JPH0438773B2 - - Google Patents
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- Publication number
- JPH0438773B2 JPH0438773B2 JP30678887A JP30678887A JPH0438773B2 JP H0438773 B2 JPH0438773 B2 JP H0438773B2 JP 30678887 A JP30678887 A JP 30678887A JP 30678887 A JP30678887 A JP 30678887A JP H0438773 B2 JPH0438773 B2 JP H0438773B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- discharge
- high voltage
- film
- electrode
- 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
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- 229920001577 copolymer Polymers 0.000 description 4
- 238000003851 corona treatment Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000011737 fluorine Substances 0.000 description 4
- 229910052731 fluorine Inorganic materials 0.000 description 4
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 3
- 239000003822 epoxy resin Substances 0.000 description 3
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- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- FUSUHKVFWTUUBE-UHFFFAOYSA-N buten-2-one Chemical compound CC(=O)C=C FUSUHKVFWTUUBE-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
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- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
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- 229920011301 perfluoro alkoxyl alkane Polymers 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- -1 trifluorochloroethylene, hexafluoropropylene Chemical group 0.000 description 2
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 description 1
- KTZVZZJJVJQZHV-UHFFFAOYSA-N 1-chloro-4-ethenylbenzene Chemical compound ClC1=CC=C(C=C)C=C1 KTZVZZJJVJQZHV-UHFFFAOYSA-N 0.000 description 1
- UZKWTJUDCOPSNM-UHFFFAOYSA-N 1-ethenoxybutane Chemical compound CCCCOC=C UZKWTJUDCOPSNM-UHFFFAOYSA-N 0.000 description 1
- MBDUIEKYVPVZJH-UHFFFAOYSA-N 1-ethylsulfonylethane Chemical compound CCS(=O)(=O)CC MBDUIEKYVPVZJH-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 229920003319 Araldite® Polymers 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- OWYWGLHRNBIFJP-UHFFFAOYSA-N Ipazine Chemical compound CCN(CC)C1=NC(Cl)=NC(NC(C)C)=N1 OWYWGLHRNBIFJP-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
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- 238000001816 cooling Methods 0.000 description 1
- 238000002788 crimping Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical compound FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 238000003384 imaging method Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052743 krypton Inorganic materials 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 229910052754 neon Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229920003223 poly(pyromellitimide-1,4-diphenyl ether) Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- HKJYVRJHDIPMQB-UHFFFAOYSA-N propan-1-olate;titanium(4+) Chemical compound CCCO[Ti](OCCC)(OCCC)OCCC HKJYVRJHDIPMQB-UHFFFAOYSA-N 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Treatments Of Macromolecular Shaped Articles (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はプラスチツクフイルムなどの高分子樹
脂の表面改質方法に関するものであり、更に詳し
くはフツ素樹脂の表面改質方法に関するものであ
る。
[従来の技術]
今日、高分子樹脂は広範に使用されているが、
種々の用途において、高分子樹脂表面の接着性が
乏しいことが常に問題になつている。このためコ
ロナ放電処理、プラズマ処理、あるいはケミカル
エツチング処理、サンドブラスト処理など種々の
