JPS6097829A - Drawing method of plastic film - Google Patents

Drawing method of plastic film

Info

Publication number
JPS6097829A
JPS6097829A JP20665283A JP20665283A JPS6097829A JP S6097829 A JPS6097829 A JP S6097829A JP 20665283 A JP20665283 A JP 20665283A JP 20665283 A JP20665283 A JP 20665283A JP S6097829 A JPS6097829 A JP S6097829A
Authority
JP
Japan
Prior art keywords
film
heated air
oil mist
hot air
temperature
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.)
Granted
Application number
JP20665283A
Other languages
Japanese (ja)
Other versions
JPH039853B2 (en
Inventor
Junkichi Watanabe
渡辺 純吉
Kenji Tsubouchi
健二 坪内
Shunichi Kawakita
川北 俊一
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.)
Unitika Ltd
Original Assignee
Unitika Ltd
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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP20665283A priority Critical patent/JPS6097829A/en
Publication of JPS6097829A publication Critical patent/JPS6097829A/en
Publication of JPH039853B2 publication Critical patent/JPH039853B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To prevent a drawing film to be contaminated by monomar or oil mist by a method wherein heated air in a drawing device or circulating ducts is contacted to an absorbing device and monomer or oil mist is absorbed. CONSTITUTION:In the biaxial drawing device which uses heated air as heating source, heated air is contacted with absorb agent and monomar, oligomer, and oil mist etc. in the heated air are absorbed and removed by the method heated air is flown in the circurating duct therein an absorb agent layer is arranged or absorb agent is placed at the part of a biaxial drawing device, for instance, on the floor surface, or on the surface of a tenter clip running cover. Because biaxially oriented film without contamination can be got through this method, the said film is useful for a food package material without printing defects or condenser material without defecting electric insulation.

Description

【発明の詳細な説明】 本発明は、延伸プラスチックフィルムの製造法に関する
ものであり、さらに詳しくは表面がモノマー、オリゴマ
ー、オイルミスト等で汚染されない延伸フィルムの製造
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a stretched plastic film, and more particularly to a method for producing a stretched film whose surface is not contaminated with monomers, oligomers, oil mist, etc.

ポリアミド、ポリエステル等の二軸延伸フィルムは強度
、耐熱性、透明性、加工性等に優れ食品包装用途、金銀
糸、コンデンザー、磁気テープ等の工業用途に広く使用
される。
Biaxially stretched films such as polyamide and polyester have excellent strength, heat resistance, transparency, processability, etc., and are widely used for food packaging, gold and silver thread, condensers, magnetic tape, and other industrial applications.

