JPS58140220A - Heat treatment of polypropylene biaxially oriented film - Google Patents
Heat treatment of polypropylene biaxially oriented filmInfo
- Publication number
- JPS58140220A JPS58140220A JP1131582A JP1131582A JPS58140220A JP S58140220 A JPS58140220 A JP S58140220A JP 1131582 A JP1131582 A JP 1131582A JP 1131582 A JP1131582 A JP 1131582A JP S58140220 A JPS58140220 A JP S58140220A
- Authority
- JP
- Japan
- Prior art keywords
- film
- heating roll
- hot air
- temperature
- roll
- 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
Links
Abstract
Description
【発明の詳細な説明】
本発明はポリプロピレン系二軸延伸フィルムの熱処理方
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for heat treating a biaxially stretched polypropylene film.
二軸延伸さi−+たホリプロピレン糸フィルムは、加熱
収縮性及び経時的な収縮性を有しており、延伸後におい
て収縮熱処理(この明細書において、収縮を促す加熱処
理をいい、単に熱処理ということもある。)を施すこと
によってこれらの物性を短時間で改善できることは公知
の通りであり、その方法についていくつかの報告がなさ
れている。The biaxially stretched i-+ polypropylene yarn film has heat shrinkability and shrinkability over time, and after stretching, it undergoes shrinkage heat treatment (herein, heat treatment to promote shrinkage, simply heat treatment). It is well known that these physical properties can be improved in a short period of time by applying the following methods, and several reports have been made regarding this method.
例えば一般的t(テンタ一方式と呼はれているフィルム
の両端をクリップで掴んだ状態で加熱風によって処理す
る方法は、槽の長さを充分長くすることで実用されてい
るが、これは延伸工程の機構、」−、*−効であって、
装置が泡賄な上価格も高いのでフィルムのI+が狭い場
合、及びチュ−ブラ一方式による延伸フィルムの熱処理
方法としては不適格である。又、クリップの方法や、耳
ロスが問題となる。クリップ無しの熱風処理装置d゛フ
イルム巾著しく輸少し使Mlにたえない。チューブラー
二軸延伸フィルム月1熱処理方法と17で、ダフルバブ
ルカ式があるが、装置の背が高くなる点、操作が困鮒な
点から好ま(2くなく、加熱ロールによる方法の方/バ
一般的である。For example, the general method called the tenter method, in which both ends of the film are held with clips and treated with heated air, is put into practical use by making the length of the tank sufficiently long. The mechanism of the stretching process, ``-, *- effect,
Since the equipment is bulky and expensive, it is unsuitable when the I+ of the film is narrow or as a heat treatment method for stretched films using a tubular type. There are also problems with the clipping method and ear loss. A hot air processing device without a clip has a very large film width, making it difficult to transport and use. Tubular biaxially stretched film monthly heat treatment method and 17, there is a duffle bubble method, but it is preferable because the height of the equipment is high and it is difficult to operate. It is true.
加熱ロールによる方法れ」い装置が筒中であり、小型安
価という点では極めて期待の持てる方法であるが・反面
次の如き欠点を有(7ている。即ち・加熱ロールによっ
て二軸延伸フィルムの熱処理を行う際、該フィルムが加
熱ロールの表面に密着(7ていないと、該フィルムの平
J’F! [+が極めて悪化する。従って一般的には該
フィルムの製造方向(R)の加熱収縮を制限することで
加熱ロールに智着するに必要な張力を得ている、。The heating roll method is an extremely promising method in terms of being small and inexpensive, as the new equipment is in the cylinder.On the other hand, it has the following drawbacks: If the film is not in close contact with the surface of the heating roll (7), the flat J'F![+ of the film will be extremely deteriorated. By restricting the tension, the necessary tension is obtained to adhere to the heating roll.
