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JPH0360304B2 - - Google Patents
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JPH0360304B2 - - Google Patents

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Publication number
JPH0360304B2
JPH0360304B2 JP28196585A JP28196585A JPH0360304B2 JP H0360304 B2 JPH0360304 B2 JP H0360304B2 JP 28196585 A JP28196585 A JP 28196585A JP 28196585 A JP28196585 A JP 28196585A JP H0360304 B2 JPH0360304 B2 JP H0360304B2
Authority
JP
Japan
Prior art keywords
gas
film
sheet
fluorine
present
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
Application number
JP28196585A
Other languages
Japanese (ja)
Other versions
JPS62140821A (en
Inventor
Tadashi Matsushita
Toshiro Tsukamoto
Yoshiaki Kodama
Yoshio Murakami
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Sanso Co Ltd
Tosoh Corp
Original Assignee
Daido Sanso Co Ltd
Tosoh Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Sanso Co Ltd, Tosoh Corp filed Critical Daido Sanso Co Ltd
Priority to JP28196585A priority Critical patent/JPS62140821A/en
Publication of JPS62140821A publication Critical patent/JPS62140821A/en
Publication of JPH0360304B2 publication Critical patent/JPH0360304B2/ja
Granted legal-status Critical Current

Links

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  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明はインフレーシヨン成形法において吹込
みガスに、不活性ガスにフツ素ガスを含むガスを
用いたフイルム又はシートを製造する方法に関す
る。 更に詳しくは、インフレーシヨン成形法に、吹
込みガスとしてフツ素ガスを含むガスを用いるこ
とによりフイルム又はシートを製造と同時に改質
する方法に関する。 [従来の技術] フイルム又はシートのインフレーシヨン成形方
法は、公知のとおり、材料を押出機の環状ダイス
から押し出し、押し出された材料の先端をピンチ
ロールで挟持し、内部に空気を送り込むことによ
り環状チユーブ状にふくらませつつ連続的に材料
を冷却し巻き取り製品とする方法である。 このようにして得たポリエチレン、ポリプロピ
レンなどの熱可塑性のフイルム又はシートの多く
は、その使用目的により印刷性付与、接着性付与
等の表面改質を行う場合が多い。 これ等表面改質の方法としてはコロナ処理、フ
レーム処理、蒸気処理、酸処理、溶剤処理等があ
るが、これ等の処理方法は必然的に特殊な処理設
備の設置が必要となり、又処理を行なう際の条件
設定が繁雑であつたり、又、フイルム又はシート
の表面を著しく損傷したりする場合がある。 特にポリエチレン、ポリプロピレン等のオレフ
イン系樹脂の大半はインフレーシヨン成形法にて
製品化されており、この製品の多くは更に美粧性
付与、機能性付与を目的として他材料との複合化
を行う為に表面改質が行なわれている。 この表面改質方法としては、前記した処理方法
(コロナ、蒸気、フレーム、酸、溶剤等)の中で
最も簡便なコロナ処理が多く利用されているが、
このコロナ処理方法で得られるフイルム又はシー
トの表面改質度合(一般に表面濡れ張力で表示し
ている)は往々にして経時変化がありばらつきが
生ずるため、部分的に表面改質不足による問題が
発生する。 [発明が解決しようとする問題点] 本発明者等はインフレーシヨン成形方法で得た
フイルム又はシートの表面処理をいかに容易にか
つ効率良く行なうかに付いて鋭意検討した結果本
発明に到達した。 [問題点を解決するための手段] 即ち、本発明はインフレーシヨン成形方法の際
の吹込みガスに、不活性ガスにフツ素ガスを含む
混合ガスを使用することによる容易に表面改質さ
れたフイルム及びシートを得る方法にある。 フツ素ガスにより樹脂表面の性質を改質するこ
とは公知である。 本発明は、前記したようなフイルム又はシート
の改質の為の特別な処理設備の設置を必要とせ
ず、インフレーシヨン成形と同時に、これで得ら
れるフイルム又はシートの改質を行うことに特徴
がある。 インフレーシヨン成形において、押し出しダイ
スから押し出された直後の環状チユーブは熱によ
り軟化した状態であり、この状態でフツ素ガスと
接触させると極めてスムーズに樹脂の表面が改質
されることも本発明の一つの特徴である。 インフレーシヨン成形法を利用して製品とする
熱可塑性樹脂としては、ポリエチレン、ポリプロ
ピレンに代表されるオレフイン系樹脂、塩化ビニ
ル樹脂、ポリアミド樹脂、アイオノマー樹脂、
1,2ポリブタジエン、ポリスチレン樹脂等があ
げられ、又これ等熱可塑性樹脂の変性樹脂および
他モノマーとの重合体があげられる。本発明にお
いても勿論これらの樹脂が用いられる。 本発明で使用する混合ガスとしては不活性ガス
にフツ素を0.1〜20容量%(バルブ入口濃度…以
下同じ)を含有するガスが使用できるが、更に望
ましくはフツ素0.1〜10容量%を含有するガスで
ある。 フツ素濃度0.1容量%未満であると、本製造法
においてはフイルム又はシートの表面改質の効果
が少なく又、改質の度合が不均一となる。又フツ
素濃度を大にすれば得られるフイルム又はシート
は、長時間にわたり高い表面濡れ張力を維持させ
ることができるが、その濃度が必要以上に大にな
ると、フツ素ガスによる樹脂の焼損が起る傾向が
著しく増大する。 本発明に於て、樹脂のインフレーシヨン加工の
際、バブルに吹き込みガス中のフツ素ガスは、時
間と共に順次消費されるが、バブル入口ガス量、
排出ガス量を調節することによりほぼ一定に保つ
ことができる。 本発明で、フツ素ガスを含むガスとシート又は
フイルムとの接触時間は、目的とする表面改質の
度合により決定されるが、通常は前記したガス濃
度及び環状チユーブ(バルブ)の引張速度を調節
することにより行なわれる。又、本発明で実施す
るインフレーシヨン方法は、特に制限はなく、前
記したような、通常一般に行なわれている方法で
ある。 即ち、シート又はフイルムを構成する樹脂の軟
化点以上(通常は前記軟化点の約10℃〜30℃上の
温度)に加熱して溶融状態にした樹脂を、環状ダ
イスより上向又は下向に押し出し、内部にガスを
吹き込みバルブを形成させ、次いでそれを空冷又
は水冷により冷却しフイルム又はシートする方法
である。得られるフイルム又はシートの厚さは
10μ〜150μである。 [発明の効果] 本発明は、吹き込みガスにフツ素を含むガスを
用いるのみの簡単な方法で実施することができ、
又本発明の表面改質法で得られるフイルム又はシ
ートの表面濡れ張力は製造直後の表面濡れ張力を
長期間保持するため、表面改質不足による問題発
生はない。 [実施例] 次に本発明を実施例で更に詳細に説明する。 実施例 インフレーシヨン方法は第1図のフローシート
に示した装置で行なつた。 表−1に本試験で使用した樹脂とインフレーシ
ヨン加工条件を示す。 表−2に使用したガスを示す。 操作は次のようにして行なつた。 押出機4で溶融された樹脂を環状ダイス5より
押し出し、得られたチユーブ状フイルムをニツプ
ロール10にて挟持し、フイルムは巻取機7で巻
き取つた。吹き込みガスは、ガス貯槽2のガスを
ポンプ13により自動弁17を通じてダイス5中
心部より導入した。ガス導入されると溶融樹脂は
膨腸しバブル6となつた。バブル6が一定巾、一
定厚みとなつた後カツター11にて切断し巻取機
7で巻き取つた。 吹き込みガスに、フツ素混合ガスを使用の際
(実施例1〜5、比較例1)ガスポンプ13と排
出ガスポンプ14とバブル径検出器8を連動させ
バブル径が一定となるよう調節した。排出ガスポ
ンプ14より排出されたガスは自動弁18を通じ
排ガス処理装置3へ送り処理した。 又、吹き込みガスに空気を使用の際(比較例2
〜4)はバブル径検出器8とポンプ13を調節し
てバブル径を一定とした。 以上の条件で実施例1〜5及び比較例1〜4の