これらのフィルムは溶融製膜後、同時二軸延伸機あるい
はロール式の縦延伸機とテンタ一式の横延伸機の組め合
わされた二段二軸延伸機で二軸延伸されるのが一般的で
あり、さらに同時二軸延伸機あるいは横延伸機は熱風を
加熱源としてフィルムを延伸、結晶化するための温度に
加熱する方法が最も広く用いられる。この場合フィルム
中に含まれる千ツマ〜、オリゴマー等の低分子量物がフ
ィルムより昇華して熱風中に浮遊し1機内の低温部で凝
縮、付着したりあるいは走行するフィルムに随伴して機
外へ流出して冷却されたフィルムに凝縮、付着すること
がしばしば生じる。又延伸機のテンタークリップ走行装
置に給油される潤滑油がオイルミストとなって熱風中に
浮遊し、これがフィルムを汚染することがある。モノマ
ー、オリゴマーあるいはオイルミスト等の何着したフィ
ルムは使用時に種々の問題をひき起こす。食品包装用フ
ィルムの場合は印刷欠陥等の外観不良で問題となりコン
デンサーに使用される場合は電気絶縁不良の原因となる
。特公昭57−36851号公報しこはステンクーの結
晶化ゾーンから冷却ゾーン又は中間ゾーンに流出する加
熱空気を排気ダクトで吸引排出することによりオリゴマ
ーがフィルムに付着するのを防ぐ方法が提案されている
。しかしながらこの方法で実質的な効果を得るには排気
量を大きくする必要があり高温空気の排気によるエネル
ギーロスという問題があり、又ステンター内部の高温設
定ゾーンでもテンタークリップ走行カバー等の局所的低
温部にオリゴマーが凝縮、付着して延伸切断等で熱風の
流れ状態が変化した場合に堆積シタオリゴマー塊が剥離
してフィルムに付着スるというl・ラブルが残る。特開
昭58−65731号公報には熱風を酸化触媒層に通し
てオリゴマーを燃焼させて除去する方法が提案されてい
る。しかしながら酸化触媒は高価であり、オイルミスト
中に含まれる触媒毒により劣化するため寿命が短くあま
り経済的な方法とはいえない。又この方法はポリエステ
ルフィルムには効果があるがポリエステルより融点の低
い樹脂1例えばナイロン6に適用する場合、ナイロン6
の延伸及び熱固定に適した熱風温度では触媒能力は小さ
く、従ってナイロン6等の融点の低い樹脂に適用する場
合は循環熱風の一部を機外に引き出して触媒機能が高く
なる温度まで昇温した後、酸化触媒層に通し、再度降温
してから機内に戻す等の方法を採用しなければならない
After melt-forming, these films are generally biaxially stretched using a simultaneous biaxial stretching machine or a two-stage biaxial stretching machine that combines a roll-type longitudinal stretching machine and a tenter-equipped horizontal stretching machine. Furthermore, the most widely used simultaneous biaxial stretching machine or transverse stretching machine is a method in which hot air is used as a heating source to heat the film to a temperature for stretching and crystallizing the film. In this case, low-molecular-weight substances such as polymers and oligomers contained in the film sublimate from the film and float in the hot air, condensing and adhering in the low-temperature parts of the aircraft, or accompanying the traveling film and leaving the aircraft. Condensation and deposition on the cooled film often occurs. Furthermore, the lubricating oil supplied to the tenter clip traveling device of the stretching machine becomes oil mist that floats in the hot air, which may contaminate the film. Films coated with monomers, oligomers or oil mist cause various problems during use. In the case of food packaging films, there are problems with poor appearance such as printing defects, and when used in capacitors, it causes electrical insulation defects. Japanese Patent Publication No. 57-36851 proposes a method for preventing oligomers from adhering to a film by suctioning and discharging heated air flowing from the crystallization zone to the cooling zone or intermediate zone through an exhaust duct. . However, in order to obtain a substantial effect with this method, it is necessary to increase the displacement, and there is a problem of energy loss due to the exhaust of high-temperature air.Also, even in the high-temperature setting zone inside the stenter, there are local low-temperature parts such as the tenter clip running cover. When the oligomer condenses and adheres to the film and the hot air flow conditions change due to stretching and cutting, etc., the accumulated oligomer mass peels off and adheres to the film, leaving a problem. JP-A-58-65731 proposes a method in which hot air is passed through an oxidation catalyst layer to burn and remove oligomers. However, the oxidation catalyst is expensive and deteriorates due to the catalyst poison contained in the oil mist, so it has a short lifespan and is not a very economical method. This method is effective for polyester films, but when applied to resins 1, such as nylon 6, which have a lower melting point than polyester, nylon 6
The catalytic ability is small at the hot air temperature suitable for stretching and heat fixing. Therefore, when applying to resins with low melting points such as nylon 6, part of the circulating hot air is drawn out of the machine and heated to a temperature that increases the catalytic function. After that, it must be passed through an oxidation catalyst layer, cooled again, and then returned to the inside of the aircraft.

本発明者らは循環熱風中のモノマー、オリゴマー、オイ
ルミスト等の異物を除去する方法について鋭意研究した
結果、これらの異物は活性炭、アルミナ、白土等の安価
な吸着剤で簡単に吸着、除去できること、熱風温度に制
約が少ないこと、再生が容易なことを知り本発明に到達
した。
The inventors of the present invention have conducted intensive research on methods for removing foreign substances such as monomers, oligomers, and oil mist from circulating hot air, and have found that these foreign substances can be easily adsorbed and removed using inexpensive adsorbents such as activated carbon, alumina, and white clay. They discovered that there are few restrictions on hot air temperature and that regeneration is easy, and arrived at the present invention.