技術を用いて表面改質の検討がなされている。中
でも、フツ素樹脂は他の樹脂に比べて、改質の効
果が低く、極めて改質しにくい樹脂として知られ
ている。このことは逆に耐熱性高分子樹脂の改質
に有効な技術は他の樹脂の表面改質にも有効な技
術となるものと考えられる。
さて、このような表面改質しにくいフツ素樹脂
に対し、いくつかの改質技術が提案されている。
米国特許第3296011には、グリシジルメタクリ
レート、メチルメタクリレート、アクリロニトリ
ル、スチレン、p−クロロスチレン、ビニルブチ
ルエーテル、メチルビニルケトン、ビニルアセテ
ート、1−ヘキサン、キシレン、ヘキサン、シク
ロヘキサン、カーボンテトラクロライド、クロロ
ホルム、テトラヒドロフラン、ジエチルスルホ
ン、N−ビニル−2−ピロリドン、テトラプロピ
ルチタネートなどを含むガス中でコロナ放電処理
する方法が提案され、また特開昭49−12900には
アセトン中でコロナ放電する方法が開示されてい
る。これらの方法によると表面が改質され、接着
性の向上が認められるが次の欠点がある。
フツ素材樹脂は表面改質によつてヒートシー
ルによつて樹脂同志が接着するようになる。こ
のヒートシール温度は低い方が良いが、これら
の方法では未だ温度低下効果が十分でない。例
えば4フツ化エチレン−6フツ化プロピレン共
重合体ではこれらの方法によると240℃程度で
接着するようになるが、実際の用途では200℃
以下、好ましくは180℃程度で使用望まれてい
る。
これらの方法で改質されたフツ素樹脂をヒー
トシール後高温高湿下におくと急激に接着力が
低下する。また紫外線照射に際しても同様の劣
化特性を示す。
種々の用途においては、改質される表面は、
改質したい面のみに限定されることが望まし
い。特にフツ素樹脂についてはこの要求が強
い。しかしこれらの方法では処理面の裏面がま
ばらに処理される重大な欠点がある。このため
処理後ロール状態で放置すると、フイルム同志
がくつつく、いわゆるブロツキングが生じる。
この現象は裏うつりと呼ばれ、コロナ放電処理
では良く生じる現象である。
本発明者らは、特開昭60−9734において、空
気、CO2、H2、N2、NH3、Arを用い、特定の低
温プラズ条件で処理する方法を提案した。本方
法、なかでもNH3ガスを用いた低温プラズマ処
理は極めて有効で、処理された四フツ化エチレン
−六フツ化エチレン共重合フイルム同志は処理条
件を選定すれば、180℃〜200℃の温度条件で接着
でき、またエポキシ樹脂などとの接着力も著しく
向上する。しかしながら、本発明者らがさらに検
討した結果、有効な改質処理をするにはNH3を
ガス濃度で2%以上含有するガスを用いて、低温
プラズマ処理する必要があり、このためアンモニ
アによる処理装置の腐食、真空排気ポンプオイル
の劣化および装置内に残存するアンモニア臭のた
め、実際に工業的に使用することが困難であるこ
とが明確になつた。
[発明が解決しようとする問題点]
本発明は、かかる従来技術の諸欠点に鑑み創案
されたものであり、その目的は作業性が良好で、
かつ経時変化や裏うつりがなく、フツ素樹脂成形
体に良好で安定したヒートシール性と接着性を付
与することのできる処理方法を提供することにあ
る。
[問題点を解決するための手段]
かかる本発明の目的は、高分子樹脂の表面を改
質するに際し、CoH2o+2(nは1〜8の整数)で
表わされる化合物のガスを含むガス雰囲気中で高
電圧の印加によつて開始、維持され、かつプラズ
マ重合物を形成しない放電に上記高分子樹脂表面
をさらすことを特徴とする高分子樹脂の表面改質
方法により達成される。
本発明において使用される高分子樹脂として
は、公知のものがすべて使用できるが、改質効果
の大きい点ではフツ素樹脂であることが好まし
い。
フツ素樹脂としては、4フツ化エチレン、3フ
ツ化塩化エチレン、6フツ化プロピレン、パーフ
ルオロアルコキシエチレン、フツ化ビニル、フツ
化ビニリデンなどのフツ素系モノマの重合体およ
び共重合体、あるいはこれらのモノマとフツ素系
以外のモノマとの共重合体、さらにはこれらの重
合体と他の高分子物との混合物などを挙げること
ができる。なかでもポリテトラフルオロエチレ
ン、4フツ化エチレン−6フツ化プロピレン共重
合体(以下FPEという)、4フツカエチレン−パ
ーフルオロアルコキシエチレン共重合体(以下
PFAという)、4フツ化エチレン−6フツ化プロ
ピレン−パーフルオロアルコキシエチレン共重合
体(以下EPEという)などが好ましく、特に
FEP、PFA、EPEが好ましい。
これらの高分子樹脂の形態は特に限定されるも
のではなく、ブロツク状、板状、シート状、フイ
ルム状、棒状、チユーブ状など各種形態が取りう
るが、特にフイルム状が好ましい。
本発明における放電は、CoH2o+2ガスを含むガ
ス雰囲気中に高電圧を印加し、開始、維持され、
かつプラズマ重合物を形成しない放電である。通
常、有機化合物ガス中で放電処理すると、表面に
プラズマ重合物からなる層が形成されるが、この
重合物が形成されるとフツ素フイルムではヒート
シール性が得られなくなる。
本発明において使用されるCoH2o+2ガスを含む
ガス雰囲気の圧力としては特に限定されないが、
プラズマ重合が形成させず、かつ有効な改質処理
を施すためのより好ましい条件としては、1〜
1,000Torrの範囲が好ましく、より好ましくは
3〜800Torrの範囲である。フツ素樹脂を処理す
るに再し、1Torr未満ではプラズマ重合しやすい
ため、放電電力および処理時間などの最適条件の
範囲が狭く、このため処理の再現性が悪く、また
ヒートシールによる接着性を付与する最適条件と
エポキシ樹脂などに対する接着性改善最適条件と
が異なるなどの問題がある。また1000Torrを越
えると、放電を安定に維持させることが困難で、
処理の効果が低下する。
ガス雰囲気域が1Torr以上になると、放電がア
ーク放電になりやすく、放電を維持することが困
難になるので、高電圧を印加する電極は、ガラス
などの誘電体で被覆することが好ましく、また電
極内部は水冷などして、電極の温度を適切に保つ
ことが好ましい。
高電圧印加電極としては中空棒状構造を有する
ものが好ましく、内部を流す冷媒としては空気、
フレオンまたは水などが挙げられるが、水が好ま
しい。導体の表面を覆う誘電体としてはゴム、ガ
ラス、セラミツクなどが挙げられるが、ガラスが
好ましく、その厚さは0.1〜5mmが好ましい。誘
電体の材質は印加される電圧に対し、十分な耐電
圧をもつものを選択するのがよい。
被処理物を支持する電極の形状は、被処理物の
形態に応じて選択されるが、フイルムなどの長尺
物の場合は被処理物を搬送自在に支持できるドラ
ム状電極であることが好ましく、その大きさは例
えば前記棒状高電圧印加電極の直径に対し、2倍
以上の直径をもつように形成するのがよい。ドラ
ム状電極の少なくとも放電が形成される面は同様
に誘電体で被覆することが重要であり、該誘電体
の厚さ、材質など棒状電極の場合と同様のものが
使用される。
高電圧印加電極と被処理物を支持する電極とは
同数である必要はなく、被処理物を支持する電極
1個に対し、高電圧印加電極を2個以上設けるの
がよい。
電極間の距離は放電条件に応じて適切に設定す
るのがよく、通常圧力条件に応じて0.05〜10cmの
範囲で適切に選択される。
高電圧印加電極に印加する高電圧の周波数は特
に限定されないが、20kHz〜55MHzの範囲で選択
するのが好ましく、よの好ましくは50KHz〜500k
Hzである。