資料を作成した。 比較の為、樹脂Aを使用して空気e)を用いた
前記加工方法にてフイルムを作成時にコロナ処理
機9を使用し表面処理を行つた(比較例5)。 表−3に実施例1〜5と比較例1〜4の表面濡
れ張力をJIS K6768に基づいて測定した結果と表
面変色についての結果を示す。 表−4に実施例4と比較例5の表面濡れ張力の
経時変化を示す。
[Industrial Field of Application] The present invention relates to a method for producing a film or sheet using a gas containing fluorine gas as an inert gas in an inflation molding method. More specifically, the present invention relates to a method of modifying a film or sheet at the same time as production by using a gas containing fluorine gas as an blown gas in an inflation molding method. [Prior Art] As is well known, the inflation molding method for a film or sheet involves extruding a material from an annular die of an extruder, pinching the tip of the extruded material with pinch rolls, and blowing air into the inside. This method involves continuously cooling the material while inflating it into an annular tube shape to form a rolled product. Many thermoplastic films or sheets, such as polyethylene and polypropylene, obtained in this manner are often subjected to surface modification such as imparting printability or adhesion, depending on the purpose of use. These surface modification methods include corona treatment, flame treatment, steam treatment, acid treatment, and solvent treatment, but these treatment methods inevitably require the installation of special treatment equipment, and they also require the installation of special treatment equipment. Setting conditions for this process may be complicated, and the surface of the film or sheet may be significantly damaged. In particular, the majority of olefin resins such as polyethylene and polypropylene are manufactured using the inflation molding method, and many of these products are composited with other materials for the purpose of adding cosmetic properties and functionality. surface modification has been carried out. As this surface modification method, corona treatment, which is the simplest of the treatment methods mentioned above (corona, steam, flame, acid, solvent, etc.), is often used.
The degree of surface modification of the film or sheet obtained by this corona treatment method (generally expressed as surface wetting tension) often changes over time and varies, resulting in problems due to insufficient surface modification in some areas. do. [Problems to be Solved by the Invention] The present inventors have arrived at the present invention as a result of intensive study on how to easily and efficiently surface-treat a film or sheet obtained by an inflation molding method. . [Means for Solving the Problems] That is, the present invention facilitates surface modification by using a mixed gas containing an inert gas and a fluorine gas as the blown gas during the inflation molding method. The present invention is directed to a method for obtaining films and sheets. It is known to modify the properties of resin surfaces with fluorine gas. The present invention is characterized in that the resulting film or sheet is modified at the same time as inflation molding, without requiring the installation of special processing equipment for modifying the film or sheet as described above. There is. In inflation molding, the annular tube immediately after being extruded from the extrusion die is in a softened state due to heat, and the present invention also shows that when brought into contact with fluorine gas in this state, the surface of the resin is modified extremely smoothly. This is one of the characteristics of Thermoplastic resins manufactured using the inflation molding method include olefin resins such as polyethylene and polypropylene, vinyl chloride resins, polyamide resins, ionomer resins,