本発明に使用される吸着装置としては、流動層式2回転
式、移動層式等の一般的な吸着装置を機外に設けて機内
の熱風をこの装置で処理することも可能であるが2通常
は循環ダクト中に吸着剤層を設けて熱風を流すかあるい
は機内の一部2例えば床面、テンタークリップ走行カバ
ー面等に吸着剤を敷く程度の簡単な方法で効果がある。
As the adsorption device used in the present invention, it is also possible to install a general adsorption device such as a two-rotation fluidized bed type or a moving bed type outside the machine and treat the hot air inside the machine with this device. Usually, a simple method is effective, such as providing an adsorbent layer in the circulation duct and blowing hot air through it, or spreading an adsorbent on a part of the interior of the machine, such as the floor or tenter clip travel cover.

この場合吸着剤としてはできるだけ強固に成形された活
性炭ベレットが最も適している。熱風循環ダクトに吸着
剤層を設ける場合は2例えばこの部分のダクト断面積を
拡大し、圧損を小さくするためと吸着剤ベレット中に残
る微粉を飛ばさないために風速1m/sec以下、さら
に好ましくは0.5m/sec以下とし金銅でサンドイ
ンチした適当厚さの活性炭層を設ける方法が効果的であ
る。又ひとっの循環ダクトに切換ダンパーで流路を選ぶ
ことのできる2組の吸着剤充填ダクトを設け、交互に再
生しながら連続運転を行う方法も採用することができる
。吸着剤による低分子量物質の分離効果は温度が低いほ
ど強いが、フィルムより昇華したモノマー、オリゴマー
等が凝縮する温度以下で使用する場合は吸着剤層の表層
部に凝固物が堆積して効果が急激に低下することがあり
、これを防ぐために吸着装置に種々の工夫を要すること
がある。ナイロンフィルムの場合は、予熱延伸、熱処理
温度。
In this case, the most suitable adsorbent is an activated carbon pellet formed as strongly as possible. When an adsorbent layer is provided in the hot air circulation duct, for example, the cross-sectional area of the duct in this part is expanded, and the wind speed is preferably 1 m/sec or less, more preferably in order to reduce pressure loss and to prevent the fine powder remaining in the adsorbent pellet from being blown away. An effective method is to provide an activated carbon layer with an appropriate thickness sandwiched with gold and copper at a speed of 0.5 m/sec or less. It is also possible to adopt a method in which one circulation duct is provided with two sets of adsorbent-filled ducts whose flow paths can be selected by a switching damper, and continuous operation is performed while regenerating alternately. The lower the temperature, the stronger the effect of the adsorbent on separating low-molecular weight substances, but if it is used below the temperature at which monomers, oligomers, etc. sublimated from the film condense, the effect will be reduced due to the accumulation of coagulates on the surface of the adsorbent layer. There may be a sudden drop, and in order to prevent this, various measures may be required for the adsorption device. For nylon film, preheat stretching and heat treatment temperature.

すなわち約150〜200°Cの広い範囲で効果があり
In other words, it is effective over a wide range of about 150 to 200°C.

ポリエステルフィルムの場合は熱固定ゾーンの温度範囲
すなわち150〜230’cの任意の温度で効果5− がある。七ツマ−、オリゴマー、オイルミスト等を吸着
した活性炭は発火温度が下がり特に空気の流れが停止し
たときなどに活性炭層中に吸着熱による局部的高温部が
生じて発火することがある。
In the case of polyester film, the effect 5- is obtained at any temperature within the temperature range of the heat setting zone, that is, from 150 to 230'C. Activated carbon that has adsorbed nitrates, oligomers, oil mist, etc. may ignite if the ignition temperature decreases, and especially when the air flow is stopped, a localized high temperature area is generated in the activated carbon layer due to the heat of adsorption.

そのため活性炭層には異常時の散水装置又は窒素パージ
装置を設けておくことが望ましい。吸着剤の再生は高温
のスチーム、窒素による脱着又は真空下で脱着すること
により行うことができる。
Therefore, it is desirable to provide the activated carbon layer with a water sprinkler device or a nitrogen purge device in case of an abnormality. Regeneration of the adsorbent can be carried out by desorption with hot steam, nitrogen or desorption under vacuum.

再生及び充填時には吸着剤ベレット中のm粉を除去する
ことが特に重要である。
It is particularly important to remove m powder in the adsorbent pellet during regeneration and filling.