被処理物を支持する電極は接地していてもよい
し、あるいは該電極を大地より浮かし、高電圧電
源の高電圧印加電極との結像端子の対となる出力
端子と結線してもよい。
また当然のことながら、高電圧電源は整合回路
をもつていることが好ましい。
本発明においては、雰囲気のガス組成が極めて
重要であり、少なくともCoH2o+2(nは1〜8)
化合物のガスを含む必要があり、より好ましくは
nが1〜4、最も好ましくはn=1であるCH4で
ある。
雰囲気ガスはCoH2o+2のガスを少なくとも1モ
ル%以上、好ましくは3モル%以上、より好まし
くは5モル%以上含むことが好ましい。
CoH2o+2ガスを希釈するガスとしては、O2およ
びO2を含むガスを除く、He、Ne、Ar、Kr、
Xe、CO2、N2などの不活性ガスまたはこれらの
混合ガスが好ましく、より好ましくは、Arまた
はArを40モル%以上含む不活性ガスである。ま
た好ましい希釈ガスの組み合せはArとCO2、ま
たはArとN2である。
CoH2o+2ガスを含むガス雰囲気下では圧力が高
くなるにしたがい、放電が安定した状態で開始、
維持しにくくなるが、CoH2o+2ガスをArで希釈す
ることによつて安定して放電を開始することが可
能になる。圧力1Torr以上では50モル%以上の
Arを含むガス組成にすることが好ましい。さら
に表面張力を向上させる上で、CO2ガスを添加す
ることがより好ましい。CO2の添加量としては10
〜60モル%が好ましい。
高分子樹脂を処理する際の放電電力としては、
30〜3000W・min/m2の放電電力密度が好まし
く、より好ましくは100〜20000W・min/m2以
上、さらに好ましくな350〜1500W・min/m2で
ある。
なおここでいう放電電力密度とは放電空間へ投
入した電力と時間の積を放電面積を除した量であ
り、フイルムなどのような長尺シートを連続的に
処理する場合は、放電空間に投入した電力をフイ
ルムの長手方向に直角の方向(フイルムの幅方
向)における放電空間の長さと、放電空間を通過
するフイルムの走行速度とで除した量となる。
次に本発明方法を実施装置の1例を用いて説明
する。
第1図において、高分子樹脂フイルム1は送り
出しロール2により放電処理部へ送り出され、ガ
ス導入系8より供給される所定組成のガス中で、
高電圧印加電極3とドラム状電極4との間に、高
電圧電源5より供給、印加された高電圧によつて
開始、維持される放電にふれ、その表面が改質さ
れた後、巻き取りロール7に巻き取られる。
本装置ではドラム状電極4は大地に対し絶縁さ
れているが、出力トランス6のドラム状電極への
配線とドラム状電極とを接地してもよい。またこ
の装置は大気圧より低い圧力雰囲気下で処理する
ものを例示したため、真空排気系9などが設けら
れているが、大気圧以上の圧力雰囲気下で処理す
る場合は、第2図に示すごとく、ガス雰囲気空間
形成用設備10の構造が簡単になり、処理装置全
体が簡易になる。
[実施例]
以下実施例により本発明を具体的に説明する
が、実施例中の物性はそれぞれ次の方法で測定し
たものである。
[物性の測定方法、評価基準]
接着剤によるフイルム同志の貼り合わせ
接着剤として、アラルダイトラピツド(チバガ
イギー・リミテツド、スイス製造、昭和高分子(株)
販売)を用い、これをフイルムの片面に塗布し
て、フイルム同志を貼り合せ、直径10mmのガラス
棒を手でころがしながら圧着した後、100℃で30
分間キユアした。
熱接着によるフイルム同志の貼り合わせ
ヒートシーラを用い、熱板温度180〜240℃、圧
力1.5Kg/cm2、ヒートシール時間10秒の条件で接
着した。
接着力の測定
得られた試料を、万能引つ張り試験機(東洋ボ
ールドウイン製、テンシロン)を用い、180度剥
離テストを行なつた。引張速度は200mm/minで
ある。
実施例 1〜11
厚さ25μのFEPフイルム(東レ(株)製、“トヨフ
ロン”)をCH4を含む混合ガスを用い、第1図の
装置で、第1表に示す条件で処理した。なお高電
圧印加電極としては厚さ1mmのガラスで被覆し、
内部を25℃の水で冷却した鉄管を用い、電極間間
隙は10mmに設定した。
評価結果を第1表に示す。
第1表から明らかなごとく、本発明により得ら
れたサンプルはいずれも180℃でのヒートシール
およびエポキシ樹脂との接着において、380g/
cm以上の接着力を示した。厚さ25μのFEPフイル
ムは380g/cmの張力でネツキング延伸が始まり、
フイルムが伸びた。このため、380g/cm以上の
接着力があれば、FEPを用いる用途においては
実用上十分な接着力があると判断できる。
実施例12,13、比較例1
第2図の装置を用い、実施例1〜11で用いたも
のと同じFEPフイルムを処理した。ガス組成は、
実施例12、13はCH4−CO2−Ar(15:10:75)、
比較例1はアセトン−N2(10:90)とし、放電電
力密度(W・min/m2)は実施例12は520、実施
例13と比較例1はそれぞれ767とした。
各実施例および比較例とも圧力はほぼ大気圧
(760Torr)で、高圧印加電極はガラスで被覆し、
内部は水冷した。またドラム状電極はゴムで被覆
し、同じく内部を水冷した。電極間ギヤツプは1
mmとした。
これらのサンプルの接着力を前述のヒートシー
ルの方法で調べた。また裏うつりの有無を調べる
ため、マジツクインキ(ペンテルペンN50、油
性)で、非処理面に書けるかどうか調べた。
その結果、実施例12,13では180℃のヒートシ
ールで380(g/cm)以上と十分な接着力が得ら
れ、裏うつりも見られなかつた。
これに対し、比較例1では180℃のヒートシー
ルでは30(g/cm)、210℃のヒートシールで120
(g/cm)と不十分で、240℃において始めて380
(g/cm)以上と十分な接着力が得られた。また
比較例1では非処理面に部分的にマジツクインキ
で書ける部分があり、裏うつりが認められた。
実施例 14
実施例1で用いたものと同じFEPフイルムと、
厚さ25μのポリイミドフイルム(東レ(株)製“カプ
トン”)をそれぞれ実施例12と同じ装置を用い、
同一条件で処理した。次いで該処理フイルムの処
理面同志を合せ、ロール温度260℃に調整したロ
ールラミネータを用い、ラミネート速度0.5m/
min、線圧10Kg/cmで貼り合せた。このフイルム
のフイルム間の接着力を測定したところ、0.4
Kg/cm以上の高い接着力を示し、FEPフイルム
がネツキングを起した。
[発明の効果]
本発明は上述のごとく構成したので、フツ素フ
イルムのごとき表面改質のしにくい樹脂に対して
も顕著な改質効果を達成することができるうえ、
従来の方法のように装置の腐蝕や環境汚染をもた
らすことなく、放電による改質を工業的に可能と
なすものである。
【表】DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for surface modification of polymer resins such as plastic films, and more particularly to a method for surface modification of fluororesins. [Prior Art] Today, polymer resins are widely used;