一方該フイルムの巾方向(横)の加熱収縮度(へ)、加
熱ロール表面との接触摩擦力によってのみ制限されるた
め、縦方向の収縮度に比べ大きくなる。これらの結来得
られた熱処理後の延伸フィルム仁11、縦方向と横力向
の物性に式・があるのみなら−r、縦方向に対しでわj
、充分な熱処理効果が得られていない1゜
本発明の14的C1前記従来の収縮熱処理方法の欠点を
吏1服するととである14
本発明は、未熟収縮処理のポリプロピレン系二軸延伸フ
ィルムを、■加熱ロールに接触させながら収縮熱処理し
7、この際核加熱lコール上での前記フィルムの熱収縮
を制限することによって該フィルj−を該加熱ロールに
密着きせ、■次いで熱風に、l:る4y縮熱処理をする
ことを要旨とする。On the other hand, the degree of heat shrinkage in the width direction (horizontal) of the film is limited only by the contact friction force with the surface of the heating roll, so it is larger than the degree of shrinkage in the longitudinal direction. As a result, if the physical properties of the stretched film layer 11 after heat treatment have the following formulas in the machine direction and the transverse force direction, -r, and the properties in the machine direction are
14th point C1 of the present invention The disadvantages of the conventional shrink heat treatment method are to be addressed. , (2) Heat treatment for shrinkage while contacting with a heating roll 7. At this time, the film is brought into close contact with the heating roll by limiting the heat shrinkage of the film on a nuclear heating coil, (2) Then, heat treatment is carried out in hot air. : The gist is to perform a 4y heat shrinkage treatment.
前記加熱rj−ルにより加熱されたフィルムの最高温度
(1士50・〜150°C程此を採用]2うるが80〜
130“′Cが好11〜V)。この温度が低過ぎると熱
処理が不充分となり、高過き゛ると、フィルムの強度が
低下(−7たり、粘着性に々っでロールに巻き伺!!易
くなったり、異常に収縮して使用不能になったり、二軸
延伸フィルムとしての特性を失なったりするので好葦し
くない。この加熱ロールで熱処理され該ロールを離れる
直前のフィルムは該ロールの表面温度とほぼ等しくなっ
ているので、該ロールの表面温度は50−150“C程
度、より好ましくは80〜130℃がよい。The maximum temperature of the film heated by the heating rj-ru (approximately 50 to 150°C) 2 Uruga 80 to
130"'C is preferable 11-V). If this temperature is too low, the heat treatment will be insufficient, and if it is too high, the strength of the film will decrease (-7, or it will become sticky and roll easily!! This is not desirable because the film may shrink abnormally, become unusable, or lose its properties as a biaxially stretched film.The film that has been heat-treated with this heating roll and just before leaving the roll has a surface of the roll. The surface temperature of the roll is approximately 50-150"C, more preferably 80-130"C.
前記熱風処理におけるフィルムの最高温度り50〜15
(1”C程度を採用しうるが、好ましくはこの範囲内
で80〜180 ’Cがよい。このような加熱をするた
めに熱風の温度は50−170°C1好ましくは80〜
150°Cを採用しうる。この熱風加熱処理におけるフ
ィルムの最高温度が50 ”Cより低いと熱収縮処理が
不充分となシ、150 ’Cを越えるとフィルムが粘着
性となってロールに巻き付き易くなり、また横方向の収
縮が大きくなり過ぎて好ましくない1゜他方、熱風処理
におけるフィルムの最高温度が、加熱ロールで加熱され
たフィルムの最高温度よす低過ぎると縦方向の収縮が不
充分となり、高−5=
過き゛ると縦方向の収縮だけでなく横方向の収縮も大き
くなって好ま(7くない。このためこの工程におけるフ
ィルムの最高流度は、50〜150°Cの範囲において
、加熱ロールで加熱されたフィルムの最高温度より20
°C低い温度ないし20℃高い温度が好ましい。The maximum temperature of the film in the hot air treatment is 50 to 15
(A temperature of about 1"C can be adopted, but preferably 80 to 180'C within this range. For such heating, the temperature of the hot air is 50 to 170 degrees Celsius, preferably 80 to 180'C.
