によつてコ
ロナ放電処理効果が向上する。
(4) 又夫々の雰囲気による特有の効果、例えば
N2ガスの存在によるプラスチツク成形物表面
でのアミノ基やイミノ基の形成効果(酸素遮断
性の向上効果)等が極めて高度に発揮される。
(5) 第2表に示される様に本発明方法ではフイル
ム表面のO2付着量を少なくすることができ、
単なる不活性ガス雰囲気では達成できない放電
処理効果(接着性等の向上)を得ることができ
る。[Table] As shown in Table 2, in Comparative Examples 1 and 2 (O/
C) ratio is high and removal of air from the film surface is insufficient, whereas in Examples the (O/C) ratio is significantly lower. In the example, the (N/C) ratio after treatment effectively increases and [Δ(O/
C)/Δ(N/C)] is also a low value of 1.09 (indicating excellent adhesion). In other words, based on the results in Table 2, it is only by spraying low oxygen concentration gas onto the film surface that the accompanying atmosphere on the film surface can be removed, simply creating a low oxygen concentration gas atmosphere inside the electrode cover (comparative example). It was confirmed that 2) alone does not remove the entrained air. Thus, as shown in Tables 1 and 2, in the example, a high current was obtained even at the same voltage as in Comparative Examples 1 and 2, and extremely excellent results were obtained in terms of adhesive properties. . In particular, clearly better results were obtained than in Comparative Example 2 (simple low-oxygen atmosphere). In addition, when the oxygen concentration in the electrode cover was increased to 1% and both the Example and Comparative Example 2 were tested, the results in Comparative Example 2 were similar to those in Comparative Example 1, but the good results in the Example were maintained. . Since the configuration of the present invention is as described above, various effects can be obtained as summarized below. (1) The atmospheric layer carried into the corona discharge treatment section along with the surface of the plastic molded article is reliably destroyed and dispersed by the low oxygen concentration gas sprayed onto the surface. Therefore, it is extremely unlikely that air will be mixed into the atmosphere of the corona discharge area.
Even if the amount of gas is small, the desired atmosphere is reliably formed. (2) On the other hand, since the blown gas has a lower oxygen concentration than the atmosphere, the atmosphere is emitted from the corona discharge atmosphere and the residual concentration is low.
The oxygen concentration in the discharge atmosphere becomes low. (3) Therefore, by discharging uniformly over the entire surface of the electrode, the effective electrode area is expanded, and the current value and power value per unit area are increased. In other words, the current increases dramatically even under the same voltage, and the corona discharge treatment effect improves due to the increase in effective power density. (4) Also, the unique effects of each atmosphere, e.g.
Due to the presence of N 2 gas, the effect of forming amino groups and imino groups on the surface of plastic moldings (improving oxygen barrier properties), etc. is exhibited to an extremely high degree. (5) As shown in Table 2, the method of the present invention can reduce the amount of O 2 attached to the film surface,
It is possible to obtain discharge treatment effects (improvement in adhesion, etc.) that cannot be achieved with a simple inert gas atmosphere.
第1図は本発明の実施状況を示す概念図、第2
図は本発明において用いる放電側電極の見取図、
第3図は随伴大気層の破壊状況を示す説明図、第
4図は電極カバーの一例を示す説明図、第5〜2
5図は本発明において用いる電極と噴出ガスの流
れを例示的に示す説明図である。
1…金属ドラム、2…電極カバー、3…放電側
電極、5…ガス噴出口。
Figure 1 is a conceptual diagram showing the implementation status of the present invention, Figure 2
The figure is a sketch of the discharge side electrode used in the present invention,
Fig. 3 is an explanatory diagram showing the state of destruction of the accompanying atmospheric layer, Fig. 4 is an explanatory diagram showing an example of the electrode cover, and Figs.