In various applications, poor adhesion of polymer resin surfaces has always been a problem. For this reason, surface modification is being investigated using various techniques such as corona discharge treatment, plasma treatment, chemical etching treatment, and sandblasting treatment. Among these, fluororesins are known to have a lower modification effect than other resins and are extremely difficult to modify. This means that, conversely, techniques that are effective for modifying heat-resistant polymer resins are also considered to be effective techniques for surface modification of other resins. Now, several modification techniques have been proposed for such fluororesins, which are difficult to surface modify. U.S. Pat. No. 3,296,011 includes glycidyl methacrylate, methyl methacrylate, acrylonitrile, styrene, p-chlorostyrene, vinyl butyl ether, methyl vinyl ketone, vinyl acetate, 1-hexane, xylene, hexane, cyclohexane, carbon tetrachloride, chloroform, tetrahydrofuran, A method of corona discharge treatment in a gas containing diethyl sulfone, N-vinyl-2-pyrrolidone, tetrapropyl titanate, etc. has been proposed, and a method of corona discharge treatment in acetone is disclosed in JP-A No. 12900/1983. . These methods modify the surface and improve adhesion, but they have the following drawbacks. Surface modification of the resin material allows the resins to adhere to each other through heat sealing. Although it is better to lower this heat sealing temperature, these methods still do not have a sufficient temperature lowering effect. For example, using these methods, a tetrafluoroethylene-hexafluoropropylene copolymer will bond at about 240°C, but in actual use it will bond at about 200°C.
Below, it is preferably used at about 180°C. If the fluororesin modified by these methods is placed under high temperature and high humidity after heat sealing, the adhesive strength will rapidly decrease. It also exhibits similar deterioration characteristics when exposed to ultraviolet rays. In various applications, the surface to be modified is
It is desirable to limit the modification to only the surface to be modified. This requirement is particularly strong for fluororesins. However, these methods have the serious drawback that the back side of the treated side is sparsely treated. For this reason, if the film is left in a rolled state after processing, so-called blocking occurs, in which the films stick together.
This phenomenon is called Ura Utsuri, and is a phenomenon that often occurs during corona discharge treatment. In JP-A-60-9734, the present inventors proposed a method of processing under specific low-temperature plasma conditions using air, CO 2 , H 2 , N 2 , NH 3 , and Ar. This method, especially the low-temperature plasma treatment using NH 3 gas, is extremely effective, and the treated tetrafluoroethylene-hexafluoride ethylene copolymer film can be produced at temperatures of 180°C to 200°C if the processing conditions are selected. It can be bonded under certain conditions, and its adhesive strength with epoxy resins is also significantly improved. However, as a result of further study by the present inventors, in order to carry out effective reforming treatment, it is necessary to perform low-temperature plasma treatment using a gas containing NH 3 at a gas concentration of 2% or more, and therefore treatment with ammonia is necessary. It became clear that it would be difficult to actually use it industrially due to corrosion of the equipment, deterioration of the vacuum pump oil, and residual ammonia odor within the equipment. [Problems to be Solved by the Invention] The present invention was devised in view of the various drawbacks of the prior art, and its purpose is to improve workability,