本発明方法の適用を受けるプラスチックフィルムとは延
伸配向可能な任意のものであるが、特にポリエチレンテ
レフタレートで代表されるポリエステルフィルム、ナイ
ロン6、ナイロン66で代表されるポリアミドフィルム
はモノマー、オリゴマーの発生量が多くしかもこれらの
延伸フィルムはフィルムに付着する異物を極度に嫌う用
途に使われることが多いため1本発明方法の効果が大き
い。
The plastic film to which the method of the present invention is applied is any film that can be stretched and oriented, but especially polyester films represented by polyethylene terephthalate and polyamide films represented by nylon 6 and nylon 66 produce monomers and oligomers in large quantities. Moreover, these stretched films are often used in applications where foreign matter adhering to the film is extremely disliked, so the method of the present invention is highly effective.

以下に比較例と実施例により本発明方法う具体的に説明
する。
The method of the present invention will be specifically explained below using comparative examples and examples.

6− 比較例 ナイロン6二軸延伸フィルムを製造中の同時二軸延伸機
、熱固定ゾーン(温度200°C)の熱風循環ダクト中
にハニカム形状のセラミックス甲材に白金触媒のコーテ
ィングされた触媒層を設置し。
6- Comparative Example Simultaneous biaxial stretching machine during production of nylon 6 biaxially stretched film, catalyst layer coated with platinum catalyst on honeycomb-shaped ceramic upper material in hot air circulation duct of heat fixing zone (temperature 200°C) Set up.

ナイロン6フィルムより昇華する低分子量物質及び機内
に浮遊するオイルミストを酸化分解して除去しようと試
みた。触媒層の両側にサンプリング用パイプを挿入し、
小型ファンで触媒層で酸化処理する前と酸化処理した後
の熱風を当量吸い出し。
An attempt was made to remove low molecular weight substances sublimated from the nylon 6 film and oil mist floating inside the machine by oxidative decomposition. Insert sampling pipes on both sides of the catalyst layer,
A small fan sucks out equal amounts of hot air before and after oxidation treatment in the catalyst layer.

コンデンサーに導いて二種類の熱風中に含まれる低分子
M物質とオイルミストの量を調べた。コンデンサーに付
着する白色粉末(低分子量物質)はテスト開始後10目
は処理前と処理後で明確な差異が現れたが、20目でそ
の差は1/2以下と少なくなり33日日では全く差がな
くなった。コンデンサーで凝縮するオイルミストを定量
したところ次の結果をiMだ。(単位g/ day )
従ってテンタ一式目時二軸延伸機でナイロン6フィルム
を製造する際に熱風中に浮遊する低分子量物質及びオイ
ルミストを酸化触媒層で除去する場合、触媒の有効期間
は短かすぎて実用的でないことが判明した。
The amount of low-molecular M substance and oil mist contained in two types of hot air was investigated by introducing it into a condenser. There was a clear difference between the white powder (low molecular weight substance) adhering to the capacitor before and after the treatment on the 10th test after the start of the test, but on the 20th test, the difference decreased to less than 1/2, and on the 33rd day it was completely different. The difference is gone. After quantifying the amount of oil mist that condenses in the condenser, iM has the following results. (Unit: g/day)
Therefore, when using an oxidation catalyst layer to remove low molecular weight substances and oil mist floating in hot air when producing nylon 6 film using a biaxial stretching machine in the first set of tenters, the effective period of the catalyst is too short to be practical. It has been found.

実施例1 比較例と同し装置で触媒層の代わりに活性炭層を用いた
。熱固定ゾーン(温度200°C)の熱風循環ダクトの
断面積を一部拡大して熱風の空塔流速0.5m/sec
とし、ここにステンレス金鋼でサンドイッチした活性炭
ベレット(成田薬品工業(tI製。
Example 1 The same device as in the comparative example was used, except that an activated carbon layer was used instead of the catalyst layer. The cross-sectional area of the hot air circulation duct in the heat fixation zone (temperature 200°C) was partially expanded to increase the superficial flow velocity of hot air to 0.5 m/sec.
Activated carbon pellets (manufactured by Narita Pharmaceutical Industries (tI)) sandwiched between stainless steel and gold steel.