150°C can be adopted. If the maximum temperature of the film in this hot air heating treatment is lower than 50'C, the heat shrinkage treatment will be insufficient, and if it exceeds 150'C, the film will become sticky and tend to wrap around the roll, and it will shrink in the lateral direction. On the other hand, if the maximum temperature of the film in the hot air treatment is too low compared to the maximum temperature of the film heated with a heating roll, the shrinkage in the longitudinal direction will be insufficient, and if the temperature is too high - 5 = Not only the shrinkage in the longitudinal direction but also the shrinkage in the transverse direction is large (7), which is preferable. Therefore, the maximum flow rate of the film in this process is in the range of 50 to 150°C, when the film heated with a heating roll is 20 above the maximum temperature
Temperatures from 0.degree. C. lower to 20.degree. C. higher are preferred.
以下図面によって本発明を更に詳しく説明する。The present invention will be explained in more detail below with reference to the drawings.
ニップロール2.4及び加熱ロール8は加熱ロール方式
の熱処理工程であシ、未熱処理二軸延伸フィルム1け加
熱ロール3の表面に接することによっで鹸フィルムの走
行方向(縦)、巾方向(横)共に収縮応力が生じ、該フ
ィルムの張力を緩和すれば収縮を起こす1.この工程で
重要な点は、該フィルムが加熱ロール3に密着しない場
合は、該フィルムの平担性が極めて悪くなり、良好な製
品は得られない。従ってニップロール2.4間の該フィ
ルムには張力が必要であり、ニップロール2の周速(加
熱ロールへの送り出し速度)に対するニップロール4の
周速 6−
(加熱ロールからの引取速度)の減速度e」、該フィル
ムの自由11又縮度よシ/」1さくなければならない。The nip roll 2.4 and the heating roll 8 are used in the heating roll type heat treatment process, and by contacting the surface of the heating roll 3 with one unheated biaxially stretched film, the nip roll 2.4 and the heating roll 8 are used in the running direction (longitudinal) and width direction ( 1. Horizontal) Shrinkage stress occurs in both cases, and if the tension of the film is relaxed, shrinkage will occur.1. The important point in this step is that if the film does not come into close contact with the heating roll 3, the flatness of the film will be extremely poor and a good product will not be obtained. Therefore, tension is required in the film between the nip rolls 2 and 4, and the deceleration e of the circumferential speed of the nip roll 4 relative to the circumferential speed of the nip roll 2 (speed of delivery to the heating roll) 6 - (take-up speed from the heating roll) '', the freedom of the film must be reduced by 11 and the degree of shrinkage must be reduced by 1.
一方該フイルムの横方向の収縮に対(、ては、該フィル
ムと加熱ロール3の接触摩擦力に」こって抑制を受ける
が、収縮応力に対する摩擦力11極めて小さく、該フィ
ルムは充分に収縮(2イ得る。On the other hand, the shrinkage of the film in the lateral direction is suppressed by the contact friction force between the film and the heating roll 3, but the friction force 11 against the shrinkage stress is extremely small, and the film does not shrink sufficiently. Get 2 points.
この結果ニップロール4を経た段階で得らt]る熱処理
フィルムは、横方向に対して6:はは充分な収縮を伴う
熱処理がな濾ねているが、縦方向に対してはこれらが充
分でない。このことが次工程において問題となる事は一
般に知られている。As a result, the heat-treated film obtained after passing through the nip roll 4 has been heat-treated with sufficient shrinkage in the transverse direction, but this is not sufficient in the longitudinal direction. . It is generally known that this poses a problem in the next process.