Another object of the present invention is to provide a processing method that can impart good and stable heat-sealing properties and adhesive properties to a fluororesin molded article without causing any change over time or backing. [Means for Solving the Problems] The object of the present invention is to use a gas of a compound represented by C o H 2o+2 (n is an integer from 1 to 8) when modifying the surface of a polymer resin. This is achieved by a method for surface modification of a polymer resin, characterized in that the surface of the polymer resin is exposed to an electric discharge that is initiated and maintained by the application of a high voltage in a gas atmosphere containing plasma and that does not form a plasma polymer. . As the polymer resin used in the present invention, all known polymer resins can be used, but fluorocarbon resins are preferable because they have a large modifying effect. Examples of fluororesins include polymers and copolymers of fluorine-based monomers such as tetrafluoroethylene, trifluorochloroethylene, hexafluoropropylene, perfluoroalkoxyethylene, vinyl fluoride, and vinylidene fluoride, or polymers and copolymers of these monomers. copolymers of these monomers with monomers other than fluorine-based monomers, and mixtures of these polymers with other polymers. Among them, polytetrafluoroethylene, tetrafluoroethylene-hexafluoropropylene copolymer (hereinafter referred to as FPE), and tetrafluoroethylene-perfluoroalkoxyethylene copolymer (hereinafter referred to as FPE)
PFA), tetrafluoroethylene-hexafluoropropylene-perfluoroalkoxyethylene copolymer (hereinafter referred to as EPE), etc. are preferred, and particularly
FEP, PFA, EPE are preferred. The form of these polymeric resins is not particularly limited, and may take various forms such as block, plate, sheet, film, rod, and tube, but film is particularly preferred. The discharge in the present invention is started and maintained by applying a high voltage in a gas atmosphere containing C o H 2o +2 gas,
In addition, the discharge does not form plasma polymers. Normally, when discharge treatment is performed in an organic compound gas, a layer made of a plasma polymer is formed on the surface, but when this polymer is formed, the fluorine film cannot obtain heat sealing properties. The pressure of the gas atmosphere containing C o H 2o+2 gas used in the present invention is not particularly limited;
More preferable conditions for not forming plasma polymerization and for effective modification treatment are 1 to 1.
A range of 1,000 Torr is preferred, and a range of 3 to 800 Torr is more preferred. When processing fluororesin, plasma polymerization tends to occur at less than 1 Torr, so the range of optimal conditions such as discharge power and processing time is narrow, resulting in poor processing reproducibility, and adhesion by heat sealing. There are problems such as the optimum conditions for improving adhesion to epoxy resins and the like are different. Moreover, if it exceeds 1000Torr, it is difficult to maintain the discharge stably.