Examples include 1,2 polybutadiene and polystyrene resins, as well as modified resins of these thermoplastic resins and polymers with other monomers. Of course, these resins are also used in the present invention. The mixed gas used in the present invention can be an inert gas containing 0.1 to 20% by volume of fluorine (valve inlet concentration...the same applies hereinafter), and more preferably 0.1 to 10% by volume of fluorine. It is a gas that If the fluorine concentration is less than 0.1% by volume, the effect of surface modification of the film or sheet in this production method will be small and the degree of modification will be non-uniform. Films or sheets obtained by increasing the fluorine concentration can maintain high surface wetting tension for a long period of time, but if the concentration becomes higher than necessary, the resin may be burnt out by the fluorine gas. The tendency to increase significantly. In the present invention, during resin inflation processing, the fluorine gas in the gas blown into the bubble is gradually consumed over time, but the amount of gas at the bubble inlet,
By adjusting the amount of exhaust gas, it can be kept almost constant. In the present invention, the contact time between the gas containing fluorine gas and the sheet or film is determined depending on the desired degree of surface modification, but usually the above-mentioned gas concentration and tension speed of the annular tube (valve) are determined. This is done by adjusting. Further, the inflation method used in the present invention is not particularly limited, and may be a commonly used method as described above. That is, the resin that has been heated to a temperature above the softening point of the resin constituting the sheet or film (usually at a temperature of about 10 to 30 degrees Celsius above the softening point) is heated to a molten state, and then passed upward or downward through an annular die. This is a method of extruding, blowing gas into the inside to form a valve, and then cooling it with air or water cooling to form a film or sheet. The thickness of the film or sheet obtained is
It is 10μ to 150μ. [Effects of the Invention] The present invention can be carried out simply by using a fluorine-containing gas as the blowing gas.
Furthermore, since the surface wetting tension of the film or sheet obtained by the surface modification method of the present invention maintains the same surface wetting tension immediately after production for a long period of time, problems due to insufficient surface modification will not occur. [Example] Next, the present invention will be explained in more detail with reference to Examples. EXAMPLE The inflation method was carried out using the apparatus shown in the flow sheet of FIG. Table 1 shows the resins used in this test and the inflation processing conditions. Table 2 shows the gases used. The operation was performed as follows. The resin melted by the extruder 4 was extruded from the annular die 5, and the resulting tube-shaped film was held between nip rolls 10 and wound up by the winder 7. As the blowing gas, gas from the gas storage tank 2 was introduced from the center of the die 5 through an automatic valve 17 using a pump 13. When the gas was introduced, the molten resin expanded and became bubbles 6. After the bubble 6 had a certain width and a certain thickness, it was cut with a cutter 11 and wound up with a winder 7. When a fluorine mixed gas was used as the blowing gas (Examples 1 to 5, Comparative Example 1), the gas pump 13, exhaust gas pump 14, and bubble diameter detector 8 were linked to adjust the bubble diameter to be constant. The gas discharged from the exhaust gas pump 14 was sent to the exhaust gas treatment device 3 through an automatic valve 18 for treatment. Also, when using air as the blowing gas (Comparative Example 2)
-4) Adjusted the bubble diameter detector 8 and pump 13 to keep the bubble diameter constant. Materials for Examples 1 to 5 and Comparative Examples 1 to 4 were created under the above conditions. For comparison, a film was prepared by the above-mentioned processing method using air e) using resin A, and a corona treatment machine 9 was used to perform surface treatment (Comparative Example 5). Table 3 shows the results of measuring the surface wetting tension of Examples 1 to 5 and Comparative Examples 1 to 4 based on JIS K6768, and the results regarding surface discoloration. Table 4 shows changes over time in surface wetting tension of Example 4 and Comparative Example 5.