本発明ではこれらの問題を解決するためにニップロール
4の直後に熱風加熱室5を設けている。加熱ロール3に
よって熱処理されたフィルムは、熱風加熱室5によって
再加熱することによって再び収縮応力を生じるが、該フ
ィルムの横方向に対する収縮を伴なう熱処理(・」ニッ
プロール4以前で充分に行われているため再加熱による
収縮応力の発生は小さい1.一方該フイルムの縦方向に
対j2では前処理工程での効果が少なかったため、当工
程に訃いて再び大きな収縮応力を生じ、ニップロール4
に対するニップロール6の周速を減速することによって
縦方向に対しての収縮処理ができる。従ってニップロー
ル6を経て得られる熱処理後のフィルム7は縦・横方向
共に収縮を伴う熱処理がなされており、その物性は満足
のいくものとなる。In the present invention, a hot air heating chamber 5 is provided immediately after the nip roll 4 in order to solve these problems. The film that has been heat treated by the heating roll 3 is reheated by the hot air heating chamber 5 to generate shrinkage stress again. 1.On the other hand, in the longitudinal direction of the film, the effect of the pretreatment process was small, so large shrinkage stress was generated again in this process, and the nip roll 4
By reducing the circumferential speed of the nip roll 6 relative to the length, shrinkage processing can be performed in the longitudinal direction. Therefore, the heat-treated film 7 obtained through the nip roll 6 has been heat-treated to cause shrinkage in both the longitudinal and transverse directions, and its physical properties are satisfactory.
加熱ロールの次の段階の加熱方法と(7ては温度が安定
(〜、かつ遠赤外脚加熱方式が持つような高滉部を持/
こない熱風加熱方式が最も適しているのである1、熱風
加熱室5の有効長さについては、本発明の目的とする効
果を得るために該フィルムの通過時間を1秒以上とする
長さとするのが好ましい。The heating method for the next step of the heating roll (7) is that the temperature is stable (~ and has a high temperature part like the far infrared leg heating method).
The hot air heating method is most suitable.1.The effective length of the hot air heating chamber 5 should be such that the passage time of the film is 1 second or more in order to obtain the desired effect of the present invention. is preferred.
この様に本発明によれば欠点のある加熱ロール方式の熱
溶」!11装置の直後に簡単な熱風加熱域を設けること
に、1′って、全体とU〜で簡素で小型かつ操作が容易
な装置によって優秀な熱処理効果が得られる。In this way, according to the present invention, the heating roll method has disadvantages! By providing a simple hot air heating area immediately after the device 11, excellent heat treatment effects can be obtained with the device 1' which is simple, compact and easy to operate.
実施例1,2
MFRl、0の結晶性ポリプロピレンを用いナユーブラ
一方式によって6×6倍の二軸延伸フィルムを作り、こ
れを図面に]J<す2つり熱溶」111装置を用いて第
1表に示す条件の1・で収縮1熱処川!した。得られた
フィルムの性質を同表に示す。Examples 1 and 2 A biaxially stretched film of 6 x 6 times was made using the Naubular method using crystalline polypropylene with an MFRl of 0, and this was drawn using a 111 equipment. Shrinkage 1 heat treatment river under 1 of the conditions shown in the table! did. The properties of the obtained film are shown in the same table.
これらのフィルムはこの表に示すように良好な性質をボ
しており、実用トの評価も優秀であ′−)だ。As shown in this table, these films have good properties and have excellent practical evaluations.
比較例1.2
実施例1.2と同じポリプロピレンを用い、同様にして
作った二軸延伸フィルムを図7ft1に示す加熱ロール
のみを用いて第2表に示す条件の下で収縮熱処理した。Comparative Example 1.2 A biaxially stretched film made in the same manner as in Example 1.2 using the same polypropylene was subjected to shrinkage heat treatment under the conditions shown in Table 2 using only the heating roll shown in FIG. 7ft1.