Treatment becomes less effective. When the gas atmosphere exceeds 1 Torr, the discharge tends to become arc discharge and it becomes difficult to maintain the discharge. Therefore, it is preferable to cover the electrode to which high voltage is applied with a dielectric material such as glass. It is preferable to maintain an appropriate temperature of the electrodes by cooling the inside with water or the like. The high voltage application electrode preferably has a hollow rod-like structure, and the refrigerant flowing inside is air,
Examples include freon and water, with water being preferred. Examples of the dielectric material covering the surface of the conductor include rubber, glass, and ceramic, but glass is preferred, and its thickness is preferably 0.1 to 5 mm. It is preferable to select a dielectric material that has sufficient withstand voltage for the applied voltage. The shape of the electrode that supports the object to be processed is selected depending on the form of the object to be processed, but in the case of a long object such as a film, a drum-shaped electrode that can support the object to be processed is preferable. The size thereof is preferably formed to have a diameter twice or more, for example, the diameter of the rod-shaped high voltage applying electrode. It is also important to cover at least the surface of the drum-shaped electrode with a dielectric material, and the thickness and material of the dielectric material are the same as in the case of the rod-shaped electrode. The number of high voltage applying electrodes and the electrodes supporting the object to be processed does not need to be the same, and it is preferable to provide two or more high voltage applying electrodes for one electrode supporting the object to be processed. The distance between the electrodes is preferably set appropriately depending on the discharge conditions, and is usually appropriately selected in the range of 0.05 to 10 cm depending on the pressure conditions. The frequency of the high voltage applied to the high voltage application electrode is not particularly limited, but it is preferably selected in the range of 20kHz to 55MHz, more preferably 50kHz to 500kHz.
It is Hz. The electrode supporting the object to be processed may be grounded, or it may be floated above the ground and connected to an output terminal that is a pair of an imaging terminal with a high voltage application electrode of a high voltage power source. Naturally, it is also preferable that the high voltage power supply has a matching circuit. In the present invention, the gas composition of the atmosphere is extremely important, and at least C o H 2o +2 (n is 1 to 8)
It is necessary to contain a compound gas, more preferably CH 4 where n is 1 to 4, most preferably n=1. It is preferable that the atmospheric gas contains at least 1 mol% or more, preferably 3 mol% or more, and more preferably 5 mol% or more of C o H 2o+2 gas. Gases for diluting C o H 2o+2 gas include He, Ne, Ar, Kr, excluding O 2 and gases containing O 2 .