【表】【table】

【表】【table】

【表】 す。
【represent.

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

図−1は、本発明を実施する装置の一実施態様
を示すフロー図である。 図中1は空気貯槽、2はフツ素混合ガス貯槽、
3は排ガス処理装置、4は押出機、5はダイス、
6はバブル、7は巻取機、8はバブル径検出器、
9は比較例で用いたコロナ処理機、10はニツプ
ロール、11はカツター、12は空気ポンプ、1
3は混合ガスポンプ、14は排ガスポンプ、15
は空気排ガスポンプ、16は空気自動弁、17は
混合ガス自動弁、18は排ガス自動弁を夫々示
す。
FIG. 1 is a flow diagram showing one embodiment of an apparatus implementing the present invention. In the figure, 1 is an air storage tank, 2 is a fluorine mixed gas storage tank,
3 is an exhaust gas treatment device, 4 is an extruder, 5 is a die,
6 is a bubble, 7 is a winder, 8 is a bubble diameter detector,
9 is the corona treatment machine used in the comparative example, 10 is Nipprol, 11 is the cutter, 12 is the air pump, 1
3 is a mixed gas pump, 14 is an exhaust gas pump, 15
16 is an air exhaust gas pump, 16 is an air automatic valve, 17 is a mixed gas automatic valve, and 18 is an exhaust gas automatic valve.

Claims (1)

【特許請求の範囲】[Claims] 1 インフレーシヨン成形法により熱可塑性樹脂
のフイルム又はシートを製造する方法において吹
込みガスに不活性ガスにフツ素ガスを含む混合ガ
スを使用することを特徴とする改質フイルム又は
シートの製造方法。
1. A method for producing a modified film or sheet using an inflation molding method, characterized in that a mixed gas containing an inert gas and a fluorine gas is used as the blown gas. .
JP28196585A 1985-12-17 1985-12-17 Manufacture of modified film or sheet Granted JPS62140821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28196585A JPS62140821A (en) 1985-12-17 1985-12-17 Manufacture of modified film or sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28196585A JPS62140821A (en) 1985-12-17 1985-12-17 Manufacture of modified film or sheet

Publications (2)

Publication Number Publication Date
JPS62140821A JPS62140821A (en) 1987-06-24
JPH0360304B2 true JPH0360304B2 (en) 1991-09-13

Family

ID=17646363

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28196585A Granted JPS62140821A (en) 1985-12-17 1985-12-17 Manufacture of modified film or sheet

Country Status (1)

Country Link
JP (1) JPS62140821A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2587688B2 (en) * 1988-08-18 1997-03-05 大日本印刷株式会社 Antistatic film and method of manufacturing the same
JP2777645B2 (en) * 1988-11-02 1998-07-23 大同ほくさん株式会社 Manufacturing method of wire covering material
US6462142B1 (en) 1999-11-03 2002-10-08 Air Products And Chemicals, Inc. Processes for improved surface properties incorporating compressive heating of reactive gases
JP4632791B2 (en) * 2004-01-09 2011-02-16 ニプロ株式会社 Cell culture vessel

Also Published As

Publication number Publication date
JPS62140821A (en) 1987-06-24

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