粒状白鷺GX、サイズ6φ×6〜1off)Ftを設け
た。
Granular Shirasagi GX, size 6φ x 6-1 off) Ft was provided.

比較例と同じ条件でナイロンフィルムを製造し ゛なが
ら同じ方法で吸着層の効果を調べたところ吸着分離効果
は良好でしかも約1ケ月間持続した効果が見られた。
When a nylon film was manufactured under the same conditions as in the comparative example and the effect of the adsorption layer was investigated using the same method, it was found that the adsorption separation effect was good and continued for about one month.

実施例2 実施例1と同じ装置でポリエチレンテレフタレートニ軸
延伸フィルムを製造した。この場合は熱固定ゾーンの温
度を230°Cにして吸着層の効果を調べたところポリ
エチレンテレフタレートフィルムより昇華するオリゴマ
ーに対しても吸着分離効果は十分に強く、その効果は1
ケ月以上有効であった。
Example 2 A polyethylene terephthalate biaxially stretched film was produced using the same equipment as in Example 1. In this case, we set the temperature of the heat fixation zone to 230°C and investigated the effect of the adsorption layer, and found that the adsorption separation effect was sufficiently strong even for oligomers that sublimed from the polyethylene terephthalate film.
It has been in effect for over a month.

特許出願人 ユニチカ株式会社 9−Patent applicant: Unitika Co., Ltd. 9-

Claims (1)

【特許請求の範囲】 1、熱風を加熱源とするテンク一式延伸装置でプラスチ
ックフィルムを延伸するに際し、延伸装置内又は循環ダ
クト中の熱風を吸着装置に接触せしめて熱風中の低分子
量物及びオイルミストを吸着。 う3− i4Iすることを特徴とするプラスチックフィ
ルムの延伸方法。
[Claims] 1. When stretching a plastic film using a Tenku complete stretching device that uses hot air as a heating source, the hot air in the stretching device or circulation duct is brought into contact with an adsorption device to remove low molecular weight substances and oil in the hot air. Adsorbs mist. U3- A method for stretching a plastic film, characterized by i4I.
JP20665283A 1983-11-02 1983-11-02 Drawing method of plastic film Granted JPS6097829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20665283A JPS6097829A (en) 1983-11-02 1983-11-02 Drawing method of plastic film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20665283A JPS6097829A (en) 1983-11-02 1983-11-02 Drawing method of plastic film

Publications (2)

Publication Number Publication Date
JPS6097829A true JPS6097829A (en) 1985-05-31
JPH039853B2 JPH039853B2 (en) 1991-02-12

Family

ID=16526891

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20665283A Granted JPS6097829A (en) 1983-11-02 1983-11-02 Drawing method of plastic film

Country Status (1)

Country Link
JP (1) JPS6097829A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003025422A (en) * 2001-07-17 2003-01-29 Mitsubishi Heavy Ind Ltd Tenter oven apparatus
JP2012183833A (en) * 2001-05-30 2012-09-27 Konica Minolta Holdings Inc Method of producing cellulose ester film

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5159974A (en) * 1974-11-08 1976-05-25 Teijin Ltd SUTENTAANAISHOKABUTSUNO JOKYOHOHO
JPS5446274A (en) * 1977-09-21 1979-04-12 Daiafoil Method of making extensible polyester film
JPS5510535A (en) * 1978-07-08 1980-01-25 Fuji Electric Co Ltd Photo-acoustic analyzer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5159974A (en) * 1974-11-08 1976-05-25 Teijin Ltd SUTENTAANAISHOKABUTSUNO JOKYOHOHO
JPS5446274A (en) * 1977-09-21 1979-04-12 Daiafoil Method of making extensible polyester film
JPS5510535A (en) * 1978-07-08 1980-01-25 Fuji Electric Co Ltd Photo-acoustic analyzer

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012183833A (en) * 2001-05-30 2012-09-27 Konica Minolta Holdings Inc Method of producing cellulose ester film
JP2003025422A (en) * 2001-07-17 2003-01-29 Mitsubishi Heavy Ind Ltd Tenter oven apparatus
JP4733303B2 (en) * 2001-07-17 2011-07-27 株式会社日本製鋼所 Tenta oven device

Also Published As

Publication number Publication date
JPH039853B2 (en) 1991-02-12

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