Inert gases such as Xe, CO 2 and N 2 or mixed gases thereof are preferred, and Ar or an inert gas containing 40 mol % or more of Ar is more preferred. Further, a preferred diluent gas combination is Ar and CO 2 or Ar and N 2 . In a gas atmosphere containing C o H 2o+2 gas, as the pressure increases, discharge starts in a stable state,
Although it becomes difficult to maintain, it becomes possible to stably start the discharge by diluting the C o H 2o+2 gas with Ar. 50 mol% or more at pressures of 1 Torr or more
It is preferable to use a gas composition containing Ar. Furthermore, in order to improve the surface tension, it is more preferable to add CO 2 gas. The amount of CO 2 added is 10
~60 mol% is preferred. The discharge power when processing polymer resin is as follows:
A discharge power density of 30 to 3000 W·min/m 2 is preferable, more preferably 100 to 20000 W·min/m 2 or more, and still more preferably 350 to 1500 W·min/m 2 . The discharge power density here is the product of the power input into the discharge space and the time divided by the discharge area.When processing long sheets such as films continuously, the discharge power density is the product of the power input into the discharge space and time divided by the discharge area. It is the amount obtained by dividing the electric power generated by the length of the discharge space in the direction perpendicular to the longitudinal direction of the film (width direction of the film) and the traveling speed of the film passing through the discharge space. Next, the method of the present invention will be explained using an example of an implementation apparatus. In FIG. 1, a polymer resin film 1 is sent out to a discharge treatment section by a delivery roll 2, and in a gas having a predetermined composition supplied from a gas introduction system 8.
A discharge is started and maintained between the high voltage application electrode 3 and the drum-shaped electrode 4 by the high voltage supplied and applied from the high voltage power source 5, and the surface is modified, and then the drum-shaped electrode 4 is wound up. It is wound up on roll 7. In this device, the drum-shaped electrode 4 is insulated from the ground, but the wiring to the drum-shaped electrode of the output transformer 6 and the drum-shaped electrode may be grounded. In addition, this apparatus is provided with a vacuum exhaust system 9 etc. because it is an example of processing in a pressure atmosphere lower than atmospheric pressure, but when processing is carried out in a pressure atmosphere higher than atmospheric pressure, as shown in Fig. 2. The structure of the gas atmosphere space forming equipment 10 is simplified, and the entire processing apparatus is simplified. [Example] The present invention will be specifically described below with reference to Examples, and the physical properties in the Examples were measured by the following methods. [Measurement method and evaluation criteria for physical properties] Bonding of films together using an adhesive Araldite Rapid (Ciba Geigy Limited, manufactured in Switzerland, Showa Kobunshi Co., Ltd.) was used as the adhesive.
After applying this to one side of the film, pasting the films together, and crimping by rolling a glass rod with a diameter of 10 mm by hand, it was heated at 100℃ for 30
I was curious for a minute. Attaching the films together by thermal adhesion Using a heat sealer, the films were adhered under the conditions of a hot plate temperature of 180 to 240°C, a pressure of 1.5 Kg/cm 2 , and a heat sealing time of 10 seconds. Measurement of Adhesive Strength The obtained sample was subjected to a 180 degree peel test using a universal tensile tester (manufactured by Toyo Baldwin, Tensilon). The tensile speed was 200 mm/min. Examples 1 to 11 FEP films (Toyoflon, manufactured by Toray Industries, Inc.) having a thickness of 25 μm were treated using a mixed gas containing CH 4 in the apparatus shown in FIG. 1 under the conditions shown in Table 1. The high voltage application electrode was covered with 1 mm thick glass.
An iron tube whose interior was cooled with water at 25°C was used, and the gap between the electrodes was set to 10 mm. The evaluation results are shown in Table 1. As is clear from Table 1, all of the samples obtained according to the present invention had a yield of 380g/380g in heat sealing at 180°C and adhesion with epoxy resin.
It showed an adhesive strength of over 1 cm. The 25μ thick FEP film begins to stretch with a tension of 380g/cm.