1得られたフイルノ、の性質を同表に示す。比較例1の
フィルムは明らかに縦・横に不均衡な物性を示17、比
較例2のフィルムは平担性不良で実用に供しえないもの
であった。1 The properties of the obtained fluoro are shown in the same table. The film of Comparative Example 1 showed clearly unbalanced physical properties in the vertical and horizontal directions17, and the film of Comparative Example 2 had poor flatness and could not be put to practical use.
9− 第 1 表 10− 第2表9- Table 1 10- Table 2
図面は本発明による1軸延伸フィルムの熱処理工程の概
略を示すフローシートである。
この図において数字に次のものと示す。
1:未熱処理二軸延伸フィルム。
2:ニツブロール、 8:加熱ロール。
4:ニツブロール、 5:熱風加熱域。
6:ニップロール。
7:処坊(フィルム(製品)
以上The drawing is a flow sheet showing an outline of the heat treatment process for a uniaxially stretched film according to the present invention. In this figure, the numbers are shown as follows. 1: Unheated biaxially stretched film. 2: Nitsub roll, 8: Heating roll. 4: Nitsuburol, 5: Hot air heating area. 6: Nip roll. 7: Tokobo (film (product))
Claims (4)
熱ロールに接触させなから熱処理し、この際該加熱ロー
ル上での前記フィルムの熱収縮を制限することによって
該フィルムを該加熱ロールVこ密着させ、■次いで熱風
処理することを特徴とするポリプロピレン系二軸11[
伸フィルムの製造方法。(1) A biaxially stretched polypropylene film is q) heat-treated without contacting with a heating roll, and at this time, the film is brought into close contact with the heating roll by limiting the thermal shrinkage of the film on the heating roll. , ■ Polypropylene biaxial 11 [
Method for producing stretched film.
表面温度が被熱処理フィルムと接触する的前において5
0・〜150″Cであることを特徴とする前nC方法。(2) In addition to the method described in item 1, the surface temperature of the heating roll is 5.
A pre-nC method characterized in that the temperature is 0.~150''C.
直後のフィルムの温度が50〜150°Cであること全
特徴とする前記方法。(3) The method according to item 1 or 2, wherein the temperature of the film immediately after the hot air treatment is 50 to 150°C.
のフィルトの温度が\前記加熱ロール処理面後の温度よ
り20 ”(−;低い温度ないし20″C高い温度であ
ることを1特徴とするAtJ配方法。(4) In the method described in item 3, the temperature of the filter immediately after the hot air treatment is 20"(-; lower to 20" C higher than the temperature after the heating roll treatment surface. Characteristic AtJ arrangement method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1131582A JPS58140220A (en) | 1982-01-27 | 1982-01-27 | Heat treatment of polypropylene biaxially oriented film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1131582A JPS58140220A (en) | 1982-01-27 | 1982-01-27 | Heat treatment of polypropylene biaxially oriented film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58140220A true JPS58140220A (en) | 1983-08-19 |
JPH0261371B2 JPH0261371B2 (en) | 1990-12-19 |
Family
ID=11774576
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1131582A Granted JPS58140220A (en) | 1982-01-27 | 1982-01-27 | Heat treatment of polypropylene biaxially oriented film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58140220A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH088777A (en) * | 1994-06-15 | 1996-01-12 | Nec Corp | Radio data communication equipment |
CN102555242A (en) * | 2010-12-28 | 2012-07-11 | 苏州工业园区久禾工业炉有限公司 | Heating system for heating membrane products |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3554570B2 (en) * | 1993-12-28 | 2004-08-18 | 株式会社アイペック | Method for producing crystalline thermoplastic resin sheet or film |
-
1982
- 1982-01-27 JP JP1131582A patent/JPS58140220A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH088777A (en) * | 1994-06-15 | 1996-01-12 | Nec Corp | Radio data communication equipment |
CN102555242A (en) * | 2010-12-28 | 2012-07-11 | 苏州工业园区久禾工业炉有限公司 | Heating system for heating membrane products |
Also Published As
Publication number | Publication date |
---|---|
JPH0261371B2 (en) | 1990-12-19 |
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