FIG. 5 is an explanatory diagram illustrating the electrodes used in the present invention and the flow of ejected gas. DESCRIPTION OF SYMBOLS 1...Metal drum, 2...Electrode cover, 3...Discharge side electrode, 5...Gas outlet.
Claims (1)
ナ放電処理装置に、プラスチツク成形物を連続的
に搬入してコロナ放電処理を行なうに当り、放電
側電極の側壁面に沿つて若しくはその底面からプ
ラスチツク成形物のコロナ放電処理面に向けて、
該プラスチツク成形物搬入速度の1%以上の速度
で、空気組成よりも酸素濃度の低い気体を吹付け
ながらコロナ放電処理を行なうことを特徴とする
プラスチツク成形物表面のコロナ放電処理法。1. When plastic moldings are continuously carried into a corona discharge treatment device comprising at least one pair of electrodes facing each other and subjected to corona discharge treatment, plastic molding is carried out along the side wall surface of the discharge side electrode or from its bottom surface. towards the corona discharge treated surface of the object.
A method for corona discharge treatment of the surface of a plastic molded article, characterized in that the corona discharge treatment is carried out while blowing a gas having a lower oxygen concentration than air at a speed of 1% or more of the conveyance speed of the plastic molded article.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10821982A JPS58225133A (en) | 1982-06-22 | 1982-06-22 | Corona discharge treatment of plastic formed product surface |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10821982A JPS58225133A (en) | 1982-06-22 | 1982-06-22 | Corona discharge treatment of plastic formed product surface |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58225133A JPS58225133A (en) | 1983-12-27 |
| JPH0225935B2 true JPH0225935B2 (en) | 1990-06-06 |
Family
ID=14479049
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10821982A Granted JPS58225133A (en) | 1982-06-22 | 1982-06-22 | Corona discharge treatment of plastic formed product surface |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58225133A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2578176B1 (en) * | 1985-03-04 | 1989-01-13 | Electricite De France | PROCESS AND DEVICE FOR TREATING A FLAT SUBSTRATE BY CROWN DISCHARGE. |
| JPS61204239A (en) * | 1985-03-08 | 1986-09-10 | Idemitsu Petrochem Co Ltd | Surface-treatment of polypropylene resin |
| DE19538176A1 (en) * | 1995-10-13 | 1997-04-17 | Arcotec Oberflaechentech Gmbh | Device for treating flat substrates with a corona station |
| DE19732901C1 (en) * | 1997-07-30 | 1998-11-26 | Tdz Ges Fuer Innovative Oberfl | Surface treatment of plastics by corona discharge |
| DE10302367A1 (en) * | 2003-01-22 | 2004-08-05 | Eltex-Elektrostatik Gmbh | Device for replacing atmospheric oxygen with an inert gas from a laminar air boundary layer and using the same |
| JP4576983B2 (en) * | 2004-11-09 | 2010-11-10 | セイコーエプソン株式会社 | Plasma processing equipment |
| JP6183870B1 (en) * | 2016-05-31 | 2017-08-23 | 春日電機株式会社 | Surface reformer |
| JP6421962B1 (en) * | 2017-08-09 | 2018-11-14 | 春日電機株式会社 | Surface reformer |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5220531Y2 (en) * | 1971-09-08 | 1977-05-12 | ||
| JPS5019300B2 (en) * | 1972-06-09 | 1975-07-05 | ||
| JPS5147060A (en) * | 1974-10-21 | 1976-04-22 | Takano Denki Kogyo Kk | KOSHUHAKORONAHODENSHORISOCHI |
| JPS5496582A (en) * | 1978-01-17 | 1979-07-31 | Toray Ind Inc | Method of treating sheets with corona discharge |
| JPS5723634A (en) * | 1980-07-17 | 1982-02-06 | Tokuyama Soda Co Ltd | Discharge treating apparatus of plastic film |
-
1982
- 1982-06-22 JP JP10821982A patent/JPS58225133A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58225133A (en) | 1983-12-27 |
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