The film stretched. Therefore, if the adhesive strength is 380 g/cm or more, it can be judged that the adhesive strength is practically sufficient for applications using FEP. Examples 12 and 13, Comparative Example 1 Using the apparatus shown in FIG. 2, the same FEP films as used in Examples 1 to 11 were processed. The gas composition is
Examples 12 and 13 are CH4 - CO2 -Ar (15:10:75),
In Comparative Example 1, acetone-N 2 (10:90) was used, and the discharge power density (W·min/m 2 ) was 520 in Example 12, and 767 in Example 13 and Comparative Example 1. In each example and comparative example, the pressure was approximately atmospheric pressure (760 Torr), and the high voltage application electrode was covered with glass.
The interior was water cooled. The drum-shaped electrode was covered with rubber, and the inside was also water-cooled. The gap between the electrodes is 1
mm. The adhesive strength of these samples was examined using the heat sealing method described above. In addition, to check whether there was any back-printing, we tested whether it was possible to write on the untreated surface using Magizu ink (penterpene N50, oil-based). As a result, in Examples 12 and 13, a sufficient adhesive strength of 380 (g/cm) or more was obtained by heat sealing at 180° C., and no back side peeling was observed. On the other hand, in Comparative Example 1, heat sealing at 180°C was 30 (g/cm), and heat sealing at 210°C was 120 (g/cm).
(g/cm) and 380% at 240°C.
(g/cm) or more, sufficient adhesive strength was obtained. Furthermore, in Comparative Example 1, there were some areas on the untreated surface that could be written with magic ink, and back-printing was observed. Example 14 The same FEP film used in Example 1 and
A polyimide film (“Kapton” manufactured by Toray Industries, Inc.) with a thickness of 25 μm was prepared using the same equipment as in Example 12.
It was treated under the same conditions. Next, the treated surfaces of the treated films were aligned and laminated at a lamination speed of 0.5 m/min using a roll laminator whose roll temperature was adjusted to 260°C.
min, and bonded at a linear pressure of 10 kg/cm. When we measured the adhesive strength between the films, we found that it was 0.4
It showed a high adhesive strength of more than Kg/cm, and the FEP film caused netting. [Effects of the Invention] Since the present invention is configured as described above, it is possible to achieve a remarkable modification effect even on resins that are difficult to surface modify, such as fluorine films, and
This makes modification by electrical discharge industrially possible without causing corrosion of equipment or environmental pollution unlike conventional methods. 【table】
第1図は本発明を実施するための装置の1例を
示す概略断面図、第2図は他の例を示す概略断面
図である。
1…被処理高分子樹脂、3…高電圧印加電極、
4…対向電極、5…高電圧電源、6…出力トラン
ス。
FIG. 1 is a schematic sectional view showing one example of an apparatus for implementing the present invention, and FIG. 2 is a schematic sectional view showing another example. 1...Polymer resin to be treated, 3...High voltage application electrode,
4...Counter electrode, 5...High voltage power supply, 6...Output transformer.
Claims (1)
H2o+2(nは1〜8の整数)で表わされる化合物
のガスを含むガス雰囲気中で、高電圧の印加によ
つて開始、維持され、かつプラズマ重合物を形成
しない放電に上記高分子樹脂表面をさらすことを
特徴とする高分子樹脂の表面改質方法。1 When modifying the surface of polymer resin, C o
In a gas atmosphere containing a gas of a compound represented by H 2o +2 (n is an integer from 1 to 8), the above-mentioned polymer A method for surface modification of polymer resin, characterized by exposing the resin surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30678887A JPH01146930A (en) | 1987-12-03 | 1987-12-03 | Surface modification of polymeric resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30678887A JPH01146930A (en) | 1987-12-03 | 1987-12-03 | Surface modification of polymeric resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01146930A JPH01146930A (en) | 1989-06-08 |
| JPH0438773B2 true JPH0438773B2 (en) | 1992-06-25 |
Family
ID=17961258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30678887A Granted JPH01146930A (en) | 1987-12-03 | 1987-12-03 | Surface modification of polymeric resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01146930A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05318553A (en) * | 1992-05-26 | 1993-12-03 | Daikin Ind Ltd | Tubular laminate and production thereof |
| CN101068860A (en) * | 2004-12-03 | 2007-11-07 | 旭硝子株式会社 | Molded product of ethylene-tetrafluoroethylene copolymer and method for producing the same |
-
1987
- 1987-12-03 JP JP30678887A patent/JPH01146930A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01146930A (en) | 1989-06-08 |
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